Document ID: EPA-HQ-OAR-2011-0817-0108
Agency: epa
Document Type: Supporting & Related Material
Title: 
Posted Date: 2012-07-18T04:00Z

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)

In accordance 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 authorizes 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 accompanying 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



RECORD OF REVISIONS

Revision

Number	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.

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
silos 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 revisions to Permit File, Main File, District EQC
Office, US EPA, and Facility Contact.



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	APPLICABILITY

Part 3.0	GENERAL CONDITIONS

A.	Permit Issuance

B.	Permit Expiration and Renewal

C.	Severability

D.	Fee Assessment and Payment

E.	Submittal of Information

F.	Public Participation

G.	Permit Reopening

H.	Temporary Sources

I.	Emergency Provisions

J.	Property 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



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 Federal and State
Regulations



PART 1.0  GENERAL INFORMATION

A.	APPLICABLE PERMIT DATES

ISSUE DATE					: April 15, 2003

EFFECTIVE DATE				: July 1, 2003

EXPIRATION DATE				: June 30, 2008

RENEWAL APPLICATION DUE		: December 31, 2007

B.	FACILITY INFORMATION

ENVIRONMENTAL CONTACT		: Glenn Raynor

CONTACT TELEPHONE NUMBER	: (803) 496-2756

INTERNET E-MAIL ADDRESS		: glenn.raynor@holcim.com

FACILITY LOCATION			: 200 Safety Street / Highway 453

COUNTY					: Orangeburg

SIC CODE(S)					: 3241

AFS CODE					: 4507500005

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



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 source, 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 because 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 source in a source category designated by the Administrator of
the US Environmental Protection Agency (US EPA) (Administrator) pursuant
to this Section; and

6.	Any source 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 person 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)]

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 be issued only if 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 of 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 facility from 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 be 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.

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 fees 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 furnish 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 for
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 major 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 effective date
of the requirement is later than the date on which the permit is due to
expire, unless the original permit or any of 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.

In addition, the permit may be 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)]

In accordance with SC Regulation 61-62.70.6(e), the Department may issue
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 IV of the
Act shall be permitted as a temporary source.

I.	EMERGENCY PROVISIONS [SC Regulation 61-62.70.6(g)(3)]  (Revised
05/21/99)

In the case of an emergency, as defined in SC Regulation 61-62.70.6(g),
the permittee shall verify an affirmative defense of emergency through
properly signed, contemporaneous operating logs, or other relevant
evidence that:

1.	An emergency occurred 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 reasonable
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 applicable 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 approved 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 Regulation 61-62.70.6(a)(4)]

The permittee is prohibited from emissions exceeding any allowances that
the source lawfully holds under Title IV of 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.

Where an applicable requirement of the Act is more stringent than an
applicable requirement of regulations promulgated under Title IV of the
Act, both provisions shall be incorporated into the permit and shall be
enforceable by the Administrator. [SC Regulation 61-62.70.6(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 the 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 upon 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).  Significant 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.

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 permit 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 be 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 facilities, 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 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 judicial consent decree or
administrative order to which the source is 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 and be included in the acid rain portion of a compliance
plan for an affected source, except as specifically superseded by
regulations promulgated under Title IV of 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)]

It shall not be a defense for a permittee in an enforcement action that
it would have been necessary to halt or reduce 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)]

In accordance with SC Regulation 61-62.70.7(e)(5), a permitted facility
is authorized to make changes within their facility without requiring a
permit revision, if the changes are not modifications under Title I of
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

Requirement	Condition Number

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

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 type 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 Number	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 modeling (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 modeling 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
modified.  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 these 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 owner/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

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.  Attachment 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
equipment 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 prompt 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 owners 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.  If
the permittee performs a service on motor (fleet) vehicles that involves
ozone-depleting substance refrigerant in MVACs, the permittee is subject
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

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	PM

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

BH94A	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

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	2003	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 acfm 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

Control Device 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 Collector	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

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

Clay 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

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	S118

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 Description	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	BH95	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	Installation 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 Bypass	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

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

C328	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, F731

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 Finish 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

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	BH172	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	2003	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

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	Cement 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

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	Exhaust 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	2003	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

D.	EMISSION LIMITS AND STANDARDS

Tables 5.15 through 5.22 contain summaries of emission unit emission
limits and standards.

