# Part 70 Air Quality Permit
**Holcim (US) Inc.**

**– Holly Hill Plant**  **200 Safety Street Holly Hill, South Carolina 29059**  (permit updated 6/27/05 and 8/19/05)
Inaccordance with the provisions of the Pollution Control Act, Sections 48

- 1

- 50(5) and 48

- 1

- 110(a), and the 1976 Code of Laws of South Carolina, as amended, Regulation 61

- 62, the above named permittee is hereby

granted permission to discharge air contaminants into the ambient air. The Bureau of Air Quality

a uthorizes the operation of this facility and its applicable equipment specified herein in accordance with the plans, specifications and other information submitted in the Title V permit application dated April 1996, August 2000, November 2000, and November 2002. This permit is subject to and conditioned upon the terms, limitations, standards, and schedules contained in or specified on the 106 pages, with the accompany ing attachments, of this permit.

**Permit Number: TV** **- 1860**  **- 0005**  **Effective Date: July 1, 2003**  **Issue Date: April 15, 2003**  **Expiration Date: June 30, 2008** 

**Director, Engineering Services Division Bureau of Air Quality** **Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **2 of 106**  (permit updated 6/27/05 and 8/19/05)

**RECORD OF REVISIONS Revision**  **Num ber**  **Final**

**Revision Date**  **Type of Revision**

**(AA, MM, SM) Description of Change (Specific Parts,**  **Sections, and Tables Revised or Added)**

1 5/14/03 AA Updated sections 5 through 10 for missing equipment; updated attachment B for insignificant activities; updated attachment C for regulations not applicable to

the facility. 2 9/23/03 AA Changing the control device description for BH85 within table 5.6 control devices unit ID 06

- Cement

Loadout Equipment 2 9/23/03 MM Reflect changes done to the piping system to Tank 146 (Table 5.14 unit ID 07

- Tank Equipment).

3 10/22/03 AA R170, R171, R174, R175, R178 , R180, R195, R204 has been moved from Table 5.16 and Table 5.9 into Table 5.15 and Table 5.8, to reflect applicability to NSPS, Subpart OOO and not MACT, Subpart LLL. R183 and R185 has moved from Table 5.15 and Table 5.9 into Table 5.16 and Table 5.8, to reflect applicability to MACT, Subpart LLL and not NSPS,

Subpart OOO.

4 6/27/05 MM Adding construction permit 1860

- 0005

- CZ: 1. Truck Load Out Silo System. W902 through W905 has been added to Tables 5.13, 5.20 and 6.7. Condition 5.E.6(g) has been added to reflect a process weight rate limitation for the system.

4 6/27/05 MM Adding construction permit 1860

- 0005

-DA: 1. Adding the Sampson Feeder System to Table 5.4, 5.11, 5.18, and 6.5. Condition 5.E.4(ii) has been added to reflect a process weight rate limitation for

the system.

4 6/27/05 MM Adding construction permit 1860

- 0005

-DB: 1. Relocate an existing 100,000 gallon No.6 Fuel Oil Storage Tank and modify it to serve as a non

hazardous waste derived fuel (NHWDF) storage tank. 2. Addition of three new 60, 000 gallon NHWDF storage tanks and a new 5.0 million Btu/hr boiler to heat two of the four NHWDF storage tank lines. Changes have been made to Tables 5.1, 5.7, 5.14, 5.21, 6.8, and conditions 5.E.7(j)(k)(l)(m) and 6.B.8(m) have been added.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **3 of 106**  (permit updated 6/27/05 and 8/19/05) **RECORD OF REVISIONS Revision**  **Num ber**  **Final**

**Revision Date**  **Type of Revision**

**(AA, MM, SM) Description of Change (Specific Parts,**  **Sections, and Tables Revised or Added)**

4 6/27/05 MM Adding construction permit 1860

- 0005

-DC: 1. Cement Dome Bucket Elevator Retrofit Project (Aliviator project), to improve the product recovery associated with the transfer of cement from Finishing Mills 5 and 6 to the existing dome, truck surge bin, rail silo s and the new cement silos. Two new dust collectors (S188 and S189) will be installed for PM/PM10 control. The existing cement dome emission source, C319 (S85). Changes have been made to Tables 5.5, 5.12, 5.19 and 6.6 and condition

5.E.4(d) has been added 4 6/27/05 MM Adding conditions to allow for maintenance activities to be perform on the inlet pressure port without

shutting off the HWDF. 4 6/27/05 MM Voiding out all references to the old facility in Parts 8.0 and 9.0. 4 6/27/05 AA Updated condition 4 .B.6. 5 8/19/05 AA Removing of all non

- applicable 40 CFR 63, Subpart DD requirements, originally added through construction permit 1860

- 0005

- CB. AA = Administrative Amendment MM = Minor Modification SM = Significant Modification Send copies of all revis ions to Permit File, Main File, District EQC Office, US EPA, and Facility Contact.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **4 of 106**  (permit updated 6/27/05 and 8/19/05)
**TABLE OF CONTENTS**

**Part 1.0 GENERAL INFORMATION**  A. Applicable Permit Dates B. Facility

Information C. Facility

Address D. Facility

Billing Address

**Part 2.0 APPLICABILI**  **TY**

**Part 3.0 GENERAL CONDITIONS**  A. Permit Issuance B. Permit Expiration and Renewal C. Severability D. Fee Assessment and Pay ment E. Submittal of Information F. Public Participation G. Permit Reopening H. Temporary

Sources I. Emergency

Provisions J. Prop erty

Rights K. Economic Incentives, Marketable Permits, Emission Trading L. Title IV Sources M. Administrative Permit Amendments N. Minor Permit Modifications O. Significant Modification Procedures P. Duty

to Comply Q. Inspection and Entry R. Compliance Requirements S. Schedule of Compliance T. Need to Halt or Reduce Activity Not a Defense U. Operational Flexibility**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **5 of 106**  (permit updated 6/27/05 and 8/19/05)
**Part 4.0 FACILITY WIDE REQUIREMENTS**  A. Emissions Limits and Standards B. Facility

Wide Conditions

**Part 5.0 EMISSION UNIT REQUIREMENTS**  A. Emission Unit Description B. Control Devices Description C. Equipment Description D. Emissions Limits and Standards E. Emission Unit Conditions

**Part 6.0 MONITORING AND REPORTING REQUIREMENTS**  A. Monitoring and Reporting B. Monitoring and Reporting Conditions

**Part 7.0 ADDITIONAL CONDITIONS**  A. Specific Conditions B. Operational Flexibility C. Compliance Schedule D. Permit Shield

**ATTACHMENT A -**  **Modeled Emission Rates ATTACHMENT B**  **- Insignificant Activities**  **ATTACHMENT C -**  **Applicable and Non -**  **applicable Fe deral and State Regulations** **Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **6 of 106**  (permit updated 6/27/05 and 8/19/05)
**PART 1.0 GENERAL INFORMATION**

**A. APPLICABLE PERMIT DATES**  IS SUE DATE : April 15, 2003 EFFECTIVE DATE : July 1, 2003 EXPIRATION DATE : June 30, 2008 RENEWALAPPLICATION DUE : December 31, 2007

B. FACILITY I

NFORMATION ENVIRONMENTALCONTACT : Glenn Ray nor CONTACT TELEPHONE NUMBER : (803) 496

-2756 INTERNET E

-MAIL ADDRESS : glenn.ray nor@holcim.com FACILITY LOCATION : 200 Safety Street / Highway

453 COUNTY : Orangeburg SIC CODE(S) : 3241 AFS CODE : 45 07500005 **C. FACILITY ADDRESS**  FACILITY NAME : Holcim (US) Inc.

– Holly Hill Plant ADDRESS : 200 Safety Street / Highway

453 : Holly Hill, South Carolina 29059 D. FACILITY BILLING ADDRESS FACILITY BILLING NAME : Holcim (US) Inc.

– Holly Hill Plant ADDRESS : 200 Safety Street / highway

453 : Holly Hill, South Carolina 29059**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **7 of 106**  (permit updated 6/27/05 and 8/19/05)
**PART 2.0 APPLICABILITY** [SC Regulation 61

- 62.70.3(a)] The following sources are subject to permitting requirements of Part 70: 1. Any

major source; 2. Any source, including an area source, subject to a standard, limitation, or other requirement under Section 111 of the Clean Air Act (Act); 3. Any

s ource, including an area source, subject to a standard or other requirement under Section 112 of the Act, except that a source is not required to obtain a permit solely b ecause it is subject to regulations or requirements under Section 112(r) of the Act; 4. Any

affected source under the Title IV Acid Rain Program; 5. Any

s ource in a source category designated by the Administrator of the US Environmental Protection Agency (US EPA) (Administrator) pursuant to this Section; and 6. Any

s ource listed in SC Regulation 61

- 62.70.3(a) that is exempt from the requirement to obtain a permit under SC Regulation 61

- 62.70.3(b) may opt to apply for a permit under this Part 70 program. The following source categories are exempted from the obligation to obtain a Part 70 permit, but are not exempted from other SC Department of Health and Environmental Control (Department) and US EPA requirements [SC Regulation 61

- 62.70.3(b)(4)]: 1. All sources and source categories that would be required to obtain a permit solely because they

are subject to 40 CFR 60, Subpart AAA

- Standards of Performance for New Residential Wood Heaters; and 2. All sources and source categories that would be required to obtain a permit solely because they

are subject to 40 CFR 61, Subpart M

- National Emission Standard for Hazardous Air Pollutants for Asbestos, Section 61.145, Standard for Demolition and Renovation. Any p erson that operates or proposes to operate a particular source or installation may submit a request in writing that the Department makes a determination as to whether a particular source or installation is subject to the permit requirements of this regulation. The request must contain such information as is believed sufficient for the Department to make the requested determination. [SC Regulation 61

- 62.70.3(e)]**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **8 of 106**  (permit updated 6/27/05 and 8/19/05)
**PART 3.0 GENERAL CONDITIONS**  This section describes conditions and provisions applicable to all Part 70 sources. Specific source category conditions and requirements are contained in Part 5.0 of this permit. (Revised 05/21/99)
**A. PERMIT ISSUANCE**  [SC Regulation 61

- 62.70.7(a)(1)] A permit, permit modification, or renewal may b e issued only

i f the following conditions have been met: 1. The Department has received a complete application for a permit, permit

modification, or permit renewal; 2. Except for modifications qualifying for minor permit modification procedures under SC Regulation 61

- 62.70.7(e)(2) and (3), the Department has complied with the requirements for public participation under SC Regulation 61

- 62.70.7(h); 3. The Department has complied with the requirements for notifying and responding to affected States under SC Regulation 61

- 62.70.8(b); 4. The conditions of the permit provide for compliance with all applicable requirements and the requirements of Part 70; and 5. The Administrator has received a copy o f the proposed permit and any notices required under SC Regulation 61

- 62.70.8(a) and (b), and has not objected to issuance of the permit under SC Regulation 61

- 62.70.8(c) within the required time frame. A Title V operating permit does not excuse any f acility f rom the preconstruction permitting requirements under SC Regulation 61

- 62.1.

**B. PERMIT EXPIRATION AND RENEWAL**  [SC Regulation 61

- 62.70.7(c)] (Revised 11/13/98) Permit expiration terminates the source’s right to operate unless a timely and complete renewal application has been submitted consistent with SC Regulation 61

- 62.70.5(a)(1)(iii), 62.70.5(a)(2)(iv), and 62.70.7(b). In this case, the permit shall not expire until the renewal permit has been issued or denied. All terms and conditions of the permit including any permit shield that may b e granted pursuant to SC Regulation 61

- 62.70.6(f) shall remain in effect until the renewal permit has been issued or denied. Permits being renewed are subject to the same procedural requirements, including those for public participation, affected State and US EPA review, that apply to initial permit issuance.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **9 of 106**  (permit updated 6/27/05 and 8/19/05)

**C. SEVERABILITY**  [SC Regulation 61

- 62.70.6(a)(5)] The provisions of this permit are severable, and if any provision of this permit, or application of any provision of this permit to any circumstance is held invalid, the application of such provision to other circumstances, and the remainder of this permit shall not be affected thereby

.
**D. FEE ASSESSMENT AND PAYMENT**  [SC Regulation 61

- 62.70.6(a)(7)] The owners or operators of Part 70 sources shall pay f ees to the Department consistent with the fee schedule approved pursuant to South Carolina Regulation 61

- 62.70.9.

**E. SUBMITTAL OF INFORMATION**  [SC Regulation 61

- 62.70.6(a)(6)(v)] The permittee shall furnish to the Department, within a reasonable time, any information that the Department may

request, in writing, to determine whether cause exists for modifying, revoking, reissuing, or terminating the permit or to determine compliance with the permit. Upon request, the permittee shall also furnish to the Department copies of records required to be kept by the permit or, for information claimed to be confidential, the permittee may f urnish such records directly to the Administrator along with a claim of confidentiality

. The Department may also request that the permittee furnish such records directly to the Administrator along with a claim of confidentiality

.
**F. PUBLIC PARTICIPATION**  [SC Regulation 61

- 62.70.7(h)] Except for modifications qualifying for minor permit modification procedures, all permit proceedings, including initial permit issuance, significant modifications, and renewals, shall provide adequate procedures for public notice including offering an opportunity f or public comment and hearing on the draft permit. These procedures shall meet all requirements of SC Regulation 61

- 62.70.7(h).

**G. PERMIT REOPENING**  [SC Regulation 61

- 62.70.7(f)] (Revised 05/21/99) This permit shall be reopened and revised under any of the following circumstances: 1. Additional applicable requirements under the Act become applicable to a ma jor Part 70 source for which three or more years remain on the original term of the permit. Such revisions shall be made not later than eighteen (18) months following promulgation of relevant standards or regulations unless the regulation specifically provides for a longer compliance period. No such reopening is required if the**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **10 of 106**  (permit updated 6/27/05 and 8/19/05) effective date of the requirement is later than the date on which the permit is due to expire, unless the original permit or any o f its terms and conditions has been extended pursuant to SC Regulation 61

- 62.70.7(c)(1)(ii). 2. Additional requirements, including excess emission requirements, become applicable to an affected source under the acid rain program. Excess emissions offset plans shall be deemed to be incorporated into this permit upon approval by the Administrator. 3. The Department or EPA determines that the permit contains a material mistake or that inaccurate statements were made in establishing the emissions standards or other terms or conditions of the permit. 4. The Administrator or the Department determines that the permit must be revised or revoked to assure compliance with the applicable requirements. Inaddition, the permit may b e modified, revoked, reopened, and reissued, or terminated for cause by the Department. The filing of a request by the permittee for a permit modification, revocation and reissuance, or termination, or of a notification of planned changes or anticipated noncompliance does not stay any permit condition. [SC Regulation 61

- 62.70.6(a)(6)(iii)] Proceedings to reopen and issue a permit shall follow the same procedures as apply to initial permit issuance and shall affect only those parts of the permit for which cause to reopen exists. Such reopenings shall be as expeditious as practicable. Reopenings shall not be initiated before a notice of such intent is provided to the Part 70 source by the Department at least thirty (30) days in advance of the date that the permit is to be reopened, except that the Department may provide a shorter time period in the case of an emergency

.
**H. TEMPORARY SOURCES**  [SC Regulation 61

- 62.70.6(e)] Inaccordance with SC Regulation 61

- 62.70.6(e), the Department may i ssue a single permit authorizing emissions from similar operations by the same source owner or operator at multiple temporary

locations. The operation must be temporary and involve at least one change in location during the term of the permit. No sources subject to Title IVo f the Act shall be permitted as a temporary

source.
**I. EMERGENCY PROVISIONS**  [ SC Regulation 61

- 62.70.6(g)(3)] (Revised 05/21/99) Inthe case of an emergency, as defined in SC Regulation 61

- 62.70.6(g), the permittee shall verify a n affirmative defense of emergency through properly

signed, contemporaneous operating logs, or other relevant evidence that:**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **11 of 106**  (permit updated 6/27/05 and 8/19/05) 1. An emergency

o ccurred and that the permittee can identify the cause(s) of the emergency; 2. The permitted facility was at the time being properly operated; and 3. During the period of the emergency the permittee took all reasona ble steps to minimize levels of emissions that exceeded the emission standards, or other requirements in the permit. Additionally, the permittee shall submit verbal notification of the emergency to the Department within twenty
- four (24) hours of the time when emission limitations were exceeded, followed by written notifications within thirty (30) days. This notice fulfills the requirement of SC Regulation 61

- 62.70.6(a)(3)(iii)(B). This notice must contain a description of the emergency, any steps taken to mitigate emissions, and corrective actions taken. This provision is in addition to any emergency

or upset provision contained in any a pplicable requirement. In any

enforcement proceeding, the permittee seeking to establish the occurrence of an emergency has the burden of proof.

**J. PROPERTY RIGHTS**  [SC Regulation 61

- 62.70.6(a)(6)(iv)] This permit does not convey any property rights of any

sort, or any

exclusive privilege.

**K. ECONOMIC INCENTIVES, MARKETABLE PERMITS, EMISSION TRADING**  [SC Regulation 61

- 62.70.6(a)(8)] No permit revision shall be required, under any a pproved economic incentives, marketable permits, emissions trading and other similar programs or processes for changes that are provided for in this permit.

**L. TITLE IV SOURCES**  [SC Regulati on 61

- 62.70.6(a)(4)] The permittee is prohibited from emissions exceeding any allowances that the source lawfully holds under Title IVo f the Act or the regulations promulgated thereunder. No permit revision shall be required for increases in emissions that are authorized by allowances acquired pursuant to the acid rain program, provided that such increases do not require a permit revision under any other applicable requirement. No limit shall be placed on the number of allowances held by a source. The source may

not, however, use allowances as a defense for noncompliance with any other applicable requirement. Any

such allowances shall be accounted for according to the procedures established in regulations promulgated under Title IV of the Act.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **12 of 106**  (permit updated 6/27/05 and 8/19/05) Where an applicable requirement of the Act is more stringent than an applicable requirement of regulations promulgated under Title IVo f the Act, both provisions shall be incorporated into the permit and shall be enforceable by the Administrator. [SC Regulation 6 1

- 62.70.6(a)(1)(ii)]

**M. ADMINISTRATIVE PERMIT AMENDMENTS**  [SC Regulation 61

- 62.70.7(d)(3)] An administrative permit amendment as defined in SC Regulation 61

- 62.70.7(d) can be made by t he Department consistent with the following: 1. The Department shall take no more than sixty ( 60) days from receipt of a request for an administrative permit amendment to take final action on such request, and may incorporate such changes without providing notice to the public or affected States provided that it designates any such permit revisions as having been made pursuant to this paragraph. 2. The Department shall submit a copy of the revised permit to the Administrator. 3. The source may

implement the changes addressed in the request for an administrative amendment immediately

u pon submittal of the request, except transfer/ownership which must comply

with SC Regulation 61

- 62.1, Section II(E).

**N. MINOR PERMIT MODIFICATIONS**  [SC Regulation 61

- 62.70.7(e)(2)] Minor permit modifications can be made by the Department in accordance with SC Regulation 61

- 62.70.7(e)(2)(i). An application requesting the use of minor permit modification procedures shall meet the requirements of SC Regulation 61

- 62.70.5(c) and shall include items as specified in SC Regulation 61

- 62.70.7(e)(2)(ii). The Department may

modify the procedure outlined in SC Regulation 61

- 62.70.7(e)(2) to process groups of a source’s applications for certain modifications eligible for minor permit modification processing. Group processing of minor permit applications will proceed as outlined in SC Regulation 61

- 62.70.7(e)(3).

**O. SIGNIFICANT MODIFICATION PROCEDURES**  [SC Regulation 61

- 62.70.7(e)(4)] Significant permit modification procedures shall be used for applications requesting permit modifications listed in SC Regulation 61

- 62.70.7(e)(4)(i). S ignificant permit modifications shall meet all requirements of this Part 70, including those for applications, public participation, review by affected States, and review by EPA, as they

apply to permit issuance and permit renewal.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **13 of 106**  (permit updated 6/27/05 and 8/19/05) **P. DUTY TO COMPLY**  [SC Regulation 61

- 62.70.6(a)(6)(i)] The permittee must comply with all of the conditions of this permit. Any p ermit noncompliance constitutes a violation of the SC Pollution Control Act and/or the Federal Clean Air Act and is grounds for enforcement action; for permit termination, revocation and reissuance, or modification; or for denial of permit renewal application.
**Q. INSPECTION AND ENTRY**  [SC Regulation 61

- 62.70.6(c)(2)] Upon presentation of credentials and other documents as may b e required by

law, the permittee shall allow the Department or an authorized representative to perform the following: 1. Enter upon the permittee’s premises where a Part 70 source is located or emissions

related activity

is conducted, or where records must be kept under the conditions of the permit. 2. Have access to and copy, at reasonable times, any records that must be kept under the conditions of the permit. 3. Inspect any

f acilities, equipment (including monitoring and air pollution control equipment), practices, or operations regulated or required under this permit. 4. As authorized by

the Act and/or the SC Pollution Control Act, sample or monitor at reasonable times substances or parameters for the purpose of assuring compliance with the permit or applicable requirements.

**R. COMPLIANCE REQUIREMENTS**  [SC Regulation 61

- 62.70.6(c)(5)] (Revised 05/21/99) Consistent with SC Regulation 61

- 62.70.6(a)(3), this permit contains compliance certification, testing, monitoring, reporting, and record keeping requirements sufficient to assure compliance with the terms and conditions of this permit. Any document (including reports) shall contain a certification by

a responsible official or designee that meets the requirements of SC Regulation 61

- 62.70 .5(d). The responsible official or designee shall certify, annually, compliance with the conditions of this permit. The compliance certification shall include the following: 1. The identification of each term or condition of the permit that is the basis of the certification. 2. The identification of the methods or means used for determining the compliance status with each term and condition during the certification period, and whether such**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **14 of 106**  (permit updated 6/27/05 and 8/19/05) methods or means provide continuous or intermittent data. 3. The status of compliance with the terms and conditions of the permit for the period covered by

the certification. 4. Such other facts as the Department may require to determine the compliance status of the source. 5. All compliance certifications shall be submitted to the Administrator as well as to the Department. The annual compliance certification shall be sent to the Environmental Protection Agency (EPA) and the South Carolina Department of Health and Environmental Control

- Bureau of Air Quality (SC DHEC

- BAQ) at the following addresses:

**US EPA, Region 4 SC DHEC**  **- BAQ**  **Air Enforcement Branch Technical Management Section**  **61 Forsyth Street 2600 Bull Street**  **Atlanta, GA 30303 Columbia, SC 29201**  **S. SCHEDULE OF COMPLIANCE**  [SC Regulation 61

- 62.70.5(c)(8)] (Revised 5/21/99) The permittee shall submit a compliance schedule that contains the following for all Part 70 sources that are not in compliance with all applicable rules: 1. A description of the source’s compliance status and where appropriate a compliance schedule with respect to all applicable requirements as follows: (a) For applicable requirements with which the source is in compliance, a statement that during the permit term the source will continue to comply with such requirements. (b) For applicable requirements that will become effective during the permit term, a statement that the source will meet such requirements on a timely basis, unless a more detailed schedule is expressly required by

the applicable requirement. (c) A schedule of compliance for sources that are not in compliance with all applicable requirements at the time of permit issuance. This schedule shall include a narrative description of how the source will achieve compliance, a schedule of remedial measures, including an enforceable sequence of actions with milestones, leading to compliance with all applicable requirements. This compliance schedule shall be at least as stringent as that contained in any j udicial consent decree or administrative order to which the source is**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **15 of 106**  (permit updated 6/27/05 and 8/19/05) subject. Any

such schedule of compliance shall be supplemental to, and shall not sanction noncompliance with, the applicable requirements on which it is based. 2. A schedule for submission of certified progress reports no less frequently than every six (6) months for sources required to have a schedule of compliance to remedy a violation. Progress reports shall meet the requirements of SC Regulation 61

- 62.70.6(c)(4)(i) and (ii). 3. The compliance plan content requirements specified in this paragraph shall apply a nd be included in the acid rain portion of a compliance plan for an affected source, except as specifically

superseded by

regulations promulgated under Title IVo f the act with regard to the schedule and method(s) the source will use to achieve compliance with acid rain emissions limitations. **T. NEED TO HALT OR REDUCE ACTIVITY NOT A DEFENSE**  [SC Regulation 61

- 62.70.6(a)(6)(ii)] Itshall not be a defense for a permittee in an enforcement action that it would have been necessary to halt or reduc e the permitted activity in order to maintain compliance with the conditions of this permit. **U. OPERATIONAL FLEXIBILITY**  [SC Regulation 61

- 62.70.7(e)(5)] Inaccordance with SC Regulation 61

- 62.70.7(e)(5), a permitted facility i s authorized to make changes within their facility without requiring a permit revision, if the changes are not modifications under Title Iof the Act and the changes do not exceed the emissions allowable under this permit. The permitted facility

shall provide the Administrator and the Department written notification as required by

SC Regulation 61

- 62.70.7(e)(5) at least seven (7) days prior to such changes. **PART 4.0 FACILITY WIDE REQUIREMENTS**  **A. EMISSIONS LIMITS AND STANDARDS**  Table 4.1 contains summaries of facility wide emission limits and standards. **TABLE 4.1 EMISSION LIMITS AND STANDARDS**  **Pollutant Limit/Standard**  **Regulation State Only**  **Requirem ent**  **Condition**

**Num ber**  State New

Source Review As Specified in

Attachment A SC Regulation 61

- 62.1, Section II (A) Yes 4.B.2 4.B.3 Toxic Air Pollutants As Specified in Attachment A SC Regulation 61

- 62.5, Std No. 8 Yes 4.B.3 Hazardous Air Pollution Comply With Regulation SC Regulation 61

- 62.4 No N/A**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **16 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 4.1 EMISSION LIMITS AND STANDARDS**  **Pollutant Limit/Standard**  **Regulation State Only**  **Requirem ent**  **Condition**

**Num ber**  Open Burning Comply With Regulation SC Regulation 61

- 62.2 No N/A Fugitive Emissions Comply With Regulation SC Regulation 61

- 62.6, Sec III No N/A Ozone Depleting Substances * 40 CFR Part 82, Subpart F No 4.B.7 Asbestos * 40 CFR Part 61.145 No 4.B.8 N/A = Not Applicable * Specific To Subpart The maximum allowable emission limits above are derived from the various Federal and State regulations that govern the operation of this ty pe of facility. All applicable facility wide emission limits and corresponding regulations are listed above. Additional operating requirements, which may be more stringent than those above, are contained in Part 5.0, Part 6.0, and Part 7.0 of this permit.

**B. FACILITY WIDE CONDITIONS**  (Revised 11/13/98) **Condition Num** **ber Condition** 
4.B.1 In accordance with SC Regulation 61

- 62.1, Section II, the permittee must comply with all applicable

statutes and regulations of the United States and the State of South Carolina. This permit does not relieve the permittee from compliance with applicable local laws, ordinances, and regulations.

4.B.2 Air dispersion mo deling (or other method) has demonstrated that this facility’s operation will not

interfere with the attainment and maintenance of any state or federal standard. Any changes in the parameters used in the air dispersion mo deling may require a review by the facility to determine continuing compliance with these standards. These potential changes include any decrease in stack height, decrease in stack velocity, increase in stack diameter, decrease in stack exit temperature, increase in building height or building additions, increase in emission rates, decrease in distance between stack and property line, changes in vertical stack orientation, and installation of a rain cap that impedes vertical flow. Parameters that are not required in the determination will not invalidate the demonstration if they are mo dified. The emission rates used in the determination are listed in Attachment A of this permit. Higher emission rates may be administratively incorporated into Attachment A of this permit provided a demonstration using thes e higher emission rates shows the attainment and maintenance of any state or federal standard or with any other applicable requirement. Variations from the input parameters in the demonstration shall not constitute a violation unless the maximum allowable ambient concentrations identified in the standard are exceeded.

