 1 For the reasons stated in the preamble, title 40,

chapter I, part 63 of the Code of the Federal Regulations is amended as follows:

PART 63[ AMENDED]

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

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

Subpart FFFF [ Amended]

2. Section 63.2435 is amended as follows:

a. Revising " product transfer racks" to read " transfer racks" in paragraph ( b) introductory text;

b. Revising paragraphs ( b)( 1)( i), ( ii), and ( 2);

c. Revising paragraph ( c) introductory text;

d. Revising paragraph ( c)( 4); and e. Adding new paragraph ( c)( 7).

§ 63.2435 Am I subject to the requirements of this subpart?

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( b) * * *

( 1) * * *

( i) An organic chemical( s) classified using the 1987 version of SIC code 282, 283, 284, 285, 286, 287, 289, or 2 386, except as provided in paragraph ( c)( 5) of this section.

( ii) An organic chemical( s) classified using the 1997 version of NAICS code 325, except as provided in paragraph ( c)( 5) of this section.

* * * * *

( 2) The MCPU processes, uses, or generates any of the organic HAP listed in section 112( b) of the CAA or hydrogen halide and halogen HAP, as defined in § 63.2550.

* * * * *

( c) The requirements in this subpart do not apply to the operations specified in paragraphs ( c)( 1) through ( 7)

of this section.

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( 4) Fabricating operations ( such as spinning or compressing a solid polymer into its end use); compounding operations ( in which blending, melting, and resolidification of a solid polymer product occur for the purpose of incorporating additives, colorants, or stabilizers); and extrusion and drawing operations ( converting an already produced solid polymer into a different shape by melting or mixing the polymer and then forcing it or pulling it through an orifice to create an 3 extruded product). An operation is not exempt if it involves processing with HAP solvent or if an intended purpose of the operation is to remove residual HAP monomer.

* * * * *

( 7) Carbon monoxide production.

* * * * *

3. Section 63.2445 is amended as follows:

a. Revising paragraph ( b) and the first sentence in paragraph ( c); and b. Adding new paragraphs ( d), ( e), and ( f).

§ 63.2445 When do I have to comply with this subpart?

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( b) If you have an existing source on November 10,

2003, you must comply with the requirements for existing sources in this subpart no later than May 10, 2008.

( c) You must meet the notification requirements in § 63.2515 according to the dates specified in that section and in subpart A of this part 63. * * *

( d) If you have a Group 2 emission point that becomes a Group 1 emission point after the compliance date for your affected source, you must comply with the Group 1 requirements beginning on the date the switch occurs. An initial compliance demonstration as specified in this 4 subpart must be conducted within 150 days after the switch occurs.

( e) If, after the compliance date for your affected source, hydrogen halide and halogen HAP emissions from process vents in a process increase to more than 1,000 lb/ yr, or HAP metals emissions from a process at a new affected source increase to more than 150 lb/ yr, you must comply with the applicable emission limits specified in Table 3 to this subpart and the associated compliance requirements beginning on the date the emissions exceed the applicable threshold. An initial compliance demonstration as specified in this subpart must be conducted within 150 days after the switch occurs.

( f) If you have a small control device for process vent or transfer rack emissions that becomes a large control device, as defined in § 63.2550( i), you must comply with monitoring and associated recordkeeping and reporting requirements for large control devices beginning on the date the switch occurs. An initial compliance demonstration as specified in this subpart must be conducted within 150 days after the switch occurs.

4. Section 63.2450 is amended as follows:

a. Revising paragraphs ( d), ( e), and ( f); 5 b. Revising the first sentence in paragraph ( h);

c. Revising paragraph ( k) introductory text,

paragraph ( k)( 3), paragraph ( k)( 4) introductory text, and paragraph ( k)( 4)( i); and d. Adding new paragraphs ( k)( 4)( iv), ( k)( 5), and ( k)( 6).

§ 63.2450 What are my general requirements for complying with this subpart?

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( d) Reserved ( e) Requirements for control devices. ( 1) Except when complying with § 63.2485, if you reduce organic HAP emissions by venting emissions through a closed vent system to any combination of control devices ( except a flare) or recovery devices, you must meet the requirements of § 63.982( c) and the requirements referenced therein.

( 2) Except when complying with § 63.2485, if you reduce organic HAP emissions by venting emissions through a closed vent system to a flare, you must meet the requirements of § 63.982( b) and the requirements referenced therein.