TABLE 5.15 EMISSION LIMITS AND STANDARDS - UNIT ID 01 QUARRY SYSTEM
EQUIPMENT

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

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 Number

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 Method	Regulation	State Only	Condition Number

C400, C401, C402, C403, C413, C414, C417, C418, C419, C421, C422, C423,
C424, C425	Opacity	20%	Method 9	40CFR60.252 Subpart Y	No	5.E.3(b)

C412	PM	0.031 gr/dscf	Method 5	40CFR60 Subpart Y	No	5.E.3(c)

C412	NOx 	4.48 lb NOx/ton clinker (first year) 4.33 lb NOx/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)

C412	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	SO2 	3.26 lb SO2/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	Temperature	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	State Only	Condition Number

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% O2, or 0.40 ng TEQ/dscm Dioxin/Furan limit corrected to 7% O2 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)

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	NOx 	4.48 lb NOx/ton clinker (first 12 months) 4.33 lb
NOx/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	SO2 	3.26 lb SO2/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)

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 ppmv THC (as propane), or 100 ppmv
CO, dry basis, corrected to 7% O2	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 ppmv (expressed as HCl
equivalents) on a dry basis corrected to 7% O2	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 efficiency	Method 25
40CFR

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

K300A, K300B	Mercury Emissions	(120 μg/dscm, corrected to 7% O2	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% O2	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% O2	Method 29	40CFR

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

K300A, K300B	Temperature	Less than Temperature in Performance Test for
APCD	As Approved	40CFR63 Subpart EEE	No	5.E.4(ee)

K300A, K300B	Temperature	>Temperature 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)

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 Number

F402, F404, F405, F500, F501, F600, F601, F700, F701, F704, F709, F710,
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, R124B, 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 Number

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)

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, C322, 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

Equipment  ID	Pollutant/

Standard	Limit	Reference Method	Regulation	State Only	Condition Number

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, T115	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)

T101, T102, T103, T104, T105, T106, T146	VOC	95% removal	Portable FID	40
CFR 61 Subpart FF	No	5.E.7(h)

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/106 Btu Input	Method 5	SC Regulation 61-62.5,

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

Boiler	SO	3.5 lb/106 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 type 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

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.

(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 affected 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 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.  Since 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 for 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 affected 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 40CFR60.8 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. 

(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) NOx emissions from the kiln,
in-line raw mill system and coal mill are limited to 4.48 lb NOx / ton
clinker (first year) and 4.33 lb NOx / ton clinker (after first year) 30
day rolling average - sum of both the main kiln stack and the coal mill
stack.

(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.

(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.

(SC Regulation 61-62.5, Standard No. 7) SO2 emissions from the kiln,
in-line raw mill system and coal mill are limited to 3.26 lb SO2 / ton
clinker 30 day rolling average - sum of both the main kiln stack and the
coal mill stack.

(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.

(40 CFR 60.253) 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 ±1.7°C
(±3°F). All monitoring devices of this section are to be recalibrated
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 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. 

(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.

(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.

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 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) (P0.11) - 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.

(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.

(SC Regulation  61-62.5 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.

(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.

(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.

(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.

(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.

These sources are subject to S.C. Reg 61-62.5 Standard No. 5.1, VOC
LAER.  For these sources, VOC LAER is determined to be process
optimization.

(SC Regulation 61-62.5, Standard No. 7) NOx 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 of NOx 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 NOx 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 years of commercial operation).  Upon review, the NOx emission
limitation and/or the NOx averaging time may be adjusted downward if
deemed appropriate by the Bureau.  The intent of this condition is not
to remove operational and process flexibility from Holcim, but to show a
realistic permit limit relative to actual operation.

(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.

(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.

(SC Regulation 61-62.5, Standard No. 7) 30-day rolling average SO2
emissions shall not exceed 3.26 lb/ton of clinker from the sum of both
the main kiln stack and the coal mill.

(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.

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.

(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.