4.B.3 The ow

ner/operator shall maintain this facility in compliance with the pollutant limitations in Part 4, Part 5, Part 6, Part 7, Part 8, Part 9, Part 10 and/or the emission rates as listed in Attachment A of this Part 70 operating permit, whichever is more restrictive. This is a State Only enforceable requirement. Should the facility wish to increase the emission rates listed in Attachment A, it may do so by the administrative process specified in condition 4.B.2**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **17 of 106**  (permit updated 6/27/05 and 8/19/05) **Condition Num** **ber Condition** 

4.B.4 A list of equipment which are considered insignificant pursuant to SC Regulation 61

- 62.70.5(c) has

been submitted with your Title V application and reviewed by our staff. The list, including source descriptions and citation for exemption, is summarized in Attachment B of the permit. A ttachment B excludes those activities identified in Part A of the insignificant activities list. Written notification to the Bureau of Air Quality is required for the addition of any new e quipment which may meet the definition of insignificant or exempt as described above, excluding those sources listed in Part A of the insignificant activities list. (Revised 11/13/98)

4.B.5 In accordance with SC Regulation 61

- 62.1 Section II, (C)(3), for all sources not required to have

continuous emissions monitors, in the event of any malfunction of air pollution control equipment or system, process upset or other equipment failure which results in discharges of air contaminants lasting for one hour or more and which are greater than those discharges described for normal operation in the permit application shall be reported to the local Environmental Quality Control (EQC) District office within twenty
- four (24) hours after the beginning of the occurrence . The permittee shall also submit a written report within thirty (30) days of the occurrence. This report shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality (BAQ). The report shall contain as a minimum, the following: the identity of the emission unit and associated equipment where excess emissions occurred, the magnitude of excess emissions, the time and duration of excess emissions, the steps taken to remedy the malfunction and to prevent a recurrence, documentation that control equipment and processes were at all times maintained and operated, to the maximum extent practicable, in a manner that was consistent with good practice for minimizing emissions. Such a report shall in no way serve to excuse, otherwise justify, or in any manner affect any potential liability or enforcement action resulting from the occurrence. This defines the Department’s definition of prom pt in its relation to the degree of reporting as specified by SC Regulation 61

- 62.70.6(a)(3)(iii) (b).
4.B.6 The ow

ners or operators of Part 70 sources shall complete and submit emissions inventories as required consistent with the schedule approved pursuant to SC Regulation 61

- 62.1, Section III. This requirement notwithstanding, an emissions inventory may be required at any time in order to determine the compliance status of any facility

.

4.B.7 The permittee shall comply with the standards for recycling and emissions reduction pursuant to 40

CFR Part 82, Subpart F, Protection of Stratospheric Ozone, Recycling and Emissions Reduction, except as provided for motor vehicle air conditioners (MVACs) in Subpart B. I f the permittee performs a service on motor (fleet) vehicles that involves ozone - depleting substance refrigerant in MVACs, the permittee is su bject to all applicable requirements of 40 CFR Part 82, Subpart B, Servicing of MVACs. 4.B.8 The permittee shall comply with the standards of performance for asbestos abatement operations

pursuant to 40 CFR Part 61.145 and SC Regulation 61

- 86.1, including , but not limited to, requirements governing training, licensing, notification, work practice, cleanup, and disposal.

(Part 5 updated 5/14/03) **PART 5.0 EMISSION UNIT REQUIREMENTS** 

**– NEW FACILITY**  **A. EMISSION UNIT DESCRIPTION**  Table 5.1 is a description of emission units located at this facility

. **TABLE 5.1 EMISSION UNITS** **Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **18 of 106**  (permit updated 6/27/05 and 8/19/05) **Unit ID**  **Unit Description Control Device Description**  01 Quarry System None 02 Raw Mill System Baghouse 03 Coal Mill System Baghouse 04 Kiln System Baghouse 05 Finish Mill System Baghouses 06 Cement Loadout Baghouses 07 Tanks Carbon Adsorption System (T

- 100, T147 though T

149), None (non hazardous waste tanks); Industrial furnace (Kiln) and/or Carbon Adsorber (HWDF only)

**B. CONTROL DEVICE DESCRIPTION**  Table 5.2 through 5.7 list descriptions of control devices located at this facility

. **TABLE 5.2 CONTROL DEVICES UNIT ID 02**  **- RAW MILL SYSTEM EQUIPMENT**  **Control Device ID Control Device Description**  **Installation Date**  **Pollutant(s)**

**Controlled** BH99 2,943 acfm Fabric Dust Collector 2003 P M BH100 5,592 acfm Fabric Dust Collector 2003 PM BH101 7,946 acfm Fabric Dust Collector 2003 PM BH102 5,886 acfm Fabric Dust Collector 2003 PM BH103 4,709 acfm Fabric Dust Collector 2003 PM BH118 3,532 acfm Fabric Dust Collector 2003 PM BH123 2,943 acfm Fabric Dust Collector 2003 PM BH127 5,297 acfm Fabric Dust Collector 2003 PM **TABLE 5.3 CONTROL DEVICES UNIT ID 03**  **- COAL MILL SYSTEM EQUIPMENT**  **Control Device ID Control Device Description**  **Installation Date**  **Pollutant(s)**

**Controlled** BH31 2,000 acfm Pulse Jet Dust Collector 1982 PM BH32 650 acfm Shaker Dust Collector 1980 PM BH33 2,000 acfm Fabric Dust Collector 1980 PM BH34 1,500 acfm Fabric Dust Collector 1980 PM BH95 66,323 acfm Fabric Dust Collector 2003 PM BH130 3,072 acfm Fabric Dust Collector 2003 PM BH132 1,001 acfm Fabric Dust Collector 2003 PM **TABLE 5.4 CONTROL DEVICES UNIT ID 04**  **- KILN EQUIPMENT**  **Control Device ID Control Device Description**  **Installation Date**  **Pollutant(s)**

**Controlled** BH83 8,920 acfm Pulse Jet Dust Collector 1997 PM BH9 4A 873,842 acfm Fabric Dust Collector 2003 PM BH94B 103,764 acfm Fabric Dust Collector 2003 PM BH104 3,826 acfm Fabric Dust Collector 2003 PM BH105 3,826 acfm Fabric Dust Collector 2003 PM**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **19 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.4 CONTROL DEVICES UNIT ID 04**  **- KILN EQUIPMENT**  **Control Device ID Control Device Description**  **Installation Date**  **Pollutant(s)**

**Controlled** BH78 3,532 acfm Pulse Jet Dust Collector 1982 PM BH106 6,475 acfm Fabric Dust Collector 2003 PM BH107 10,301 acfm Fabric Dust Collector 2003 PM BH108 4,415 acfm Fabric Dust Collector 2003 PM BH22 13,000 acfm Pulse Dust Collector 1982 PM BH23 1,000 acfm Pulse Jet Dust Collector 1997 PM BH187 12,000 acfm Pulse Jet Baghouse, utilized as a product recovery unit (PRU). 2005 PM
(page updated 9/23/03) **TABLE 5.5 CONTROL DEVICES UNIT ID 05**  **- FINISH MILL EQUIPMENT**  **Control Device ID Control Device Description**  **Installation Date**  **Pollutant(s)**

**Controlled** BH54 40,000 acfm Pulse Jet Dust Collector 1982 PM BH55 11,000 acfm Pulse Jet Dust Collector 1982 PM BH56 3,800 acfm Pulse Jet Dust Collector 1982 PM BH57 2,943 acfm Pulse Jet Dust Collector 1982 PM BH96 92,421 acfm Fabric Dust Collector 2003 PM BH97 92,421 acfm Fabric Dust Collector 2003 PM BH175 5,886 acfm Fabric Dust Collector 2003 PM BH115 7,063 acfm Fabric Dust Collector 2003 PM BH117 10,301 acfm Fabric Dust Collector 2003 PM BH119 7,063 acfm Fabric Dust Collector 2003 PM BH120 3,532 acfm Fabric Dust Collector 2 003 PM BH135 6,475 acfm Fabric Dust Collector 2003 PM BH114 7,063 acfm Fabric Dust Collector 2003 PM BH116 10,301 acfm Fabric Dust Collector 2003 PM BH121 3,532 acfm Fabric Dust Collector 2003 PM BH126 3,532 acfm Fabric Dust Collector 2003 PM BH136 6 ,475 acfm Fabric Dust Collector 2003 PM BH146 92,421 acfm Fabric Dust Collector 2003 PM BH147 92,421 acfm Fabric Dust Collector 2003 PM BH174 4,415 acfm Fabric Dust Collector 2003 PM BH169 5,300 acfm Plenum Pulse Dust Collector 1973 PM BH170 11,000 ac fm Pulse Jet Dust Collector 1982 PM BH171 5,737 acfm Shaker Dust Collector 1966 PM BH172 11,000 acfm Plenum Pulse Dust Collector 1970 PM BH177 4,415 acfm Fabric Dust Collector 2003 PM BH178 4,415 acfm Fabric Dust Collector 2003 PM BH180 4,709 acfm Fabric Dust Collector 2003 PM BH181 1,766 acfm Fabric Dust Collector 2003 PM BH188 8,000 acfm Fabric Dust Collector 2005 PM/PM10 BH189 8,000 acfm Fabric Dust Collector 2005 PM/PM10 **TABLE 5.6 CONTROL DEVICES UNIT ID 06** **- CEMENT LOADOUT EQUIPMENT** **Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **20 of 106**  (permit updated 6/27/05 and 8/19/05)
**Control D evice ID**  **Control Device Description Installation**  **Date Pollutant(s)** 

**Controlled** BH67 16,000 acfm Pulse Jet Dust Collector 1966 PM BH68 16,000 acfm Pulse Jet Dust Collector 1966 PM BH63 2,250 acfm Pulse Jet Dust Collector 1966 PM BH64 1,500 acfm Pulse Jet Dust Collector Prior to 1971 PM BH65 2,000 acfm Pulse Jet Dust Collector Prior to 1971 PM BH66 1,667 acfm Shaker Dust Collector Prior to 1971 PM BH90 1,800 acfm Fabric Dust Collector 2003 PM BH91 1,800 acfm Fabric Dust Collector 2003 PM BH122 8,829 acfm Fabric Dust Collector 2003 PM BH113 8,800 acfm Pulse Jet Baghouse 1996 PM BH85 12,000 acfm Pulse Jet Dust Collector 1999 PM BH86 12,000 acfm Pulse Jet Dust Collector 1999 PM BH87 6,900 acfm Pulse Jet Dust Collector 1999 PM BH88 4,300 acfm Pulse Jet Dust Collector 1999 PM BH89 2,000 acfm Pulse Jet Dust Collector 1999 PM BH144 1,825 acfm Pulse Jet Dust Collector 1999 PM BH145 1,825 acfm Pulse Jet Dust Collector 1999 PM BH137 6,475 acfm Fabric Dust Collector 2003 PM BH138 7,357 acfm Fabric Dust C ollector 2003 PM BH176 2,943 acfm Fabric Dust Collector 2003 PM BH179 12,949 acfm Fabric Dust Collector 2003 PM BH183 8,829 acfm Fabric Dust Collector 2003 PM BH184 2,943 acfm Fabric Dust Collector 2003 PM **TABLE 5.7 CONTROL DEVICES UNIT ID 07**  **- TANK**  **EQUIPMENT Control Device ID**  **Control Device Description Installation**  **Date Pollutant(s)** 

**Controlled** VRU111 Backup Carbon Adsorption System 2000 VOC K300 Industrial Furnace (Kiln) 2003 VOC VRU112 Backup Carbon Adsorption System 2003 VOC CC

- 1 Carbon Adsorption System (Carbon Canister) 2004 VOC CC

-2 Carbon Adsorption System (Carbon Canister) 2004 VOC **C. EQUIPMENT DESCRIPTION**  A description of the equipment located at this facility is provided in the following tables: **TABLE 5.8 UNIT ID 01**  **- QUARRY SYSTEM**  **EQUIPMENT** (table updated 10/22/03) **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** R143 2003 Marl Quarrying Equipment #1 17,380,952 None NP8**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **21 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.8 UNIT ID 01**  **- QUARRY SYSTEM**  **EQUIPMENT** (table updated 10/22/03) **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** R170 R174 R195 2003 Iron Ore Hopper to Conveyor, R170 Conveyor to Iron Ore Bin, R174 Iron Ore Stamler Feeder, R195 202,777 Each None NP35 NP39 NP91 R178 2003 Iron Ore Bin to Conveyor, R178 202,777 Each None NP43 R171 R175 R204 2003 Wet Fly Ash Hopper to Conveyor, R171 Conveyor to Wet Fly Ash Bin, R175 Fly Ash Conveyor Transfer Point, R204 1,158,730 Each None NP36a NP36b NP40 NP128 R180 2003 Wet Fly Ash Bin to Conveyor, R180 1,158,730 Each None NP45 R139 R140 R141 R142 R190 R191 R193 2003 Clay Hopper, R139 Clay Crusher, R140 Clay Crusher to Conveyor, R141 C lay Conveyors, R142, R190, R191,

R193 1,931,230 Each None NP4 NP5 NP6 NP7 NP86 NP87 NP88 NP89 NP90 R155 R156 R157 R158 2003 Clay Conveyors, R155

- 158 1,931,230 Each None NP20 NP21 NP22 NP23 R159 R202 R203 2003 Clay Conveyors, R159, R202, R203 1,158,730 Each None NP24 NP126 NP127 R160 R161 R196 R197 R198 R199 R200 R201 2003 Marl Conveyors, R160, R161, R196

- R199, Marl Crusher, R200 Marl Crusher to Hopper, R201 17,380,952 Each None NP25 NP26 NP80a,NP80b NP81a,NP81b NP82 NP83 NP84a,NP84b NP85 R164 R184 R205 2003 Marl Conveyors, R164, R184, R205 5,986,772 Each None NP29 NP49 NP42 R162 R163 2003 Pile #1 Reclaimer to Conveyor, R162 Pile #2 Reclaimer to Conveyor, R163 5,793,688 Each None NP27 NP28 **TABLE 5.9 UNIT ID 02**  **- RAW MILL SYSTEM EQUIPMENT**  (table updated 10/22/03) **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** R183 2003 Clay Conveyors, R183 1,158,730 Each None NP48 R185 2003 Marl Conveyors, R185 5,986,772 Each None NP50**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **22 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.9 UNIT ID 02**  **- RAW MILL SYSTEM EQUIPMENT**  (table updated 10/22/03) **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** R179 2003 Iron Ore Bin to Conveyor, R178 Iron Ore Conveyor, R179 202,777 Each None NP44 R181 2003 Wet Fly Ash Bin to Conveyor, R180 Wet Fly Ash Conveyor, R181 1,158,730 Each None NP46 R186 2003 Raw Mill Reject Bin 4,906 None NP51 R126 2003 Raw Mill Cyclone Separator N/A BH99 S99 R127 2003 Blending Silo Feed Bucket Elevator

– Bottom N/A BH100 S100 R128 2003 Blending Silo Top N/A BH101 S101 R129 2003 Raw Mill Silo Withdrawal N/A BH102 S102 R130 2003 Kiln Feed Elevator

– Top N/A BH103 S103 R131 2003 Dry Marl Bin N/A BH118 S1 18 R132 2003 Pump Station at Existing Silos (Fly Ash To Bin) N/A BH123 S123 R134 2003 Top of Existing Silos (Fly Ash) N/A BH127 S127 N/A = Not Applicable

**TABLE 5.10 UNIT ID 03**  **- COAL MILL SYSTEM EQUIPMENT**  **Equip ID**  **Installation**

**Date Equipment Descripti** **on Design Capacity**  **(TPY) Control** 

**Device ID Exhaust Point** 

**ID** C400 1980 Coal Unloading Room N/A BH32 S32 C401 1980 Coal Unloading Belt N/A BH31 S31 C402 1980 Coal Dust Silo N/A BH33 S33 C403 1980 Carbon Feeder N/A BH34 S34 C412 2003 Coal Mill Vent N/A B H95 S95 C413 2003 Carbon Dust Tank N/A BH130 S130 C414 2003 Coal Bin System Dedusting N/A BH132 S132 C417 2003 Coal Conveyor to Radial Stacker 3,328,800 None NP57 C418 C419 2003 Radial Stackers to Coal/SVF Pile 1,664,400 Each None NP58 NP59 C421 C422 C423 C424 C425 2003 Coal/SVF Conveyors, C421, C422, C424 Coal/SVF Bin, C423 Coal/SVF Hopper, C425 402,347 Each None NP93 NP94 NP95 NP96 NP129 N/A = Not Applicable (page updated 10/22/03) **TABLE 5.11 UNIT ID 04**  **- KILN SYSTEM EQUIPMENT**  **Equip ID**  **Installatio n** 

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhaust Point** 

**ID** K300A 2003 Preheater/Precalciner Kiln Main 2,896,844 BH94A S94 K300B 2003 Preheater/Precalciner Kiln By pass 2,896,844 BH94B S94 K301 2003 Alkali Bypass Dust Loadout N/A BH104 S104 K302 2003 Alkali Bypass Dust Loadout N/A BH105 S105**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **23 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.11 UNIT ID 04**  **- KILN SYSTEM EQUIPMENT**  **Equip ID**  **Installatio n** 

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhaust Point** 

**ID** C304 1982 Common Conveyor N/A BH22 S22 C305 1982 Pan Conveyor North N/A BH23 S23 C313 1982 Belt Conveyor North Clinker Silo #4 N/A BH78 S78 C326 1997 Clinker Reclaim Area N/A BH83 S83 C 328 2003 Clinker Cooler Transfer Point N/A BH106 S106 C329 2003 Top of New Clinker Silo N/A BH107 S107 C330 2003 Clinker Transfer Under Existing Silos To Finish Mill #4 N/A BH108 S108 C501 2005 Sampson Feeder System 300,000 BH187 S187

**TABLE 5.12 UNIT**  **ID 05 -**  **FINISH MILL SYSTEM EQUIPMENT Equip**  **ID Installation** 

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** F402 1982 #4 Finish Mill Collecting Belt to Incline Belt NA BH57 S57 F403 1982 #4 Finish Mill Main DC NA BH54 S54 F403 1982 #4 Finish Mill Classifier DC NA BH55 S55 F404 1982 #4 Finish Mill Fines Airslide to Cement Elevator DC NA BH56 S56 F726 F727 F728 F709 F710 F711 F712 F713 F714 F729 F730 F731 2003 Conveyor, F726, F727, F728, F709, F710, F711, F729, F730, F 731 Pigment Bin to Conveyor, F712 Slag Bin to Conveyor, F713 Synthetic Gypsum Bin to Conveyor, F714 289,681 Each None NP97 NP98 NP99 NP100 NP101 NP102 NP103 NP104 NP105 NP106 NP107 NP108 F725 2003 Sugar Silo to #4 Mill Feed 1,927 None NP74 F405 1982 #4 F inish Mill Dribble Bin NA BH175 S175 F700 2003 Clinker Additives Bins

- Top (FM5) NA BH115 S115 F701 2003 Clinker/Additives Bins

- Bottom (FM5) NA BH116 S117 F702 2003 Finish Mill Feed End Dedusting (FM5) NA BH120 S120 F703 2003 Finish Mill Discharge End Dedusting (FM5) NA BH135 S135 F704 F732 F733 2003 Hopper to Additive Feed Belt, F704 Wet Slag/Synthetic Gypsum Conveyor Transfer Point, F732, F733 270,370 Each None NP79 NP109 NP110**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **24 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.12 UNIT**  **ID 05 -**  **FINISH MILL SYSTEM EQUIPMENT Equip**  **ID Installation** 

**Date Equipment Description**  **Design Capacity**  **(TPY) Control** 

**Device ID Exhaust** 

**Point ID** F734 F735 F736 F715 F716 F717 F718 F719 F720 F721 F722 F737 2003 Conveyor to Wet Slag Bin, F734, F736 Conveyor to Gypsum Bin, F735, F715 Wet Slag Bin to Conveyor, F716, F720 Gypsum Bin to Conveyor, F717, F721 Conveyor Transfer, F718, F719, F722,

F737 270,370 None NP111 NP112 NP113 NP114 NP115 NP116 NP117 NP118 NP119 NP120 NP121 NP122 F705 2003 #5/#6 Finish Mill Transfer & Storage NA BH174 S174 F738 F739 2003 #5/#6 Transition Clinker Silo 482,804 None NP123 NP124 F800 2003 Clinker /Additives Bins

- Top (FM6) NA BH114 S114 F801 2003 Clinker/Additives Bins

- Bottom (FM6) NA BH117 S116 F802 2003 Finish Mill Feed End Dedusting (FM6) NA BH121 S121 F803 2003 Finish Mill Discharge End Dedusting (FM6) NA BH136 S136 F500 1966 Top of Finish Mill #1 Cement Silos NA BH171 S171 F501 1970 Top of Finish Mill #2 Cement Silos NA BH17 2 S172 F600 1973 Top of Finish Mill #3 Cement Silos NA BH169 S169 F601 1982 Top of Finish Mill #4 Cement Silos NA BH170 S170 F740 2003 Cement Feed to Cooler

– FM#6 NA BH177 S177 F741 2003 Finish Mill #5 and #6 Dribble Bin Bottom NA BH178 S178 F742 200 3 Marl/Lime Alleviator NA BH180 S180 F743 2003 Dry Marl Transport From 8

-Pack NA BH181 S181 R123A 2003 Mill Separator

– FM5 N/A BH96 S96 R123B 2003 Ball Mill

– FM5 N/A BH97 S96 R124A 2003 Mill Separator

– FM6 N/A BH146 S97 R124B 2003 Ball Mill

– FM6 N/A BH147 S97 R133 2003 New Additive System

– Dry Lime N/A BH126 S126 O103 2003 Off

- Spec Clinker Silo

– Top N/A BH119 S119 C324 2005 Cement Dome Bucket Elevator

– Upper N/A BH188 S188 C325 2005 Cement Dome Bucket Elevator

– Lower N/A BH189 S189 N/A = Not Applicable (page updated 10/22/03)

**TABLE 5.13 UNIT ID 06**  **- CEMENT LOADOUT EQUIPMENT**  **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhaust Point** 

**ID** C319 2003 Cement Dome Conveyor & Collection Box NA BH85 S85 C320 2003 Cement Dome Alleviator NA BH86 S86 C321 2003 Top of Cement Dome NA BH87 S87**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **25 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.13 UNIT ID 06**  **- CEMENT LOADOUT EQUIPMENT**  **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhaust Point** 

**ID** C322 2003 Cement Dome Reclaim Tower NA BH88 S88 (updated 10/22/03) C323 2003 Cement Dome Surge Bin NA BH89 S89 C337 2003 Rail Loading Bin NA BH122 S122 C333 2003 C ement Transport

- Post

- Cooler & Elevator Bottom NA BH137 S137 C334 2003 Cement Transport

- Elevator Top NA BH138 S138 B100 1988 East Packer NA BH67 S67 B101 1988 West Packer NA BH68 S68 W101 1966 #1 Truck Scale NA BH63 S63 W201 Prior to 1971 #2 Truck/Rail Scale NA BH64 S64 W301 Prior to 1971 #3 Truck/Rail Scale NA BH65 S65 W401 2003 #4 Truck Scale NA BH66 S66 W501 2003 #5 Truck Scale NA BH90 S90 W601 2003 #6 Truck Scale NA BH91 S91 W701 2003 #7 Truck Scale NA BH144 S144 W801 2003 #8 Truck Scale NA BH145 S145 W901 2003 #9 Truck Scale NA BH176 S176 W902 2004 Truck Load Out Silo N/A BH183 S183 W903 2004 Truck Load Out Silo N/A BH184 S184 W904 2004 Truck Load Out Silo N/A BH185 S185 W905 2004 Truck Load Out Silo N/A BH186 S186 RAI1 1996 Rainbow Products 1,314,000 BH113 S113 RAI2 1996 Rainbow Products 438,000 BH113 S113 RAI3, RAI4 1996 Rainbow Raw Material Bins, Hoppers, Weigh Belts, Mixer, &

Bag Spouts NA BH113 S113 V112 NA Haul Trucks Exporting CKD 150,000 NA NA V200 NA Clay Haul Trucks from Quarry to Crusher 437,600 NA NA V201 NA Wet Fly Ash Haul Trucks 170,871 NA NA V202 NA Dry Fly Ash Haul Trucks 151,447 NA NA V203 NA Iron Ore Haul Trucks 51,416 NA NA V204 NA Slag Haul Trucks 132,834 NA NA V205 NA Synthetic Gypsum Haul Trucks 143,299 NA NA V207 NA Lime Haul Trucks 1,659 NA NA V208 NA Pigment Haul Trucks 4,630 NA NA V209 NA Sugar Haul Trucks 995 NA NA V210 NA Carbon Dust Haul Trucks 10,099 NA NA V211 NA Tire Chips Haul Trucks 32,832 NA NA V212 NA High Viscosity Oil Haul Trucks 13, 006 NA NA V213 NA HWDF Haul Trucks 50,000 NA NA V214 NA Oxygen Haul Trucks 40,000 NA NA V215 NA Bulk Cement Haul Trucks 932,930 NA NA V216 NA Bagged Cement Haul Trucks 387,114 NA NA**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **26 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.13 UNIT ID 06**  **- CEMENT LOADOUT EQUIPMENT**  **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhaust Point** 

**ID** V217 NA CKD Haul Trucks from Kiln to Storage 24,687 NA NA V218 NA Fuel Trucks from Quarry to Garage 1,500 NA NA V219 NA Rainbow Products Crushed Marble Haul Trucks 1,268 NA NA V220 NA Rainbow Products Lime Haul Trucks 1,268 NA NA V221 NA Haul Trucks Bringing SVF to Facility 347,250 NA NA V222 NA Calcium Fluoride Haul Trucks 3,473 NA NA V223 NA Mill Scale Haul Trucks 23,150 NA NA (page updated 9/23/03and 10/22/03) N/A = Not Applicable
**TABLE 5.14 UNIT ID 07**  **- TANK EQUIPMENT**  **Equip ID**  **Installation**

**Date Equipment Description**  **Design Capacity (TPY)**  **Control**

**Device ID Exhau**  **st Point**

**ID** T101 1974 HWDF Storage & Supply for Kilns 844,000 VRU111 S111 T102

- T106 1988 HWDF Blending & Storage 39,152 (each) VRU111 S111 T111 2003 HWDF Storage & Supply for Kilns 250,048 VRU112 S94/S128 H100 1988 HWDF Delivery System (pumps, valves, etc.) N/A None N/A T146 2003 HWDF Storage & Supply for Kilns 150,000 VRU112 S94/S128

T100 1988/modified

in 2004 NHWDF

Heated Storage Tank 100,000 gal (378.5514 m3 ) Closed

Vent System and CC

- 1 S129
T115 1998 No. 2 Diesel Storage 12,000 None S149 T144 2 003 FM #5 & #6 Grinding Aid Tank 12,000 None S140
T

- 148 2004 NHWDF Heated Storage Tank 60,000 gal (227.1309 m3 ) Closed

Vent System and CC

- 1 N/A

T

- 147, T

- 148, T

- 149 Future Two (2) NHWDF Non

-Heated Storage Tanks 60,000 gal (227.1309 m3 ) Each Closed

Vent System and CC

-2 N/A

Boiler 2004 5.0 million Btu/hr natural gas fired Boiler. -- -- N/A N/A = Not Applicable**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **27 of 106**  (permit updated 6/27/05 and 8/19/05)

**D. EMISSION LIMITS AND STANDARDS**  Tables **5.15 through 5.22** contain summaries of emission unit emission limits and standards. **TABLE 5.15 EMISSIO** **N LIMITS AND STANDARDS -**  **UNIT ID 01 QUARRY SYSTEM EQUIPMENT**  **Equipment ID**  **Pollutant/**

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition**  **Num ber**  R140, R200 Opacity 15% Method 9 40CFR60.675(4)(i)

- Subpart OOO No 5.E.1(b) R139, R141, R142, R143 , R155, R156, R157, R158, R159, R160, R161 **,** R162, R163, R164, R170, R171, R174, R175, R178, R180, R184, R190, R191, R193, R195, R196, R197, R198, R199, R201, R202, R203, R204, R205 Opacity See condition Method 22 Method 9 40CFR60.672(b)

-

Subpart OOO No 5.E .1(c)

**TABLE 5.16 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 02 RAW MILL**  **EQUIPMENT Equipment ID**  **Pollutant/**