( 3) If you use a halogen reduction device to reduce hydrogen halide and halogen HAP emissions from halogenated 6 vent streams, you must meet the requirements of § 63.994 and the requirements referenced therein. If you use a halogen reduction device before a combustion device, you must determine the halogen atom emission rate prior to the combustion device according to the procedures in § 63.115( d)( 2)( v).

( f) Requirements for flare compliance assessments.

( 1) As part of a flare compliance assessment required in § 63.987( b), you have the option of demonstrating compliance with the requirements of § 63.11( b) by complying with the requirements in either § 63.11( b)( 6)( i) or § 63.987( b)( 3)( ii).

( 2) If you elect to meet the requirements in § 63.11( b)( 6)( i), you must keep flare compliance assessment records as specified in paragraphs ( f)( 2)( i) and ( ii) of this section.

( i) Keep records as specified in § 63.998( a)( 1)( i),

except that a record of the heat content determination is not required.

( ii) Keep records of the flare diameter, hydrogen content, exit velocity, and maximum permitted velocity.

Include these records in the flare compliance report required in § 63.999( a)( 2). 7 * * * * *

( h) Design evaluation. To determine the percent reduction of a small control device that is used to comply with an emission limit specified in Table 1, 2, 3, or 5 to this subpart, you may elect to conduct a design evaluation as specified in § 63.1257( a)( 1) instead of a performance test as specified in subpart SS of this part 63. * * *

* * * * *

( k) Continuous parameter monitoring. The provisions in paragraphs ( k)( 1) through ( 6) of this section apply in addition to the requirements for continuous parameter monitoring system ( CPMS) in subpart SS of this part 63.

* * * * *

( 3) As an alternative to continuously measuring and recording pH as specified in § § 63.994( c)( 1)( i) and 63.998( a)( 2)( ii)( D), you may elect to continuously monitor and record the caustic strength of the effluent. For halogen scrubbers used to control only batch process vents you may elect to monitor and record either the pH or the caustic strength of the scrubber effluent at least once per day.

( 4) As an alternative to the inlet and outlet temperature monitoring requirements for catalytic 8 incinerators as specified in § 63.988( c)( 2) and the related recordkeeping requirements specified in § 63.998( a)( 2)( ii)( B)( 2) and ( c)( 2)( ii), you may elect to comply with the requirements specified in paragraphs ( k)( 4)( i) through ( iv) of this section.

( i) Monitor and record the inlet temperature as specified in subpart SS of this part 63.

* * * * *

( iv) Recording the downstream temperature and temperature difference across the catalyst bed as specified in § 63.998( a)( 2)( ii)( B)( 2) and ( b)( 2)( ii) is not required.

( 5) For absorbers that control organic compounds and use water as the scrubbing fluid, you must conduct monitoring and recordkeeping as specified in paragraphs ( k)( 5)( i) through ( iii) of this section in addition to the monitoring and recordkeeping requirements specified in § § 63.990( c)( 1), 63.993( c)( 1), and 63.998( a)( 2)( ii)( C).

( i) You must use a flow meter capable of providing a continuous record of the absorber influent liquid flow.

( ii) You must determine gas stream flow using one of the procedures specified in § 63.994( c)( 1)( ii)( A) through ( D). 9 ( iii) You must record the absorber liquid to gas ratio averaged over the time period of any performance test.

( 6) For a control device with total inlet HAP emissions less than 1 tpy, you must establish an operating limit( s) for a parameter( s) that you will measure and record at least once per averaging period ( i. e., daily or block) to verify that the control device is operating properly. You may elect to measure the same parameter( s)

that is required for control devices that control inlet HAP emissions equal to or greater than 1 tpy. If the parameter will not be measured continuously, you must request approval of your proposed procedure in the precompliance report. You must identify the operating limit( s) and the measurement frequency, and you must provide rationale to support how these measurements demonstrate the control device is operating properly.

* * * * *

5. Section 63.2460 is amended as follows:

a. Revising paragraph ( b) introductory text and paragraphs ( b)( 1), ( b)( 2) and ( b)( 3);

b. Redesignating paragraph ( b)( 4) as paragraph ( b)( 5)

and revising " paragraph ( b)( 4)( i) or ( ii)" to read 10 " paragraph ( b)( 5)( i) or ( ii)" in redesignated paragraph ( b)( 5) introductory text;

c. Adding new paragraphs ( b)( 4), ( b)( 6), and ( b)( 7);

d. Revising paragraph ( c) introductory text,

paragraph ( c)( 1), paragraph ( c)( 2)( iii), and the first sentence in paragraph ( c)( 2)( v); and e. Adding new paragraphs ( c)( 8) and ( c)( 9).