This source is subject to SC Regulation 62.5 Standard No. 7.  Upon
review, BACT for this source is determined to be:

NOx- Low NOx burners, Burner Optimization, Kiln Optimization, Multistage
Combustion

CO - Process Optimization

VOC - Process Optimization

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 year 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 NOx, CO, and SO2
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 postmarked no later than 30 calendar days after the end
of the reporting period.  These conditions shall not supersede any State
or Federal requirements such as National Emission Standards for
Hazardous Air Pollutants, unless these conditions would impose a more
restrictive limit.

The kiln will be allowed to burn various types of fuel due to high
temperatures and long residence times including:

(v)(1)	Hazardous waste derived fuel (HWDF) which 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 burner and 61MW hot gas generator.  

(v)(4)	No RCRA coded D/F containing wastes shall be combusted in the
kiln.  

(v)(5)	Other types 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 SC Regulation 61-62.1 shall have a
waste analysis performed as required by SC Regulation 61-62.5, Standard
3.

For the control period that begins on May 31, 2004, an owner or operator
of any Portland cement kiln subject to SC Regulation 61-62.99 shall not
operate the kiln during May 31 through September unless the kiln has
installed and operates during May 31 to September 30 with low- NOx
burners, mid-kiln firing, or alternative control techniques, as defined
under section 99.42(a). In all subsequent control periods, an owner or
operator of any Portland cement kiln subject to this rule shall not
operate the kiln during May 1 through September 30 unless the kiln has
installed and operates during May 1 to September 30 with low-NOx
burners, mid-kiln firing, or alternative control techniques, as defined
under section 99.42(a).

(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 bypass 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 basis 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 40CFR
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 basis, 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.

(40CFR63.1204(b)(6)) Combined HCl & Cl2, expressed as HCl equivalents,
shall not exceed 86 ppmv on a dry basis corrected to 7% O2 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 emissions
when non-hazardous fuels are being used. 

(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.

(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 condition 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 40CFR63.60, for each
waste to be burned.  The Permittee must base this specification on the
degree of difficulty of 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.

μg / dscm, corrected to 7% oxygen, when burning hazardous waste.

(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.

(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.

(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 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 affected 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 process weight rates of greater than 30 tons per hour:

E = (55.0) (P0.11) - 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.

(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.

(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) (P0.11) - 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 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.

(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.

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

(SC Regulation 61-62.1, II (H)) Cement throughput from the Rainbow
Process Line (RAI1, RAI2, RAI3, RAI4) must not exceed 300,000 ston/yr. 
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.  

(SC Regulation 61-62.1, II (H))  PM emissions from the cement dome
sources shall not exceed 3.05 lb/hr.

(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/yr. The
facility shall maintain daily throughput records and make such records
available to Department personnel upon request.

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) (P0.11) - 40

Where:  E = the allowable emission rate in pounds per hour

  P = process weight rate in tons per hour

For the Truck Load 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).  

(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 of 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.

(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).

In accordance 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%.

(SC Regulation 61-62.5, Standard No. 5.1, Standard No. 7) VOC emissions
for the HWDF Tank (T111) shall not exceed 1.07 ton/yr.

The HWDF tanks shall be equipped and controlled as required by 40 CFR
61.343 in regards to the following:

(1)	The tank shall be covered by a fixed 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 year by the methods specified in 40CFR61.355(h).

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 year by the methods specified in
40CFR61.355(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.

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 during 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 SO2 emissions
from the Boiler shall not exceed 3.5 lb/million Btu heat input.

5.E.8 Facility Wide Emissions Limits

(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 emissions at least to the levels required by all relevant
standards. 

(40CFR63.6(e)(3)(i), Subpart A)  Startup, 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
describes, 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.

(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%.

(SC Regulation 61-62.5, Standard 4, Section X – Non-Enclosed
Operations)

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.

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. 