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition** 

**Num ber**  R126, R127, R128, R129, R130, R131, R132, R134, R179, R181, R183, R185, R186 Opacity 10% Method 9 40CFR63.1347, Subpart LLL No 5.E.2(b)
(page updated 10/22/03) **TABLE 5.17 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 03 COAL MILL** 

**SYSTEM (coal/coke crushing and processing equipment) Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Meth**  **od Regulation**  **State Only**  **Condition Num** **ber** C400, C401, C402, C403, C413, C414, C417, C418, C419, C421, C422, C423, C424, C425 Opacity 20% Method 9 40CFR60.2 52 Subpart Y No 5.E.3(b)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **28 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.17 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 03 COAL MILL** 

**SYSTEM (coal/coke crushing and processing equipment) Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Meth**  **od Regulation**  **State Only**  **Condition Num** **ber** C412 PM 0.031 gr/dscf Method 5 40CFR60 Subpart Y No 5.E.3(c)

C412 NO x 4. 48 lb NO x/ton clinker (first year) 4.33 lb NO x/ton clinker (after first year) CEM SC 61

- 62.5, Standard No. 7 No 5.E.3(d)

C412 CO 8.00 lb CO/ton clinker (first year) 6.8 lb CO/ton clinker (after first year) CEM SC 61

- 62.5, Standard No. 7 No 5.E.3(e)

C4 12 VOC 0.27 lb VOC/ton clinker Bureau

Approved SC 61

- 62.5,

Standard No. 5.1 & Standard No. 7 No 5.E.3(f)

C412 SO 2 3.26 lb SO 2/ton clinker CEM SC 61

- 62.5, Standard No. 7 No 5.E.3(g)

C412 Opacity 20% COM or Method 9 40 CFR 60

Subpart Y, 40 CFR 63.1204( a)( 7) Subpart EEE No 5.E.3(h)

C412 Tem

perature See Condition Thermo

couple 40 CFR 60

Subpart Y No 5.E.3(i)
**TABLE 5.18 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 04 KILN SYSTEM**  **EQUIPMENT Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation St** **ate Only**  **Condition Num** **ber** K300A, K300B Opacity 20% COM or Method 9 40CFR

63.1204(b)(7) Subpart EEE No 5.E.4(b)

K300A, K300B Dioxin/Furan 0.20 ng TEQ/dscm Dioxin/Furan limit corrected to 7% O 2 , or 0.40 ng TEQ/dscm Dioxin/Furan limit corrected to 7% O 2 when temp <400  F Method 0023A (SW

- 846) 40CFR

63.1204(b)(1) Subpart EEE No 5.E.4(c)

K300A, K300B PM 0.15 kg/Mg dry feed Method 5 40CFR 63.1204(b)(7) Subpart EEE No 5.E.4(d) K300A, K300B PM 56.97 lb/hr Method 5 SC 61

- 62.5 Standard No. 4 No 5.E.4(e)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **29 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.18 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 04 KILN SYSTEM**  **EQUIPMENT Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation St** **ate Only**  **Condition Num** **ber** K300A, K300B Ni 0.006 lb/million BTU total heat input Method 29 SC Reg. 61

- 62.5 Standard No. 3 Yes 5.E.4(f) K300A, K300B Cd 1.0 E

-4 lb/million BTU total heat input Method 29 SC Reg. 61

- 62.5 Standard No. 3 Yes 5.E.4(g) K300A, K300B Cr 5.0 E

-4 lb/million BTU total heat input Method 29 SC Reg. 61

- 62.5 Standard No. 3 Yes 5.E.4(h) K300A, K300B As 2.5 E

-4 lb/million BTU total heat input Method 29 SC Reg. 61

- 62.5 Standard No. 3 Yes 5.E.4(i) K300A, K300B Pb 0.005 lb/million BTU total heat input Method 29 SC Reg. 61

- 62.5 Standard No. 3 Yes 5.E.4(j)

K300A, K300B HCl Emissions

from the Kiln In

Line Raw Mill System 0.45 lb HCl/million

BTU total heat input Method 26A Method 320 Method 321 SC Reg. 61

-

62.5 Standard No. 3 Yes 5.E.4(k)

K300A, K300B NO x 4.48 lb NO x/ton c linker (first 12 months) 4.33 lb NO x/ton clinker (after first 12 months) CEM SC 61

- 62.5, Standard No. 7 No 5.E.4(m)

K300A, K300B CO 8.00 lb CO/ton clinker (first 12 months) 6.8 lb CO/ton clinker (after first 12 months) CEM SC 61

- 62.5, Standard No. 7 No 5.E.4(n)

K300A, K300B VOC 0.27 lb VOC/ton clinker Bureau

Approved SC 61

- 62.5,

Standard No. 5.1, Standard No. 7 No 5.E.4(o) K300A, K300B SO 2 3.26 lb SO 2/ton clinker CEM SC 61

- 62.5, Standard No. 7 No 5.E.4(p)
K301 K302 Opacity 10% Method 22 Method 9 40 CFR

63.1348 Subpart LLL No 5.E.4(q) K300A, K300B Benzene  99% Destruction Efficiency 40 CFR

61.355(c) 40 CFR

61.348(a)(1)(iii ) Subpart FF No 5.E.4(s) K300A, K300B Clinker production 2,462,318 short ton/yr of clinker produced Record

keeping SC 61

- 62 .5,

Standard No. 7 No 5.E.4(u)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **30 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.18 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 04 KILN SYSTEM**  **EQUIPMENT Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation St** **ate Only**  **Condition Num** **ber** K300A, K300B Kiln Fuel

Limitations See Condition Record keeping SC Reg. 61

-

62.1 and 62.5 Standard No. 3 Yes 5.E.4(v) K300A, K300B Ozone Use of low NOx burners during control period N/A SC Reg. 61

- 62.99 No 5.E.4(w)
K300A, K300B THC or CO

Emissions 10 ppm v THC (as propane), or 100 ppm v CO, dry basis, corrected to 7% O 2 Method 25,

Method 10, CEM 40CFR

63.1204(b)(5) Subpart EEE No 5.E.4(x)

K300A, K300B Combined HCl and

Cl Emissions 86 ppm v (expressed as HCl equivalents) on a dry basis corrected to 7% O 2 Method 26A, 320,or 321 40CFR

63.1204(b)(6) Subpart EEE No 5.E.4(y) K300A, K300B POHC Emissions  99.99% destruction efficiency Method 25 SC 61

- 62.5, Standard No. 3 No 5.E.4(z) K300A, K300B POHC Emissions  99.99% destruction ef ficiency Method 25 40CFR 63.1204(c)(1) Subpart EEE No 5.E.4(aa) K300A, K300B Mercury Emissions  120 μg/dscm, corrected to 7% O 2 Method 29 40CFR 63.1204(b)(1) Subpart EEE No 5.E.4(bb) K300A, K300B Combined Lead &

Cadmium emissions  180 μg/dscm,

corrected to 7% O 2 Method 29 40CFR 63.1204(b)(3) Subpart EEE No 5.E.4(cc)
K300A, K300B Combined Arsenic,

Beryllium, & Chromium emissions  54 μg/dscm,

corrected to 7% O 2 Method 29 40CFR 63.1204(b)(4) Subpart EEE No 5.E.4(dd)

K300A, K300B Tem

perature Less than

Tem p erature in Performance Test for APCD As

Approved 40CFR63

Subpart EEE No 5.E.4(ee)

K300A, K300B Tem

perature >Tem

perature in performance test for combustion zone chamber As

Approved 40 CFR Interim

Subpart EEE No 5.E.4(ff)
K300A, K300B THC Emissions See condition CEM Alternate Method of Operation No 5.E.4(gg) C304, C305, C313, C326, C328, C329, C330, C501 Opacity 10% Method 22 Method 9 40CFR63.1348

Subpart LLL No 5.E.4(hh)

C501 PM 61.0 lb/hr Method 9 SC Regulation 61

- 62.5, Standard 4, Section VIII No 5.E.4 (ii)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **31 of 106**  (permit updated 6/27/05 and 8/19/05)

**TABLE 5.19 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 05 FINISH MILL**  **SYSTEM EQUIPMENT Equipment ID**  **Pollutant/ Standard**  **Limit Reference**  **Method Regulation**  **State Only**  **Condition**

**Num ber**  F402, F404, F405, F500, F501, F600, F601, F700, F701, F704, F709, F 710, F711, F712, F713, F714, F715, F716, F717, F718, F719, F720, F721, F722, F725, F726, F727, F728, F729, F730, F731, F732, F733, F734, F735, F736, F737, F738, F739, F740, F741, F742, F743, F802, F703, F800, F801, F702, F803, F705, R123A, R123B, R124A, R1 24B, R133, O103, C324, C325 Opacity 10% Method 22 Method 9 40CFR63.1348,

Subpart LLL No 5.E.5(c)

F403 Opacity 10% Method 22 Method 9 40 CFR

63.1347 Subpart LLL No 5.E.5(b)

C324, C325 PM 70.1 lb/hr Method 5 SC Regulation 61

- 62.5, Standard 4, Section VIII No 5.E.5(d)

**TABLE 5.20 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 06 CEMENT**  **LOADOUT EQUIPMENT Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition** 

**Num ber**  B100, B101 W101, W201, W301, W401, W501, W601, W701, W801, W901, W902, W903, W904, W905, C337, RAI1, RAI2, RAI3, RAI4, C319, C320, C321, C322, C323, C333, C334 Opacity 10% Method 22 Method 9 40CFR63.1348

Subpart LLL No 5.E.6(b)

RAI1, RAI2, RAI3, RAI4 PM 0.6 lb/hr Method 5 SC 61

- 62.1, II(H) No 5.E.6(c)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **32 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.20 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 06 CEMENT**  **LOADOUT EQUIPMENT Equipment**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition** 

**Num ber** 
RAI1, RAI2, RAI3 , RAI4 Production

limits 300,000 ston/yr

of cement throughput; and 100 ston/hr of unloaded raw materials Record

keeping SC 61

- 62.1,

II(H) No 5.E.6 (d)

C319, C320, C321, C322, C323 PM 3.05 lb/hr Method 5 SC 61

- 62.1, II(H) No 5.E.6(e) C319, C320, C321, C32 2, C323 Production

limits 4,440,000

stons/yr throughput Record

keeping SC 61

- 62.1,

II(H) No 5.E.6(f) W902, W903, W904, W905 PM 52.8 lb/hr Method 5 SC 61

- 62.5 Standard No. 4 No 5.E.6(g)
**TABLE 5.21 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 07 TANKS**  **Equipm ent**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition** 

**Num ber**  T101, T102, T103, T104, T105, T106, T111, T146 VOC 95% VOC Removal Method 21 40CFR61 Subpart FF No 5.E.7(b)
T101, T102, T103, T104, T105, T106, T111, T146, T100, T 115 Opacity 20% Method 9 SC 61

- 62.5, Standard No. 4 No 5.E.7(d)

T111 VOC 1.07 TPY Method 21 SC 61

- 62.5, Standard No. 5.1, Standard No. 7 Yes

(5.1), No (7) 5.E.7(e)
T101, T102, T103, T104, T105, T106, T111, T146 HWDF Tank

VOC Control and Emission Standards No detectable

VOC emissions (<500 ppmv) Portable

FID 40 CFR 61

Subpart FF No 5.E.7(f)
T101, T102, T103, T104, T105, T106, T111, T146 Closed Vent

System Standards No detectable

VOC emissions (<500 ppmv) Portable

FID 40 CFR 61

Subpart FF No 5.E.7(g)
T10 1, T102, T103, T104, T105, T106, T146 VOC 95% removal Portable FID 40 CFR 61

Subpart FF No 5.E.7(h)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **33 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 5.21 EMISSION LIMITS AND STANDARDS**  **- UNIT ID 07 TANKS**  **Equipm ent**  **ID Pollutant/** 

**Standard Limit**  **Reference Method**  **Regulation State**  **Only Condition** 

**Num ber** 
Boiler Opacity 20% Opacity \ Method 9 SC Regulation

61

- 62.5, Standard 1, Section I No 5.E.7(k)

Boiler PM 0.6 lb/10 6 Btu Input Method 5 SC Regulation 61

- 62. 5, Standard 1, Section II No 5.E.7(l)

Boiler SO 3.5 lb/10 6 Btu Input Method 6 SC Regulation 61

- 62.5, Standard 1, Section III No 5.E.7(m) N/A=Not Applicable The maximum allowable emission limits above are derived from the various Federal and State regulations that govern the operation of this ty pe of source. All applicable facility wide emission limits and corresponding regulations are listed above. Additional operating requirements which may be more stringent than those above are contained in Part 4.0, Part 6.0, and Part 7.0 of this permit. **E. EMISSION UNIT CONDITIONS**  **5.E.1 Unit ID 01**

**– Quarry/Marl Handling Equipment**  (a) These sources are subject to New Source Performance Standards (NSPS), 40 CFR 60 subparts A and OOO, Standards Of Performance For Nonmetallic Mineral Processing Plants. (b) (40CFR60.11(c) and 40CFR60.672(c), (d)) On and after the sixtieth day after achieving the maximum production rate at which the affected facility will be operated, but not later than 180 days after initial startup as required under 40 CFR60.11, no owner or operator shall cause to be discharged into the atmosphere from any crusher, at which a capture system is not used, fugitive emissions which exhibit greater than 15 percent opacity

. Truck dumping of nonmetallic minerals into any screening operation, feed hopper, or crusher is exempt from these requirements. (c) (40CFR60.11(c) and 40CFR60.672(b), (d), (h)) For non- saturated materials, on and after the sixtieth day

after achieving the maximum production rate at which the aff ected facility

will be operated, but not later than 180 days after initial startup as required under 40CFR60.11, no owner or operator subject to the provisions of this subpart shall cause to be discharged into the atmosphere from any transfer point on belt conveyors or from any other affected facility any fugitive emissions which exhibit greater than 10 percent opacity

. On and after the sixtieth day after achieving the maximum production rate at which the affected facility

will be operated, but not later than 180 days after initial startup, no owner or**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **34 of 106**  (permit updated 6/27/05 and 8/19/05) operator shall cause to be discharged into the atmosphere any visible emissions from wet screening operations and subsequent screening operations, bucket elevators, and belt conveyors that process saturated material in the production line up to the next crusher, grinding mill or storage bin. Truck dumping of nonmetallic minerals into any screening operation, feed hopper, or crusher is exempt from these requirements. **5.E.2 Unit ID 02 -**  **Raw Mill Equipment** (a) The supplementary raw mill sources are subject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and LLL, National Emission Standards for Hazardous Air Pollutants from the Portland Cement Manufacturing Industry

. S ince the raw mill is part of the in

- line kiln/raw mill, the raw mill is subject to 40 CFR 63 Subparts A and EEE, National Emission Standards for Hazardous Air Pollutants from Hazardous Waste Combustors, and emissions limitations f or it will be covered under 5.E.4. (b) (40CFR63.1347, 40 CFR63.1348) The owner or operator of each new or existing raw mill or finish mill at a facility

which is a major source subject to the provisions of this subpart shall not cause to be discharged from the mill sweep or air separator air pollution control devices of these affected sources any gases which exhibit opacity in excess of ten percent. The owner or operator of each new or existing raw material, clinker, or finished product storage bin; conveying system transfer point; bagging system; and bulk loading or unloading system; and each existing raw material dryer, at a facility which is a major source subject to the provisions of this subpart shall not cause to be discharged any gases from these af

fected sources which exhibit opacity in excess of ten percent. **5.E.3 Emissions Limits from the Coal Mill Equipment** (a) These sources are subject to New Source Performance Standards (NSPS), 40 CFR 60 subparts A and Y, Standards Of Performance For Coal Preparation Plants. Since the coal mill utilizes part of the kiln exhaust gases for drying in the vertical roller mill, the coal mill is subject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and EEE, National Emission Standards for Hazardous Air Pollutants from Hazardous Waste Combustors. (b) (40CFR60.252(c)) On and after the date on which the performance test required to be conducted by

4 0CFR60.8 is completed, an owner or operator subject to the provisions of this subpart shall not cause to be discharged into the atmosphere from any coal processing and conveying equipment, coal storage system, or coal transfer and loading system processing coal, gases which exhibit 20 percent opacity or greater.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **35 of 106**  (permit updated 6/27/05 and 8/19/05) (c) (40CFR60 Subpart Y) On and after the date on which the performance test required to be conducted by

§ 60.8 is completed, an owner or operator subject to the provisions of this subpart shall not cause to be discharged into the atmosphere from any thermal dryer gases which contain particulate matter in excess of 0.070 g/dscm (0.031 gr/dscf). (d) (SC Regulation 61

- 62.5, Standard No. 7) NO x emissions from the kiln, in

- line raw mill system and coal mill are limited to 4.48 lb NO x / ton clinker (first ye ar) and 4.33 lb NO x / ton clinker (after first year) 30 day rolling average - sum of both the main kiln stack and the coal mill stack. (e) (SC Regulation 61

- 62.5, Standard No. 7) CO emissions from the kiln, in

-line raw mill system and coal mill are limited to 8.00 lb CO / ton clinker (first year) and 6.8 lb CO / ton clinker (after first year) 30 day

rolling average

- sum of both the main kiln stack and the coal mill stack. (f) (SC Regulation 61

- 62.5, Standard No. 5.1, Standard No. 7) VOC emissions from the kiln, in

line raw mill system and coal mill are limited to 0.27 lb VOC / ton clinker 3 hr block average

- sum of both the main kiln stack and the coal mill stack. (g) (SC Regulation 61

- 62.5, Standard No. 7) SO 2 emissions from the kiln, in

- line raw mill system and coal mill are limited to 3.26 lb SO 2 / ton clinker 30 day rolling average - sum of both the main kiln stack and the coal mill stack. (h) (40 CFR 60.252(a2), 40CFR63.1204(b)(7)) On and after the date on which the performance test required to be conducted by 40 CFR60.8 is completed, an owner or operator subject to the provisions of this subpart shall not cause to be discharged into the atmosphere from any thermal dryer gases which exhibit 20 percent opacity or greater. The owner or operator must not discharge or cause combustion gases to be emitted into the atmosphere that contain opacity greater than 20 percent. (i) (40 CFR 60.253) The owner or operator of any t hermal dryer shall install, calibrate, maintain, and continuously

operate a monitoring device for the measurement of the temperature of the gas stream at the exit of the thermal dryer on a continuous basis. The monitoring device is to be certified by

the manufacturer to be accurate within ±1.7°C (±3°F). All monitoring devices of this section are to be rec alibrated annually in accordance with procedures under 40 CFR 60.13(b). **5.E.4 Emissions Limits from the Kiln In -** **Line Raw Mill System Equipment** (a) These sources are subject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and EEE, National Emission Standards for Hazardous Air Pollutants from Hazardous Waste Combustors. Per 40 CFR 63.1340(b)(1), the in

- line kiln/raw mill are not subject to 40 CFR 63 Subpart LLL,National**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **36 of 106**  (permit updated 6/27/05 and 8/19/05) Emission Standards for Hazardous Air Pollutants from the Portland Cement Manufacturing Industry. The clinker handling sources are subject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and LLL, National Emission Standards for Hazardous Air Pollutants from the Portland Cement Manufacturing Industry

. (b) **(**40CFR63.1204(b)(7)) The owner or operator must not discharge or cause combustion gases to be emitted into the atmosphere that contain opacity greater than 20 percent. (c) (40CFR63.1204(b)(1)) Dioxin/Furan emissions from the combination of the kiln stack and the coal mill stack shall not exceed 0.20 ng TEQ/dscm corrected to 7% oxygen, or dioxin/furan emissions from the kiln shall not exceed 0.40 ng TEQ/dscm corrected to 7% oxygen provided that the combustion gas temperature at the inlet to the initial dry particulate matter control device is less than or equal to 204  C (400  F) based on the average of the test run average temperatures. (d) (40CFR63.1204(b)(7)) Particulate Matter emissions from the combination of the kiln stack and the coal mill stack shall not exceed 0.15 kg/Mg dry feed. (e) These processes are subject to particulate matter emission limitations from SC Regulation 61

- 62.5, Standard No. 4. The emiss ion limitation is determined as listed below for all process equipment except for the equipment that is included in the main kiln system and associated stack. For process weight rates up to 30 tons per hour: E = (4.10) (P 0.67) For process weight rates of greater than 30 tons per hour: E = (55.0) (P 0.11 )

- 40 Where: E = the allowable emission rate in pounds per hour P = process weight rate in tons per hour For the kiln system the PM emission limitation is 56.97 lb/hr when operating at full capacity

. The averaging time for these emission limitations is three hours. (f) (SC Regulation 61

- 62.5 Standard No. 3) Ni emissions from the kiln in

- line raw mill system shall not exceed 0.006 lb Ni/million BTU total heat input. (g) (SC Regulation 6 1

- 62.5 Standard No. 3) Cd emissions from the kiln in

- line raw mill system shall not exceed 1.0 E

-4 lb Cd/million BTU total heat input. (h) (SC Regulation 61

- 62.5 Standard No. 3) Cr emissions from the kiln in

- line raw mill system shall not exceed 5.0 E

-4 lb Cr/million BTU total heat input.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **37 of 106**  (permit updated 6/27/05 and 8/19/05) (i) (SC Regulation 61

- 62.5 Standard No. 3) As emissions from the kiln in

- line raw mill system shall not exceed 2.5 E

-4 lb As/million BTU total heat input. (j) (SC Regulation 61

- 62.5 Standard No. 3) Pb emissions from the kiln in

- line raw mill system shall not exceed 5.0 E

- 3 lb Pb/million BTU total heat input. (k) (SC Regulation 61

- 62.5 Standard No. 3) HCl emissions from the kiln in

-line raw mill system shall not exceed 0.45 lb HCl/million BTU total heat input. (l) These sources are subject to S.C. Reg 61

- 62.5 Standard No. 5.1, VOC LAER. F or these sources, VOC LAER is determined to be process optimization. (m) (SC Regulation 61

- 62.5, Standard No. 7) NO x emissions from the kiln in

- line raw mill system shall not exceed 4.48 lb/ton of clinker during the first 12 months of commercial operation. After the first 12 months of commercial operation, 30 day rolling average ofNOx emissions from the kiln in

- line raw mill system and coal mill stack shall not exceed 4.33 lb/ton of clinker. The emission limitation for NO x is based on the site

- specific raw material properties, fuel usage and design of the system. The Bureau shall review the raw material testing, Continuous Emission Monitor data, and any other pertinent information periodically (beginning after the first two ye ars of commercial operation). Upon review, the NO x emission limitation and/or the NO x averaging time may b e adjusted downward if deemed appropriate by

the Bureau. The intent of this condition is not to remove operational and process flexibility

f rom Holcim, but to show a realistic permit limit relative to actual operation. (n) (SC Regulation 61

- 62.5, Standard No. 7) CO emissions from the kiln in

-line raw mill system shall not exceed 8.00 lb/ton of clinker during the first 12 months of commercial operation. After the first 12 months of commercial operation, 30 day rolling average of CO emissions from the kiln in

- line raw mill system and coal mill stack shall not exceed 6.8 lb/ton of clinker. The emission limitation for CO is based on the use of bottom and fly ash as a source of alumina to the cement process. If in the future, the raw material changes or the carbon content of the ash substantially decreases, the emission limitations in this permit for CO may be reviewed and revised as appropriate. In no event shall revised CO emission limitations allow greater emissions than the limitations listed. (o) (SC Regulation 61

- 62.5, Standard No. 5.1, Standard No. 7) 3

-hr block average VOC emissions shall not exceed 0.27 lb/ton of clinker from the sum of both main the kiln stack and the coal mill stack tested simultaneously or ratioed appropriately

.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **38 of 106**  (permit updated 6/27/05 and 8/19/05) (p) (SC Regulation 61

- 62.5, Standard No. 7) 30

- day rolling average SO 2 emissions shall not exceed 3.26 lb/ton of clinker from the sum of both the main kiln stack and the coal mill. (q) (40CFR63.1348) The owner or operator of each new or existing raw material, clinker, or finished product storage bin; conveying system transfer point; bagging system; and bulk loading or unloading system; and each existing raw material dryer, at a facility which is a major source subject to the provisions of this subpart shall not cause to be discharged any gases from these affected sources which exhibit opacity in excess of ten percent. (r) The kiln system is used both as the primary control device for the HWDF burn tank (T111) and the treatment process for the benzene containing waste received at the facility

. (s) (40 CFR 61.348(a)(1)(iii)) The owner or operator shall design, install, operate, and maintain a treatment process that destroys benzene from the waste stream by incinerating the waste in a combustion unit that achieves a destruction efficiency of 99% or greater for benzene. (t) This source is subject to SC Regulation 62.5 Standard No. 7. Upon review, BACT for this source is determined to be: NO x- Low NO x burners, Burner Optimization, Kiln Optimization, Multistage Combustion CO

- Process Optimization VOC

- Process Optimization (u) Per SC Regulation 61

- 62.5, Standard No. 7, this source is limited to a maximum production rate of 2,462,318 short tons per ye ar of clinker. Holcim must record the actual monthly production rates and maintain these records on- site for a period of at least five (5) years from the date generated. The facility shall also maintain daily

clinker production records for the calculation of the NO x , CO, and SO 2 emissions. These records shall be made available to Department personnel upon request. Annual reports including all recorded parameters and calculated values including the annual clinker production rate shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. These conditions shall not supersede any

S tate or Federal requirements such as National Emission Standards f or Hazardous Air Pollutants, unless these conditions would impose a more restrictive limit. (v) The kiln will be allowed to burn various ty pes of fuel due to high temperatures and long residence times including: (v)(1) Hazardous waste derived fuel (HWDF) whi ch will be burned at the burner of the rotary kiln only; (v)(2) Tire derived fuel (TDF) which will be burned in the precalciner; (v)(3) Non

-hazardous liquid fuels which will be burned in the rotary kiln burner, precalciner**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **39 of 106**  (permit updated 6/27/05 and 8/19/05) burner and 61MW hot gas generator. (v)(4) No RCRA coded D/F containing wastes shall be combusted in the kiln. (v)(5) Other ty

pes of fuel may

also be used as approved by the Bureau. These requests shall be submitted to the Division of Engineering Services for review. Any waste materials as defined by S C Regulation 61

- 62.1 shall have a waste analysis performed as required by SC Regulation 61

- 62.5, Standard 3. (w) For the control period that begins on May 3 1, 2004, an owner or operator of any Portland cement kiln subject to SC Regulation 61

- 62.99 shall not operate the kiln during May 3 1 through September unless the kiln has installed and operates during May 3 1 to September 30 with low

- NO x burners, mid

-kiln firing, or alternative control techniques, as defined under section 99.42(a). Inall subsequent control periods, an owner or operator of any P ortland cement kiln subject to this rule shall not operate the kiln during May 1 t hrough September 30 unless the kiln has installed and operates during May 1 to September 30 with low

-NO x burners, mid

-kiln firing, or alternative control techniques, as defined under section 99.42(a). (x) (40CFR63.1204(b)(5)) For kilns equipped with a by

-pass duct or mid

-kiln gas sampling system, carbon monoxide and hydrocarbon emissions are limited in both the by pass duct or midkiln gas sampling system and the main kiln stack as follows. Emissions in the by

-pass or midkiln gas sampling system are limited to either: (x)(1) Carbon monoxide in excess of 100 ppmv, over an hourly rolling average (monitored continuously with a continuous emissions monitoring system,) dry b asis and corrected to 7 percent oxygen. If the permittee elects to comply with this carbon monoxide standard rather than the hydrocarbon standard under paragraph (aa)(2) of this section, the permittee also must document that, during the destruction and removal efficiency

(DRE) test runs or their equivalent as provided by 4 0CFR 63.1206(b)(7), hydrocarbons do not exceed 10 ppmv during those runs, over an hourly rolling average (monitored continuously with a continuous emissions monitoring system), dry

b asis, corrected to 7 percent oxygen, as reported as propane; or (x)(2) Hydrocarbons in the by

