## From: Topham.Nathan@epamail.epa.gov Sent: Wednesday, November 02, 2011 3:26 PM To: Higgins, Cortney Cc: French.Chuck@epamail.epa.gov; Hanzel, Veronica; Talcott.Fred@epamail.epa.gov; tierney.jan@epamail.epa.gov; Benner.Tim@epamail.epa.gov; Garlow.Charlie@epamail.epa.gov; Doolan.Stephanie@epamail.epa.gov Subject: RE: E.O. 12866 NESHAP Primary Lead Processing Final AQ

- 43

- Revised preamble/rule responding to interagency review comments Attachments: EO12866 NESHAP Primary Lead Processing Final AQ

- 43_DRAFT_11

- 2

- 11_Resonse_to

- commentOMB_RuleRdln.doc

Hi Cortney,

Here is the redline of the regulatory text comparing the 1999 NESHAP reg text to the draft you received at about 5:15 yesterday. Let me know if you hav e any questions.

Nathan Topham Environmental Engineer US EPA/OAQPS/SPPD/MIG Phone

- (919)541

- 0483

From: "Higgins, Cortney" <Cortney_Higgins@omb.eop.gov> To: Nathan Topham/RTP/USEPA/US@EPA Date: 11/02/2011 01:42 PM Subject

: RE: E.O. 12866 NESHAP Primary Lead Processing Final AQ

- 43

- Revised preamble/rule responding to interagency review comments

Hi Nate, Is it possible to get a side by side or redline of the existing CFR for Subpart TTT compared to the draft final regulatory text?

Many thanks, Cortney

## From: Topham.Nathan@epamail.epa.gov [mailto:Topham.Nathan@epamail.epa.gov] Sent: Tuesday, November 01, 2011 5:17 PM To: Higgins, Cortney Cc: French.Chuck@epamail.epa.gov; Talcott.Fred@epamail.epa.go v; tierney.jan@epamail.epa.gov; Stewart.Michael@epamail.epa.gov; vahanzel@rti.org; Doolan.Stephanie@epamail.epa.gov; Benner.Tim@epamail.epa.gov; Garlow.Charlie@epamail.epa.gov Subject: E.O. 12866 NESHAP Primary Lead Processing Final AQ

- 43

- Revised prea mble/rule responding to interagency review comments

Hi Cortney,
I've attached a revised preamble/rule in redline and a clean version. Please take a look and let me know if you think we need to have another phone call to discuss things.

If you think another call is needed, please let me know your availability as soon as possible so I can get something on the calendar.

In place of the ambient monitoring, a few specific work practices have been laid out in the regulatory text. Feel fr ee to give me a call if you have any questions about these.

Thanks, look forward to hearing from you.

Nathan Topham Environmental Engineer US EPA/OAQPS/SPPD/MIG Phone

- (919)541

- 0483

### PART 63

-- NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR

POLLUTANTS

FOR SOURCE CATEGORIES

1. The authority citation for part 63 continues to read as

follows:

Authority: 42 U.S.C. 7401 et seq.

2. Part 63 is amended by adding subpart TTT, to read as
follows:

Subpart TTT

-- National Emission Standards for Hazardous Air Pollutants for Primary Lead Smelting Processing

Sec.

§ 63.1541 Applicability.

§ 63.1542 Definitions.

§ 63.1543 Standards for process and process fugitive sources.

§ 63.1544 Stand ards for fugitive dust sources.

§ 63.1545 Compliance dates.

§ 63.1546 Test methods Performance Testing

. § 63.1547 Monitoring requirements.

§ 63.1548 Notification requirements.

§ 63.1549 Recordkeeping and reporting requirements.

§ 63.1550 Delegation of autho rity.
§63.1551 Affirmative defense for exceedance of emission limit during malfunction.

Subpart TTT

-- National Emission Standards for Hazardous Air

### Pollutants for Primary Lead Smelting Processing

Sec. **§ 63.1541**  **Applicability.**

(a) The provisions of t his subpart apply to apply to any facility engaged in producing lead metal from ore concentrates. The category includes, but is not limited to, the following

affected sources at primary lead smelters: sinter machine, blast
furnace, dross furnace smelting pr ocesses: sintering, reduction, preliminary treatment, refining and casting operations , process fugitive sources, and fugitive dust sources. The sinter process includes an updraft or downdraft sintering machine. The reduction process includes the blast furn ace, electric smelting furnace with a converter or reverberatory furnace, and slag fuming furnace process units. The preliminary treatment process includes the drossing kettles and dross reverberatory furnace process units. The refining process includes t he refinery process unit. The provisions of this subpart do not apply to secondary lead smelters, lead refiners, or lead remelters. (b) Table 1 of this subpart specifies the provisions of subpart A that apply and those that do not apply to owners and

o perators of primary lead smelters. The following sections of part 63 apply to this subpart as stated in subpart A and Table 1: Sec. 63.1 (Applicability), Sec. 63.2 (Definitions), Sec. 63.3 (Units and abbreviations), Sec. 63.4 (Prohibited activities and
cir cumvention), Sec. 63.5 (Construction and reconstruction), Sec. 63.7 (Performance testing requirements), Sec. 63.8 (Monitoring requirements), Sec. 63.12 (State authority and delegations), Sec. 63.13 (Addresses of State air pollution

control agencies and EPA Regional Offices), Sec. 63.14 (Incorporations by reference), and Sec. 63.15 (Availability of Formatted: Font: Bold
Formatted: Font: Bold

### information confidentiality). The following sections of part 63 apply to the extent specified in this subpart and Table 1: Sec. 63.6 (Compliance with standards a nd maintenance requirements), Sec. 63.9 (Notification requirements), and Sec. 63.10 (Recordkeeping and reporting requirements). Section Sec. 63.11 Control device requirements) does not apply to this subpart.

Sec. (b) Table 1 of this subpart specifies the provisions of subpart A of this part that apply and those that do not apply to owners and operators of primary lead processors.