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/ Parameter	Limit	Required Monitoring	Monitoring
Frequency	Reporting Frequency	Condition Number

02-06	Initial Notice of Intent to Comply with MACT Standards	N/A
Reporting	N/A	One-time initially	6.B.1(a)

02-06	Notification of Compliance Status with MACT Standards	N/A
Reporting	60 days after compliance 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, Recordkeeping	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/ Parameter	Limit	Required Monitoring	Monitoring
Frequency	Reporting Frequency	Condition Number

01

Quarry	General Reporting Requirements	N/A	Reporting	See Condition	See
Condition	6.B.2(a)

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/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

S99	Raw Mill Transfer Point	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)

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)

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)

S127	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)

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)

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/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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 applicable 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)

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, SO2, 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/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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)

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)

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)

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%
O2 or 0.40 ng TEQ @ 7% O2 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)

S94	Preheater/ Precalciner Kiln	Inlet APCD Temperature Monitoring
Determine during compliance performance 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
Determine during compliance performance 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, SO2, 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 Inspection	N/A
Monitoring	Annually	Semi-Annually	6.B.5(s)

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, O2	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<Ambient 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)

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/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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)

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 within
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 Classifier	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% 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)

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)

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
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)

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)

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 test, 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
emissions 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)

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 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)

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)

S181	Dry Marl Transport from 8-pack	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)

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 Dome 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)

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)

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)

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 Feed 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)

TABLE 6.7 MONITORING AND REPORTING – ID 06 CEMENT LOADOUT SYSTEM

Stack ID	Unit Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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 for 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	West 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)

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)

S91	#6 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)

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	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)

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)

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 for
semi-annual test, 	Semi-annually	6.B.7(a)

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 emissions 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)

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)

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)

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 observed 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)

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/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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 Thereafter	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 Bypass
Requirements	N/A	Visual Inspection of Closed Vent System Bypass	Daily
(Valves); Monthly (Monitoring Devices)	Semi-Annually	6.B.8(h)

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 Description	Pollutant/ Parameter	Limit	Required Monitoring
Monitoring Frequency	Reporting Frequency	Condition Number

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/dscf 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

The Notification of Compliance with 40 CFR 63 standards shall contain
the information 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 performance 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 type and quantity of 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.

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 60th day following 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 type and quantity of hazardous air pollutants emitted by the
source, accompanied by units of measurement and averaging times;

(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.

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

(xiii)	The report date.

(2)	If the total duration of excess emissions for the reporting period
is less 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.

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 be
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 following 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 be submitted
simultaneously with the excess emissions and continuous monitoring
system performance (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 of reporting for the
latter as specified by 40CFR63.10(e), the frequency of reporting for the
startup, shutdown, and malfunction reports also may be reduced if the
Department does not object to the intended change. The procedures to
implement the allowance in the preceding sentence shall be the same as
the procedures specified in 40CFR63.10(e)(3).  A copy of the report
shall also be kept on-site and on-file and made available to Department
personnel upon request.

Notwithstanding the allowance to reduce the frequency of reporting for
periodic startup, shutdown, and malfunction reports as specified in
condition 6.B.1(d), any time an action taken by the Permittee  during 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 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 certifying 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.

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.

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 40 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.

The owner/operator shall maintain on file all measurements required by
this 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 Department personnel for at least five
(5) years following the date of such measurement, maintenance, report
and record. 

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.  These records shall be retained for at least five
years following the date of such maintenance.  A reasonable inventory of
routine replacement items shall be kept on site to facilitate timely
repair of any malfunctioning systems.

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.

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

Failure to comply with any provision of the operations and maintenance
plan developed shall be in noncompliance with 40CFR63, Subpart LLL.

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.

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.  A copy of the comprehensive test plan shall also be
submitted to the Director of the Division of Engineering Services.

In accordance with 40 CFR63.1356, any affected source subject to the
provisions of 40CFR63 Subpart LLL is exempted from 40 CFR 60, Subpart F.

The emission limitations for NOx 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 of 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) 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.

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.

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.  A change 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))

If an emergency safety 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))

The permittee must 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. Such persons
include, but are not limited to, chief facility operators, control room
operators, continuous monitoring system operators, persons that sample
and analyze 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.
Passing of this test shall be 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

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.

In accordance 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 conveyors 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 for crushers or 10
percent opacity for 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 startup.  Source 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 be present if desired.  Rescheduled source tests
require 7 days notification.