-pass duct or midkiln gas sampling system in excess of 10 parts per million by

volume, over an hourly

rolling average (monitored continuously with a continuous emissions monitoring system), dry basis, corrected to 7 percent oxygen, and reported as propane. (y ) (40CFR63.1204(b)(6)) Combined HCl & Cl2 , expressed as HCl equivalents, shall not exceed 86 ppmv on a dry

basis corrected to 7% O 2 when burning hazardous waste. The alternate method of operation listed in Part 7.0(B) of this permit does not impose a limit for HCl & Cl2**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **40 of 106**  (permit updated 6/27/05 and 8/19/05) emissions when non

-hazardous fuels are being used. (z) (SC 61

- 62.5, Standard No. 3(III)(L)(2)) All principal organic hazardous constituents (POHC) must be destroyed with an efficiency of at least 99.99% when burning hazardous waste. (aa) (40CFR63.1204(c)(1)) The Permittee must achieve a destruction and removal efficiency (DRE) of 99.99% for each principal organic hazardous constituent (POHC) designated under the next two paragraphs of this permit condition. The Permittee must calculate DRE for each POHC from the following equation: DRE = [1

- (Wout / Win)] x 100% Where: Win = mass feedrate of one POHC in a waste feedstream; and Wout = mass emission rate of the same POHC present in exhaust emissions prior to release to the atmosphere. The Permittee must treat the POHCs in the waste feed that the permittee specifies under the next paragraph of this permit c ondition to the extent required by the first paragraph of this permit condition. The Permittee must specify one or more POHCs from the list of hazardous air pollutants established by

42 U.S.C. 7412(b)(1), excluding caprolactam (CAS number 105602) as provided by

4 0CFR63.60, for each waste to be burned. The Permittee must base this specification on the degree of difficulty o f incineration of the organic constituents in the waste and on their concentration or mass in the waste feed, considering the results of the waste analyses or other data and information. (bb) (40CFR63.1204(b)(2)) Mercury emissions from the kiln in

- line raw mill system shall not exceed 120 μg / dscm, corrected to 7% oxygen, when burning hazardous waste. (cc) (40CFR63.1204(b)(3)) The sum of Pb & Cd emissions (semivolatile metals) from the kiln in

line raw mill system shall not exceed 180 μg/dscm, corrected to 7% oxygen, when burning hazardous waste. (dd) (40CFR 63.1204(b)(4)) The sum of As, Be, & Cr emissions (low volatile metals) from the kiln in

- line raw mill system shall not exceed 54 μg/dscm, corrected to 7% oxygen, when burning hazardous waste. (ee) (40CFR63.1209(k)(1)) For hazardous waste burning incinerators and cement kilns, if the combustor is equipped with an electrostatic precipitator, baghouse (fabric filter), or other dry emissions control device where particulate matter is suspended in contact with combustion gas, the permittee must establish a limit on the maximum temperature of the gas at the inlet to the device on an hourly rolling average. The permittee must establish the hourly rolling**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **41 of 106**  (permit updated 6/27/05 and 8/19/05) average limit as the average of the test run averages. (ff) (40 CFR 63.1209(k)(2)) The Permittee must measure the temperature of each combustion chamber at a location that best represents, as practicable, the bulk gas temperature in the combustion zone. The Permittee must document the temperature measurement location in the test plan the permittee submitted under §§63.1207(e) and (f); the permittee must establish a minimum hourly

rolling average limit as the average of the test run averages. The alternate method of operation listed in Part 7.0(B) of this permit does not impose a limit for combustion zone chamber temperature when non

-hazardous fuel(s) are being used. (gg) The Permittee has incorporated an Alternate Method of Operation for an occasion in which only non-hazardous fuel(s) are being supplied to the kilns. The Alternate Method of Operation, located in Part 7.0(B) of this permit, does not impose a limit for THC when only non-hazardous fuel(s) are being used. (hh) (40CFR63.1348, Subpart LLL) The owner or operator of each new or existing raw material, clinker, or finished product storage bin; conveying system transfer point; bagging system; and bulk loading or unloading system; and each existing raw material dryer, at a facility which is a major source subject to the provisions of this subpart shall not cause to be discharged any

gases from these af

fected sources which exhibit opacity in excess of ten percent. (ii) The Sampson Feeder System is subject to particulate matter emission limitations from SC Regulation 61

- 62.5, Standard No. 4. The emission limitation is determined as listed below. For pro cess weight rates of greater than 30 tons per hour: E = (55.0) (P 0.11 )

- 40 Where: E = the allowable emission rate in pounds per hour P = process weight rate in tons per hour For the Sampson Feeder System the PM emission limitation is 61.0 lb/hr when operating at full capacity

at 250 tons per hour. **5.E.5 Emissions Limits for the Finish Mill System Equipment** (a) The finish mill sources are subject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and LLL,National Emission Standards for Hazardous Air Pollutants from the Portland Cement Manufacturing Industry

. (b) (40CFR63.1347, Subpart LLL) The owner or operator of each new or existing raw mill or finish mill at a facility

which is a major source subject to the provisions of this subpart shall not cause to be discharged from the mill sweep or air separator air pollution control devices of these affected sources any gases which exhibit opacity in excess of ten percent.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **42 of 106**  (permit updated 6/27/05 and 8/19/05) (c) (40CFR63.1348, Subpart LLL) The owner or operator of each new or existing raw material, clinker, or finished product storage bin; conveying system transfer point; bagging system; and bulk loading or unloading system; and each existing raw material dryer, at a facility which is a major source subject to the provisions of this subpart shall not cause to be discharged any

gases from these affected sources which exhibit opacity in excess of ten percent. (d) These processes are subject to particulate matter emission limitations from SC Regulation 61

- 62.5, Standard No. 4. The emission limitation is determined as listed below. For process weight rates of greater than 30 tons per hour: E = (55.0) (P 0.11 )

- 40 Where: E = the allowable emission rate in pounds per hour P = process weight rate in tons per hour For the Cement Dome Bucket Elevator the PM emission limitation is 70.1 lb/hr when operating at full capacity

at 550 tons per hour. **5.E.6 Emissions Limits for the Cement Loadout Equipment** (a) The cement loadout sources are sub ject to the National Emission Standards for Hazardous Air Pollutants for Affected Source Categories, 40 CFR 63 Subparts A and LLL,National Emission Standards for Hazardous Air Pollutants from the Portland Cement Manufacturing Industry

. (b) **(**40CFR63.1348, Subpart LLL) The owner or operator of each new or existing raw material, clinker, or finished product storage bin; conveying system transfer point; bagging system; and bulk loading or unloading system; and each existing raw material dryer, at a facility which is a major source subject to the provisions of this subpart shall not cause to be discharged any

gases from these affected sources which exhibit opacity in excess of ten percent. (c) (SC Regulation 61

- 62.1, II (H)) PM emissions from the Rainbow products line shall not exceed 0.6 lb/hr. (d) (SC Regulation 61

- 62.1, II (H)) Cement throughput from the Rainbow Process Line (RAI 1, RAI2, RAI3, RAI4) must not exceed 300,000 ston/y r. Unloaded raw materials must not exceed 100 ston/hr. The facility shall maintain daily production records and shall make such records available to Department personnel upon request. (e) (SC Regulation 61

- 62.1, II (H)) PM emissions from the cement dome sources shall not exceed 3.05 lb/hr.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **43 of 106**  (permit updated 6/27/05 and 8/19/05) (f) (SC Regulation 61

- 62.1, II (H)) Cement throughput from the Cement Dome (C319, C320, C321, C322, C323) must not exceed 4,440,000 stons/y r. The facility

shall maintain daily throughput records and make such records available to Department personnel upon request. (g) These processes are subject to particulate matter emission limitations from SC Regulation 61

- 62.5, Standard No. 4. The emission limitation is determined as listed below. For process weight rates of greater than 30 tons per hour: E = (55.0) (P 0.11 )

- 40 Where: E = the allowable emission rate in pounds per hour P = process weight rate in tons per hour For the Truck Lo ad Out Silos the PM emission limitation is 52.8 lb/hr when operating at full capacity at 116.2 tons per hour. **5.E.7 Emissions Limits for the Tanks** (a) The HWDF tanks and closed vent system, including control devices, are subject to all applicable provisions of 40 CFR Part 61 Subpart A (General Provisions), Subpart V (National Emission Standard for Equipment Leaks (Fugitive Emission Sources)), and Subpart FF (National Emission Standard for Benzene Waste Operations); and 40 CFR Part 63 Subpart A (General Provisions) and Subpart DD (National Emission Standards for Hazardous Air Pollutants from Off

- Site Waste and Recovery Operations). (b) (40CFR61.349(a)(2)(ii)) For each closed

-vent system and control device used to comply with standards in accordance with 40 CFR 61.343 through 40 CFR 61.348, the owner or operator shall properly

design, install, operate, and maintain the control device in accordance with the following requirements: A vapor recovery system (e.g., a carbon adsorption system or a condenser) shall recover or control the organic emissions vented to it with an efficiency o f 95 weight percent or greater, or shall recover or control the benzene emissions vented to it with an efficiency

of 99 weight percent or greater. (c) (40CFR60 Subpart Kb) The tanks and closed vent system, including control devices, are subject to all applicable provisions of 40 CFR Part 60 Subpart A (General Provisions) and Subpart Kb (Standards of Performance for VOL Storage Vessels). (d) Inaccordance with SC Regulation 61

- 62.5, Standard No. 4

- Emissions from Process Industries, Section IX

- Visible Emissions (Where Not Specified Elsewhere), where construction or modification began after December 31, 1985, emissions (including fugitive emissions) shall not exhibit an opacity greater than 20%. (e) (SC Regulation 61

- 62.5, Standard No. 5.1, Standard No. 7) VOC emissions for the HWDF**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **44 of 106**  (permit updated 6/27/05 and 8/19/05) Tank (T111) shall not exceed 1.07 ton/y r. (f) The HWDF tanks shall be equipped and controlled as required by 4 0 CFR 61.343 in regards to the following: (1) The tank shall be covered by a f ixed roof as defined in 40CFR61.343(a)(1) and vented directly

through a closed

-vent system to a control device in accordance with 40CFR61.349. (2) The cover and all openings shall be designed to be operated with no detectable emission as indicated by an instrument reading of less than 500 ppmv above background as determined initially and thereafter at least once per ye ar by the methods specified in 40CFR61.355(h)

. (g) The closed vent system per 40CFR61.349 (a)(1) and shall be designed to be operated with no detectable emission as indicated by an instrument reading of less than 500 ppmv above background as determined initially and thereafter at least once per ye ar by the methods specified in 40CFR61.355(h). (h) The control device shall be designed and operated in accordance with 40CFR61.349(a)(2). The vapor recovery

system (carbon adsorber) shall control the organic emissions vented to it with an efficiency

of 95 weight percent or greater. (i) These tanks are subject to LAER requirements (SC Regulation 61

- 62.5, Standard No. 5.1) and PSD requirements (SC Regulation 61

- 62.5, Standard No. 7). LAER and BACT have been determined to be a vapor balance line with the emissions vented through a closed vent system to control devices with at least a 95% efficiency

. (k) As per SC Regulation 61

- 62.5 Standard 1 Section I

- Visible emissions from the Boiler shall not exhibit an opacity

that exceeds 20%. This visible emissions limit does not apply d uring periods of startup, shutdown and malfunction. (l) As per SC Regulation 61

- 62.5 Standard 1 Section II Particulate matter emissions from the Boiler shall not exceed 0.6 lb/million Btu heat input. (m) As per SC Regulation 61

- 62.5 Standard 1 Section III SO 2 emissions from the Boiler shall not exceed 3.5 lb/million Btu heat input. **5.E.8 Facility Wide Emissions Limits** (a) (40CFR63.6(e)(1)(i), Subpart A) Operation and Maintenance (O&M) Requirements: At all times, including periods of startup, shutdown, and malfunction, owners or operators shall operate and maintain any affected source, including associated air pollution control equipment, in a manner consistent with good air pollution control practices for minimizing**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **45 of 106**  (permit updated 6/27/05 and 8/19/05) emissions at least to the level s required by all relevant standards. (b) (40CFR63.6(e)(3)(i), Subpart A) S tartup , Shutdown, and Malfunction (SSM) Plan: The owner or operator of an affected source shall develop and implement a written startup, shutdown, and malfunction plan that describe s, in detail, procedures for operating and maintaining the source during periods of startup, shutdown, and malfunction and a program of corrective action for malfunctioning process and air pollution control equipment used to comply with the relevant standard. As required under Sec. 63.8(c)(1)(i), the plan shall identify all routine or otherwise predictable CMS malfunctions. This plan shall be developed by the owner or operator by

the sources = compliance date for that relevant standard. The plan shall be incorporated by

reference into the sources = Title V permit. Also, per 40 CFR 63, Interim Subpart EEE, (40 CFR 63 (c)(2)(B)) the SSM Plan needs to be submitted to the Administrator for review and approval. (c) **(** SC Regulation 61

- 62.5, Standard 4, Section IX

– Visible Emissions (Where Not Specified Elsewhere) Where construction or modification began on or before December 31, 1985, emissions (including fugitive emissions) shall not exhibit an opacity greater than 40%. Where construction or modification began after December 31, 1985, emissions (including fugitive emissions) shall not exhibit an opacity greater than 20%. (d) (SC Regulation 61

- 62.5, Standard 4, Section X

– Non

-Enclosed Operations) 1. All non- enclosed operations shall be conducted in such a manner that a minimum of particulate matter becomes airborne. In no case shall established ambient air quality standards be exceeded at or beyond the property line. 2. The owner or operator of all such operations shall maintain dust control of the premises and any

roadway owned or controlled by the owner or operator by paving or other suitable measures. Oil treatment is prohibited. 3. All crushing, drying, classification and like operations shall employ a suitable control device acceptable to the Department, and shall discharge no more particulate matter than that specified in Section VIII of SC Regulation 61

- 62.5, Standard 4. (Part 6 updated 5/14/03) **PART 6.0 MONITORING AND REPORTING REQUIREMENTS** 

**– NEW FACILITY**  [SC Regulation 61

- 62.1, Section II] ; [SC Regulation 61

- 62.70.6 (a)(3)(i)(B)] **A. MONITORING AND REPORTING**  Table 6.1 contains summaries of the monitoring and reporting required of this facility

. **TABLE 6.1 MONITORING AND REPORTING** 

**– UNIT ID 01**  **- 07 GENERAL**  **Unit ID**  **Pollutant/ Param eter**  **Limit Required**  **Monitoring Monitori** **ng**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  02

- 06 Initial Notice of Intent to

Comply with MACT Standards N/A Reporting N/A One

-time initially 6.B.1(a)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **46 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 6.1 MONITORING AND REPORTING** 

**– UNIT ID 01**  **- 07 GENERAL**  **Unit ID**  **Pollutant/ Param eter**  **Limit Required**  **Monitoring Monitori** **ng**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  02

- 06 Notification of Compliance

Status with MACT Standards N/A Reporting 60 days after complianc e demonstration Every 5 years 6.B.1(b)
02

- 07 Compliance/Performance

Testing Summary Report N/A Reporting, Recordkeeping Semi

- annually Semi

- annually 6.B.1(c) 02

- 07 SSM Reporting N/A Reporting See Condition See Condition 6.B.1(d) 02

- 07 Immediate SSM Reports N/A Reporting See Condition See Condition 6.B.1(e) 02

- 07 Operation & Maintenance

Plan N/A Reporting N/A See Condition 6.B.1(f) 02

- 07 General Reporting

Requirements N/A Reporting See Condition See Condition 6.B.1(g) 02

- 07 General Recordkeeping

Requirements N/A Recordkeeping See Condition See Condition 6.B.1(h)
02

- 07 Air Pollution Control

Device Operation & Maintenance Program N/A Recordkeeping As Performed As Requested by DHEC 6.B.1(i)
02

- 07 General PC MACT

Notification Requirements N/A Reporting N/A See Condition 6.B.1(j) 01

- 07 Submittal of Reports to

DHEC N/A Reporting N/A As Required by DHEC 6.B.1(k) 01

- 07 Failure to Comply with

O&M Plan N/A Recordkeeping N/A As Required by DHEC 6.B.1(l) 07 Leak Detection and Repair

Program N/A Reporting, Recordkeeping Per Approved

LDAR Program Per Approved

LDAR Program 6.B.1(m) 01

- 07 Source Test Protocol N/A Reporting N/A One time 6.B.1(n) 02

- 07 Exemption From NSPS

Requirements N/A N/A N/A N/A 6.B.1(o)
04 Raw material parameters N/A Monitoring, Reporting, Rec ordkeeping See Condition See Condition 6.B.1(p)

04 Applicability of 40 CFR 63 Interim Subpart EEE (HWC MACT) to Kiln System N/A See Condition See Condition See Condition 6.B.1(q)

04 Changes in Design, Operation, or Maintenance of Kiln System N/A N/A N/A N/A 6.B.1(r)

04 Emergency Safety Vent Operating Plan and Failure Provisions N/A Reporting, Recordkeeping N/A Within 5 days of ESV opening that results in emission limit failure 6.B.1(s)

03

- 04 Certified Operator Training

for Waste Fuel Usage N/A N/A N/A N/A 6.B.1(t) N/A = Not Applicable **TABLE 6.2 MONITORING AND REPORTING** 

**– UNIT ID 01 QUARRY SYSTEM**  **Unit ID**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  01 Quarry General Reporting

Requirements N/A Reporting See Condition See Condition 6.B.2(a)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **47 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 6.2 MONITORING AND REPORTING** 

**– UNIT ID 01 QUARRY SYSTEM**  **Unit ID**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 
01 Quarry Opacity Monitoring

of Quarry Equipment 10% Opacity for

transfer points and 15% Opacity for crushers Method 9 Once within 180 days after startup of quarry Once after

conclusion of Method 9 testing 6 .B.2(b)

**TABLE 6.3 MONITORING AND REPORTING** 

**– UNIT ID 02 RAW MILL SYSTEM**  **Stack ID**  **Unit Description Pollutant/**  **Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S99 Raw Mill Transfer

Point Visible

Emissi ons Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S100 Blending Silo Feed

Bucket Elevator - Bottom Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S101 Blending Silo Top Visible Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **48 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 6.3 MONITORING AND REPORTING** 

**– UNIT ID 02 RAW MILL SYSTEM**  **Stack ID**  **Unit Description Pollutant/**  **Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S102 Raw Mill Silo

Withdrawal Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S103 Kiln Feed Elevator

Top Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S118 Dry Marl Bin Visible Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S123 Fly Ash Receiving

Station Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.3(a)

S12 7 Top of Fly Ash

Receiving Silos Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6 .B.3(a)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **49 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 6.3 MONITORING AND REPORTING** 

**– UNIT ID 02 RAW MILL SYSTEM**  **Stack ID**  **Unit Description Pollutant/**  **Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S99 Raw Mill Transfer

Point Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S100 Blending Silo Feed

Bucket Elevator
- Bottom Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S101 Blending Silo Top Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S102 Raw Mill Silo

Withdrawal Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S103 Kiln Feed Elevator

Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S118 Dry Marl Bin Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **50 of 106**  (permit updated 6/27/05 and 8/19/05) **TABLE 6.3 MONITORING AND REPORTING** 

**– UNIT ID 02 RAW MILL SYSTEM**  **Stack ID**  **Unit Description Pollutant/**  **Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S123 Fly Ash Receiving

Station Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S127 Top of Fly Ash

Receiving Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

annually 6.B.3(a)

S94 Roller Mill

Emission Limitations N/A See Condition 6.B.5 See

Condition 6.B.5 See

Condition 6.B.5 See

Condition 6.B.5 6.B.3(b)

N/A Traffic Fugitives PM No Fugitive Limit N/A N/A N/A 6.B.3(c)
**TABLE 6.4 MONITORING AND REPORTING** 

**– ID 03 COAL MILL SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Requi** **red Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S31 Coal Unloading

Belt General

Monitoring and Reporting Requirements N/A Reporting As indicated by each applicable requirement of 40 CFR 60 Semi

annually 6.B.4(a)

S32 Coal Unloading

Room General

Monitoring and Reporting Requirements N/A Reporting As indicated by each applicable requirement of 40 CFR 60 Semi

annually 6.B.4(a)

S33 Carbon Dust Silo General Monitoring and Reporting Requirements N/A Reporting As indicated by each applic able requirement of 40 CFR 60 Semi

annually 6.B.4(a)

S34 Carbon Feeder General Monitoring and Reporting Requirements N/A Reporting As indicated by each applicable requirement of 40 CFR 60 Semi

annually 6.B.4(a)

S130 Carbon Dust

Unloading General

Monitoring and Reporting Requirements N/A Reporting As indicated by each applicable requirement of 40 CFR 60 Semi

annually 6.B.4(a)**Holcim (US) Inc.**

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**– ID 03 COAL MILL SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Requi** **red Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S132 Coal Bin System

Dedusting General

Monitoring and Reporting Requirements N/A Reporting As indicated by each applicable requirement of 40 CFR 60 Semi

annually 6.B.4(a)

S31 Coal Unloading

Belt Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b)

S32 Coal Unloading

Room Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b) S33 Carbon Dust Silo Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b) S34 Carbon Feeder Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b)

S130 Carbon Dust

Unloading Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b)

S132 Coal Bin System

Dedusting Opacity 20% Visual Inspection Monthly Semi

annually 6.B.4(b)

S95 Coal Mill Opacity Monitoring 20%

Opacity COM or 30

-

minute Method 9 when COM is offline Continuous

monitoring or daily when COM is offline See

condition 6.B.4(c)

S95 Coal Mill PM Emission Monitoring 0.031

gr/dscf Method 5

Reference Test Every 2.5

years Every 2.5

years 6.B.4(d)
S95 Coal Mill Temperature N/A Thermo

couple Continuously Semi

annually 6.B.4(e) S95 Coal Mill VOC See 5.E.4(o) Bureau

Approved Every 2.5

years Every 2.5

years 6.B.4(f)
S95 Coal Mill NOx, SO 2 , CO see 5.E.4(m), (n), (p) CEM Continuous Quarterly 6.B.4(g) S31, S32, S95, S130, S132 Coal Preparation

Plant NSPS Applicability N/A N/A N/A N/A N/A 6.B.4(h)

S95 Applicability of 40

CFR 63 Interim Subpart EEE (HWC MACT) N/A N/A N/A N/A N/A 6.B .4(i)

**TABLE 6.5 MONITORING AND REPORTING** 

**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S22 Clinker Reclaim

Stamler Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S23 Pan Conveyor

North Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S78 #4 Clinker Silo Visible Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S83 Clinker Reclaim

Area Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S22 Clinker Reclaim

Stamler Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S23 Pan Conveyor

North Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S78 #4 Clinker Silo Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S83 Clinker Reclaim

Area Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

C501 Sampson Feeder

System Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S104 Alkali Bypass

Dust Loadout

- Elevator Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S105 Alkali Bypass

Dust Loadout

- Tank Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S106 Clinker Cooler

Transfer Point Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S107 New Clinker Silo

Top Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S108 Clinker Transfer

Under Existing Silos Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

C501 Sampson Feeder

System Visible

Emissions Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; Semi

annually 6.B.5(a)

S104 Alkali Bypass

Dust Loadout

- Elevator Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S105 Alkali Bypass

Dust Loadout

- Tank Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S106 Clinker Cooler

Transfer Point Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S107 New Clinker Silo

Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S108 Clinker Transfer

Under Existing Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

Annual 6.B.5(a)

S94 Preheater/

Precalciner Kiln Opacity

Monitoring 20%

Opacity COM or 30

-

minute Method 9 when COM is offline Continuous

monitoring or daily when COM is offline Quarterly 6.B.5(b)

S94 Preheater/

Precalciner Kiln Dioxin/Furan

Monitoring 0.20 ng

TEQ @ 7% O 2 or 0.40 ng TEQ @ 7% O 2 if avg. temp  400  F Method

0023A (SW

846) Initially and

every 2.5 years thereafter Quarterly 6.B.5(c)

S94 Preheater/

Precalciner Kiln PM Emission

Monitoring 0.15

kg/Mg (0.30 lb/ton) 56.97 lb/hr Method 5 Every 2.5 years Quarterly 6.B.5(d)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S94 Preheater/

Precalciner Kiln Inlet APCD

Temperature Monitoring Determin

e during complianc e performan ce test Thermo

couple Continuous

monitoring Semi

- annual 6.B.5(e)

All Kiln System

Sources General

Reporting Requirements N/A Reporting See condition See condition 6.B.5(f)

S94 Preheater/

Precalciner Kiln General

Benzene Waste Requirements N/A Reporting, Monitoring See condition See condition 6.B.5(g)
S94 Preheater/

Precalciner Kiln Benzene Waste

Monitoring DRE>99

% N/A N/A N/A 6.B.5(h)

S94 Preheater/

Precalciner Kiln Minimum

Combustion Zone Temperature Determin

e during complianc e performan ce test Temperature Continuous N/A 6.B.5(i)

S94 Preheater/

Precalciner Kiln Vent stream location changes N/A Reporting N/A For each occurrence 6.B .5(j)
S94 Preheater/

Precalciner Kiln Raw material content See

Condition Reporting See Condition Semi

annually 6.B.5(k)
S94 Preheater/

Precalciner Kiln Quarterly COMs Reporting N/A COM Continuous Quarterly 6.B.5(l)

S94 Preheater/

Precalciner Kiln Standard No. 3

Waste Feed Rate N/A CMS Continuous Exceedances reported quarterly 6.B.5(m)
S94 Preheater/

Precalciner Kiln Kiln System

Plan Reporting N/A Reporting N/A Prior to operation 6.B.5(n) S94 Preheater/

Precalciner Kiln NOx, SO 2 , CO CEMS 5.E.4(m,

n, p) CEM Continuous Quarterly 6.B.5(o)

S94 Preheater/

Precalciner Kiln Emission Limits and Requirements During Kiln Venting to Coal Mill 6.B.5 See Condition See

Condition See

Condition 6.B.5(p)

S94 Preheater/

Precalciner Kiln Production rate 2,462,318 ston clinker/yr Record

keeping Daily Semi

Annual 6.B.5(q)

S94 Preheater/

Precalciner Kiln Initial

Compliance Demonstration 40CFR

63.1349 (b) and 63.7 See

Condition See

Condition See

Condition 6.B.5(r)

S94 Preheater/

Precalciner Kiln Combustion System Inspecti on N/A Monitoring Annually Semi

Annually 6.B.5(s)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 
S94 Preheater/

Precalciner Kiln HWDF System

Control Device Recordkeeping Requirements N/A Record

keeping N/A N/A 6.B.5(t)

S94 Preheater/

Precalciner Kiln Kiln Source

Testing

– Ni, Cd, Cr, As, Pb, HCl, POHC, DRE, PM, CO, O 2 SC Reg.