§ 63.2460 What requirements must I meet for batch process vents?

* * * * *

( b) Group status. If a process has batch process vents, as defined in § 63.2550, you must determine the group status of the batch process vents by determining and summing the uncontrolled organic HAP emissions from each of the batch process vents within the process using the procedures specified in § 63.1257( d)( 2)( i) and ( ii), except as specified in paragraphs ( b)( 1) through ( 7) of this section.

( 1) To calculate emissions caused by the heating of a vessel without a process condenser to a temperature lower than the boiling point, you must use the procedures in § 63.1257( d)( 2)( i)( C)( 3). 11 ( 2) To calculate emissions from depressurization of a vessel without a process condenser, you must use the procedures in § 63.1257( d)( 2)( i)( D)( 10).

( 3) To calculate emissions from vacuum systems for the purposes of this subpart, the receiving vessel is part of the vacuum system, and terms used in Equation 33 to 40 CFR part 63, subpart GGG, are defined as follows:

Psystem = absolute pressure of the receiving vessel; Pi = partial pressure of the HAP determined at the exit temperature and exit pressure conditions of the condenser or at the conditions of the dedicated receiver; Pj = partial pressure of condensables ( including HAP) determined at the exit temperature and exit pressure conditions of the condenser or at the conditions of the dedicated receiver; MWHAP = molecular weight of the HAP determined at the exit temperature and exit pressure conditions of the condenser or at the conditions of the dedicated receiver.

( 4) To calculate uncontrolled emissions when a vessel is equipped with a process condenser, you must use the procedures in § 63.1257( d)( 3)( i)( B), except as specified in paragraphs ( b)( 4)( i) through ( vii) of this section.

( i) You must determine the flowrate of gas ( or volume of gas), partial pressures of condensables, temperature ( T), and HAP molecular weight ( MWHAP) at the exit temperature and exit pressure conditions of the condenser or at the conditions of the dedicated receiver. 12 ( ii) You must assume that all of the components contained in the condenser exit vent stream are in equilibrium with the same components in the exit condensate stream ( except for noncondensables).

( iii) You must perform a material balance for each component, and it must be determine through iterative solutions if more than one condensable is present.

( iv) For the emissions from gas evolution, the term for time, t, must be used in Equation 12 to 40 CFR part 63,

subpart GGG.

( v) Emissions from empty vessel purging shall be calculated using Equation 36 to 40 CFR part 63, subpart GGG and the exit temperature and exit pressure conditions of the condenser or the conditions of the dedicated receiver.

( vi) You must conduct an engineering assessment as specified in § 63.1257( d)( 2)( ii) for each emission episode that is not due to vapor displacement, purging, heating,

depressurization, vacuum operations, gas evolution, air drying, or empty vessel purging. The requirements of paragraphs ( b)( 3) through ( 4) of this section shall apply.

( vii) You may elect to conduct an engineering assessment if you can demonstrate to the Administrator that the methods in § 63.1257( d)( 3)( i)( B) are not appropriate. 13 * * * * *

( 6) You may change from Group 2 to Group 1 in accordance with either paragraph ( b)( 6)( i) or ( ii) of this section. You must comply with the requirements of this section and submit the test report in the next Compliance report.

( i) You may switch at anytime after operating as Group 2 for at least one year so that you can show compliance with the 10,000 lb/ yr threshold for Group 2 batch process vents for at least 365 days before the switch. You may elect to start keeping records of emissions from Group 2 batch process vents before the compliance date. Report a switch based on this provision in your next compliance report in accordance with § 63.2520( e)( 10)( i).

( ii) If the conditions in paragraph ( b)( 6)( i) of this section are not applicable, you must provide a 60 day advance notice in accordance with § 63.2520( e)( 10)( ii)

before switching.

( 7) As an alternative to determining the uncontrolled organic HAP emissions as specified in § 63.1257( d)( 2)( i) and ( ii), you may elect to demonstrate that non reactive organic HAP usage in a process is less than 10,000 lb/ yr. 14 You must provide data and supporting rationale in your notification of compliance status report explaining why the non reactive organic HAP usage will be less than 10,000 lb/ yr. You must keep records of the non reactive organic HAP usage as specified in § 63.2525( e)( 2) and include information in compliance reports as specified in § 63.2520( e)( 5)( iv).