6.B.3 RAW MILL SYSTEM

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 of testing from monthly to semi-annually for that
affected source. If visible emissions are observed during any
semi-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 for 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 part 60 of this
chapter. The Method 9 test must begin within one hour of any observation
of visible emissions.

All emission 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.

Fugitive emissions shall be controlled using dust suppression techniques
including paving, brooming and watering for problem areas.

6.B.4 COAL MILL SYSTEM

These sources are subject to all applicable provisions of 40 CFR 60
Subpart A (General Provisions) and Subpart Y (Coal Preparation Plants).

The permittee shall perform a visual inspection on a monthly basis. 
Visual Inspection means a qualitative observation of opacity during
daylight hours where the inspector records results in a log, noting
color, duration, density (heavy or light), cause and corrective action
taken for any abnormal 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.  Logs 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 postmarked 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.  Logs 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.  Continuous
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 postmarked 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
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”(9/96), as amended.
The report shall include the following minimum information:

All opacity measurements for periods during which the above emission
limitations for opacity have been exceeded, together with their nature
and cause.

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 be required by the Department
whenever repairs or adjustments have been made.

Particulate matter emissions from the coal mill shall be monitored every
2.5 years.

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.

Continuous Emission Monitors for SO2, CO and NOx 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 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 SO2, CO and
NOx 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
Continuous 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 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.

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 be 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

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 of testing from monthly to semi-annually for that
affected source. If visible emissions are observed during any
semi-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 for 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 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.

Logs 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
postmarked no later than 30 calendar 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 40 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
for any 6-minute block period does not exceed 20 percent.  If the
average opacity for any 6-minute block period exceeds 20 percent, 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 postmarked 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 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”(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 be required by the Department
whenever repairs or adjustments have been made.

The permittee must comply with the dioxin and furans emission standard
by establishing 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 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 average limit as the average of the test run
averages.

	(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.

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 bypass 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 postmarked 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 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”(9/96), as amended. The report shall
include the following minimum information:

All temperature measurements for periods during which the above
temperature limitations have been exceeded, together with their nature
and cause.

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.

All notifications 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.

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).

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)).

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.  

For each occurrence mentioned below, reports shall be submitted to the
Manager of the Technical 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 for NOx 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 of 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) years from the date
generated and shall be made available to a Department representative
upon request.  Semi-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.

Quarterly Continuous 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 be required by
the Department whenever repairs or adjustments have been made.

The waste feed rate shall be monitored continuously and recorded as
required by SC Regulation 61-62.5 Standard No. 3, section VI(A)(2)(k).

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.

Continuous Emission Monitors for SO2, CO, and NOx 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 SO2, CO, and NOx 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 Continuous 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 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: 

(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 be required by the
Department whenever repairs or adjustments have been made.

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.

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) years from the date generated.  The facility shall also
maintain daily clinker production records for the calculation of the
NOx, CO, and SO2 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 Technical 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 State or Federal
requirements such as National Emission Standards for Hazardous Air
Pollutants, unless these conditions would impose a more restrictive
limit.

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.  Performance
test results shall be documented in complete test report that contain
the information required by 40 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. 

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. 
Semi-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.

(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 source test for PM, Metals, POHC removal and reduction efficiency,
CO, O2, 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-up of burning
HWDF’s.  The Bureau must be notified at least two weeks prior to any
source test so that a Bureau representative may be present.  The testing
shall be done at least every two and a half years.  Source test
methodology must be approved by the Bureau and comply with SC Regulation
62.1, Section IV, Source Testing.

The particulate matter emission rate must be computed by the equation
specified in 40 CFR § 63.1204(a)(7)(ii).  E=(Cs x Qsd)/P.

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 40 CFR § 63.1204(c)(3).

(w)	The DRE standard must be documented only once provided that no
modifications of the source are done which could affect the ability of
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 emission standards and operating requirements set forth apply at
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 of 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)).

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 hazardous waste and has been granted
approval  (40 CFR § 63.1206(c)(1)).

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 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 if hazardous waste is
in the combustion chamber and the HWDF residency time has not expired
(40 CFR § 63.1206(c)(2)).