61

- 62.5 Standard No. 3 Monitoring,

Reporting Every 2.5

years Every 2.5

years 6.B.5(u)

S94 Preheater/

Precalciner Kiln PM Emission

Calculations for the Kiln 40 CFR

63.1204 (a) (7)(ii) N/A N/A N/A 6.B.5(v)

S94 Preheater/

Precalciner Kiln Kiln DRE Standard at least

99.99% for each POHC N/A Initial N/A 6.B.5(w)

S94 Preheater/

Precalciner Kiln Applicability of

HWC MACT During SSM Conditions N/A N/A N/A N/A 6.B.5(x)

S94 Preheater/

Precalciner Kiln Hazardous Waste Residence Time Calculations N/A Reporting, Record

keeping N/A Each time a notification of compliance is submitted 6.B.5(y)

S94 Preheater/

Precalciner Kiln Operating

Requirements for Kiln N/A N/A N/A Record keeping 6.B.5(z)

S94 Preheater/

Precalciner Kiln SSM Plan for

Hazardous Waste Combustor N/A Record

keeping N/A Record keeping 6.B.5(aa)

S94 Preheater/

Precalciner Kiln Automatic

Waste Feed Cutoff System Requirements N/A Visual Inspection and System Testing Weekly alarm

checks; monthly cutoff system operability checks Record

keeping 6.B.5(bb)

S94 Preheater/

Precalciner Kiln Control of

Combustion System Leaks Kiln

Delta P<Ambie nt P N/A N/A Record keeping 6.B.5(cc)

S94 Preheater/

Precalciner Kiln O&M Plan for

Hazardous Waste Combustor N/A Record

keeping N/A Record keeping 6.B.5(dd)

S94 Preheater/

Precalciner Kiln THC Emissions

In Alkali Bypass Stack 10 ppm CEM Continuous Quarterly 6.B.5(ee)

S94 Preheater/

Precalciner Kiln Opacity 20% Opacity COM or 30

-

minute Method 9 when COM is offline Monitoring

daily when COM is offline Quarterly 6.B.5(ff)**Holcim (US) Inc.**

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**– ID 04 KILN SYSTEM**  **Stack ID**  **Unit**

**Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  S94 Preheater/

Precalciner Kiln Kiln Feedstream Analysis N/A See Condition See

Condition Record

keeping 6.B.5(gg)

S94 Preheater/

Precalciner Kiln DRE, D/F, Hg,

PM, Semi

- and low volatile metals, HCl, Cl and max. combustion chamber pressure 40 CFR

63.1209 (EEE) See

Condition See

Condition Record

keeping 6.B.5(hh)

S94 Preheater/

Precalciner Kiln See Condition 40 CFR 63.1210 (EEE) Notification See Condition N/A 6.B.5(ii)

S94 Preheater/

Precalciner Kiln See Condition 40 CFR 63.1211 (EEE) Record

keeping and Reporting See

Condition See

condition 6.B.5(jj)
**TABLE 6.6 MONITORING AND REPORTING** 

**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber**  All All Finish Mill

Equipment General PC

MACT Requirements N/A N/A N/A Semi

annually 6.B.6(a)

S55 #4 Finish Mill

Classifier Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test Semi

annually 6.B.6(b)(2)

S56 #4 Finish Mill

Fines Classifier Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test Semi

annually 6.B.6(b)(2)

S57 #4 Finish Mill Collector Belt Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test Semi

annually 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S54 #4 Finish Mill Visible Emission Monitoring No visible

emissions 6

-minute

Method 22 If visible emission is observed, perform follow

up Method 22 test wit hin 24 hours Daily Semi

- annual 6.B.6(b)(3)

S96 #5 Finish Mill Separator and Baghouse Visible

Emission Monitoring No visible

emissions 6

-minute

Method 22 If visible emission is observed, perform follow

up Method 22 test within 24 hours Daily Semi

- annual 6 .B.6(b)(3)

S97 #6 Finish Mill Separator and Baghouse Visible

Emission Monitoring No visible

emissions 6

-minute

Method 22 If visible emission is observed, perform follow

up Method 22 test within 24 hours Daily Semi

- annual 6.B.6(b)(3)

S55 #4 Finish Mill

C lassifier Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S56 #4 Finish Mill

Fines Classifier Opacity

Monitoring 10%

Op acity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S57 #4 Finish Mill Collector Belt Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S54 #4 Finish Mill Opacity Monitoring 10%

Opacity 30

-minute

Method 9 Initially and

every 5 years thereafter Semi

annually 6.B.6(b)(1)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber**  S96 #5 Finish Mill Separator and Baghouse Opacity

Monitoring 10%

Opacity 30

-minute

Method 9 Initially and

every 5 years thereafter Semi

annually 6.B.6(b)(1)

S97 #6 Finish Mill Separator and Baghouse Opacity

Monitoring 10%

Opacity 30

-minute

Method 9 Initially and

every 5 years thereafter Semi

annually 6.B.6(b)(1)

C324 Cement Dome

Bucket Elevator

- Upper Opacity

Monitoring 10%

Opacity 30

-minute

Method 9 Initially and

every 5 years thereafter Semi

annually 6.B.6(b)(1)

C325 Cement Dome

Bucket Elevator

- Lower Opacity

Monitoring 10%

Opacity 30

-minute

Method 9 Initially and

every 5 years thereafter Semi

annually 6.B.6(b)(1)

S114 #6 Finish Mill

Clinker/ Additives Bins

- Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

vi sible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S115 #5 Finish Mill

Clinker/ Additives Bins

- Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S116 #6 Finish Mill

Clinker/ Additives Bins

- Bottom Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S117 #5 Finish Mill

Clinker/ Additives Bins

- Bottom Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S120 #5 Finish Mill

Feed End Dedusting Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S121 #6 Finish Mill

Feed End Dedusting Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S135 #5 Finish Mill Discharge End Dedusting Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual te st, then annually Semi

annually 6.B.6(b)(2)

S136 #6 Finish Mill Discharge End Dedusting Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emiss ions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S169 Top of Finish

Mill #3 Silos Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S170 Top of Finish

Mill #4 Silos Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S171 Top of Finish

Mill #1 Silos Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S172 Top of Finish

Mill #2 Silos Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S174 #5 & #6

Finish Mill Hopper Dedusting Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S175 #4 Finish Mill

Dribble Bin Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

vis ible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S180 Marl/Lime

Alleviator Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S119 Off Spec Clinker Silo

– Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S126 New Additive

System

– Dry Lime Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S177 Cement Feed

to Cooler

– FM#6 Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S178 Finish Mill #5/#6 Dribble Bin Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S181 Dry Marl

Transport from 8

-pack Visible

Emis sion Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

C324 Cement Dome

Bucket Elevator

- Upper Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

C325 Cement D ome

Bucket Elevator

- Lower Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, then annually Semi

annually 6.B.6(b)(2)

S114 #6 Finish Mill

Clinker/ Additives Bins

- Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S115 #5 Finish Mill

Clinker/ Additives Bins

- Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S116 #6 Finish Mill

Clinker/ Additives Bins

- Bottom Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S117 #5 Finish Mill

Clinker/ Additives Bins

- Bottom Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S120 #5 Finish Mill

Feed End Dedusting Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S121 #6 Finish Mill

Feed End Dedusting Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S135 #5 Finish Mill Discharge End Dedusting Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S136 #6 Finish Mill Discharge End Dedusting Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S169 Top of Finish

Mill #3 Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S170 Top of Finish

Mill #4 Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S171 Top of Finish

Mill #1 Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S172 Top of Finish

Mill #2 Silos Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S174 #5 & #6

Finish Mill Hopper Dedusting Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S175 #4 Finish Mill

Dribble Bin Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 05 FINISH MILL SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condit** **ion**

**Num ber** 

S180 Marl/Lime

Alleviator Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S119 Off Spec Clinker Silo

– Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S126 New Additive

System

– Dry Lime Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S177 Cement Fe ed

to Cooler

– FM#6 Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S178 Finish Mill #5/#6 Dribble Bin Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)

S181 Dry Marl

Transport from 8

-pack Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 if the equipment continues to operate Semi

-Annual 6.B.6(b)(2)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S63 #1 Truck

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S64 #2 Truck/Rail

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions f

or semi

- annual test, Semi

annually 6.B.7(a)

S65 #3 Truck/Rail

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S66 #4 Truck

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S67 East Packer Visible Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S68 We st Packer Visible Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S85 Cement Dome Conveyor and Collection Box Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S86 Cement Dome

Alleviator Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S87 Cement Dome

Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S88 Cement Dome

Reclaim Tower Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S89 Cement Dome

Surge Bin Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S90 #5 Truck

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S91 #6 Truck

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Metho d 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S113 Rainbow

Products Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S122 Cement

Transport to Rail Loading Bin Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S137 Cement

Transport Elevator Bottom Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Mont

hly; if no visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S138 Cement

Transport Elevator Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S144 #7 Rail Scale Visible Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S145 #8 Rail Scale Visible Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S176 #9 Truck

Scale Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S179 Rail Car Surge

Bin Top Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S183 Truck Load

Out Silo Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S184 Truck Load

Out Silo Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S185 Truck Load

Out Silo Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions f

or semi

- annual test, Semi

annually 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S186 Truck Load

Out Silo Visible

Emission Monitoring No visible

emissions 1

-minute

Method 22 Monthly; if no

visible emissions for 6 consecutive months, then semi

- annually; if no visible emissions for semi

- annual test, Semi

annually 6.B.7(a)

S63 #1 Truck

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S64 #2 Truck/Rail

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S65 #3 Truck/Rail

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S66 #4 Truck

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emi ssions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S67 East Packer Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S68 West Packer Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S85 Cement Dome Conveyor and Collection Box Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S86 Cement Dome

Alleviator Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S87 Cement Dome

Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S88 Cement Dome

Reclaim Tower Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S89 Cement Dome

Surge Bin Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S90 #5 Truck

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S91 #6 Truck

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S113 Rainbow

Products Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S122 Cement

Transport to Rail Loading Bin Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S137 Cement

Transport Elevator Bottom Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S138 Cement

Transport Elevator Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S144 #7 Rail Scale Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S145 #8 Rail Scale Opacity Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S176 #9 Truck

Scale Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S179 Rail Car Surge

Bin Top Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S183 Truck Load

Out Silo Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions ob served during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S184 Truck Load

Out Silo Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)**Holcim (US) Inc.**

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**– ID 06 CEMENT LOADOUT SYSTEM**  **Stack ID**  **Unit Description**  **Pollutant/**

**Param eter**  **Limit Re**  **quired Monitoring**  **Monitoring**

**Frequency Reporting** 

**Frequency Condition** 

**Num ber** 

S185 Truck Load

Out Silo Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

S186 Truck Load

Out Silo Opacity

Monitoring 10%

Opacity 6

-minute

Method 9 No later than 1

hour after visible emissions observed during a Method 22 Test if the equipment continues to operate Semi

Annual 6.B.7(a)

**TABLE 6.8 MONITORING AND REPORTING** 

**– ID**  **07 TANK SYSTEM Stack**  **ID Unit**  **Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  S111, S128 HWDF Tanks

and Closed Vent System General

Regulatory Requirements See

Condition See

Condition See Condition See Condition 6.B.8(a) S111, S128 HWDF Tanks

and Closed Vent System General

Reporting Requirements See

Condition See

Condition Semi

-

Annually See Condition 6.B.8(b)
S111, S128 HWDF Tanks

and Closed Vent System VOC 500 ppmv above background Portable

Flame Ionization Detector Daily Semi

- annually 6.B.8(c)
S111, S128 HWDF Tanks

and Closed Vent System VOC N/A Monitoring of Pumps See Condition Semi

-Annually 6.B.8(d)
S111, S128 HWDF Tanks

and Closed Vent System VOC N/A Visual Inspection of Closed Vent System Initially, and

Quarterly Thereafter Semi

-Annually 6.B.8(e)

S111, S128 HWDF Tanks

and Closed Vent System HWDF Tank

Requirements 500 ppmv

above background Visual

Inspection, and Portable Flame Ionization Detector Initially, and

Quarterly Thereaf ter Semi

-Annually 6.B.8(f)

S111, S128 HWDF Tanks

and Closed Vent System Monitoring of

Closed Vent System N/A Portable Flame Ionization Detector Monthly Semi annual LDAR report 6.B.8(g)

S111, S128 HWDF Tanks

and Closed Vent System Closed Vent

System Bypas s Requirements N/A Visual Inspection of Closed Vent System Bypass Daily

(Valves); Monthly (Monitoring Devices) Semi

-Annually 6.B.8(h)**Holcim (US) Inc.**

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**– ID**  **07 TANK SYSTEM Stack**  **ID Unit**  **Description Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  07 HWDF

Delivery System VOC See Condition See

Condition See Condition See Condition 6.B.8(a

-h)

S111, S128) HWDF Tanks

and Closed Vent System Visual

Inspections of Benzene Emissions from HWDF System N/A Monitoring, Record Keeping As Performed N/A 6.B.8(i)

S111, S128) HWDF Tanks

and Closed Vent System Records of

Tests of No Detectable Emissions for HWDF System No

Detectable Emissions Monitoring,

Record Keeping Annual N/A 6.B.8(j)

S111, S128) HWDF Tanks

and Closed Vent System Recordkeeping

for Closed Vent System Control Device N/A Record Keeping N/A N/A 6.B.8(k)
S111, S128) HWDF Tanks

and Closed Vent System Opacity 20% Visual inspection Semi

- annual Semi

- annual 6.B.8(l) T100, T147, T148, T149 NHWDF

tanks Operational

requirements See

Condition See

Condition See Condition See Condition 6.B.8(m)

**TABLE 6.9 MONITORING AND REPORTING** 

**– PERFORMANCE TESTING**  **Stack ID**  **Unit Descriptio**  **n Pollutant/** 

**Param eter**  **Limit Required**  **Monitoring Monitoring** 

**Frequency Reporting** 

**Frequency Condition** 

**Num ber**  ID03 (S95) and ID04 (S95) Preheater/

Precalciner Kiln and Coal Mill HWC MACT

Compliance See

Condition See

Condition See

Condition See

Condition 6.B .9(a)

Facility Wide Facility Wide

except ID 03 S95 and ID 04 S94 PC MACT

Performance Testing Requirements See

Condition See

Condition See

Condition See

Condition 6.B.9(b)

ID03 (S95) Coal Mill Coal Mill System Performance Testing Requirements 0.031

gr/dsc f PM Method 5 See Condition See

Condition 6.B.9(c)
Facility Wide All Affected

Sources Source Testing

Requirements See

Condition Monitoring

(Performance Testing) N/A As Performed 6.B.9(d)
**B. MONITORING AND REPORTING CONDITIONS**  **6.B.1 GENERAL** (a) The Notific ation of Compliance with 40 CFR 63 standards shall contain the information**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **77 of 106**  (permit updated 6/27/05 and 8/19/05) listed in paragraphs (a)(1) through (a)(7) of this condition. The operating requirements specified in the Notification of Compliance will be incorporated in the Title V permit through the use of a Section 502(b)(10) change or a minor permit modification. (1) The methods that were used to determine compliance. (2) The results of any

p erformance tests, opacity or visible emission observations, CMS performance evaluations, and/or other monitoring procedures or methods that were conducted. (3) The methods that will be used for determining continuing compliance, including a description of monitoring and reporting requirements and test methods. (4) The ty

pe and quantity

o f hazardous air pollutants emitted by the source (or surrogate pollutants if specified in the relevant standard), reported in units and averaging times and in accordance with the test methods specified in the relevant standard. (5) An analysis demonstrating whether the affected source is a major source or an area source (using the emissions data generated for this notification). (6) A description of the air pollution control equipment (or method) for each emission point, including each control device (or method) for each hazardous air pollutant and the control efficiency

(percent) for each control device (or method); (7) A statement by

the owner or operator of the affected existing, new, or reconstructed source as to whether the source has complied with the relevant standard or other requirements. (b) A notification of compliance status with 40 CFR 63 standards must be submitted before a Title V Operating Permit will be renewed or reissued to the Permittee. The notification must be submitted before the close of business on the 60 th day f ollowing the completion of the compliance demonstration. The notification must contain the following information (40 CFR 63.9(h)): (1) Methods used to determine compliance; (2) Results from any

monitoring procedures or methods conducted; (3) Methods to be used to determine continuing compliance, including a description of monitoring and reporting requirements and test methods; (4) The ty

pe and quantity

o f hazardous air pollutants emitted by t he source, accompanied by units of measurement and averaging times;**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **78 of 106**  (permit updated 6/27/05 and 8/19/05) (5) An analysis demonstrating whether the source is a major or area source; (6) A description of the air pollution control equipment and its associated control efficiency; and (7) A statement from the owner or operator as to whether the source has complied with the relevant standard or other requirements. (c) An excess emissions and monitoring system performance testing summary report shall be submitted no later than 30 days following the end of each calendar half or quarter that presents the results of all performance testing, monitoring system performance tests, and excess emissions episodes. (40 CFR 63.10(e)(3)) (1) The following information must be included in the summary report entitled “Summary

Report
- Gaseous and Opacity Excess Emission and Continuous Monitoring System Performance”: (i) Company

name and address; (ii) Each hazardous air pollutant monitored; (iii) Beginning and ending dates of the reporting period; (iv) Brief description of process units; (v) Emission and operating parameter limitations; (vi) Monitoring equipment manufacturer(s) and model number(s) (vii) Date of latest CMS certification or audit; (viii) Total operating time of the source during the monitoring period; (ix) An emission data summary or control system parameter summary that illustrates excess emission episodes and their causes; (x) A CMS performance summary or control system parameter summary that describes CMS downtime periods and their causes; (xi) A description of CMS, process, or control changes since the last reporting period; (xii) The name, title, and signature of the responsible official certifying the accuracy of the report; and**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **79 of 106**  (permit updated 6/27/05 and 8/19/05) (xiii) The report date. (2) If the total duration of excess emissions for the reporting period is le ss than 1 percent of total operating time for the period and CMS downtime for the reporting period is less than 5 percent of total operating time for the period, then only the summary report will need to be submitted. The full excess emissions and performance testing report need not be submitted unless otherwise stated. (3) If the total duration of excess emissions is greater than or equal to 1 percent of total operating time for the period and CMS downtime for the reporting period is greater than or equal to 5 percent of total operating time for the period, then the summary report and full excess emissions and performance testing reports must be submitted. (d) For all sources subject to 40CFR63 Subpart A, if actions taken by the Permittee during a startup, shutdown, or malfunction of an affected source (including actions taken to correct a malfunction) are consistent with the procedures specified in the source's startup, shutdown, and malfunction plan, then the Permittee shall state such information in a startup, shutdown, and malfunction report. Reports shall only b e required if a startup, shutdown, or malfunction occurred during the reporting period. The report shall consist of a letter, containing the name, title, and signature of the responsible official who is certifying its accuracy, which shall be submitted to the Department semiannually. It shall be delivered or postmarked by the 30th day f ollowing the end of each calendar half (or other calendar reporting period, as appropriate). If the Permittee is required to submit excess emissions and continuous monitoring system performance (or other periodic) reports, then the startup, shutdown, and malfunction reports may b e submitted simultaneously with the excess emissions and continuous monitoring system perf ormance (or other) reports. If startup, shutdown, and malfunction reports are submitted with excess emissions and continuous monitoring system performance (or other periodic) reports and the Permittee receives approval to reduce the frequency o f reporting for the latter as specified by 4 0CFR63.10(e), the frequency o f reporting for the startup, shutdown, and malfunction reports also may b e reduced if the Department does not object to the intended change. The procedures to implement the allowance in the prec eding sentence shall be the same as the procedures specified in 40CFR63.10(e)(3). Ac opy o f the report shall also be kept on- site and on- file and made available to Department personnel upon request. (e) Notwithstanding the allowance to reduce the frequency o f reporting for periodic startup, shutdown, and malfunction reports as specified in condition 6.B.1(d), any time an action taken by the Permittee d

uring a startup, shutdown, or malfunction (including actions taken to correct a malfunction) is not consistent with the procedures specified in the affected source's startup, shutdown, and malfunction plan, the Permittee shall report the actions taken for that event within 24

-hours after commencing actions inconsistent with the plan followed by a letter within seven (7) working days after the end of the event. The immediate report shall consist of a telephone call (or facsimile [FAX] transmission) to the appropriate Trident**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **80 of 106**  (permit updated 6/27/05 and 8/19/05) District Office and Lower Savannah District Office personnel within 24 hours after commencing actions inconsistent with the plan, and it shall be followed by a letter, delivered or postmarked within seven (7) working days after the end of the event, that contains the name, title, and signature of the responsible official who is certify ing its accuracy, explaining the circumstances of the event, the reasons for not following the startup, shutdown, and malfunction plan, and whether any excess emissions and/or parameter monitoring exceedances are believed to have occurred. The letter shall also be sent to Technical Management Section of the Bureau of Air Quality

. (f) The owner or operator shall prepare for each affected source, a written operations and maintenance plan, per 40 CFR 63 Subpart A. The plan shall be submitted to the Bureau for review and approval for applicable 40 CFR 63 Subpart LLL sources as part of the renewal or reissue application for a Title V permit. (g) All reports required by 40CFR63, Subpart A shall be submitted as required including: (1) The results of performance tests (including opacity test results) and results of the performance evaluation of the continuous monitoring system, (2) Startup, shutdown, or malfunction report if consistent with the startup, shutdown, or malfunction plan required by 4 0 CFR63.10(d)(5) (semi

- annual) , if not consistent with above plan a report shall be made within 24

-hours by phone or fax. The immediate report shall be followed by a letter, certified by

the owner or operator or other responsible official explaining the circumstances of the event, the reasons for not following the startup, shutdown, and malfunction plan, and whether any excess emission and/or parameter monitoring exceedances are believed to have occurred, (3) All failures to comply with any provisions of the operation and maintenance plan. (h) The owner/operator shall maintain on file all measurements required by t his permit including continuous monitoring system or monitoring device performance measurements; all continuous monitoring system performance evaluations; all continuous monitoring system or monitoring device calibration checks; adjustments and maintenance performed on these systems or devices; and all other information required in a permanent form suitable for inspection by

D epartment personnel for at least five (5) ye ars following the date of such measurement, maintenance, report and record. (i) The Permittee shall implement a program for routine inspection and subsequent maintenance on all air pollution control equipment including duct work, piping, or any other materials pertaining to material transport or storage where there is potential for generation or release of regulated air pollutants. Maintenance events shall be recorded in a permanent form suitable and available for inspection by representatives of this Department. The se records shall be retained for at least five years following the date of such maintenance. Areasonable inventory o f routine replacement items shall be kept on site to facilitate timely repair of any**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **81 of 106**  (permit updated 6/27/05 and 8/19/05) malfunctioning systems. (j) All notifications as required by 40CFR63, Subpart A shall be submitted as required to the Technical Management Section, including notification of performance tests, opacity and visible emission observations, continuous emission monitor performance evaluation and compliance status. (k) This permit contains compliance certification, testing, monitoring, reporting, and record keeping requirements sufficient to assure compliance with the terms and conditions of this permit. All submittals required by these conditions shall be sent to the South Carolina Department of Health and Environmental Control

- Bureau of Air Quality ( SC DHEC

- BAQ) at the following address: SC DHEC

- BAQ Technical Management Section 2600 Bull Street Columbia, SC 29201 (l) Failure to comply

with any provision of the operations and maintenance plan developed shall be in noncompliance with 40CFR63, Subpart LLL. (m) The Bureau of Air Quality has reviewed and approved a Leak Detection and Repair (LDAR) program as an acceptable preventative maintenance program for the existing facility. The Permittee must submit an updated program and gain Bureau approval prior to the operation of the new equipment at the facility

. The plan should also incorporate all applicable provisions of 40 CFR 61 Subpart V (National Emission Standard for Equipment Leaks (Fugitive Emission Sources)) including monitoring, recordkeeping and reporting frequencies as required. The Permittee must adhere to all terms and conditions contained in the approved LDAR program, including all required reporting and recordkeeping requirements. All reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality

. The LDAR plan shall be maintained on site for inspection and review by a Department representative. (n) The facility

shall submit a source test protocol in compliance with the appropriate federal regulations and also SC Regulations 61

- 62.1, Section IV

- Source Tests. Ac opy o f the comprehensive test plan shall also be submitted to the Director of the Division of Engineering Service s. (o) Inaccordance with 40 CFR63.1356, any affected source subject to the provisions of 40CFR63 Subpart LLL is exempted from 40 CFR 60, Subpart F. (p) The emission limitations for NO x and CO are based on several process assumptions such as raw material moisture content, carbon content, nitrogen content and sulfur content. The facility shall monitor raw material moisture content, carbon content, nitrogen content and**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **82 of 106**  (permit updated 6/27/05 and 8/19/05) sulfur content on a semi

- annual basis for the first two years of commercial operation and annually thereafter. The Department reserves the right to request material testing at any time that conditions warrant, or to increase the frequency o f testing. The method of testing shall be approved by

the Department. Records of the material testing shall b e maintained on site for a period of at least five (5) years from the date generated and shall be made available to a Department representative upon request. Annual reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality, postmarked no later than 30 calendar days after the end of the reporting period. (q) The kiln system is subject to all applicable provisions of 40CFR63, Subpart A (General Provisions) and Interim Subpart EEE (National Emission Standards for Hazardous Air Pollutants from Hazardous Waste Combustors) until the permittee: (1) Ceases hazardous waste
- derived fuel burning operations (i.e., hazardous waste
derived fuel is no longer in the combustion chamber); and (2) Complies with all other applicable federal and state regulations. (r) If any

changes are made in the design, operation, or maintenance of the system that may adversely affect compliance with any standard that is not monitored by a CEM, the change must be determined, and 40 CFR § 63.1206(b)(5) must be complied with. Achange is defined for this condition as any change in design, operation, or maintenance practices that were documented in the comprehensive performance test plan, Notification of Compliance, or startup, shutdown, and malfunction plan. (40 CFR § 63.1206(b)(5)) (s) If an emergency

s afety vent (ESV) opens when hazardous waste remains in the combustion chamber such that combustion gases are not treated as during the most recent comprehensive performance test, it is evidence of the permittee’s failure to comply with the emissions limitations of the HWC MACT. An ESV operating plan must be developed, complied with and kept in the operating record. The plan requirements are listed in 40 CFR § 63.1206(c)(4). A written report is required within 5 days of an ESV opening that results in failure to meet the emission limitations documenting the result of the investigation and corrective measures taken. (40 CFR § 63.1206(c)(4)) (t) The permittee must establish training programs for all categories of personnel whose activities may

reasonably

b e expected to directly

affect emissions of hazardous air pollutants from the source. Such persons include, but are not limited to, chief facility operators, control room operators, continuous monitoring system operators, persons that sample and analy ze feed streams, persons that manage and charge feed streams to the combustor, persons that operate emission control devices, and ash and waste handlers. Each training program shall be of a technical level commensurate with the person's job duties specified in the training manual. Each commensurate training program shall require an examination to be administered by

the instructor at the end of the training course. Pas sing of this test shall be**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **83 of 106**  (permit updated 6/27/05 and 8/19/05) deemed the "certification" for personnel, except that, for control room operators, the training and certification program shall be as specified in paragraphs (c)(6)(iii) through (c)(6)(vi) of 40 CFR 63.1206. **6.B.2 QUARRY SYSTEM** (a) These sources are subject to all applicable requirements of Federal New Source Performance Standards (NSPS) 40 CFR Part 60, Subpart OOO. The requirements for inspections, testing, reporting, monitoring, etc. listed in 40 CFR Parts 60, Subparts A and OOO shall be completed and reported as specified. (b) Inaccordance with 40 CFR Part 60, Subpart OOO

- Standards of Performance for Nonmetallic Mineral Processing Plants, crushers shall not exhibit an opacity greater than 15%. In accordance with 40 CFR Part 60, Subpart OOO (Standards of Performance for Nonmetallic Mineral Processing Plants), belt convey ors or other affected facilities as defined in 40 CFR § 60.670 except crushers shall not exhibit an opacity greater than 10% when conveying unsaturated materials. Source tests for opacity indicating compliance with permit standards are required prior to a permit to operate being issued. The owner/operator of these sources may

use the alternative Method 9 testing to show compliance with the appropriate opacity standard. This Method 9 allows belt conveyor transfer points and screens without emission capture systems to reduce the duration of observations of fugitive emissions from 3 hours (thirty

6

-minute averages) to 1 hour (ten 6

-minute averages) if there are no individual readings greater than 15 percent opacity f or crushers or 10 percent opacity f or other affected emission units and there are no more than 3 readings of 15 percent for crushers or 10 percent for other affected emission units for the first 1

-hour period. If the alternative Method 9 testing fails to prove compliance, the traditional Method 9 testing is required. These tests shall be performed within 60 days of achieving the maximum production rate, but no later than 180 days after the initial startu p. S ource test methodology must be approved by

the BAQ. The Manager of Source Evaluation, BAQ shall be notified of the anticipated date of the required opacity

testing, postmarked not less than 45 days prior to such date so that a Bureau representative may b e present if desired. Rescheduled source tests require 7 days notification. **6.B.3 RAW MILL SYSTEM** (a) The owner or operator must conduct a monthly 1

-minute visible emissions test of each affected source in accordance with Method 22 of Appendix A to 40 CFR 60. The test must be conducted while the affected source is in operation. If no visible emissions are observed in six consecutive monthly tests for any

affected source, the owner or operator may decrease the frequency

o f testing from monthly

to semi

- annually

f or that affected source. If visible emissions are observed during any s emi

- annual test, the owner or operator must resume testing of that affected source on a monthly b asis and maintain that schedule until no visible emissions are observed in six c onsecutive monthly tests. If no visible emissions are observed during the semi

- annual test for any affected source, the owner or operator may decrease the**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **84 of 106**  (permit updated 6/27/05 and 8/19/05) frequency o f testing from semi

- annually to annually

f or that affected source. If visible emissions are observed during any annual test, the owner or operator must resume testing of that affected source on a monthly b asis and maintain that schedule until no visible emissions are observed in six consecutive monthly tests. If visible emissions are observed during any Method 22 test, the owner or operator must conduct a 6