**§ 63.1542**  **Definitions.**

Terms used in this subpart are defined in the Act, in subpart A of this part, or in this sec tion as follows:
Affirmative defense means, in the context of an enforcement proceeding, a response or defense put forward by a defendant, regarding which the defendant has the burden of proof, and the merits of which are independently and objectively evaluated in a judicial or administrative proceeding. Bag leak detection system means a system that is capable of continuously monitoring relative particulate matter (dust) loadings in the exhaust of a baghouse in order to detect bag leaks and other up set conditions. A bag leak detection system includes, but is not limited to, an instrument that operates on triboelectric, light scattering, light transmittance, or other effect to continuously monitor relative particulate matter loadings. Formatted: Font: Bold
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### Blast furnac e means any reduction furnace to which sinter is charged and which forms separate layers of molten slag and lead
bullion. Building means a roofed and walled structure with limited openings to allow access and egress for people and vehicles. Chargin g location means the physical opening through which raw materials are introduced into a sinter machine, blast
furnace, or dross furnace.
Dross furnace means any smelting furnace to which drosses are charged and which chemically and physically separates lead from other impurities. Drossing and refining kettle means an open

- top vessel that is constructed of cast iron or steel and is indirectly heated from below and contains molten lead for the purpose of drossing, refining, or alloying lead. Included are pot furnaces, receiving kettles, and holding kettles. Fugitive dust source means a stationary source of hazardous air pollutant emissions at a primary lead smelter processor resulting from the handling, storage, transfer, or other management of lead

- bearing materials where the source is not
associated with part of a specific process, process vent, or stack. Fugitive dust sources include roadways, storage piles, materials handling transfer points, and materials transport

areas.

Furnace area means a ny area of a primary lead

smelter processor in which a blast furnace or dross furnace is

located.
Lead refiner means any facility that refines lead metal that is not located at a primary lead processor.

Lead remelter means any facility that remelts lead metal that is not located at a primary lead processor. Formatted: Font: Italic

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### Malfunction means any sudden, infrequent, and not reasonably preventable failure of air pollution control and monitoring equipment, process equipment, or a process to operate in a

normal or us ual manner which causes, or has the potential to cause, the emission limitations in an applicable standard to be exceeded. Failures that are caused in part by poor maintenance or careless operation are not malfu n ctions

. Failures that are caused in part by poor maintenance or careless operation are not malfunctions. Materials storage and handling area means any area of a primary lead smelter processor in which lead

- bearing materials (including ore concentrate, sinter, granulated lead, dross, slag, and fl ue dust) are stored or handled between process steps, including areas in which materials are stored in piles, bins, or tubs, and areas in which material is prepared for charging to a sinter achine machine or smelting furnace or other lead processing operati on

. Operating time means the period of time in hours that an affected source is in operation beginning at a startup and ending at the next shutdown. Plant operating time means the period of time in hours that
either a sinter machine or blast furnac e is in operation. Plant roadway means any area of a primary lead

smelter processor that is subject to vehicle traffic, including traffic by fork lifts forklifts , front

- end loaders, or vehicles carrying ore concentrates or cast lead ingots.

Excluded fro m this definition are employee and visitor parking areas, provided they are not subject to traffic by vehicles carrying lead

- bearing materials. Primary lead smelter processor means any facility engaged in the production of lead metal from lead sulfide o re concentrates through the use of pyrometallurgical or other techniques. Formatted: Font: Italic

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### Process fugitive source means a source of hazardous air pollutant missions emissions at a primary lead smelter processor that is associated with lead smelting , processing or refin ing but is not the primary exhaust stream and is not a fugitive dust source. Process fugitive sources include sinter machine charging locations, sinter machine discharge locations, sinter crushing and sizing equipment, furnace charging locations, furnace t aps,
and drossing kettles, kettle and refining kettles kettle charging or tapping locations

. Refining and casting area means any area of a primary lead

smelter processor in which drossing or refining operations occur, or casting operations occur.

Seco ndary lead smelter means any facility at which lead

bearing scrap material, primarily, but not limited to, lead

- acid batteries, is recycled into elemental lead or lead alloys by smelting.

Shutdown means the cessation of operation of an affected

source for any purpose. Sinter machine means any device in which a lead sulfide ore concentrate charge is heated in the presence of air to eliminate sulfur contained in the charge and to agglomerate the charge into a hard porous mass called sinter.
Sinter machine area means any area of a primary lead

smelter processor where a sinter machine, or sinter crushing and sizing equipment is located. Sinter machine discharge end means the physical opening at
the end of a sinter machine where the sinter exits th e sinter
machine.
Startup means the setting in operation of an affected source for any purpose. Tapping location means the opening thru through which lead and slag are removed from the furnace. Formatted: Font: Italic

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### Sec. **§ 63.1543**  **Standards for process and process fugi tive** 

**sources.**

(a) No owner or operator of any existing, new, or reconstructed primary lead smelter processor shall discharge or cause to be discharged into the atmosphere lead compounds in

excess of 500 grams of lead per megagram of lead metal produced
(1. 0

. 97 pounds of lead per ton of lead metal produced ) from the aggregation of emissions discharged from the air pollution
control devices used to control emissions from the sources listed in paragraphs (a)(1) through (a)( 9 ) of this section. (1) Sinte r machine;
(2) Blast furnace;
(3) Dross furnace; (4) Dross furnace charging location; (5) Blast furnace and dross furnace tapping location; (6) Sinter machine charging location; (7) Sinter machine discharge end; (8) Sinter crush ing and sizing equipment; and (9) Sinter machine area

. (b) No owner or operator of any existing, new, or reconstructed primary lead processor shall discharge or cause to be discharged into the atmosphere lead compounds in excess of

1.2 tons per yea r from the aggregation of the air pollution
control devices used to control emissions from furnace area and refining and casting operations.
(c) The process fugitive sources listed in paragraphs (a)(4) through (a)(8) of this section shall must be equipp ed with a hood

and shall must be ventilated to a baghouse or equivalent control device. The hood design and ventilation rate shall must be Formatted: Font: Bold
Formatted: Font: Bold

### consistent with American Conference of Governmental Industrial Hygienists recommended practices.
( c d ) The sinter ma chine area shall must be enclosed in a building that is ventilated to a baghouse or equivalent control device at a rate that maintains a positive in