( c) Exceptions to the requirements in subparts SS and WW of this part 63 are specified in paragraphs ( c)( 1)

through ( 9) of this section.

( 1) Process condensers. Process condensers, as defined in § 63.2550( i), are not considered to be control devices for batch process vents. You must determine whether a condenser is a control device for a batch process vent or a process condenser from which the uncontrolled HAP emissions are evaluated as part of the initial compliance demonstration for each MCPU and report the results with supporting rationale in your notification of compliance status report.

( 2) * * *

( iii) As an alternative to conducting a performance test or design evaluation to demonstrate initial compliance with a percent reduction requirement for a condenser, you 15 may determine controlled emissions using the procedures specified in § 63.1257( d)( 3)( i)( B) and paragraphs ( b)( 3)

through ( 4) of this section.

* * * * *

( v) If a process condenser is used for any boiling operations, you must demonstrate that it is properly operated according to the procedures specified in § 63.1257( d)( 2)( i)( C)( 4)( ii) and ( d)( 3)( iii)( B), and the demonstration must occur only during the boiling operation.

* * *

* * * * *

( 5) Reserved * * * * *

( 8) Terminology. When the term " storage vessel" is used in subpart WW of this part 63, the term " process tank," as defined in § 63.2550( i), applies for the purposes of this section.

( 9) Requirements for a biofilter. If you use a biofilter to meet either the 95 percent reduction requirement or outlet concentration requirement specified in Table 2 to this subpart, you must meet the requirements specified in paragraphs ( c)( 9)( i) through ( iv) of this section. 16 ( i) Operational requirements. The biofilter must be operated at all times when emissions are vented to it.

( ii) Performance tests. To demonstrate initial compliance, you must conduct a performance test according to the procedures in § 63.997 and paragraphs ( c)( 9)( ii)( A)

through ( D) of this section. The design evaluation option for small control devices is not applicable if you use a biofilter.

( A) Keep up to date, readily accessible continuous records of either the biofilter bed temperature averaged over the full period of the performance test or the outlet total organic HAP or TOC concentration averaged over the full period of the performance test. Include these data in your notification of compliance status report as required by § 63.999( b)( 3)( ii).

( B) Record either the percent reduction of total organic HAP achieved by the biofilter determined as specified in § 63.997( e)( 2)( iv) or the concentration of TOC or total organic HAP determined as specified in § 63.997( e)( 2)( iii) at the outlet of the biofilter, as applicable.

( C) If you monitor the biofilter bed temperature, you may elect to use multiple thermocouples in representative 17 locations throughout the biofilter bed and calculate the average biofilter bed temperature across these thermocouples prior to reducing the temperature data to 15 minute ( or shorter) averages for purposes of establishing operating limits for the biofilter. If you use multiple thermocouples, include your rationale for their site selection in your notification of compliance status report.

( D) Submit a performance test report as specified in § 63.999( a)( 2)( i) and ( ii). Include the records from paragraph ( c)( 9)( ii)( B) of this section in your performance test report.

( iii) Monitoring requirements. Use either a biofilter bed temperature monitoring device ( or multiple devices) capable of providing a continuous record or an organic monitoring device capable of providing a continuous record. Keep records of temperature or other parameter monitoring results as specified in § 63.998( b) and ( c), as applicable. General requirements for monitoring are contained in § 63.996. If you monitor temperature, the operating temperature range must be based on only the temperatures measured during the performance test; these data may not be supplemented by engineering assessments or manufacturer's recommendations as otherwise allowed in 18 § 63.999( b)( 3)( ii)( A). If you establish the operating range ( minimum and maximum temperatures) using data from previous performance tests in accordance with § 63.996( c)( 6),

replacement of the biofilter media with the same type of media is not considered a process change under § 63.997( b)( 1). You may expand your biofilter bed temperature operating range by conducting a repeat performance test that demonstrates compliance with the 95 percent reduction requirement or outlet concentration limit, as applicable.

( iv) Repeat performance tests. You must conduct a repeat performance test using the applicable methods specified in § 63.997 within 2 years following the previous performance test and within 150 days after each replacement of any portion of the biofilter bed media with a different type of media or each replacement of more than 50 percent ( by volume) of the biofilter bed media with the same type of media.