-minute test of opacity in accordance with Method 9 of appendix A to part 60 of this chapter. The Method 9 test must begin within one hour of any

observation of visible emissions. (b) All emiss ion limitations for the roller mill, which is considered as part of an in

-line raw mill/ kiln system, are included in section 6.B.5. (c) Fugitive emissions shall be controlled using dust suppression techniques including paving, brooming and watering for problem areas.
**6.B.4 COAL MILL SYSTEM** (a) These sources are subject to all applicable provisions of 40 CFR 60 Subpart A (General Provisions) and Subpart Y (Coal Preparation Plants). (b) The permittee shall perform a visual inspection on a monthly b asis. Visual Inspection means a qualitative observation of opacity d uring daylight hours where the inspector records results in a log, noting color, duration, density (heavy or light), cause and corrective action taken for any a bnormal emissions. The observer does not ne ed to be certified to conduct valid visual inspections. However, at a minimum, the observer should be trained and knowledgeable about the effects on visibility o f emissions caused by

b ackground contrast, ambient lighting, observer position relative to lighting, wind, and the presence of uncombined water. Lo gs shall be kept to record all visual inspections, including cause and corrective action taken for any a bnormal emissions and visual inspections from date of recording. The logs shall be maintained for a period of five (5) ye ars and be made available to the Department upon request. The owner/operator shall submit semi

- annual reports to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (c) Opacity

for the coal mill shall be monitored using a continuous opacity monitor (COM). If the COM should go off

- line, opacity

shall be monitored daily using a 30

-minute EPA Method 9 test. Lo gs shall be kept to record all visual inspections, including cause and corrective action taken for any a bnormal emissions and visual inspections from date of recording. The logs shall be maintained for a period of five (5) ye ars and be made available to the Department upon request. C ontinuous Opacity Monitors are required in order to verify compliance with the emission limitations for the coal mill. Quarterly reports detailing any excursions (if applicable) or downtime shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. Semi

- annual Continuous Opacity Monitor reports shall be**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **85 of 106**  (permit updated 6/27/05 and 8/19/05) submitted to the Manager of the Technical Management Section, Bureau of Air Quality po stmarked no later than 30 calendar days after the end of the reporting period. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan”(9/96), as amended. The report shall include the following minimum information: A. All opacity

measurements for periods during which the above emission limitations for opacity

have been exceeded, together with their nature and cause. B. For periods of monitoring system malfunction: i. The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. ii. The nature of monitoring system repairs or adjustments. iii. Proof of COM system performance may b e required by

the Department whenever repairs or adjustments have been made. (d) Particulate matter emissions from the coal mill shall be monitored every 2.5 years. (e) The owner or operator of any thermal dryer shall install, calibrate, maintain, and continuously operate a monitoring device for the measurement of the temperature of the gas stream at the exit of the thermal dryer on a continuous basis. The monitoring device is to be certified by the manufacturer to be accurate within + 3 degrees F. The monitoring device is to be calibrated annually

. (f) VOC emissions shall be monitored every 2.5 years from the coal mill stack. (g) Continuous Emission Monitors for SO 2 , CO and NO x are required in order to verify compliance with the emission limitations for the kiln system. CEMs shall be installed on both the coal mill stack and on the main kiln stack. Quarterly reports detailing any excursions (if applicable) or downtime shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. These reports shall include the 30

- day rolling average (24 1

- hour measurements in tonnage of SO 2 , CO and NO x summed together and added to the previous 29 day

sum). The lb/ton clinker value shall be calculated using the daily production records for clinker. These records shall be maintained as required. Quarterly C ontinuous Emission Monitor reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan” (9/96), as amended. The report shall include the following minimum information: a. All measurements for periods during which the above emission limitations have been exceeded, together with their nature and cause.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **86 of 106**  (permit updated 6/27/05 and 8/19/05) b. For periods of monitoring system malfunction: i. The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. ii. The nature of monitoring system repairs or adjustments. iii. Proof of the monitoring system performance may b e required by the Department whenever repairs or adjustments have been made. (h) These sources are subject to all applicable provisions of 40 CFR 60 Subpart A (General Provisions) and Subpart Y (Coal Preparation Plants). (i) The coal mill stack (S95) is subject to applicable provisions of 40CFR63 Interim Subpart EEE (Hazardous Waste Combustors). **6.B.5 KILN SYSTEM** (a) The owner or operator must conduct a monthly 1

-minute visible emissions test of each affected source in accordance with Method 22 of Appendix A to 40 CFR 60. The test must be conducted while the affected source is in operation. If no visible emissions are observed in six consecutive monthly tests for any

affected source, the owner or operator may decrease the frequency

o f testing from monthly

to semi

- annually

f or that affected source. If visible emissions are observed during any s emi

- annual test, the owner or operator must resume testing of that affected source on a monthly b asis and maintain that schedule until no visible emissions are observed in six consecutive monthly tests. If no visible emissions are observed during the semi

- annual test for any affected source, the owner or operator may decrease the frequency o f testing from semi

- annually to annually

f or that affected source. If visible emissions are observed during any annual test, the owner or operator must resume testing of that affected source on a monthly b asis and maintain that schedule until no visible emissions are observed in six consecutive monthly tests. If visible emissions are observed during any Method 22 test, the owner or operator must conduct a 6

-minute test of opacity in accordance with Method 9 of appendix A to part 60 of this chapter. The Method 9 test must begin within one hour of any

observation of visible emissions. The owner or operator subject to opacity limitations for the other sources under this permit besides the in

- line kiln/raw mill shall monitor opacity in accordance with the operation and maintenance plan developed for those situations when the in

-line kiln/raw mill is in operation using non

-hazardous fuels. Lo gs shall be kept to record all visual inspections, including cause and corrective action taken for any

abnormal emissions and visual inspections from date of recording. The logs shall be maintained for a period of five (5) years and be made available to the Department upon request. The owner/operator shall submit semi

- annual reports to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **87 of 106**  (permit updated 6/27/05 and 8/19/05) days after the end of the reporting period. (b) The owner or operator shall install, calibrate maintain, and continuously operate a continuous opacity monitor (COM) located at the outlet of the PM control device to continuously monitor the opacity

(at both the main kiln stack and the coal mill stack). The COM shall be installed maintained, calibrated, and operated as required by 4 0 CFR 63 Subpart A and PS

- 1 of Appendix B of 40 CFR 60. To remain in compliance, the opacity must be maintained such that the 6

-minute average opacity f or any 6

-minute block period does not exceed 20 percent. If the average opacity f or any 6

-minute block period exceeds 20 p ercent, this shall constitute a violation of the standard for those situations when the in

- line kiln/raw mill is in operation using non-hazardous fuels. Quarterly reports detailing any

excursions (if applicable) or downtime shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. Semi

- annual Continuous Opacity Monitor reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan”(9/96), as amended. The report shall include the following minimum information:

a. All opacity

measurements for periods during which the above emission limitations for opacity

have been exceeded, together with their nature and cause. b. For periods of monitoring system malfunction: i. The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. ii. The nature of monitoring system repairs or adjustments. iii. Proof of COM system performance may b e required by

the Department whenever repairs or adjustments have been made. (c) The permittee must comply with the dioxin and furans emission standard by e stablishing and complying with the following operating parameter limits. The permittee must base the limits on operations during the comprehensive performance test, unless the limits are based on manufacturer specifications. (1) For hazardous waste burning incinerators and cement kilns, if the combustor is equipped with an electrostatic precipitator, baghouse (fabric filter), or other dry emis sions control device where particulate matter is suspended in contact with combustion gas, the permittee must establish a limit on the maximum temperature of the gas at the inlet to the device on an hourly rolling average. The permittee must establish the hourly

rolling average limit as the average of the test run averages.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **88 of 106**  (permit updated 6/27/05 and 8/19/05) (2) The permittee must measure the temperature of each combustion chamber at a location that best represents, as practicable, the bulk gas temperature in the combustion zone. The permittee must document the temperature measurement location in the test plan the permittee submits under 40CFR63.1207(e) and (f); the permittee must establish a minimum hourly rolling average limit as the average of the test run averages. (3) As an indicator of gas residence time in the control device, the permittee must establish and comply

with a limit on the maximum flue gas flowrate, the maximum production rate, or another parameter that the permittee documents in the site

- specific test plan as an appropriate surrogate for gas residence time, as the average of the maximum hourly

rolling averages for each run. The permittee must comply with this limit on an hourly

rolling average basis. (4) The permittee must establish limits on the maximum pumpable and total (pumpable and non-pumpable) waste feedrate for each location where waste is fed. The permittee must establish the limits as the average of the maximum hourly rolling averages for each run. The permittee must comply with the feedrate limit(s) on an hourly rolling average basis. (5) The permittee shall maintain these records on- site for a period of at least five (5) years. These records shall be made available to a Department representative upon request. Quarterly

reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality

postmarked no later than 30 calendar days after the end of the reporting period. (d) The permittee must install, calibrate, maintain, and operate a particulate matter CEMS to demonstrate and monitor compliance with the particulate matter standards under this subpart. However, compliance with the requirements in this section to install, calibrate, maintain and operate the PM CEMS is not required until such time that the Agency promulgates all performance specifications and operational requirements applicable to PM CEMS. (e) A thermocouple shall be installed, calibrated, maintained, and continuously operated to monitor the temperature of the exhaust kiln gases from the in

- line kiln/raw mill and alkali by pass at the inlet of the particulate matter control device. Quarterly reports detailing any excursions (if applicable) or downtime shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. Semi

- annual Continuous Monitor reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmar ked no later than 30 calendar days after the end of the reporting period. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan”(9/96), as amended. The report shall include the following minimum information:**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **89 of 106**  (permit updated 6/27/05 and 8/19/05)
a. All temperature measurements for periods during which the above temperature limitations have been exceeded, together with their nature and cause. b. For periods of monitoring system malfunction: i. The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. ii. The nature of monitoring system repairs or adjustments. iii. Proof of system performance may be required by

the Department whenever repairs or adjustments have been made. (f) All notif

ications required for those situations when the in

- line kiln/raw mill is in operation using non-hazardous fuels, shall be submitted as required including notification of performance tests, opacity and visible emission observations, continuous emission monitor performance evaluation and compliance status. All reports required for submission include, but are not limited to, the following: (1) The results of performance tests (including opacity test results) and results of the performance evaluation of the continuous monitoring system, (2) Startup, shutdown, or malfunction report if consistent with the startup, shutdown, or malfunction plan required by 40 CFR § 63.10(d)(5) (semi

- annual), if not consistent with above plan a report shall be made within 24

-hours by phone or fax. The immediate report shall be followed by a letter within seven (7) days, certified by the owner or operator or other responsible official explaining the circumstances of the event, the reasons for not following the startup, shutdown, and malfunction plan, and whether any

excess emission and/or parameter monitoring exceedances are believed to have occurred, (3) All failures to comply with any provisions of the operation and maintenance plan. (g) The kiln system is subject to all applicable provisions of 40 CFR 61, Subpart A (General Provisions) and Subpart FF (National Emission Standard for Benzene Waste Operations). (h) The owner or operator shall design, install, operate, and maintain a treatment process that destroys benzene from the waste stream by incinerating the waste in a combustion unit that achieves a destruction efficiency of 99% or greater for benzene. (40 CFR § 61.348(a)(1)) The treatment process consisting of an industrial furnace burning hazardous waste for energy recovery which has been issued a final permit under 40 CFR 270 and complies with 40 CFR 266 Subpart D is exempt from performance test requirements of 40 CFR 61 Subpart FF (40 CFR 61.348 (d)).**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **90 of 106**  (permit updated 6/27/05 and 8/19/05) (i) The kiln must be equipped with a monitoring device equipped with a continuous recorder to measure a parameter (such as temperature) that indicates good combustion operating practices are being used at the point of control or treatment. (j) For each occurrence mentioned below, reports shall be submitted to the Manager of the Technic al Management Section, Bureau of Air Quality as required in 40 CFR § 61.357(d). (1) Each occurrence when there is a change in the location at which the vent stream is introduced into the flame zone of an industrial furnace. (k) The emission limitations f or NO x and CO are based on several process assumptions such as raw material moisture content, carbon content, nitrogen content and sulfur content. The facility shall monitor raw material moisture content, carbon content, nitrogen content and sulfur content on a semi

- annual basis for the first two years of commercial operation and annually thereafter. The Department reserves the right to request material testing at any time that conditions warrant or to increase the frequency o f testing. The method of testing shall be approved by

the Department. Records of the material testing shall be maintained on site for a period of at least five (5) ye ars from the date generated and shall be made available to a Department representative upon request. S emi

- annual rep orts including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (l) Quarterly

C ontinuous Opacity

Monitor reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality, postmarked no later than 30 calendar days after the end of the reporting period. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan”(6/99), as amended. The report shall include the following minimum information: (1) All integrated six minute opacity measurements for periods during which the applicable emission limitations have been exceeded, together with their nature and cause. (2) For periods of monitoring system malfunction: (i) The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. (ii) The nature of monitoring system repairs or adjustments. (iii) Proof of opacity

monitoring system performance may b e required by

the Department whenever repairs or adjustments have been made.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **91 of 106**  (permit updated 6/27/05 and 8/19/05) (m) The waste feed rate shall be monitored continuously and recorded as required by S C Regulation 61

- 62.5 Standard No. 3, section VI(A)(2)(k). (n) The owner/operator shall submit to the Bureau prior to operation of the kiln system a plan detailing the specifics of the burner, process and kiln optimization that will be done on the source which is considered to be part of the BACT determination. This plan shall be submitted to the Director of Engineering Services, Bureau of Air Quality

. (o) Continuous Emission Monitors for SO 2 , CO, and NO x are required in order to verify compliance with the above emission limitations for the kiln system. CEMs shall be installed on both the coal mill stack and on the main kiln stack. Quarterly reports detailing any excursions (if applicable) or downtime shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality, postmarked no later than 30 calendar days after the end of the reporting period. These reports shall include the 30 day rolling average (24 1

- hour measurements in tonnage of SO 2 , CO, and NO x summed together and added to the previous 29 day

sum). The lb/ton clinker value shall be calculated using the daily production records for clinker. These records shall be maintained on- site for a period of at least five (5) years from the date generated. These records shall be made available to Department personnel upon request. Quarterly C ontinuous Emission Monitor reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality, postmarked no later than 30 calendar days after the end of the reporting peri od. Monitor operations shall be subject to South Carolina’s “Continuous Monitoring System Evaluation Plan”(9/96), as amended. The report shall include the following minimum information: (1) All measurements for periods during which the above emission limitations have been exceeded, together with their nature and cause. (2) For periods of monitoring system malfunction: (i) The date and time identifying each period during which the monitoring system was inoperative, except for zero and span checks. (ii) The nature of monitoring system repairs or adjustments. (iii) Proof of the monitoring system performance may b e required by

the Department whenever repairs or adjustments have been made. (p) Emission limitations and requirements applicable to the main kiln stack are also applicable to the coal mill stack when the stack gas from the kiln system is vented through the coal mill. (q) This source is limited to a maximum production rate of 2,462,318 short tons of clinker per year. The Permittee must record the actual monthly production rates and maintain these records on- site for a period of at least five (5) ye ars from the date generated. The facility shall also maintain daily

clinker production records for the calculation of the NO x , CO, and**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **92 of 106**  (permit updated 6/27/05 and 8/19/05) SO 2 emissions. These records shall be made available to Department personnel upon request. Semi

- annual reports including applicable recorded parameters and applicable calculated values including the annual clinker production rate shall be submitted to the Manager of the Technic al Management Section, Bureau of Air Quality, postmarked no later than 30 calendar days after the end of the reporting period. These conditions shall not supersede any

S tate or Federal requirements such as National Emission Standards for Hazardous Air Pollutants, unless these conditions would impose a more restrictive limit. (r) The owner or operator shall demonstrate initial compliance with the emission limits 180 days after initial start
-up of burning HWDF using the test methods and procedures listed in 40 CFR § 63.7. P erformance test results shall be documented in complete test report that contain the information required by 4 0 CFR § 63.7, as well as all other relevant information. The plan to be followed during testing shall be made available to the Bureau prior to testing as required by

SC Regulation 61

- 62.1 Section IV

- Source Testing. (s) The owner or operator of any in- line kiln/raw mill subject to a D/F emission limit shall conduct an inspection of the components of the combustion system of each in

- line kiln raw mill at least annually

. Records of the inspection and repairs made shall be maintained on site for a period of at least five (5) years from the date generated and shall be made available to a Department representative upon request. S emi

-Annual reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (t) The owner or operator using a treatment process and control device shall maintain the following records. The documentation shall be retained for the life of the control device. (1) Engineering design documentation; (2) A statement signed and dated by the owner or operator certifying that the system as both a treatment process and control device is designed to operate at the documented performance level when the waste management unit vented to the control device is or would be operating at the highest load or capacity expected to occur; (3) A design analysis including all requirements applicable in 40 CFR § 61.356(e and f)(2); and (4) If performance tests are used to determine performance all requirements in 40 CFR § 61.356(e), and 40 CFR § 61.356(f)(3). (u) A sourc e test for PM, Metals, POHC removal and reduction efficiency, CO, O 2 , and HCl emissions from the kiln system will be required. The tests shall be performed within 60 days after achieving maximum production but not later than 180 days after initial start
-u p of burning HWDF’s. The Bureau must be notified at least two weeks prior to any source test so**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **93 of 106**  (permit updated 6/27/05 and 8/19/05) that a Bureau representative may b e present. The testing shall be done at least every two and a half years. S ource test methodology must be approved by

the Bureau and comply

with SC Regulation 62.1, Section IV, Source Testing. (u) The particulate matter emission rate must be computed by t he equation specified in 40 CFR § 63.1204(a)(7)(ii). E=(C s x Q sd)/P. (v) The kiln system shall achieve a DRE of 99.99% for each principle organic hazardous constituent (POHC) designated. To calculate the DRE for each POHC use the equation in 40 CFR § 63.1204(c)(1). The POHC shall be designated as required by 4 0 CFR § 63.1204(c)(3). (w) The DRE standard must be documented only onc e provided that no modifications of the source are done which could affect the ability o f the source to achieve the DRE standard. The facility

shall prove compliance during the initial comprehensive performance test (40 CFR § 63.1206(b)(7)). (x) The emis sion standards and operating requirements set forth apply a t all times except: during periods of startup, shutdown, and malfunction; and when hazardous waste is not in the combustion chamber (i.e., the hazardous waste feed to the combustor has been cut off for a period of time not less than the hazardous waste residence time) and the permittee has documented in the operating record that the permittee is complying with all otherwise applicable requirements and standards promulgated under authority o f sections 112 (e.g., 40 CFR 63 subpart LLL) or 129 of the Clean Air Act in lieu of the emission standards of 40 CFR63.1203 through 63.1205; the monitoring and compliance standards of this section and 40 CFR63.1207 through 63.1209, except the modes of operation requirements of 40 CFR63.1209(q); and the notification, reporting, and recordkeeping requirements of 40 CFR63.1210 through 63.1212. (40 CFR § 63.1206(b)(1)(ii)).

(y ) The hazardous waste residence time must be calculated and included in the performance test plan and operating record with calculation. The hazardous waste residence time must also be provided in the Documentation of Compliance and the Notification of Compliance (40 CFR § 63.1206(b)(11)). (z) The facility

shall operate only

under the operating requirements specified in the Documentation of Compliance or the Notification of Compliance except during performance tests under an approved test plan required by the HWC MACT or if the facility has requested to be operated in compliance without burning haza rdous waste and has been granted approval (40 CFR § 63.1206(c)(1)). (aa) A startup, shutdown, and malfunction plan requirements of 40 CFR § 63.6(e)(3) shall be complied with including a projected oxygen correction factor based on normal operations to**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **94 of 106**  (permit updated 6/27/05 and 8/19/05) use during periods of startup and shutdown and the plan must be recorded in the operating record. Even if the startup and shutdown procedures and the corrective measures are followed upon a malfunction prescribed in the startup, shutdown, and malfunction plan, the emission standards and operating requirements of the HWC MACT and this permit apply i f hazardous waste is in the combustion chamber and the HWDF residency time has not expired (40 CFR § 63.1206(c)(2)). (bb) The hazardous waste combustor must operate with a f unctioning system that automatically cuts off the hazardous waste feed in compliance with 40 CFR § 6 3.1206(c)(3). The system and associated alarms must be tested at least weekly to verify operability

unless documented in the operation record that weekly inspection will unduly restrict or upset operation and that less frequent inspections will be adequate. At a minimum, the operability testing shall be conducted at least monthly

. The testing procedures and results shall be documented and recorded in the operating record. (cc) Combustion system leaks must be controlled by one of the following: (1) Keeping the combustion zone sealed to prevent combustion system leaks; or (2) Maintaining the maximum combustion zone pressure lower than ambient pressure using an instantaneous monitor; or (3) Upon prior written approval of the Administrator, an alternative means of control to provide control of combustion system leaks equivalent to maintenance of combustion zone pressure lower than ambient pressure. (4) The method used must be specified in the operating record (40 CFR § 63.1206(c)(5)). (dd) An operation and maintenance plan which describes in detail procedures for operation, inspection, maintenance, and corrective measures for all components of the combustor, including associated pollution control equipment, that could affect emissions of regulated air pollutants must be prepared and complied with at all times. The plan requirements are listed in 40 CFR § 63.1206(c)(7). The plan must be recorded in the operating record. (ee) The facility

shall install a CEM in the alkali by pass to demonstrate and monitor compliance with the hydrocarbon emission limitations. An oxygen CEM must also be used to continuously

correct hydrocarbon levels to 7% oxygen (40 CFR § 63.1209(a)(1 )(I)). (ff) The facility

shall install a COM to demonstrate and monitor compliance with the opacity limitations at each point (both the main kiln stack and the coal mill stack) where emissions are vented from these sources as required by 40 CFR § 63.1209(a)(1)(ii). Daily Method 9 opacity readings will be required when the COM is off line. (gg) Prior to feeding the material to the kiln, an analysis of each feedstream is required in order to**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **95 of 106**  (permit updated 6/27/05 and 8/19/05) document compliance with the feedrate limits as required by 4 0 CFR § 63.1209(c). A feedstream analysis plan shall be developed and implemented and recorded into the operating record. The plan must include all requirements listed in 40 CFR § 63.1209(c). This plan shall be submitted to the Bureau for approval. The feedrate limits will be included in the aforementioned plan. C ompliance with these limits shall be monitored by determining and recording the value of the parameter for each feedstream, the mass or volume flowrate of each feedstream by

a C ontinuous Monitoring System, and calculating and recording the mass feedrate of the parameter per unit time. (hh) The following are the operating parameters required to show compliance with the emission limitations. These operating parameters are determined in the comprehensive performance test and shall be kept in the operating record. Operating record means a documentation retained at the facility

f or ready inspection by

a uthorized officials of all information required by the standards to document and maintain compliance with the applicable regulations, including data and information, reports, notifications, and communications with regulatory officials. The permittee shall maintain these records on

- site for a period of at least five (5) years. These records shall be made available to a Department representative upon request. Quarterly reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. The facility shall be in compliance with all requirements in 40 CFR § 63.1209 with regards to each monitoring system. (1) DRE

- Minimum combustion chamber temperature (hourly rolling average limit), maximum flue gas flowrate or production rate (indicator of gas residence time

- hourly rolling average limit), maximum hazardous waste feedrate (maximum pumpable and total hazardous waste feedrate for each location fed

- hourly rolling average limit), operation of waste firing system (parameters and limits to ensure that good operation of each hazardous waste firing system is maintained). (2) D/F

- maximum gas temperature at the inlet to a dry p articulate matter control device (hourly rolling average limit), minimum combustion chamber temperature (hourly rolling average limit), maximum flue gas flowrate or production rate (gas residence time

- hourly

rolling average limit), maximum hazardous waste feedrate (maximum pumpable and total hazardous waste feedrate for each location fed

- hourly rolling average limit). (3) Mercury

- a hazardous waste feedrate corresponding to a maximum theoretical emission concentration (MTEC) of 120 g/dscm on a 12

-hour rolling average (40CFR63.1204(b)(2); 40CFR63.1206(b)(15)). (4) PM

- Reserved. (5) Semivolatile and Low volatile metals

- maximum gas temperature at the inlet to a dry**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **96 of 106**  (permit updated 6/27/05 and 8/19/05) particulate matter control device (hourly rolling average limit), feedrate of total mercury ( 12 hour rolling average) or other allowed parameter, minimum pressure drop and maximum pressure drop across each baghouse cell based on manufacturer’s specifications (hourly

rolling average), maximum total chlorine and chloride feedrate (12 hour rolling average limit), maximum flue gas flowrate or production rate (gas residence time

- hourly

rolling average limit). (6) HCl and Chlorine gas - maximum total chlorine and chloride feedrate (12 hour rolling average limit), maximum flue gas flowrate or production rate (gas residence time

- hourly

rolling average limit). (7) According to the alternative maintenance on the Differential Pressure Ports granted to the facility

(letter from BAQ dated May 2 5, 2005) the facility

must abide by

the following: 1. Visual monitoring must be must be performed around the area each time the port at the kiln inlet is taken off line and cleaned (this is relevant only f or when it is day

light hours). 2. The preventative cleaning can be preformed for no longer than 20 minutes in any 24

-hour period. 3. The IDF an must be kept operational for the entire cleaning period within ±10% of the speed (RPMs) it had prior to the port being taken off

- line for cleaning. 4. Records of each maintenance period must be maintained for a period of five (5) years and be made available to the Department upon request. The records must include, at a minimum, the following a. Time and duration of the maintenance event. b. Any

visual observations made (applicable only d uring daylight hours). c. IDFan speed (RPMs). If the facility

operates under different modes of operation, operating parameter limits of each mode must be determined. The change of mode of operation shall be documented in the operating record and the rolling averages must be calculated. (ii) All notification requirements of 40 CFR § 63.1210 shall b e complied with as applicable. (jj) All recordkeeping and reporting requirements of 40 CFR § 63.1211 shall be complied with as applicable. **6.B.6 FINISH MILL SYSTEM** (a) These sources are subject to all applicable provisions of 40 CFR 63 Subpart A (General Provisions) and LLL (Portland Cement Manufacturing).**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **97 of 106**  (permit updated 6/27/05 and 8/19/05) (b) Opacity

Requirements (1) The owner or operator shall demonstrate initial compliance and then every f ive years with the affected source opacity limit by conducting a test in accordance with Method 9. The performance test shall be conducted under the conditions that exist when the affected source is operating at the highest load or capacity level reasonably

expected to occur. The maximum six

-minute average opacity exhibited during the test period shall be used to determine whether the affected source is in initial compliance with the standard. The duration of the Method 9 performance test shall be 3 hours (30 6

- minute averages), except that the duration of the Method 9 performance test may b e reduced to 1 hour if the following apply : 1. There are no individual readings greater than 10 percent opacity. 2. There are no more than three readings of 10 percent for the first 1

-hour period. (2) The owner or operator must conduct a monthly 1

-minute visible emi ssions test of each affected source in accordance with Method 22 of Appendix A to 40 CFR 60. The test must be conducted while the affected source is in operation. If no visible emissions are observed in six consecutive monthly tests for any

affected sourc e, the owner or operator may

decrease the frequency

o f testing from monthly to semi

annually f or that affected source. If visible emissions are observed during any s emi

annual test, the owner or operator must resume testing of that affected source on a monthly basis and maintain that schedule until no visible emissions are observed in six consecutive monthly

tests. If no visible emissions are observed during the semi

annual test for any

affected source, the owner or operator may decrease the frequency of testing from semi

- annually to annually

f or that affected source. If visible emissions are observed during any

annual test, the owner or operator must resume testing of that affected source on a monthly basis and maintain that schedule until no visible emiss ions are observed in six consecutive monthly tests. If visible emissions are observed during any

Method 22 test, the owner or operator must conduct a 6

-minute test of opacity

in accordance with Method 9 of appendix A to 40 CFR 60. The Method 9 test must b egin within one hour of any observation of visible emissions.