- draft through any doorway opening.
( d e ) Except as provided in paragraph ( e f ) of this section, following the initial test test s to demonstrate compliance with paragraph paragraphs (a ) and (b ) of this section, the owner or operator of a primary lead smelter shall processor must conduct a compliance test test s for lead compounds on an annual a quarterly basis (no la ter than 12 calendar months 100 days following any previous compliance test).
( e f ) If the three 12 most recent compliance tests demonstrate compliance with the emission limit specified in paragraph paragraphs (a ) and (b ) of this section, the owner or

oper ator of a primary lead smelter processor shall be allowed up

to 24 12 calendar months from the last compliance test to conduct the next compliance test for lead compounds.
( f g ) The owner or operator of a primary lead smelter
shall processor must maintain and operate each baghouse used to control emissions from the sources listed in paragraphs (a)(1) through (a)( 9 ) and (b) of this section such that the alarm on a bag leak detection system required under Sec. § 63.1547(c)( 9 8 )
does not sound for more than five percent of the total operating
time in a 6

- month reporting period.
( g h ) The owner or operator of a primary lead smelter
shall processor must record the date and time of a bag leak detection system alarm and initiate procedures to determine the

cause of the alarm according to the corrective action plan required under Sec. § 63.1547( c)(9 f ) within 1 hour of the alarm.

### The cause of the alarm shall must be corrected as soon as practicable.

Sec. (i) At all times, the owner or operator must operate
and mai ntain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. Determination of whether such operation and main tenance procedures are being used will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and ins pection of the source.

**§ 63.1544**  **Standards for fugitive dust sources.**

(a) Each owner or operator of a primary lead smelter

shall processor must prepare, and at all times operate according

to, a standard operating procedures manual that describes in

d etail the measures that will be put in place to control

fugitive dust emissions from the sources listed in paragraphs

(a)(1) through (a)(5) of this section : that incorporates each of

the specific work practices listed in paragraphs (a)(1) through

(a)(5) of this section:

(1) Plant roadways ;

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### (i)Paved plant roadways must be cleaned using a wet sweeper

unless the temperature falls below 39 degrees Fahrenheit or when

the application of water results in the formation of ice. During

periods when the tem perature is below 39 degrees Fahrenheit,

paved plant roadways must be cleaned using a high efficiency dry

sweeper.
(ii)Continuously operate a sprinkler system to wet plant

roadways to prevent fugitive dust entrainment. This sprinkler

system must be operat ed except during periods when the

temperature is less than 39 degrees Fahrenheit or when the

application of water results in formation of ice.

(2) Material storage and handling area(s ); )

. (i)Chemically stabilize inactive concentrate storage piles

a m inimum of once every month to reduce particulate from wind

born re

- suspension.

(ii)Finished sinter must be sufficiently wetted to ensure

fugitive dust emissions are minimized prior to loading to

railcars.

(3) Sinter machine area(s ); )

.
(i)Personnel d oors must be kept closed during operations

except when entering or exiting the furnace building by the aid

of door weights or similar device for automatic closure. Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Line spacing: Double, Tab stops: 0.5", Left + Not at 0.64"
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### (ii)Large equipment doors must remain closed except when

entering or existing the building using an automatic closure

system or equivalent lock

- and

- key method.

(iii)It may be necessary to open doors subject to the

requirements in sections 63.1544(a)(3)(i) and 63.1544(a)(3)(ii)

to prevent heat stress or exhaustion of workers inside the

sinter p lant building. Records of such periods must be included

in the report required under section 63.1549(e)(8).

(4) Furnace area(s ); and )

. (i)Personnel doors must be kept closed during operations

except when entering or exiting the furnace building by th e aid

of door weights or similar device for automatic closure.

(ii)Large equipment doors must remain closed except when

entering or existing the building using an automatic closure

system or equivalent lock

- and

- key method.

(iii)It may be necessary to op en doors subject to the

requirements in sections 63.1544(a)(4)(i) and 63.1544(a)(4)(ii)

to prevent heat stress or exhaustion of workers inside the blast

furnace building. Records of such periods must be included in

the report required under section 63.1549 (e)(8).

(5) Refining and casting area(s)

. (i)Personnel doors must be kept closed during operations

except when entering or exiting the furnace building by the aid

of door weights or similar device for automatic closure. Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Line spacing: Double, Tab stops: 0.5", Left + Not at 0.64"
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### (ii)Large equipment doors mu st remain closed except when

entering or existing the building using an automatic closure

system or equivalent lock

- and

- key method.

(iii)It may be necessary to open doors subject to the

requirements in sections 63.1544(a)(5)(i) and 63.1544(a)(5)(ii)

to pr event heat stress or exhaustion of workers inside the

refining and casting building. Records of such periods must be

included in the report required under section 63.1549(e)(8).

(b) Not withstanding paragraph (c) of this section, the

standard operating pr ocedures manual shall be submitted to the

Administrator or delegated authority for review and approval.

(c) Existing manuals that describe the measures in place to control fugitive dust sources required as part of a State implementation plan for lead shall satisfy the requirements of paragraph (a) of this section provided they address include all the work practices as described in paragraphs (a)(1) through (a)(5) of this section and provided they address all the sources listed in paragraphs (a)(1) throu gh (a)(5) of this section.

Sec. **§ 63.1545**  **Compliance dates.**

(a) Each owner or operator of an existing primary lead smelter shall achieve compliance with the requirements of this subpart no later than May 4, 2001. processor must achieve compliance wit h the requirements in § 16.1543(a) no later than
[INSERT DATE 60 DAYS FROM THE DATE OF PUBLICATION OF THESE AMENDMENTS IN THE FEDERAL REGISTER]. Each owner or operator of Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Line spacing: Double, Tab stops: 0.5", Left + Not at 0.64"

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### an existing primary lead processor must achieve compliance with the requirements of § 63.1544 no later than [INSERT DATE 90 DAYS

FROM THE DATE OF PUBLICATION OF THESE AMENDMENTS IN THE FEDERAL REGISTER]. Each owner or operator of an existing primary lead

processor must achieve compliance with the requirements in
§63.1543(b) and §63.1543(e) of this subpart no later than
[ INSERT DATE TWO YEARS FROM THE DATE OF PUBLICATION OF THESE AMENDMENTS IN THE FEDERAL REGISTER]

. (b) Each owner or operator of a new primary lead smelter that commences construction or reconstruction after April 17,
1998, shall proce s sor must achieve compliance with the requirements of this subpart by June 4, 1999 or upon no later
than [INSERT DATE 60 DAYS AFTER PUBLICATION OF THESE AMENDMENTS
IN THE FERERAL REGISTER] or startup of operations , whichever is

later.