6. Section 63.2465 is amended by revising the section heading, paragraph ( b), and paragraph ( d) to read as follows:

§ 63.2465 What requirements must I meet for process vents that emit hydrogen halide and halogen HAP or HAP metals? 19 * * * * *

( b) If any process vents within a process emit hydrogen halide and halogen HAP, you must determine and sum the uncontrolled hydrogen halide and halogen HAP emissions from each of the process vents within the process using the procedures specified in § 63.1257( d)( 2)( i) and/ or ( ii), as appropriate. When 63.1257( d)( 2)( ii)( E) requires documentation to be submitted in the precompliance report,

it means the notification of compliance status report for the purposes of this paragraph.

* * * * *

( d) To demonstrate compliance with the emission limit in Table 3 to this subpart for HAP metals at a new source,

you must comply with paragraphs ( d)( 1) through ( 3) of this section.

( 1) Determine the mass emission rate of HAP metals based on process knowledge, engineering assessment, or test data.

( 2) Conduct an initial performance test of each control device that is used to comply with the emission limit for HAP metals specified in Table 3 to this subpart.

Conduct the performance test according to the procedures in § 63.997. Use Method 29 of appendix A of 40 CFR part 60 to 20 determine the HAP metals at the inlet and outlet of each control device, or use Method 5 of appendix A of 40 CFR part 60 to determine the total particulate matter at the inlet and outlet of each control device. You have demonstrated initial compliance if the overall reduction of either HAP metals or total PM from the process is greater than or equal to 97 percent by weight.

( 3) Comply with the monitoring requirements specified in § 63.1366( b)( 1)( xi) for each fabric filter used to control HAP metals.

7. Section 63.2470 is amended as follows:

a. Removing and reserving paragraph ( b); and b. Revising paragraph ( e)( 2).

The revisions read as follows:

§ 63.2470 What requirements must I meet for storage tanks?

* * * * *

( e) * * *

( 2) To comply with § 63.1253( f)( 6)( i), the owner or operator of an offsite cleaning or reloading facility must comply with § § 63.2445 through 63.2550 instead of complying with § 63.1253( f)( 7)( ii), except as specified in paragraph ( e)( 2)( i) or ( ii) of this section. 21 ( i) The reporting requirements in § 63.2520 do not apply to the owner or operator of the offsite cleaning or reloading facility.

( ii) As an alternative to complying with § § 63.2445 through 63.2550, the owner or operator of an offsite cleaning or reloading facility may comply with any other subpart of this part 63 as specified in § 63.2535( a)( 2).

* * * * *

8. Section 63.2475 is amended by removing paragraph ( c).

9. Section 63.2480 is revised to read as follows:

§ 63.2480 What requirements must I meet for equipment leaks?

( a) You must meet each requirement in Table 6 to this subpart that applies to your equipment leaks, except as specified in paragraphs ( b) through ( d) of this section.

( b) If you comply with either subpart H or subpart UU of this part 63, you may elect to comply with the provisions in paragraphs ( b)( 1) through ( 5) of this section as an alternative to the referenced provisions in subpart H or subpart UU.

( 1) The requirements for pressure testing in § 63.179( b) or § 63.1036( b) may be applied to all processes,

not just batch processes. 22 ( 2) For the purposes of this subpart, pressure testing for leaks in accordance with § 63.179( b) or § 63.1036( b) is not required after reconfiguration of an equipment train if flexible hose connections are the only disturbed equipment.

( 3) For an existing source, you are not required to develop an initial list of identification numbers for connectors as would otherwise be required under § 63.1022( b)( 1).

( 4) For connectors in gas/ vapor and light liquid service at an existing source, you may elect to comply with the requirements in § 63.169 or § 63.1029 for connectors in heavy liquid service, including all associated recordkeeping and reporting requirements, rather than the requirements of § 63.174 or § 63.1027.

( 5) For pumps in light liquid service in an MCPU that has no continuous process vents and is part of an existing source, you may elect to consider the leak definition that defines a leak to be 10,000 parts per million or greater as an alternative to the values specified in § 63.1026( b)( 2)( i)

through ( iii).

( c) If you comply with 40 CFR part 65, subpart F, you may elect to comply with the provisions in paragraphs 23 ( c)( 1) through ( 9) of this section as an alternative to the referenced provisions in 40 CFR part 65, subpart F.

( 1) The requirements for pressure testing in § 65.117( b) may be applied to all processes, not just batch processes.

( 2) For the purposes of this subpart, pressure testing for leaks in accordance with § 65.117( b) is not required after reconfiguration of an equipment train if flexible hose connections are the only disturbed equipment.

( 3) For an existing source, you are not required to develop an initial list of identification numbers for connectors as would otherwise be required under § 65.103( b)( 1).