(3) For baghouse sources S54, S96, and S97, a daily Method 22 must be conducted. If a visible emission is observed, then a follow up method 22 test must be conducted on that source which the visible emission was observed within 24

-hours. If a visible emission is still observed after the follow up Method 22 text, a 30

-minute Method 9 test must then be conducted for the stack which the visible emission was observed. **6.B.7 CEMENT LOADOUT** (a) Opacity

Requirements**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **98 of 106**  (permit updated 6/27/05 and 8/19/05) (1) The owner or operator shall demonstrate initial compliance and then every f ive years with the affected source opacity limit by conducting a test in accordance with Method 9. The performance test shall be conducted under the conditions that exist when the affected source is operating at the highest load or capacity level reasonably

expected to occur. The maximum six

-minute average opacity exhibited during the test period shall be used to determine whether the affected source is in initial compliance with the standard. The duration of the Method 9 performance test shall be 3 hours (30 6

- minute averages), except that the duration of the Method 9 performance test may b e reduced to 1 hour if the conditions listed below apply : 1. There are no individual readings greater than 10 percent opacity

. 2

. There are no more than three readings of 10 percent for the first 1

-hour period. (2) The owner or operator must conduct a monthly 1

-minute visible emissions test of each affected source in acc ordance with Method 22 of Appendix A to 40 CFR 60. The test must be conducted while the affected source is in operation. If no visible emissions are observed in six consecutive monthly tests for any

affected source, the owner or operator may

decrease the frequency

o f testing from monthly to semi

annually f or that affected source. If visible emissions are observed during any s emi

annual test, the owner or operator must resume testing of that affected source on a monthly basis and maintain that schedule until no visible emissions are observed in six consecutive monthly

tests. If no visible emissions are observed during the semi

annual test for any

affected source, the owner or operator may decrease the frequency of testing from semi

- annually to annually

f or that affected source. If visible emissions are observed during any

annual test, the owner or operator must resume testing of that affected source on a monthly basis and maintain that schedule until no visible emissions are observed in six consecutive monthly tests. If visible emissions are observed during any

Method 22 test, the owner or operator must conduct a 6

-minute test of opacity

in accordance with Method 9 of appendix A to 40 CFR 60. The Method 9 test must begin within one hour of any observation of visible emissions. When visible emissions are observed during a Method 22 test, a 6

-minute EPA Method 9 test shall follow the observation within one hour.

**6.B.8 TANKS** (a) The HWDF tanks and closed vent system (S111, S128), including control devices, are subject to all applicable provisions of 40 CFR Part 61 Subpart A (General Provisions), Subpart V (National Emission Standard for Equipment Leaks (Fugitive Emission Sources)), and Subpart FF (National Emission Standard for Benzene Waste Operations); and 40 CFR Part 63 Subpart A (General Provisions) and performance standards only f or Subpart DD (National Emission Standards for Hazardous Air Pollutants from Off

- Site Waste and Recovery Operations). The HWDF tank and closed vent system, including control device s,**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **99 of 106**  (permit updated 6/27/05 and 8/19/05)
are subject to all applicable provisions of 40 CFR Part 60 Subpart A (General Provisions) and Subpart Kb (Standards of Performance for VOL Storage Vessels). Since this facility

processes waste streams produced by f acilities with the total potential annual benzene quantity

o f greater than 10 Mg/y r, then this facility

i s fully subject to all applicable requirements of 40 CFR 61 Subpart A (General Provisions) and Subpart FF (National Emission Standard for Benzene Waste Operations). (b) General Reporting Requirements (1) Quarterly

reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality, as required in 40CFR61.357(d). These reports shall include: (i) Each occurrence when the carbon in a carbon adsorber system that is not regenerated directly

on site in the control device is not replaced at the predetermined interval (40CFR61.357(d)(7) (iv)(J)). (2) Semi Annual reports shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality as required in 40CFR61.357(d). These reports shall include: (i) Beginning one year after the date that the equipment necessary to comply with these standards has been certified in accordance with paragraph of 40 CFR 61.357(d)(1) of this section, the owner or operator shall submit annually to the Administrator a report that summarizes all inspections required by 4 0 CFR61.342 through 61.354 during which detectable emissions are measured or a problem (such as a broken seal, gap or other problem) that could result in benzene emissions is identified, including information about the repairs or corrective action taken (40CFR61.357(d)(8)). (c) The closed vent system, per 40CFR61.349 (a)(1)(i), shall be designed to operate with no detectable emission as indicated by an instrument reading of less than 500 ppmv above background as determined initially and thereafter at least once per ye ar by the methods specified in 40CFR61.355(h). The permittee shall maintain records of these tests on- site for a period of at least five (5) years. These records shall be made available to a Department representative upon request. S emi

- annual reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality

p ostmarked no later than 30 calendar days after the end of the reporting period. (d) Any

pumps operating in the HWDF handling system are subject to monthly monitoring to detect leaks per 40 CFR 61.242

-2(a). The dual mechanical seal system is visually inspected weekly to determine if dripping leaks are present per 242

-2(d).**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **100 of 106**  (permit updated 6/27/05 and 8/19/05) (e) Each closed

-vent system and control device shall be visually inspected initially

a nd quarterly thereafter. The visual inspection shall include inspection of ductwork and piping and connections to covers and control devices for evidence of visible defects such as holes in ductwork or piping and loose connections. If visible defects are observed during an inspection, or if other problems are identified, or if detectable emissions are measured, a first effort to repair the closed

-vent system and control device shall be made as soon as practical but no later than 5 calendar days after detection. Repair shall be completed no later than 15 calendar days after the emissions are detected or the visible defect is observed (40CFR61.349(f

- g)). (f) Requirements for tank controls and inspection. (1) Tanks T101

- T106, T111, and T146 shall be equipped and controlled as required by 40 CFR 61.343 in regards to the following: (i) Each tank shall be covered by a f ixed roof as defined in 40CFR61.343(a)(1) and vented directly

through a closed

-vent system to a control device in accordance with 40CFR61.349. (ii) The cover and all openings shall be designed to operate with no detectable

emission as indicated by

an instrument reading of less than 500 ppmv above background as determined initially and thereafter at least once per year by

the methods specified in 40CFR61.355(h). (2) Each fixed

-roof, seal, access door and all other openings shall be checked by visual inspection initially

and quarterly

thereafter to ensure that no cracks or gaps occur and that access doors and other openings are closed and gasketed properly (40CFR61.343(c)). (g) The following monitoring must be done for the control devices : (1) The kiln must be equipped with a monitoring device equipped with a continuous recorder to measure a parameter that indicates good combustion operating practices are being used. (2) The owner or operator may replace the carbon in the carbon adsorption system with fresh carbon at a regular predetermined time interval that is less than the carbon replacement interval that is determined by the maximum design flow rate and either the organic concentration or the benzene concentration in the gas stream vented to the carbon adsorption system (40CFR61.354(c)(7))). (h) Owners or operators using a closed

-vent system that contains any byp ass line that could**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **101 of 106**  (permit updated 6/27/05 and 8/19/05) divert a vent stream from a control device shall: (1) Visually

inspect the by

pass line valve at least once every month, checking the position of the valve and the condition of the car- seal or closure mechanism required under 40CFR61.349(a)(1)(ii) to ensure that the valve is maintained in the closed position and the vent stream is not diverted through the by pas s line. Records of these activities and any

action taken shall be made and maintained on- site for a period of at least five (5) years. These records shall be made available to a Department representative upon request. Quarterly reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality postmarked no later than 30 calendar days after the end of the reporting period. (2) Visually

inspect the readings from each flow monitoring device required by 40CFR61.349(a)(1)(ii) at least once each operating day to check that vapors are being routed to the control device as required. Records of these activities and any action taken shall be made and maintained on- site for a period of at least five (5) years. These records shall be made available to a Department representative upon request. Quarterly reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (i) An owner or operator shall maintain a record for each visual inspection required by 61.343 through 61.347 of this subpart that identifies a problem (such as a broken seal, gap or other problem) which could result in benzene emissions. The record shall include the date of the inspection, waste management unit and control equipment location where the problem is identified, a description of the prob lem, a description of the corrective action taken, and the date the corrective action was completed (40CFR61.356(g)). These records shall be maintained on- site for a period of at least five (5) ye ars. These records shall be made available to a Department representative upon request. Quarterly reports including all recorded parameters and calculated values shall be submitted to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (j) An owner or operator shall maintain a record for each test of no detectable emissions required by

61.343 through 61.347 and 61.349 of this subpart. The record shall include the following information: date the test is performed, background level measured during test, and maximum concentration indicated by t he instrument reading measured for each potential leak interface. If detectable emissions are measured at a leak interface, then the record shall also include the waste management unit, control equipment, and leak interface location where detectable emissions were measured, a description of the problem, a description of the corrective action taken, and the date the corrective action was completed.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **102 of 106**  (permit updated 6/27/05 and 8/19/05) (k) For each control device, the owner or operator shall maintain documentation that includes the following information regarding the control device operation (40 CFR 61.356(j)): (1) Dates of startup and shutdown of the closed

-vent system and control device; (2) A description of the operating parameter to be monitored to ensure that the control device will be operated in conformance with these standards and the control device’s design specification, and an explanation of the criteria used for selection of that parameter. This documentation shall be kept for the life of the control device. (3) Periods when the closed

-vent system and control device are not operated as designed including all periods and the duration when: Any valve car- seal or closure mechanism is broken or the by

-pass line valve position has changed, or the flow monitoring devices indicate that vapors are not routed to the control device as required. (4) For the kiln (as a control device), records of each occurrence when there is a change in the location at which the vent stream is introduced into the flame zone and continuous records of the parameter monitored in accordance with the requirements of 40 CFR 61.354(c)(5)). (5) If a carbon adsorber that is not regenerated directly on site in the control device is used, then the owner or operator shall maintain records of dates and times when the control device is monitored, when breakthrough is measured, and shall record the date and time then the existing carbon in the control device is replaced with fresh carbon. (l) The per

mittee shall perform a visual inspection on a semi

- annual basis. Visual Inspection means a qualitative observation of opacity d uring daylight hours where the inspector records results in a log, noting color, duration, density (heavy or light), cause and c orrective action taken for any

a bnormal emissions. The observer does not need to be certified to conduct valid visual inspections. However, at a minimum, the observer should be trained and knowledgeable about the effects on visibility of emissions caused by

background contrast, ambient lighting, observer position relative to lighting, wind, and the presence of uncombined water. Lo gs shall be kept to record all visual inspections, including cause and corrective action taken for any a bnormal emissions and visual inspections from date of recording. The logs shall be maintained for a period of five (5) ye ars and be made available to the Department upon request. The owner/operator shall submit semi

- annual reports to the Manager of the Technical Management Section, Bureau of Air Quality p ostmarked no later than 30 calendar days after the end of the reporting period. (m) The facility

is subject to the following operational requirements for the NHWDF tanks: (1) Records of NHWDF Storage Tank Dimensions and Capacity (40CFR60.116b(b))**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **103 of 106**  (permit updated 6/27/05 and 8/19/05) The facility

shall keep on

- site and on

- file for each NHWDF Storage Tank a record showing the dimension of each tank and an analysis showing the capacity of each tank. These records shall be kept on

- site and on

- file for the life of each tank and shall be made available to Department personnel upon request. **6.B.9 PERFORMANCE TESTING** (a) The owner or operator of the kiln system shall demonstrate initial compliance with the emission limits using the test methods and procedures listed in 40CFR63.7. P erformance test results shall be documented in complete test report that contain the information required by 40CFR63.7, 40CFR63, Subpart EEE, as well as all other relevant information. The plan to be followed during testing shall be made availab le to the Bureau 60 days prior to testing as required by

SC Regulation 61

- 62.1 Section IV

- Source Testing. The facility

shall submit a source test protocol in compliance with the appropriate federal regulations and also SC Regulations 61

- 62.1, Section IV

– Source Tests. All performance testing shall be in compliance with this regulation. The owner or operator shall demonstrate initial compliance and then every f ive years with the affected source opacity

limit by c onducting a test in accordance with Method 9. The performance test shall be conducted under the conditions that exist when the affected source is operating at the highest load or capacity level reasonably

expected to occur. The maximum six

-minute average opacity exhibited during the test perio d shall be used to determine whether the affected source is in initial compliance with the standard. The duration of the Method 9 performance test shall be 3 hours (30 6

-minute averages), except that the duration of the Method 9 performance test may b e reduced to 1 hour if the following apply : 1

. There are no individual readings greater than 10 percent opacity

. 2

. There are no more than three readings of 10 percent for the first 1

-hour period. (1) Comprehensive kiln particulate matter, opacity, DRE, Hg, semi

- and low volatile metals, HCl and Cl gas, and maximum combustion chamber pressure performance tests required above shall be repeated every f ive ye ars, except that the owner or operator of an in

- line kiln/raw mill is not required to repeat the initial performance test of opacity

f or the in

- line kiln/raw mill. C onfirmatory D/F performance tests shall be repeated every

30 months (40CFR63.1207(b)(2)(i), 40CFR63.1207(d)). (2) The owner or operator is required to repeat the performance tests for the in

- line kiln/raw mills within 90 days of initiating any significant change in the feed or fuel from that used in the previous performance test. (3) A source test for VOC emissions from the kiln system will be required. The tests shall be performed within 60 days after achieving maximum production but not later than 180 days after initial start
-up of burning HWDF. The Bureau must be notified at least two weeks prior to any s ource test so that a Bureau representative may b e**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **104 of 106**  (permit updated 6/27/05 and 8/19/05) present. This testing shall then hereafter be done with the comprehensive and confirmatory

testing required by

4 0CFR63, Subpart EEE. The testing shall be done at least every

3 0 months. S ource test methodology must be approved by

the Bureau and comply

with SC Regulation 62.1, Section IV, Source testing. (4) Since the coal mill uses a part of the kiln exhaust stream, emissions from the coal mill must also be included in the above performance testing. Performance test to demonstrate initial compliance shall be conducted as specified below and in compliance with all requirements of 40CFR63, Interim Subpart EEE: Performance testing must be conducted when the raw mill is on-line and when the mill is off

line to demonstrate compliance with the emission standards, and separate operating parameters shall be established as required by 4 0 CFR § 63.1209 for each mode of operation. Each time the mode of operation is changed to an alternative mode with different operating parameter limits the change must be documented. When the mode of operation changes, the permittee must establish rolling averages for the operating parameter limits based on one of the following methods: 1. Retrieval Approach, 2. Start Anew, or 3. Seamless Transition (40 CFR § 63.1204(d)(1); 40 CFR § 63.1209(q)(1)). Comprehensive p erformance testing must be done to demonstrate compliance with the emission limitations, establish limits for the operating parameters required by 4 0 CFR § 63.1209, and to demonstrate compliance with the performance specifications for continuous monitoring systems. This testing will be done in compliance with 40 CFR § 63.1207. The initial comprehensive performance test must commence within 180 days of startup of HWDF. The comprehensive performance test must commence no later than 61 months after the date of commencing the previous comprehensive performance test. Anotification of your intention to conduct a comprehensive performance test and CMS performance evaluation and a site

- specific test plan and CMS performance evaluation plan must be submitted at least one year before the performance test and performance evaluation are scheduled to begin. The required content of the comprehensive performance test plan is listed in 40 CFR § 63.1207(f)(1). (b) For sources subject to the Portland Cement MACT (40CFR63 Su bpart LLL), the owner or operator shall demonstrate initial compliance and then every f ive ye ars with the affected source opacity

limit by c onducting a test in accordance with Method 9. The performance test shall be conducted under the conditions that exi st when the affected source is operating at the highest load or capacity

level reasonably

expected to occur. The maximum six

-minute average opacity

exhibited during the test period shall be used to determine whether the affected source is in initial compliance with the standard. The duration of the Method 9 performance test shall be 3

-hours (30 6

-minute averages), except that the duration of the Method 9 performance test may b e reduced to 1

-hour if the following apply : 1. There are no individual readings greater than 10 percent opacity

. 2

. There are no more than three readings of 10 percent for the first 1

-hour period.**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **105 of 106**  (permit updated 6/27/05 and 8/19/05) (c) Within 60 days after achieving the maximum production rate at which the affected facility will be operated, but no later than 180 days after initial startup of burning HWDF a performance test shall be conducted for the coal mill system. The source test shall be conducted in compliance with both 40CFR60 and SC Regulation 62.1, Section IV

- Source Tests. (d) The facility

shall submit a site

- specific test plan in compliance with the appropriate federal regulations and also SC Regulations 61

- 62.1, Section IV

– Source Tests. All performance testing shall be in compliance with this regulation. A copy of the comprehensive test plan shall be submitted to the Source Evaluation Section. (part 7 updated 5/14/03) **PART 7.0 ADDITIONAL CONDITIONS**  **A. SPECIFIC CONDITIONS**  **Operator Training and Certification (EFFECTIVE**  **September 30,**  **2003, 40CFR63.1206(c)(6))**  Prior to start
-up of burning HWDF, the Permittee shall establish training programs for all categories of personnel whose activities may reasonably

be expected to directly

affect emissions of hazardous air pollutants from the source(s). Such persons include, but are not limited to, chief facility operators, control room operators, continuous monitoring system operators, persons that sample and analy ze feedstreams, persons that manage and charge feedstreams to the combustor (kiln), persons that operate emission control devices, and ash and waste handlers. Each training program shall be of a technical level commensurate with the person's job duties specified in the training manual. Each commensurate training program shall require an examination to be administered by the instructor at the end of the training course. P assing of this test shall be deemed the “certification” for personnel. The Permittee shall ensure that a source is operated and maintained at all times by p ersons who are trained and certified to perform these and any other duties that may affect emissions of hazardous air pollutants. Since the Permittee operates hazardous waste burning cement kilns, the training and certification program may

b e reviewed by

the Department and be complete, reliable and conform to principles of good operator and operating practices (including training and certification). The operator training and certification program shall be recorded in the facility operating record.

**B. OPERATIONAL FLEXIBILITY**  [SC Regulation 61

- 62.70.7(e)(5)] The permittee seeks operational flexibility to operate in one or more of the following scenarios:**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **106 of 106**  (permit updated 6/27/05 and 8/19/05)
a. The permittee has developed a startup, shutdown, and malfunction plan (SSMP) pursuant to 40 CFR 63, Subpart A. During periods of startup, shutdown, or malfunction, the permittee will follow the procedures set forth in the SSMP. No hazardous waste will be burned during periods of startup or shutdown. b. The primary

operating mode for control of VOC emissions from T

- 111 is treatment in the industrial furnace (K300A). During periods of startup, shutdown, or malfunction, VOC emissions from T

- 111 will be controlled by a carbon adsorption device (VRU112).

c. The primary

operating mode for the industrial furnace (K300A) is burning hazardous waste for energy

recovery pursuant to 40 CFR 63, Subp art EEE. During periods when the unit is not burning hazardous waste and the hazardous waste residence time has expired, limits imposed by

Subpart EEE (THC limit on emissions in the by pass (K300B), kiln differential pressure, 40 CFR63 Subpart EEE metal limits, and the minimum combustion chamber temperature) will no longer be applicable or required. d. The Permittee will develop a Transition Plan (Plan) and submit the Plan to the Department for review and comment prior to operation of the new kiln system. This Plan will address how the Holly

Hill Plant plans to operate the facility d uring the time period when the portions of the existing plant equipment, including the two wet kilns, are being shut down; and the new portions of the plant, including the new preheater/precalciner kiln system, new coal mill, and new Finish Mills 5 and 6 are being brought online. **C. COMPLIANCE SCHEDULE**  [SC Regulation 61

- 62.70.5(c)(8)] Not applicable at this time. **D. PERMIT SHIELD**  [SC Regulation 61

- 62.70.6(f)] (Revised 11/13/9 8) A copy o f the “applicability

determination” Holcim submitted with its Part 70 permit application is included as Attachment C. C ompliance with the terms and conditions of this permit shall be deemed compliance with any

a pplicable requirements as of the date of permit issuance. The permittee shall also be shielded from any non- applicable requirements as agreed upon by the Department as specified in Attachment C with the exception of the following. SC Regulation 61

- 62.5, Standard No. 7 Nothing in the p ermit shield or in any Part 70 permit shall alter or affect the provisions of Section 303 of the Act, Emergency Orders, of the Clean Air Act; the liability o f the permittee for any violation of applicable requirements prior to or at the time of permit issuance; the applicable requirements of the Acid Rain Program, consistent with Section 408(a) of the Clean Air Act; or the ability o f EPA to obtain information from a source pursuant to Section 114 of the Clean Air Act. In addition, the permit shield shall not apply to emission units in noncompliance at the time of permit issuance, minor permit modifications (SC Regulation 61

- 62.70.7(e)(2)), group processing of minor**Holcim (US) Inc.**

**– Holly Hill Plant**  **TV -**  **1860 -** **0005 Page**  **107 of 106**  (permit updated 6/27/05 and 8/19/05) permit modifications (SC Regulation 61

- 62.70.7(e)(3)), or operational flexibility ( SC Regulation 61

- 62.70.7(e)(5)), except as specified in SC Regulation 61

- 62.70.7(e)(5)(iii). (part 8 updated 5/14/03) **PART 8.0 EMISSION UNIT REQUIREMENTS** 

**– EXISTING FACILITY**  **A. EMISSION UNIT DESCRIPTION**  Table 8.1 is a description of emission units located at thi s facility

. **TABLE 8.1 EMISSION UNITS**  **Unit ID**  **Unit Description Control Device Description**  08 VOID

- Raw Material Processing

-- 09 VOID

- Kiln System VOID

- ESP (Kilns), Baghouses (CKD Tanks) 10 VOID

- Clinker Cooling and Handling,

Coal Handling, Cement Kiln Dust (CKD) Handling VOID

- Baghouses 11 VOID

- Marl Dryer VOID

- Baghouse 12 VOID

- Finish Mill System VOID

- Baghouses 13 VOID

- Lime Handling VOID

- Baghouse 14 VOID

- Off Spec Cement Handling and Storage VOID

- Baghouses 15 VOID

- Bagging Operations VOID

- Baghouses 16 VOID

- Scales VOID

- Baghouses 17 VOID

- Tanks, HWDF Delivery System VOID

- Carbon Adsorption System (HWDF tanks only)

### ATTACHMENT A Modeled Emission Rates **Holcim (US) Inc.**

**– Holly Hill Plant** 

TV

- 1860

- 0005 **PAGE 1**  **OF 6 NAAQS EMISSION RATES (New Plant)**  **STACK Modeled Em** **ission Rates (lbs/hr) TSP**  **PM 10**  **SO 2**  **NO X**  **CO** Kiln (S94 ) 59.9* 53.9* 854.1* 1141 4768 Coal Mill (S95) 2.7* 2.3* 61.9* 118 524 * These emissions were not modeled due to these emissions decreasing at the facility. **CLASS II PREVENTION OF SIGNIFICANT DETERIORATION -**  **STANDARD 7 (New Plant)**

**STACK Modeled Em** **iss ion Rates (lbs/hr)**  **PM 10**  **SO 2**  **NO X**  Kiln (S94) 53.9* 854.1* 1141 Coal Mill (S95) 2.3* 61.9* 118

**NAAQS EMISSION RATES, Existing Plant Source Identification**  **TSP (LBS/HR)**  **PM10**

**(LBS/HR) SO2** 

**(LBS/HR) NO2** 

**(LBS/HR) CO** 

**(LBS/HR) HF** 

**(LBS/HR)** (01) Dust Tank 0.012 7 0.107

- - - - (02) Dust Tank Load Spout 0.0114 0.0096

- - - - (03) Dust Tank 0.0127 0.0107

- - - - (04) Dust Tank Load Spout 0.0114 0.0096

- - - - (05) #1 Kiln Clinker Cooler 3.27 2.742

- - - - (06) #2 Kiln Clinker Cooler 10.20 8.571

- - - - (07) B ’Drag Chain

– West 0.00135 0.00019

- - - - (07R) Clinker Elevator #1 0.43 .43

- - - - (08) B’Drag Chain

– Middle 0.00135 0.00019

- - - - (08R) Clinker Elevator #2 0.43 0.43

- - - - (09) B’Drag Chane

– East 0.00135 0.00019

- - - - (09R) Clinker Elevator #3 0.43 0.43

- - - - (10) A’Drag Chain

– West 0.00135 0.00019

- - - - (10R) Clinker Elevator #4 0.43 0.43

- - - - (11) A’Drag Chain

– Middle 0.00135 0.00019

- - - - (11R) A Drag Conveyor 0.17 0.17

- - - - (12) A’Drag Chain

– East 0.00135 0.00019

- - - - (12R) B Drag Conveyor 0.17 0.17

- - - - (13) Cpmmpn Conveyor 0.00136 0.00114

- - - - (13R) Common Drag Conveyor 0.40 0.4

- - - - (14) Pan Conveyor

– North 0.00136 0.00114

- - - - (14R) Clinker Silo #1 0.17 0.17

- - - - (15) Pan Conveyor

– South 0.00136 0.00114

- - - - (15R) Pan Conveyor Discharge 0.29 0.29

- - - - (16) Dome Reclaim Feeder A* See B1 See B1

- - - - (17) Dome Reclaim Feeder B* See B1 See B1

- - - - (18) Dome Reclaim Feeder C* See B1 See B1

- - - - (19) Dome Reclaim Feeder D* Se e B1 See B1

- - - - (20) Dome Reclaim Feeder E* See B1 See B1

- - - - (21) Dome Reclaim Feeder F* See B1 See B1

- - - - (22) Clinker Reclaim Stamler 0.0180 0.01508

- - - - (24) Head, Dome Reclaim Belt* See B1 See B1

- - - - (33) Carbon Dust Tank 0.020 3 0.0170

- - - - (34) Carbon Feeder D. C. 0.000117 0.000098

- - - - (35) Coal Silo

- East 00.54 0.00452

- - - - (36) Coal Silo

- WEst 0.0054 0.00452

- - - -

### ATTACHMENT A Modeled Emission Rates **Holcim (US) Inc.**

**– Holly Hill Plant** 

TV

- 1860

- 0005 **PAGE 2**  **OF 6 NAAQS EMISSION RATES, Existing Plant**  **Source Identification TSP**  **(LBS/HR) PM10** 

**(LBS/HR) SO2** 

**(LBS/HR) NO2** 

**(LBS/HR) CO** 

**(LBS/HR) HF** 

**(LBS/HR)** (37) #1 FM Main D. C. N. 1.08 0.905

- - - - (38) #1 FM Main D. C. S. 1.08 0.905

- - - - (39) #1 FM Incline Belt 0.00048 0.00040

- - - - (40) #1 FM Clk Feeder #2 (East) 0.000225 0.00019

- - - - (41) #1 FM Clk Feeder #1 (West) 0.000225 0.00019

- - - - (42) #1 FM Gy

p Weigh Belt** See B41

– 44 See B41

– 44

- - - - (42A) #1 FM Gyp Apron Feeder** Se e B41

– 44 See B41

– 44

- - - - (43) #2 FM Main D. C. 1.68 1.4127

- - - - (44) #2 FM Clk Belt D. C. 0.000470 0.000395

- - - - (45) #2 FM Incline Belt D. C. 0.000470 0.000395

- - - - (46) #2 FM Gy

p Apron Feeder D. C.** See B41

– 44 See B41

– 44

- - - - (47) #2 FM Gy

p Weigh Belt D. C.** See B41

– 44 See B41

– 44

- - - - (48) #3 FM Main D. C. 3.36 2.82

- - - - (49) #3 FM Coll. Belt

- East 0.00047 0.000395

- - - - (50) #3 FM Coll. Belt

- Middle 0.00047 0.000395

- - - - (51) #3 FM Coll. Belt

- West 0.00 094 0.00079

- - - - (52) #3 FM Gy

p Weigh Feeder 0.00006 0.00005

- - - - (53) #3 FM Gy

p Apron Feeder** See B41

– 44 See B41

– 44

- - - - (54) #4 FM Main D. C. 1.98 1.667

- - - - (55) #4 FM Classifier 1.98 1.667

- - - - (56) #4 FM Fines Airslide D. C. 0.0264 0.0222

- - - - (57) #4 FM Coll. Belt D. C.** See B41

– 44 See B41

– 44

- - - - (58) #4 Gy

p Weigh Belt D. C.** See B41

– 44 See B41

– 44

- - - - (59) #4 FM Clk Weigh Belt D. C.** See B41

– 44 See B41

– 44

- - - - (60) D/Marl D. C. 3.33 2.80 62.86 11.01 1.0

- (61) Lime Tank D. C. 0.00675 0.00567

- - - - (62) Off Spec Silo D. C. 0.000162 0.000136

- - - - (63) #1 Load Scale D. C. 0.0557 0.0468

- - - - (64) #2 Load Scale D. C.*** See B51

– 54 See B51

– 54

- - - - (65) #3 Load Scale D. C.*** See B 51

– 54 See B51

– 54

- - - - (66) #4 Load Scale D. C. 0.0557 0.0468

- - - - (67) Cement Bagging 0.0160 0.0135

- - - - (68) Mortar Bagging 0.0160 0.0135

- - - - (69) #3 FM D. C. Top of Silos 0.0324 0.0272

- - - - (70) #4 FM D. C. Top of Silos 0.0297 0. 0249

- - - - (71) #1 FM D. C. Top of Silos 0.0162 0.0136

- - - - (72) #2 FM D. C. Top of Silos 0.0162 0.0136

- - - - (73) Dribble Bin D. C.