Sec. (c) Prior to the dates specified in §63.1545(a), each owner or operator of an existing primary lead processor must continue to comply with the requirements of §63.1543 and §63.1544 as promulgated in the June 4, 1999 NESHAP for Primary Lead Smelting.
(d ) Each owner or operator of an existing primary lead processor must comply with the requirements of sections 63.1547(g)(1), 63.1547(g)(2), 63.1551, and the revisions to Table 1 of Subpart TTT of Part 63 on [INSERT DATE OF PUBLICATION

OF THESE AMENDMENTS IN THE FEDERAL REGISTER].

**§ 63.1546**  Test methods **Performance testing**
**.** Formatted: Font: Bold
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### (a) The following procedure shall procedure s must be used to
determine quarterly compliance with the emissions standard for lead compounds under Sec. § 63.1543(a ): ) and (b) for existin g

sources: (1) The lead (1) Each owner or operator of existing sources listed in §63.1543(a)(1) through ( 9 ) and (b) must
determine the lead compound emission emissions rate, in units of

grams pounds of lead per hour , for each source listed in Sec.

63 .1543(a)(1) through Sec. 63.1543(a)(9) shall be determined according to the following test methods in appendix A of part 60 of this chapter : (i) Method 1 shall must be used to select the sampling port location and the number of traverse points. (ii) Method 2 shall , 2F, 2G must be used to measure
volumetric flow rate. (iii) Method 3 shall , 3A 3B must be used for gas analysis. (iv) Method 4 shall must be used to determine moisture content of the stack gas

. (v) Method 12 shall or Method 29 mus t be used to measure
the determine lead emission emission s rate of the stack gas. The (2) A performance test shall consist of at least thr e e runs. For each test run with Method 12 or Method 29, the minimum sample time must be 60 minutes and the minimum volume shall must
be 0.85 1 dry standard cubic meters (30 meter (35 dry standard
cubic feet ) and the minimum sampling time shall be 60 minutes for each run. Three runs shall be performed and ).
(3) Performance tests shall be completed quarterly, once

ever y 3 months, to determine compliance. (4) The lead emission rate in pounds per quarter is calculated by multiplying the average of quarterly lead emission rate in pounds per hour by the three runs shall be used to Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Tab stops: 0.5", Left

### determine compliance. quarterly plant op erating time, in hours as shown in Equation 1:

(2 (Eq. 1)
Where:

E Pb 

### = quarterly lead emissions, pounds per quarter;

ER Pb 

### = quarterly lead emissions rate, pounds per hour; and QPOT = quarterly plant operating time, hours per qua rter.
(5 ) The lead production rate, in units of megagrams tons per hour, shall quarter, must be determined based on production data for the previous 12 calendar months quarter according to the procedures detailed in paragraphs (a)( 2 5 )(i) through ( a)(2)(v i v )
of this section:
( i) Total lead products production multiplied by the
fractional lead content shall must be determined in units of

megragrams tons

. (ii) Total copper matte production multiplied by the
fractional lead content shall must be determine d in units of

megragrams tons

. (iii) Total copper speiss production multiplied by the
fractional lead content shall must be determined in units of

megragrams tons

. (iv) Total quarterly lead production shall must be determined by summing the values obta ined in paragraphs (a)( 2 5 )(i) through
(a)( 2 5 )(iii) of this section.
( v) The lead 6) To determine compliance with the production

based lead compound emission rate in §63.1543(a), the quarterly production

- based lead compound emission rate, in units of

me gragrams pounds of lead emissions per hours, shall be ton of lead produced, is calculated based on the total lead production,

as determined in accordance with paragraph (a)( shown in Equation

2 )(iv) of this section, divided by the total plant operating Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Tab stops: 0.5", Left

### time, in hours, for the previous 12 months dividing lead emissions by lead production

. (3) The sum of lead compound emission rates for the sources in Sec. 63.1543(a)((1) through (a)(9), as determined in accordance with paragraph (a)(1) of this section, shall be divided by the lead production rate, as determined in accordance with paragraph (a)(2)(v) of this section, to obtain a production

- based, lead compound emission rate in units of grams

of lead per megagram of lead metal produced. The (Eq.
Where :

CE Pb 

### = quarterly production

- based , lead compound emission

rate shall be used to , in units of pounds of lead emissions per ton of lead produced;

E Pb 

### = quarterly lead emissions, pounds per quarter; and

P Pb 

### = quarterly lead production, tons per q uarter.
(7) To determine quarterly compliance with the emissions standard for lead compounds under Sec. 63.1543(a). §63.1543(b), sum the lead compound emission rates for the current and previous three quarters for the sources in §63.1543(b), as
determined in accordance with paragraphs (a)(1) through (a)(4)
of this section.
(b) Owner Owner s and operators shall must perform an initial compliance test to demonstrate compliance with the sinter building in

- draft requirements of Sec. § 63.1543( c d ) at each
doorwa y opening in accordance with paragraphs (b)(1) through (b)(4) of this section. (1) Use a propeller anemometer or equivalent device. (2) Determine doorway in

- draft by placing the anemometer in the plane of the doorway opening near its center. Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Tab stops: 0.5", Left

### (3 ) Determine doorway in

- draft for each doorway that is open during normal operation with all remaining doorways in their customary position during normal operation. (4) Do not determine doorway in

- draft when ambient wind speed exceeds 2 meters per secon d.

Sec. (c) Performance tests shall be conducted under such conditions as the Administrator specifies to the owner or operator based on representative performance of the affected source for the period being tested. Upon request, the owner or
operator shall make available to the Administrator such records as may be necessary to determine the conditions of performance

tests.

**§ 63.1547**  **Monitoring requirements.**

(a) Owners and operators of primary lead smelters
shall processors must prepare, and at a ll times operate according to, a standard operating procedures manual that describes in detail the procedures for inspection, maintenance, and bag leak detection and corrective action for all baghouses that are used to control process, process fugitive, or fugitive dust emissions from any source subject to the lead emission standards in Secs.