The hazardous waste combustor must operate with a functioning system
that automatically cuts off the hazardous waste feed in compliance with
40 CFR  § 63.1206(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.

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)).

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.

The facility shall install a CEM in the alkali bypass 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 document compliance with the feedrate
limits as required by 40 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. 
Compliance 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 Continuous 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 for ready inspection by authorized 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 postmarked 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 particulate
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 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 25,
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 for 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 ID Fan 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 during daylight hours).

c.	ID Fan 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 be
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

These sources are subject to all applicable provisions of 40 CFR 63
Subpart A (General Provisions) and LLL (Portland Cement Manufacturing).

Opacity Requirements

(1)	The owner or operator shall demonstrate initial compliance and then
every five 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 be 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
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 of testing from monthly to semi-annually for
that affected source. If visible emissions are observed during any
semi-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 for 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.

(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

Opacity Requirements

(1)	The owner or operator shall demonstrate initial compliance and then
every five 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 be 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 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 of testing from monthly to semi-annually for
that affected source. If visible emissions are observed during any
semi-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 for 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

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
for 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 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).

Since this facility processes waste streams produced by facilities with
the total potential annual benzene quantity of greater than 10 Mg/yr,
then this facility is fully subject to all applicable requirements of 40
CFR 61 Subpart A (General Provisions) and Subpart FF (National Emission
Standard for Benzene Waste Operations).

	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 40 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 year 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.  Semi-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.

(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).

Each closed-vent system and control device shall be visually inspected
initially and 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)).

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 fixed 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))).

Owners or operators using a closed-vent system that contains any bypass
line that could divert a vent stream from a control device shall:

(1)	Visually inspect the bypass 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 bypass 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 postmarked no later than 30
calendar days after the end of the reporting period.

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 problem, 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) 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.

 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 the 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.

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 permittee shall perform a visual inspection on a semi-annual
basis.  Visual Inspection means a qualitative observation of opacity
during daylight hours where the inspector records results in a log,
noting color, duration, density (heavy or light), cause and corrective
action taken for any abnormal 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.  Logs 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 postmarked 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)) 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

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.  Performance 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
available 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 five 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 be 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 five
years, except that the owner or operator of an in-line kiln/raw mill is
not required to repeat the initial performance test of opacity for the
in-line kiln/raw mill.  Confirmatory 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 source test so that a Bureau representative may be present.  This
testing shall then hereafter be done with the comprehensive and
confirmatory testing required by 40CFR63, Subpart EEE.  The testing
shall be done at least every 30 months.  Source 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 40 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 performance testing must be done to demonstrate compliance
with the emission limitations, establish limits for the operating
parameters required by 40 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.  A notification 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).

For sources subject to the Portland Cement MACT (40CFR63 Subpart LLL),
the owner or operator shall demonstrate initial compliance and then
every five 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 be 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.

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.

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 analyze 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.  Passing 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
persons 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 be 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:

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.

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).

The primary operating mode for the industrial furnace (K300A) is burning
hazardous waste for energy recovery pursuant to 40 CFR 63, Subpart 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 bypass (K300B), kiln differential
pressure, 40 CFR63 Subpart EEE metal limits, and the minimum combustion
chamber temperature) will no longer be applicable or required.

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 during 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 11/13/98)

A copy of the “applicability determination” Holcim submitted with
its Part 70 permit application is included as Attachment C.  Compliance
with the terms and conditions of this permit shall be deemed compliance
with any applicable 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 permit 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 of 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 of 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 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 this 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)

NAAQS EMISSION RATES (New Plant)

STACK	Modeled Emission Rates (lbs/hr)

	TSP	PM10	SO2	NOX	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 Emission Rates (lbs/hr)

	PM10	SO2	NOX

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	0.0127	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*	See 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	0.0203	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	-	-	-	-

(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 Gyp Weigh Belt**	See B41 – 44	See B41 – 44	-	-	-	-

(42A) #1 FM Gyp Apron Feeder**	See 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 Gyp Apron Feeder D. C.**	See B41 – 44	See B41 – 44	-	-	-
-