- North  0.000081 0.000068

- - - - (74) Dribble Bin D. C.

- South** ** See 74 See 74

- - - - (76) #2 Clinker Silo D. C.** See B41

– 44 See B41

– 44

- - - - (78) #4 Clinker Silo D. C.** See B41

– 44 See B41

– 44

- - - - (81) #1 Kiln ESP 40.00 34.00 478

- .48 431.83 218.74 0.055 (82) #2 Kiln ESP 54.6 46.43 1493.73 1348.02 422.65 0.172 (83) Reclaim Elevator, East/West Reclaim Belt, #4 Clinker Silo Conveyor, and #4 Clinker Silo 0.0460 0.0387

- - - - (84) East Reclaim Belt 0.0232 0.00194

- - - - (B1) Dome Reclaim Feeders (S16, S17, S18, S19, S20, S21, S24) 0.00578 0.00484

- - - - (B41) Sources grouped together (S42, S42A, S46, S47, S53, S57, S58, S59, S76, S78) 0.00213 0.00164

- - - - (B42) Sources grouped together (S42, S42A, S46, S47, S53, S57, S58, S59, S76, S78) 0.00213 0.00164

- - - - (B43) Sources grouped together (S42, S42A, S46, 0.00213 0.00164

- - - -

### ATTACHMENT A Modeled Emission Rates **Holcim (US) Inc.**

**– Holly Hill Plant** 

TV

- 1860

- 0005 **PAGE 3**  **OF 6 NAAQS EMISSION RATES, Existing Plant**  **Source Identification TSP**  **(LBS/HR) PM10** 

**(LBS/HR) SO2** 

**(LBS/HR) NO2** 

**(LBS/HR) CO** 

**(LBS/HR) HF** 

**(LBS/HR)** S47, S53, S57, S58, S59, S76, S78) (B44) Sources grouped together (S42, S42A, S46, S47, S53, S57, S58, S59, S76, S78) 0.00213 0.00164

- - - - (B51) Nos. 2 and 3 Load Scale D. C. (S64, S65) 0.01265 0.01063

- - - - (B52) Nos. 2 and 3 Load Scale D. C. (S64, S65) 0.01265 0.01063

- - - - (B53) Nos. 2 and 3 Load Scale D. C. (S64, S65) 0.01265 0.01063

- - - - (B54) Nos. 2 and 3 Load Scale D. C. (S64, S65) 0.01265 0.01063

- - - - (RAI) Rainbow Sources 0.72 0.600

- - - - (S85) Pneumatic Transfer System 0.58 0. 58

- - - - (S86) Top of Dome 1.03 1.03

- - - - (S87) Top of Dome 0.59 0.59

- - - - (S88) Reclaim Belt Discharge/Bucket Elevator 0.37 0.37

- - - - (S89) Top of 450 Metric Ton Surge Bin 0.17 0.17

- - - - (S90) Located Above Truck Loading Spout #1 0.15 0 .15

- - - - (S91) Located Above Truck Loading Spout #2 0.15 0.15

- - - - (U09) Transfer Point: 450' Belt to Hopper / Tripper Belt 2.83 1.40

- - - - (U10) Transfer Point: Radial Stacker to Pile 1.43 0.492

- - - - (U11) Transfer Point: Front End Loader to Reclaim Hopper 1.43 0.492

- - - - (U12) Transfer Points: Marl Hopper to Pan Feeder to Collector Belt to Incline Plane 0.342 0.175

- - - - (U13) Transfer Point: Sand Bin to Weigh Feeder to Collector Belt 0.3046 0.155

- - - - (U14) Transfer Points: Iron Ore Bin to Weigh Feeder to Collector Belt 0.00161 0.000817

- - - - (U15) Transfer Point: Collector Belt to Collector Belt 0.01611 0.00817

- - - - (U16) Transfer Point: Collector Belt to Incline Belt 0.07934 0.04087

- - - - (U18) Transfer Point: Feeder to Inclined Belt 0.00095 0.00084

- - - - (U19) Transfer Point: Dry Marl Tank to Weigh Feeder 0.00095 0.00084

- - - - (U20) Transfer Point: Dribble Bin to Inclined Belt 0.00095 0.00084

- - - - (U22) Transfer Point: Lime Tank to Weigh Feeder 0.00095 0.000 84

- - - - (U24) Transfer Point: Drag Chain to Dust Chute 0.500 0.425

- - - - (U25) Transfer Point: Drag Conveyor to Dust Chute 0.500 0.425

- - - - * These stacks are grouped in 1 stack named B1 ** These stacks are grouped and divided equally among four stacks labeled as volume sources B41, B42, B43, B44 *** These stacks are grouped and divided equally among four stacks labeled as point sources B51, B52, B53, B54   These stacks are grouped in 1 stack labeled as point source 73

### ATTACHMENT B Insignificant Activities ** Holcim (US) Inc.**

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- 0005 **PAGE 1**  **OF 5** (Attachment B updated 5 /14/03) The following table contains a list of activities which are considered insignificant pursuant to South Carolina Regulation 61

- 62.70.5(c). S ources listed below are not exempt from any otherwise applicable state or federal requirements including, but not limited to, opacity standards, ambient air quality standards, and air toxic standards.

**TABLE 1. INSIGNIFICANT QUARRY EQUIPMENT Equipment**  **Description Unit ID**  **Design Capacity**  **(tpy) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignif icant**  Clay Overburden Bulldozing NP1 1,931,230 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Front End Loader (FEL) to Clay Truck NP2 1,931,230 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Clay Truck to Clay Hopper NP3 1,931,230 2003 PM10 Emi ssions < 5 tpy PM10 Emissions < 5 tpy

**TABLE 2. INSIGNIFICANT RAW MILL SYSTEM EQUIPMENT Equipment Description**  **Unit ID**  **Design Capacity**  **(tpy) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** FEL to Iron Ore Hopper NP33 202,777 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy FEL to Wet Fly Ash Hopper NP34 a 1,158,730 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy FEL to Wet Fly Ash Hopper NP34b 1,158,730 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Iron Ore Pile NP30 51,416 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Fly Ash Pile #1 NP31 170,871 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Marl Stockpile P3 40,785 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Clay Stockpile P5 11,905 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Fly Ash Stockpile P6, P7 7,716 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Iron Ore Stockpile P8, P9 3,473 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy FEL to Clay Crusher NP132 3,473 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy FEL to Iron Ore Hopper NP133 23,150 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy **TABLE 3. INSIGNIFICANT COAL MILL SYSTEM EQUIPMENT Equipment**  **Description Unit ID**  **Design Capacity**  **(tpy) Equipment** 

**M anufacture**  **Date De Minim** **is**

**Emission Rate Reason(s)**  **Insignificant** Coal/SVF Pile#1 P2 27,558 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy FEL to Coal Hopper NP60 402,347 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Coal/SVF Pile#2 P12 27,558 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy **TABLE 4. INSIGNIFICANT KILN SYSTEM EQUIPMENT Equipment**  **Description Unit ID**  **Design Capacity**  **(tpy) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** Truck to Tire Chip Pile NP53 32 ,836 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy

### ATTACHMENT B Insignificant Activities **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 2**  **OF 5 TABLE 4. INSIGNIFICANT KILN SYSTEM EQUIPMENT**  **Equipment Description**  **Unit ID Design**  **Capacity (tpy)**  **Equipment**

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** Front End Loader to Tire Hopper NP54 29,959 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Tire Chip Stockpile P10 276 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Tire Hopper, Conveyor, T ire Elevator NP55,

NP56, NP92 29,959 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy
**TABLE 5. INSIGNIFICANT FINISH MILL SYSTEM EQUIPMENT Equipment Description**  **Unit ID**  **Design Capacity**  **(tph) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(** **s) Insignificant**  Truck to Syn. Gypsum/Pigment/ Slag Hopper NP71a

NP71b NP71c 965,615

965,615 965,615 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Sugar Truck to Silo NP73 9,636 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Wet Slag P ile NP76 93,588 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Syn. Gypsum Pile NP77 93,588 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Front End Loader to Slag/Syn. Gypsum Hopper NP78a NP78b 276,133

276,133 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Synthetic Gypsum Stockpile P1, P14 4,960 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Slag Stockpile P4, P15 4,740 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Calcium Fluoride

Pile NP130 5,986,772 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Truck to Mill Scale Pile NP131 23,150 2003 PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Natural Gypsum Stockpile P13 16,535 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Clay Overburden Pile P16 110,230 N/A P M10 Emissions < 5 tpy PM10 Emissions < 5 tpy Calcium Fluoride Stockpile P17 5,512 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Mill Scale Stockpile P18 27,558 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy Pigment Stockpile P11 1,323 N/A PM10 Emissions < 5 tpy PM10 Emissions < 5 tpy **TABLE 6. INSIGNIFICANT TANK EQUIPMENT 1**  **Equipment Description Unit**  **ID Design**  **Capacity (gal)**  **Equipment**

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** Diesel Fuel Storage Tank S112 500 Before 198 5 Tank size < 10,000 gal Tank is insignificant based on size. Quarry Gasoline Tank S139 2,000 Before 1985 Tank size < 10,000 gal Tank is insignificant based on tank size. FM#5 & #6 Grinding Aid Tank S140 9,988 2003 Tank size < 10,000 gal Tank is insignif icant based on tank size.

### ATTACHMENT B Insignificant Activities **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 3**  **OF 5 TABLE 6. INSIGNIFICANT TANK EQUIPMENT**  **1 Equipment Description**  **Unit ID**  **Design Capacity**  **(gal) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** FM #4 Grinding Aid Tank S141 9,789 Before 1978 VOC Emissions < 5 tpy and HAP emissions < 1,000 lb/yr VOC emissions < 5 tpy and

individual HAP emissions < 1,000 lb/yr FM #4 Air Entraining Tank S142 9,988 Before 1978 VOC Emissions < 5 tpy and HAP emissions < 1,000 lb/yr VOC emissions < 5 tpy and

individual HAP emissions < 1,000 lb/yr FM #4 Tall Oil Storage Tank S148 9,988 Before 1978 VOC Emissions < 5 tpy and HAP emissions < 1,000 lb/yr VOC emissions < 5 tpy and

individual HAP emi ssions < 1,000 lb/yr Hydraulic Oil Storage Tank S150 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size Motor Oil Storage Tank S151 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size Gear Oil Storage Tank S152 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size. Used Oil Storage Tank S153 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size. Heating Oil Storage Tank S154 500 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size. Transmission Oil Storage Tank S155 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size Heating Oil Storage Tank S156 1,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size Used Oil Storage Tank S157 500 Before 1980 Tank Size < 10,000 gal Tank is insignificant based on tank size Heating Oil Storage Tank S158 500 Before 1980 Tank Size < 10,000 gal Tank is insignificant based on tank size Motor Oil Storage Tank S159 500 Before 19 80 Tank Size < 10,000 gal Tank is insignificant based on tank size Used Oil Storage Tank S160 500 Before 1980 Tank Size < 10,000 gal Tank is insignificant based on tank size Hydraulic Oil Storage Tank S161 500 Before 1980 Tank Size < 10,000 gal Tank is insignificant based on tank size Diesel Fuel Storage Tank S162 200 1965 Tank Size < 10,000 gal Tank is insignificant based on tank size Diesel Fuel Storage Tank S163 200 1974 Tank Size < 10,000 gal Tank is insignificant based on tank size Drum Storage

- Various Oils S166 <10,000 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size Drum Storage

- Various Oils S167 <10,000 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size

### ATTACHMENT B Insignificant Activities **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 4**  **OF 5 TABLE 6. INSIGNIFICANT TANK EQUIPMENT**  **1 Equipment Description**  **Unit ID**  **Design Capacity**  **(gal) Equipment** 

**Manufacture Date**  **De Minim is** 

**Emission Rate Reason(s)**  **Insignificant** Drum Storage

- Various Oils S168 <1 0,000 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size Container and Drum Storage

- Various Oils S169 <10,000 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size Mobile Oil Storage Tank

- Used Oil S170 2 50 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size Mobile Oil Storage Tank

- Diesel Fuel S171 250 Before 1989 Tank Size < 10,000 gal Tank is insignificant based on tank size Mobile Oil Storage Tank

- Used Oil S172 250 Before 1 989 Tank Size < 10,000 gal Tank is insignificant based on tank size Sulfuric Acid Storage Tank S173 6,000 1998 Tank Size < 10,000 gal Tank is insignificant based on tank size HWDF Drum Handling and Storage N/A 11,000 2001 VOC Emissions < 5 tpy VOC emissions < 5 tpy

### ATTACHMENT C Regulatory applicability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 1**  **OF 7** (Attachment C updated 5/14/03) The following contains the Federal and South Carolina air pollution regulations, which were specified in the Part 70, permit application and determined as applicable and non- applicable by the Department as of the date of this permit issuance. This attachment may b e revised by

the Department in the event of a change in the nature or emission of pollutants at the source or promulgation of new or revised regulations.
**TABLE 1. STATE REGULATIONS South Carolina**  **Air Quality Rule Applicable**  **Not Applicable**  **Reason** 62.1 Section I

- Definitions X Definitions for terms used in permitting source 62.1 Section II

- Permit Requirements X Cement manufacturing equipment is a source of air contaminants 62.1 Section III

- Emissions Inventory X Facility required to submit annual emissions inventory 62.1 Section IV

- Source Tests X Is required to be tested 62.2 Prohibition of Open Burning X Open burning prohibited at the plant 62.3 Air Pollution Episodes X Facility is a major source that can contribute to pollution 62.4 Hazardous Air Pollutant Conditions X Cement manufacturing equipment is a source of HAP’s and fugitive dust 62.5 Standard 1 Fuel Burning Operations X No sources of indirect heating at the facility 62 .5 Standard 2 Ambient Air Quality Standards X Cement manufacturing equipment emits criteria pollutants 62.5 Standard 3 Waste Combustion and Reduction X Hazardous and Non

-Hazardous wastes are used as kiln fuels 62.5 Standard 3.1 Medical Waste Incineration X No medical waste is incinerated at this facility 62.5 Standard 4 Emissions from Process Industries X Kilns are specified as subject to this regulation 62.5 Standard 5 Volatile Organic Compounds X Burn tanks T111 and T146 are subject to this rule 62.5 Standard 5.1 VOC LAER X Net VOC emissions from kiln system > 100 tpy 62.5 Standard 6 Alternative Emission Limitation Options X This facility has not requested any alternative emission limitations, therefore this is not applicable. 62.5 Standard 7 Prevention of Significant Deterioration X The change from actual emissions to future potential emissions for some criteria pollutants is greater than the

PSD threshold. 62.5 Standard 8 Toxic Air Pollutants X All affected sources are covered by a MACT regulation

### ATTACHMENT C Regulatory app licability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 2**  **OF 7 TABLE 1. STATE REGULATIONS**  **South Carolina Air Quality Rule**  **Applicable Not**  **Applicable Reason**  62.6 Section I Control of Fugitive Particulate Matter In Non

-Attainment Area X Plant is located in an attainment area 62.6 Section II Control of Fugitive Particulate Matter

In Problem Areas X Plant is not located in a problem area 62.6 Section III Control of Fugitive Particulate Matter

Statewide X Cement manufacturing equipment is a source of fugitive dust 62.7 Good Engineering Practice Stack

Height X Kilns emit through stacks 62.63 Subparts A, DD, LLL, EEE National

Emission Standards For Hazardous Air Pollutants X Plant is a major HAP source 62.68 Chemical Accident Prevention

Provisions X Liquid hazardous waste fuels are not stored on

- site 62.70 Title V Operating Permit Program X Facility emissions are greater than thresholds 62.72 Acid Rain Program X A cement plant is not a source type listed in “Section III Applicability” 62.630 Subparts A, Kb, Y and OOO X State Regulation

**TABLE 2. FEDERAL REGULATIONS Federal Rule**  **Applicable Not**  **Applicable Reason**  40CFR50 National Ambient Air Quality Standards X Facility is a major source that contributes to air pollution 40CFR51 X Applies only to states 40CFR52 X Does not apply to facilities 40CFR53 X Specifies reference methods and is not an applicable requirement 40CFR54 X Applies only to citizens’ suits 40CFR55 X Specifies a requirement not applicable to Holcim’s operations 40CFR56 X Specifies a requirement not applicable to Holcim’s operations 40CFR57 X Specifies a requirement not applicable to Holcim’s operations 40CFR58 X Specifies a requirement not applicable to Holcim’s operations

### ATTACHMENT C Regulatory app licability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 3**  **OF 7 TABLE 2. FEDERAL REGULATIONS**  **Federal Rule Applicable**  **Not Applicable**  **Reason** 40CFR60 Subpart A NSPS General Provisions X Plant is applicable to 40CFR60 Subpart Kb, Subpart Y, and Subpart OOO 40CFR60 Subpart B through Subpart Eb X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR60 Subpart F NSPS for Portland Cement Plants X Plant complies with PC MACT regulations and is not subject 40CFR60 Subpart G through Subpart J X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR60 Subpart K NSPS for Storage Vessels for Petroleum

Liquids X Storage tanks do not exceed threshold capacity 40CFR60 Subpart Ka NSPS for Storage Vessels for Petroleum

Liquids X Storage tanks do not exceed threshold capacity 40CFR60 Subpart Kb NSPS for Volatile Organic Liquid Storage Vessels X Various storage tanks exceed threshold capacity 40CFR60 Subpart L through Subpart X X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR60 Subpart Y X Kiln exhaust is vented through coal mill to “thermally dry” the coal 40CFR60 Subpart Z through Subpart

NNN X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR60 Subpart OOO X The modified facility has its own quarry operations 40CFR60 Subpart PPP through WWW X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR61 Subpart A General Provisions X This facility is subject to 40CFR61 Subpart V and FF 40CFR61 Subpart B through Subpart U X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR61 Subpart V X Hazardous waste fuel delivery system is a source o f fugitive VOC emissions. 40CFR61 Subpart W through Subpart EE X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR61 Subpart FF NESHAP for Benzene Waste Operations X Facility receives benzene containing wastes from off

- site

### ATTACHMENT C Regulatory app licability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 4**  **OF 7 TABLE 2. FEDERAL REGULATIONS**  **Federal Rule Applicable**  **Not Applicable**  **Reason** 40CFR62 X Specifies a requirement not applicable to Holcim’s operations 40CFR63 Subpart A General Provisions X Specifies a requirement not applicable to Holcim’s operations 40CFR63 Subpart B Requirements for Control Technology D eterminations

for Major Sources In Accordance With Clean Air Act Sections 112(g) and 112(j) X Facility was constructed before effective date of section 112(g)(2)(B)

40CFR63 Subpart C through Subpart Y X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR63 Subpart AA through CC X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR63 Subpart DD National Emission Standards

for Hazardous Air Pollutants From Off

- Site Waste And Recovery Operations X The facility is subject to the performance standards of 40 CFR 63 Subpart DD because the facility receives off

- site waste and meets the applicability requirements of this regulation; however, the facility is not su bject to the monitoring, reporting, and record keeping requirements of 40 CFR 63 Subpart DD because the facility operates in compliance with 40 CFR 61 Subpart FF 40CFR63 Subpart EE through Subpart

YY X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR63 Subpart CCC and Subpart

DDD X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR63 Interim Subpart EEE National Emission Standards

For Hazardous Air Pollutants From Hazardous Waste Combustors X The facility uses hazardous waste derived fuel. The kiln is the only affected sources 40CFR63 Subpart FFF through Subpart

JJJ X This facility is not a source type or does not have any equipment subject to these

regulations 40CFR63 Subpart LLL X S94 and S95 are not subject to this MACT standard, since they are subject to 40CFR63 Interim Subpart EEE

### ATTACHMENT C Regulatory app licability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 5**  **OF 7 TABLE 2. FEDERAL REGULATIONS**  **Federal Rule Applicable**  **Not Applicable**  **Reason** 40CFR63 Subpart MMM through

Subpart XXX X This facility is not a source type or does not have any equipment subj ect to these

regulations 40CFR64 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR65 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR66 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR67 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR68 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR69 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR70 X Requirement for CAA Title V air permit for the Holcim (US) Inc. operations 40CFR71 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR72 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR73 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR74 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR75 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR76 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR77 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR78 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR79 X Spe cifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions 40CFR80 X Specifies a requirement not applicable since Holcim (US) Inc. operations are not subject to acid rain prohibitions

### ATTACHMENT C Regulatory app licability **Holcim (US) Inc.**

**– Holly Hill Plant** 

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- 0005 **PAGE 6**  **OF 7 TABLE 2. FEDERAL REGULATIONS**  **Federal Rule Applicable**  **Not Applicable**  **Reason** 40CFR81 X Speci fies a requirement not applicable to the Holcim (US) Inc. operations 40CFR82 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR85 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR86 X Spe cifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR87 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR88 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR89 X Specifies a requirement not applicable to the Holcim (US) Inc. operations 40CFR93 X Specifies a requirement not applicable to the Holcim (US) Inc. operations**VIA CERTIFIED MAIL**

April 15, 2003 Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Glenn Ray nor Dear Mr. Ray

nor: Enclosed with this letter is your Part 70 Air Quality (Title V Operating) Permit No. TV

- 1860

- 0005 that will become effective on July 1 , 2003. P lease note the c onditions and limitations imposed. This permit will be valid through June 30, 2008, unless otherwise provided for by S C Regulation 61

- 62.70.7(c)(1)(ii). Please review this permit carefully. Should you notice any errors or omissions, notify your permit engineer, Veronica Barringer, of this office, at (803) 898

-4127 or e -mail at barrinv@dhec.sc.gov within 15 days of receipt of this letter. Sincerely,
Carl W. Richardson, P.E., Director Engineering Services Division Bureau of Air Quality CWR:EAVB:pe Enclosure

cc: Mark Hiott, Trident EQC District Office Scott Miller, EPA Region IV (via e

-mail) TV

- 1860

- 0005May

14, 2003 Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Mr. Glenn Ray nor Dear Mr. Ray

nor: Enclosed with this letter is your updated Part 70 Air Quality (Title V Operating) Permit No. TV

1860

- 0005. P lease replace page 2, Sections 5 through 10, (pages 16 through 138) and Attachments B and C of your permit issued April 15, 2003 with these new updated pages. S ee page 2 for details of changes made in your permit. This permit will have the same expiration as the previous permit. If there are questions please do not hesitate to contact me at either (803) 898

-4074 or clar kkj@dhec.sc.gov. Sincerely,
Kevin J. Clark, P.E. Engineering Services Division Bureau of Air Quality KJC:pe Enclosure

cc: Mark Hiott, Trident EQC District Office Scott Miller, EPA Region IV (via e

-mail) TV

- 1860

- 0005September 23, 2003

Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Mr. Glenn Ray nor Dear Mr. Ray

nor: Enclosed please find Pages 2, 18, and 24 of Title V Operating Permit No. 1860

- 0005 which will replace Pages 2, 18, and 24 of the Title V operating permit previously i ssued April 15, 2003. These pages reflects changes made to Table 5.6 for the control device description change (BH85) and to Table 5.14 for the venting of vapors from the hazardous waste storage tanks (T111 and T146) to the kiln. Please do not hesitate to contact the appropriate staff member, Veronica Barringer at (803

- 898

-4127) or e -mail at barrinv@dhec.sc.gov promptly if you need any

further assistance. Sincerely,
Carl W. Richardson, P.E., D irector Engineering Services Division Bureau of Air Quality CWR:EAVB:pe Enclosure

cc: Mark Hiott, Trident District EQC Office Scott Miller, EPA Region IV (via e

-mail) Permit File: 1860

- 0005 Main File: 1900

- 0005October 22, 2003

Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Mr. Glenn Ray nor Dear Mr. Ray

nor: Enclosed please find Pages 2, 19, 20, 21, 22, 23, 24 and 24 of Title V Operating Permit No. 1860

- 0005 which will replace Pages 2, 19, 20, 21, 22, 23, 23 and 25 of the Title V operating permit previously

issued April 15, 2003. These pages reflects the following changes: 1. R170, R171, R174, R175, R178, R180, R195, R204 has been moved from Table 5.16 and Table 5.9 into Table 5.15 and Table 5.8, to reflect applicability to NSPS, Subpart OOO and not MACT, Subpart LLL. 2. R183 and R185 has been moved from Table 5.15 and Table 5.9 into Table 5.16 and Table 5.8, to reflect applicability to MACT, subpart LLL and not NSPS, Subpart OOO. Ple ase do not hesitate to contact the appropriate staff member, Veronica Barringer at (803

- 898

-4127) or e -mail at barrinv@dhec.sc.gov promptly if you need any

further assistance. Sincerely,
Carl W. Richardson, P.E., Director Engineering Services Division Bureau of Air Quality CWR:EAVB:pe Enclosure

cc: Mark Hiott, Trident District EQC Office Scott Miller, EPA Region IV (via e

-mail) Permit File: 1860

- 0005 Main File: 1900

- 0005June 27, 2005

Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Mr. Glenn Ray nor Dear Mr. Ray

nor: Enclosed please find an updated Part 70 Air Quality (Title V Operating) Permit No. 1860

- 0005, which will replace the Part 70 Air Quality (Title V Operating) Permit previously i ssued October 23, 2003. This updated permit includes previously i ssued construction permits 1860

- 0005

- CZ, DA, DB and DC, the addition of maintenance activities to be perform on the inlet pressure port without shutting off the HWDF , the voiding out of all references to the old facility, and the update of condition 4.B.6. Attachments A, B and C remain the same and will not be re

- issued. Please examine this updated permit carefully f or errors or omissions and notify the appropriate staff member, Veronica Barringer, (803

- 898

-4127) or e -mail at barrinv@dhec.sc.gov promptly if any a re discovered. Sincerely,
Carl W. Richardson, P.E., Director Engineering Services Division Bureau of Air Quality CWR:EAVB:pe Enclosure

cc: Mark Hiott, Trident District EQC Office Scott Miller, EPA Region IV (via e

-mail) Permit File: 1860

- 0005 Main File: 1860

- 0005August 19, 2005

Holcim (US) Inc.

– Holly Hill Plant 200 Safety

Street / Highway

453 Holly Hill, South Carolina 29059 **ATTENTION:** Mr. Glenn Ray nor Dear Mr. Ray

nor: Enclosed please find an updated Part 70 Air Quality (Title V Operating) Permit No. 1860

- 0005, which will replace the Part 70 Air Quality (Title V Operating) Permit previously i ssued June 27, 2005. This updated permit includes the removal of non- applicable 40 CFR 63, Subpart DD requirements to the NHWDF storage tanks (ID T

- 100, T

- 147, T

- 148 and T

- 149). Attachments A, B and C remain the same and will not be re

- issued. Please examine this updated permit carefully f or errors or omissions and notify the appropriate staff member, Veronica Barringer, (803

- 898

-4127) or e -mail at barrinv@dhec.sc.gov promptly if any a re discovered. Sincerely,
Carl W. Richardson, P.E., Director Engineering Services Division Bureau of Air Quality CWR:EAVB:pe Enclosure

cc: Mark Hiott, Region 7, Charleston EQC Office Scott Miller, EPA Region IV (via e

-mail) Permit File: 1860

- 0005 Main File: 1860

- 0005