§§ 63.1543 and 63.1544, including those used to control emissions from general ventilation systems. (b) The standard operating procedures manual for baghouses requi red by paragraph (a) of this section shall must be submitted to the Administrator or delegated authority for review and approval. Formatted: Font: Bold
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### (c) The procedures specified in the standard operating procedures manual for inspections and routine maintenance

shall must , at a minimum, include the requirements of paragraphs (c)(1) through (c)( 9 8 ) of this section. (1) Daily monitoring of pressure drop across each baghouse cell to ensure pressure drop is within the normal operating range identified in the standard operat ing procedures manual.
(2 (1 ) Weekly confirmation that dust is being removed from hoppers through visual inspection or equivalent means of ensuring the proper functioning of remova l mechanisms.
( 3 2 ) Daily check of compressed air supply for pulse

- jet baghouses.
( 4 3 ) An appropriate methodology for monitoring cleaning cycles to ensure proper operation.
( 5 4 ) Monthly check of bag cleaning mechanisms for proper functioning through visual inspection or equivalent means.
( 6 5 ) Quarterly visual check of bag tension on reverse air

and shaker

- type baghouses to ensure that bags are not kinked (kneed or bent) or laying on their sides. Such checks are not required for shaker

- type baghouses using self

- tensioning (spring loaded) devices.
( 7 6 ) Quart erly confirmation of the physical integrity of the baghouse through visual inspection of the baghouse interior for
air leaks.
( 8 7 ) Quarterly inspection of fans for wear, material buildup, and corrosion through visual inspection, vibration
detectors, or equivalent means.
( 9 8 ) Except as provided in paragraph (h) of this section, continuous operation of a bag leak detection system. (d) The procedures specified in the standard operating procedures manual for maintenance shall must , at a minimum,
incl ude a preventative maintenance schedule that is consistent

### with the baghouse manufacturer's instructions for routine and long

- term maintenance. (e) The bag leak detection system required by paragraph
(c)( 9 8 ) of this section shall must meet the specifica tions and requirements of (e)(1) through (e)(8) of this section. (1) The bag leak detection system must be certified by the manufacturer to be capable of detecting particulate matter emissions at concentrations of 10 milligram per actual cubic
meter (0 .0044 grains per actual cubic foot) or less. (2) The bag leak detection system sensor must provide output of relative particulate matter loadings, and the owner or
operator shall must continuously record the output from the bag leak detection system. (3) The bag leak detection system must be equipped with an alarm system that will sound when an increase in relative particulate loading is detected over a preset level, and the
alarm must be located such that it can be heard or otherwise
determined by t he appropriate plant personnel. (4) Each bag leak detection system that works based on the
triboelectric effect shall must be installed, calibrated, and maintained in a manner consistent with guidance provided in the U.S. Environmental Protection Agency guidance document `` ” Fabric Filter Bag Leak Detection Guidance'' Guidance ” (EPA

- 454/R

- 98

- 015). Other bag leak detection systems shall must be installed, calibrated, and maintained in a manner consistent with the manufacturer's written specifications and rec ommendations. (5) The initial adjustment of the system shall must , at a minimum, consist of establishing the baseline output by adjusting the sensitivity (range) and the averaging period of the device, and establishing the alarm set points and the alarm delay time.

### (6) Following initial adjustment, the owner or operator

shall must not adjust the sensitivity or range, averaging period, alarm set points, or alarm delay time, except as detailed in the approved SOP required under paragraph (a) of this sec tion. In no event shall the sensitivity be increased by more than 100 percent or decreased more than 50 percent over a 365

- day period unless a responsible official certifies that the baghouse has been inspected and found to be in good operating condition. (7) For negative pressure, induced air baghouses, and positive pressure baghouses that are discharged to the atmosphere through a stack, the bag leak detector must be installed downstream of the baghouse and upstream of any wet acid gas scrubber.
( 8) Where multiple detectors are required, the system's instrumentation and alarm may be shared among detectors. (f) The standard operating procedures manual required by paragraph (a) of this section shall must include a corrective action plan that speci fies the procedures to be followed in the event of a bag leak detection system alarm. The corrective action plan shall must include
, at a minimum, procedures to be used to determine the cause of an alarm, as well as actions to
be taken to minimize emissions , which may include, but are not limited to, the following. (1) Inspecting the baghouse for air leaks, torn or broken bags or filter media, or any other condition that may cause an
increase in emissions. (2) Sealing off defective bags or filter med ia. (3) Replacing defective bags or filter media, or otherwise repairing the control device. (4) Sealing off a defective baghouse compartment.

### (5) Cleaning the bag leak detection system probe, or otherwise repairing or maintaining the bag leak detection
system. (6) Shutting down the process producing the particulate
emissions. (g) The percentage of total operating time the alarm on the bag leak detection system sounds in a 6

- month reporting period

shall must be calculated in order to dete rmine compliance with the five percent operating limit in Sec. § 63.1543( f g ). The percentage of time the alarm on the bag leak detection system

sounds shall s must be determined according to paragraphs (g)(1) through (g)( 5 3 ) of this section.
(1) Alarms th at occur due solely to a malfunction of the bag leak detection system shall not be included in the calculation. (2) Alarms that occur during startup, shutdown, or
malfunction shall not be included in the calculation if the
condition is described in the startup, shutdown, and malfunction plan and the owner or operator follows all the procedures in the plan defined for this condition.
(3 (1 ) For each alarm where the owner or operator initiates procedures to determine the cause of an alarm within 1 hour of the alarm, 1 hour of alarm time shall must be counted.
( 4 2 ) For each alarm where the owner or operator does not initiate procedures to determine the cause of the alarm within 1 hour of the alarm, alarm time will be counted as the actual

amount o f time taken by the owner or operator to initiate procedures to determine the cause of the alarm.
( 5 3 ) The percentage of time the alarm on the bag leak detection system sounds shall must be calculated as the ratio of
the sum of alarm times to the total operating time multiplied by

100.