(47) #2 FM Gyp 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	0.00094	0.00079	-	-	-	-

(52) #3 FM Gyp Weigh Feeder	0.00006	0.00005	-	-	-	-

(53) #3 FM Gyp 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 Gyp 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 B51 – 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, S47, S53, S57, S58, S59,
S76, S78)	0.00213	0.00164	-	-	-	-

(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	0.00084	-	-	-	-

(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 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). 
Sources 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 Minimis

Emission Rate	Reason(s)

Insignificant

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 Emissions < 5 tpy	PM10
Emissions < 5 tpy

TABLE 2. INSIGNIFICANT RAW MILL SYSTEM EQUIPMENT

Equipment Description	 Unit 

ID	Design

Capacity

(tpy)	Equipment

Manufacture

Date	De Minimis

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

Manufacture

Date	De Minimis

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 Minimis

Emission Rate	Reason(s)

Insignificant

Truck to Tire Chip Pile	NP53	32,836	2003	PM10 Emissions < 5 tpy	PM10
Emissions < 5 tpy

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, Tire 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 Minimis

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 Pile	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	PM10 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

Equipment Description	 Unit 

ID	Design

Capacity

(gal)	Equipment

Manufacture

Date	De Minimis

Emission Rate	Reason(s)

Insignificant

Diesel Fuel Storage Tank	S112	500	Before 1985	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 insignificant based on tank size.

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
emissions < 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 1980	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

Drum Storage - Various Oils	S168	<10,000	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	250	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 1989	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 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 be 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

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

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 of 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

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 Determinations

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 subject 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

40CFR63 Subpart MMM through Subpart XXX

X	This facility is not a source type or does

not have any equipment subject 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	Specifies 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

40CFR81

X	Specifies 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	Specifies 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 Raynor

Dear Mr. Raynor:

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.  Please note the conditions and limitations imposed.  This permit
will be valid through June 30, 2008, unless otherwise provided for by SC
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-1860-0005

May 14, 2003

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street / Highway 453

Holly Hill, South Carolina 29059  

ATTENTION:	Mr. Glenn Raynor

Dear Mr. Raynor:

Enclosed with this letter is your updated Part 70 Air Quality (Title V
Operating) Permit No. TV-1860-0005.    Please 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.  See 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 clarkkj@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-1860-0005



September 23, 2003

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street / Highway 453

Holly Hill, South Carolina 29059  

ATTENTION:	Mr. Glenn Raynor

Dear  Mr. Raynor:

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 issued 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., 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:  1900-0005



October 22, 2003

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street / Highway 453

Holly Hill, South Carolina 29059  

ATTENTION:	Mr. Glenn Raynor

Dear Mr. Raynor:

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:

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 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.

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., 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:  1900-0005



June 27, 2005

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street / Highway 453

Holly Hill, South Carolina 29059  

ATTENTION:	Mr. Glenn Raynor

Dear Mr. Raynor:

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 issued October 23, 2003. This updated
permit includes previously issued 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 for 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 are 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:  1860-0005



August 19, 2005

Holcim (US) Inc. – Holly Hill Plant

200 Safety Street / Highway 453

Holly Hill, South Carolina 29059  

ATTENTION:	Mr. Glenn Raynor

Dear Mr. Raynor:

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 issued 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 for 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 are 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

Holcim (US) Inc. – Holly Hill Plant

TV-1860-0005

Page   PAGE  2  of 106

(permit updated 6/27/05 and 8/19/05)

ATTACHMENT A

Modeled Emission Rates

Holcim (US) Inc. – Holly Hill Plant

TV-1860-0005

PAGE   PAGE  3  OF 6

ATTACHMENT B

Insignificant Activities

Holcim (US) Inc. – Holly Hill Plant

TV-1860-0005

PAGE   PAGE  4  OF 5

ATTACHMENT C

Regulatory applicability

Holcim (US) Inc. – Holly Hill Plant

TV-1860-0005

PAGE   PAGE  6  OF 7

ATTACHMENT C

Regulatory applicability

Holcim (US) Inc. – Holly Hill Plant

TV-1860-0005

PAGE   PAGE  1  OF 7