### (h) Baghouses equipped with HEPA filters as a secondary filter used to control process or process fugitive sources subject to the lead emission standards in Sec. § 63.1543 are exempt from the requirement in Sec. 63.1543 paragraph (c)( 9) 8)of
this section to be equipped with a bag leak detector. The owner or operator of an affected source that uses a HEPA filter

shall must monitor and record the pressure drop across the HEPA filter system daily. I f the pressure drop is outsid e the limit(s) specified by the filter manufacturer, the owner or operator must take appropriate corrective measures, which may include, but not be limited to, the following: (1) Inspecting the filter and filter housing for air leaks

and torn or broken filters. (2) Replacing defective filter media, or otherwise repairing
the control device. (3) Sealing off a defective control device by routing air to

other comparable control devices. (4) Shutting down the process producing the particulate

em issions. (i) Owners and operators shall must monitor sinter machine building in

- draft to demonstrate continued compliance with the operating standard specified in Sec. § 63.1543( c d ) in accordance with either paragraph (i)(1), (i)(2), or (i)(3) of this se ction. (1) Owners and operators shall must check and record on a daily basis doorway in

- draft at each doorway in accordance with the methodology specified in Sec. § 63.1546(b). (2) Owners and operators shall must establish and maintain
baseline ventil ation parameters which result in a positive in

draft according to paragraphs (i)(2)(i) through (i)(2)(iv) of
this section. (i) Owners and operators shall must install, calibrate, maintain, and operate a monitoring device that continuously

### records the ac tual volumetric flow rate through each separately ducted hood; or install, calibrate, maintain, and operate a monitoring device that continuously records the volumetric flow rate at the control device inlet of each exhaust system ventilating the building. The flow rate monitoring device(s) can be installed in any location in the exhaust duct such that reproducible flow rate monitoring measurements will result. The flow rate monitoring device(s) shall must have an accuracy of plus or minus 10 percent over its t he normal process operating range and shall must be calibrated according to manufacturer's
instructions. (ii) During the initial demonstration of sinter building in

draft, and at any time the owner or operator wishes to re

establish the baseline ventila tion parameters, the owner or
operator shall must continuously record the volumetric flow rate through each separately ducted hood, or continuously record the
volumetric flow rate at the control device inlet of each exhaust system ventilating the building a nd record exhaust system damper positions. The owner or operator shall must determine the average volumetric flow rate(s) corresponding to the period of time the
in

- draft compliance determinations are being conducted. (iii) The owner or operator shall mu st maintain the volumetric flow rate(s) at or above the value(s) established during the most recent in

- draft determination at all times the sinter machine is in operation. Volumetric flow rate(s)

shall must be calculated as a 15

- minute average. (iv) If the volumetric flow rate is monitored at the control device inlet, the owner or operator shall must check and record damper positions daily to ensure they are in the positions they were in during the most recent in

- draft determination.

### (3) An owner or o perator may request an alternative monitoring method by following the procedures and requirements
in Sec. § 63.8(f) of the General Provisions.

Sec. (j) Each owner or operator of new or modified sources listed under §63.1543 (a)(1) through (a)( 9 ) and ( b) must install, calibrate, maintain, and operate a continuous emission monitoring system (CEMS) for measuring lead emissions and a continuous emission rate monitoring system (CERMS)subject to Performance Specification 6 of Appendix B to part 60.
(1) Each owner or operator of a source subject to the emissions limits for lead compounds under §63.1543(a)and (b) must install a CEMS for measuring lead emissions within 180 days of promulgation of performance specifications for lead CEMS. (i) Prior to pr omulgation of performance specifications for CEMS used to measure lead concentrations, an owner or operator must use the procedure described in §63.1546 (a)(1) through (a)(7) of this section to determine compliance.
(2) If a CEMS used to measure lead emissions is applicable, the owner or operator must install a CERMS with a sensor in a location that provides representative measurement of the exhaust gas flow rate at the sampling location of the CEMS used to measure lead emissions, taking into account the manufacturer’s recommendations. The flow rate sensor is that portion of the system that senses the volumetric flow rate and generates an output proportional to that flow rate. (i) The CERMS must be designed to measure the exhaust gas

flow rate over a range that extends from a value of at least 20 percent less than the lowest expected exhaust flow rate to a value of at least 20 percent greater than the highest expected exhaust gas flow rate.

### (ii) The CERMS must be equipped with a data acquisitio n and recording system that is capable of recording values over the entire range specified in paragraph (b)(2)(i) of this section. (iii) Each owner or operator must perform an initial relative accuracy test of the CERMS in accordance with the applicab le Performance Specification in Appendix B to part 60 of the chapter. (iv) Each owner or operator must operate the CERMS and record data during all periods of operation of the affected facility including periods of startup, shutdown, and malfunction, except for periods of monitoring system malfunctions, repairs associated with monitoring system malfunctions, and required monitoring system quality assurance or quality control activities (including, as applicable, calibration checks and required zero and span adjustments. (3) Each owner or operator must calculate the lead emissions rate in tons per year by summing all hours of CEMS data for a year to determine compliance with § 63.1543 (b). (i) When the CERMS are unable to provide quality assured

d ata the following applies: (A) When data are not available for periods of up to 48 hours, the highest recorded hourly emission rate from the previous 24 hours must be used. (B) When data are not available for 48 or more hours, the maximum daily em ission rate based on the previous 30 days must

be used.

**§ 63.1548**  **Notification requirements.**

(a) The owner or operator of a primary lead smelter
shall processor must comply with all of the notification Formatted: Font: Bold
Formatted: Font: Bold

### requirements of Sec. § 63.9 of subpart A, General Provisions as specified in Table 1 of this subpart

. (b) The owner or operator of a primary lead smelter
shall processor must submit the fugitive dust control standard operating procedures manual required under Sec. 63.1544(a) and

the standard operating procedures manual for baghouses required

under Sec. § 63.1547(a) to the Administrator or delegated authority along with a notification that the smelter primary lead

processor is seeking review and approval of these plans the
manual and procedures. Owners or operators of existing primary

lead smelters shall processor s must submit this notification no later than November 6, 2000. The owner or operator of a primary

lead smelter processor that commences construction or reconstruction after April 17, 1998, shall must submit this notification no later than 180 days before startup of the constructed or reconstructed primary lead smelter processor , but no sooner than September 2, 1999.

Sec. **§ 63.1549**  **Recordkeeping and reporting requirements.**

(a) The owner or operat or of a primary lead smelter
shall processor must comply with all of the recordkeeping requirements of Sec. § 63.10 of subpart A, General Provisions as specified in Table 1 of this subpart

. (b) In addition to the general records required by paragraph
(a) of this section, each owner or operator of a primary lead

smelter shall processor must maintain for a period of 5 years, records of the information listed in paragraphs (b)(1) through
(b)( 8 10 ) of this section. (1) Production records of the weight and l ead content of lead products, copper matte, and copper speiss. Formatted: Font: Bold
Formatted: Font: Bold

### (2) Records of the bag leak detection system output. (3) An identification of the date and time of all bag leak detection system alarms, the time that procedures to determine

the cause of the alarm were initiated, the cause of the alarm, an explanation of the actions taken, and the date and time the

cause of the alarm was corrected.
( 4 ) Any recordkeeping required as part of the practices described in the standard operating procedures manual for baghouses required under Sec. § 63. 1544 1547 (a ) for the control of fugitive dust emissions. ). (5) Any recorkeeping required as part of the practices described in the standard operating procedures manual for baghouses required under Sec. 63.15 47(a).
(6 ( 5 ) If an owner or operator chooses to demonstrate continuous compliance with the sinter building in

- draft requirement under Sec. § 63.1543( c d ) by employing the method
allowed in Sec. § 63. 1546 1547 (i)(1), the records of the daily doorway in

- draft checks, an identification of the periods when there was not a positive in

- draft, and an explanation of the
corrective actions taken.
( 7 6 ) If an owner or operator chooses to demonstrate continuous compliance with the sinter building in

- draft requi rement under Sec. § 63.1543( c d ) by employing the method
allowed in Sec. § 63. 1546 1547 (i)(2), the records of the output from the continuous volumetric flow monitor(s), an identification of the periods when the 15

- minute volumetric flow rate dropped below the minimum established during the most
recent in

- draft determination, and an explanation of the
corrective actions taken.
( 8 7 ) If an owner or operator chooses to demonstrate continuous compliance with the sinter building in

- draft requirement under Sec. § 6 3.1543( c d ) by employing the method

### allowed in Sec. § 63. 1546 1547 (i)(2), and volumetric flow rate is monitored at the baghouse inlet, records of the daily checks of damper positions, an identification of the days that the damper positions were not in the pos itions established during the most
recent in

- draft determination, and an explanation of the
corrective actions taken.
( 8 ) Records of the occurrence and duration of each malfunction of operation (i.e., process equipment) or the air pollution control equ ipment and monitoring equipment.
( 9 ) Records of actions taken during periods of malfunction to minimize emissions in accordance with §§63.1543(i) and
63.1544( d ), including corrective actions to restore malfunctioning process and air pollution control and monitoring equipment to its normal or usual manner of operation. (c) Records for the most recent 2 years of operation must be maintained on site. Records for the previous 3 years may be
maintained off site. (d) The owner or operator of a prima ry lead smelter
shall processor must comply with all of the reporting requirements of Sec. § 63.10 of subpart A, General Provisions as specified in Table 1 of this subpart

. (e) In addition to the information required under Sec.

§ 63.10 of the General Prov isions, the owner or operator

shall m us t provide semi

- annual reports containing the information specified in paragraphs (e)(1) through (e)( 7 9 ) of this section to the Administrator or designated authority. (1) The reports shall must include records of all alarms from the bag leak detection system specified in Sec. § 63.1547(e). (2) The reports shall must include a description of the actions taken following each bag leak detection system alarm
pursuant to Sec. § 63.1547(f).

### (3) The reports shall must in clude a calculation of the percentage of time the alarm on the bag leak detection system sounded during the reporting period pursuant to Sec.

§ 63.1547(g). (4) If an owner or operator chooses to demonstrate continuous compliance with the sinter building in

- draft requirement under Sec. § 63.1543( c d ) by employing the method
allowed in Sec. § 63. 1546 1547 (i)(1), the reports shall must contain an identification of the periods when there was not a positive in

- draft, and an explanation of the corrective actions

ta ken. (5) If an owner or operator chooses to demonstrate continuous compliance with the sinter building in

- draft requirement under Sec. § 63.1543( c d ) by employing the method
allowed in Sec. § 63. 1546 1547 (i)(2), the reports shall must
contain an identificat ion of the periods when the 15

- minute volumetric flow rate(s) dropped below the minimum established during the most recent in

- draft determination, and an explanation of the corrective actions taken. (6) If an owner or operator chooses to demonstrate

co ntinuous compliance with the sinter building in

- draft requirement under Sec. § 63.1543( c d ) by employing the method
allowed in Sec. § 63. 1546 1547 (i)(2), and volumetric flow rate is monitored at the baghouse inlet, the reports shall must contain
an identificati on of the days that the damper positions were not in the positions established during the most recent in

- draft determination, and an explanation of the corrective actions

taken. (7) The reports shall must contain a summary of the records maintained as p art of the practices described in the standard operating procedures manual for baghouses required under Sec.

### § 63.1547(a), including an explanation of the periods when the procedures were not followed and the corrective actions taken. (8) The reports sh all must contain a summary of the fugitive dust control measures performed during the required reporting period, including an explanation of any periods when the procedures outlined in the standard operating procedures manual required by Sec. § 63.154 4(a) we re not followed and the
corrective actions taken. The reports shall must not contain copies of the daily records required to demonstrate compliance with the requirements of the standard operating procedures manuals required under Secs. §§ 63.1544(a) and Sec. 63.1547(a).

Sec. 9) If there was a malfunction during the reporting period, the report shall also include the number, duration, and a brief description for each type of malfunction which occurred during the reporting period and which caused or may have caused any applicable emission limitation to be exceeded. The report must also include a description of actions taken by an owner or operator during a malfunction of an affected source to minimize emissions in accordance with §§63.1543(i) and 63.1544( d ), including actions taken to correct a malfunction.

**§ 63.1550**  **Delegation of authority**

(a) In delegating implementation and enforcement authority to a State under section 112(1) of the act, the authorities contained in paragraph (b) of this section shall must be retained by the Administrator and not transferred to a State. (b) Authorities which will not be delegated to States: no
restrictions. Formatted: Font: Bold
Formatted: Font: Bold

### § **63.1551 Affirmative defense for exceedance of emission limit**  **during malfunction.**
In response to an action to enforce the standards set forth in this subpart you may assert an affirmative defense to a claim for civil penalties for exceedances of such standards that are caused by malfunction, as defined at 40 CFR 63.2. Appropriate penalties may be asse ssed, however, if you fail to meet your burden of proving all of the requirements in the affirmative
defense. The affirmative defense shall not be available for claims for injunctive relief. (a) To establish the affirmative defense in any action to

enf orce such a limit, you must timely meet the notification requirements in paragraph (b) of this section, and must prove by a preponderance of evidence that: (1) The excess emissions: (i) Were caused by a sudden, infrequent, and unavoidable
failure o f air pollution control and monitoring equipment, process equipment, or a process to operate in a normal or usual

manner , and (ii) Could not have been prevented through careful planning, proper design or better operation and maintenance practices; and (iii) Did not stem from any activity or event that could have been foreseen and avoided, or planned for; and (iv) Were not part of a recurring pattern indicative of inadequate design, operation, or maintenance; and (2) Repairs were made as e xpeditiously as possible when the applicable emission limitations were being exceeded. Off

- shift and overtime labor were used, to the extent practicable to make these repairs; and

### (3) The frequency, amount and duration of the excess emissions (includi ng any bypass) were minimized to the maximum extent practicable during periods of such emissions; and (4) If the excess emissions resulted from a bypass of control equipment or a process, then the bypass was unavoidable to prevent loss of life, person al injury, or severe property damage; and (5) All possible steps were taken to minimize the impact of the excess emissions on ambient air quality, the environment and

human health; and (6) All emissions monitoring and control systems were kept
in operation if at all possible , consistent with safety and good air pollution control practices; and (7) All of the actions in response to the excess emissions were documented by properly signed, contemporaneous operating logs; and (8) At all time s, the facility was operated in a manner consistent with good practices for minimizing emissions; and (9) A written root cause analysis has been prepared , the purpose of which is to determine, correct and eliminate the primary causes of the malfunctio n and the excess emissions resulting from the malfunction event at issue. The analysis shall also specify, using best monitoring methods and engineering judgment, the amount of excess emissions that were
the result of the malfunction. (b) Notification. The owner or operator of the facility experiencing an exceedance of its emission limit(s) during a malfunction shall notify the Administrator by telephone or facsimile (FAX) transmission as soon as possible, but no later than two business days after the initi al occurrence of the malfunction, if it wishes to avail itself of an affirmative defense to civil penalties for that malfunction. The owner or

### operator seeking to assert an affirmative defense shall also submit a written report to the Administrator within 45 days of
the initial occurrence of the exceedance of the standard s in this subpart to demonstrate, with all necessary supporting documentation, that it has met the requirements set forth in paragraph ( a ) of this section. The owner or operator may seek an extension of this deadline for up to 30 additional days by submitting a written request to the Administrator before the expiration of the 45 day period. Until a request for an extension has been approved by the Administrator, the owner or operator is subj ect to the requirement to submit such report within 45 days of the initial occurrence of the exceedance.

Table 1 of Subpart TTT

-- – General Provisions Applicability to

Subpart TTT

**Reference Applies** 
**to subpart** 

**TTT** Reference

**Comment**

* * * * * * *

Sec. 63. 1 6(a), (b), (c) Yes

Sec. 63. 2 6 (d) Yes No Section reserved.

Sec. 63. 3 6(e)(1)(i) Yes No See 63.1543(i) and 63.1544( d ) for general duty requirement.

Sec. 63. 4 6(e)(1)(ii) Yes No

Sec. 63. 5 6(e)(1)(iii) Ye s Formatted: Space After: 10 pt, Don't add space between paragraphs of the same style, Line spacing: Double
Formatted: Font: Bold

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18" Formatted Table
Formatted: Font: Bold

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted Table
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"63.6(e)(2) No Section reserved.

63.6(e)(3) No

63.6(f)(1) No

Sec. 63.6(a), (b), (c), (e (f), (g), (i) and (j). 63.6(g) Yes

Sec. 63.6( d) and ( h) No No opacity limits in rule.

63.6(i) Yes

63.6(j) Yes

§63.7(a)

- (d) Yes

Sec. § 63.7 (e)(1) Yes No See 63.1546(c).

§63.7(e)(2)

- (e)(4) Yes

63.7(f), (g), (h) Yes

Sec. 63.8 (a)

- (b) Yes

63.8(c)(1)(i) No

63.8(c)(1)(ii) Yes

63.8(c)(1)(iii) No

63.8(c)(2)

- (d)(2) Yes

63.8(d)(3) Yes, except for last
sentence

63.8(e)

- (g) Yes

Se c. 63.9 (a ), ( ),( b ), ( ),( c ), (d), ( ),( e ), Yes Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted Table Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted Table Formatted: Centered
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted Table
Formatted: Centered
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted Table Formatted: Centered
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"( ),( g ), ( ),( h)(1) through (3), (h)(5) and (6), (i) and (j ). )

63.9(f) No

63.9(h)(4) No Reserved

63.10(b)(2)(i) No

Sec. 63. 9(f) and (h)(4 10(b)(2)(ii ) No No opacity or visible emission limits in rule. Se e 63.1549(b)(9) and (10) for recordkeeping of occurrence and duration of malfunctions and recordkeeping of actions taken during malfunction.

Sec. 63.10 (b)(2)(iii) Yes

63.10(b)(2)(iv)

- (b)(2)(v) No

63.10(b)(2)(vi)

- (b)(2)( xiv) Yes

63.(10)(b)(3) Yes

63.10(c)(1)

- (9) Yes

Sec. 63. 10(c)(10)

- ( 11 ) No Flares will not be used to comply with the emission limits. See 63.1549(b)(9) and (10) for recordkeeping of malfunctions.

Sec. 63. 10(c)( 12 through 63.15 )

- (c)(14) Yes

63.10(c)(15) No Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted Table Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted Table Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"
Formatted: Portuguese (Brazil)
Formatted: Portuguese (Brazil)

Formatted: Tab stops: Not at 0.64" + 1.27"

+ 1.91" + 2.54" + 3.18" + 3.82" + 4.45" + 5.09" + 5.73" + 6.36" + 7" + 7.63" + 8.27"

+ 8.91" + 9.54" + 10.18"63.10(d)(1)

- (4) Yes

63.10(d)(5) No See 63.1549(e)(9) for reporting of malfunctions.

63.10(e)

- ((f) Yes

* * * * * * *

[FR Doc. 

### 99

- 12757 Filed 6

- 3

- 99; 8:45 am] [INSERT FEDERAL REGISTER
NUMBER, DATE FILED AND TIME] ]

BILLING COD E 6560

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- M Formatted: Font: 10 pt

Formatted: Font: 10 pt