( 4) You may elect to comply with the monitoring and repair requirements specified in § 65.108( e)( 3) as an alternative to the requirements specified in § 65.108( a)

through ( d) for any connectors at your affected source.

( 5) For pumps in light liquid service in an MCPU that has no continuous process vents and is part of an existing source, you may elect to consider the leak definition that defines a leak to be 10,000 parts per million or greater as an alternative to the values specified in § 65.107( b)( 2)( i)

through ( iii). 24 ( 6) When 40 CFR part 65, subpart F refers to the implementation date specified in § 65.1( f), it means the compliance date specified in § 63.2445.

( 7) When § § 65.105( f) and 65.117( d)( 3) refer to § 65.4,

it means § 63.2525.

( 8) When § 65.120( a) refers to § 65.5( d), it means § 63.2515.

( 9) When § 65.120( b) refers to § 65.5( e), it means § 63.2520.

( d) The provisions of this section do not apply to bench scale processes, regardless of whether the processes are located at the same plant site as a process subject to the provisions of this subpart.

10. Section 63.2485 is amended by revising paragraph ( a) and paragraphs ( c)( 1) through ( 3) and by adding new paragraphs ( m), ( n), and ( o) to read as follows:

§ 63.2485 What requirements must I meet for wastewater streams and liquid streams within an MCPU?

( a) You must meet each requirement in Table 7 to this subpart that applies to your wastewater streams and liquid streams in open systems within an MCPU, except as specified in paragraphs ( b) through ( o) of this section.

* * * * * 25 ( c) * * *

( 1) The total annual average concentration of compounds in Table 8 to this subpart is greater than or equal to 10,000 ppmw at any flowrate, and the total annual load of compounds in Table 8 to this subpart is greater than or equal to 200 lb/ yr.

( 2) The total annual average concentration of compounds in Table 8 to this subpart is greater than or equal to 1,000 ppmw, and the annual average flowrate is greater than or equal to 1 l/ min.

( 3) The combined total annual average concentration of compounds in Tables 8 and 9 to this subpart is greater than or equal to 30,000 ppmw, and the combined total annual load of compounds in Tables 8 and 9 to this subpart is greater than or equal to 1 tpy.

* * * * *

( m) When § 63.132( f) refers to " a concentration of greater than 10,000 ppmw of Table 9 compounds," it means " a concentration of greater than 30,000 ppmw of total partially soluble HAP ( PSHAP) and soluble HAP ( SHAP) or greater than 10,000 ppmw of PSHAP" for the purposes of this subpart. 26 ( n) Alternative requirements for wastewater that is Group 1 for soluble HAP only. The option specified in this paragraph ( n) applies to wastewater that is Group 1 for soluble HAP in accordance with paragraph ( c)( 3) of this section and is discharged to biological treatment. Except as provided in paragraph ( n)( 4) of this section, this option does not apply to wastewater that is Group 1 for partially soluble HAP in accordance with paragraph ( c)( 1),( 2), or ( 4) of this section. For wastewater that is Group 1 for soluble HAP, you need not comply with § § 63.133 through 63.137 for any equalization unit, neutralization unit, and/ or clarifier prior to the activated sludge unit,

and you need not comply with the venting requirements in § 63.136( e)( 2)( ii)( A) for lift stations with a volume larger than 10,000 gal, provided you comply with the requirements specified in paragraphs ( n)( 1) through ( 3) of this section and all otherwise applicable requirements specified in Table 7 to this subpart. For this option, the treatment requirements in § 63.138 and the performance testing requirements in § 63.145 do not apply to the biological treatment unit, except as specified in paragraphs ( n)( 2)( i)

through ( iv) of this section. 27 ( 1) Wastewater must be hard piped between the equalization unit, clarifier, and activated sludge unit.

This requirement does not apply to the transfer between any of these types of units that are part of the same structure and one unit overflows into the next.

( 2) Calculate the destruction efficiency of the biological treatment unit using Equation 1 of this section in accordance with the procedures described in paragraphs ( n)( 2)( i) through ( vi) of this section. You have demonstrated initial compliance if E is greater than or equal to 90 percent.

where:

E = Destruction efficiency of total PSHAP and SHAP for the biological treatment unit including the equalization unit, neutralization unit, and/ or clarifier, percent QMWa = mass flow rate of total PSHAP and SHAP compounds entering the equalization unit ( or whichever of the three types of units is first), kg/ hr QMGe = mass flow rate of total PSHAP and SHAP compounds emitted from the equalization unit, kg/ hr QMGn = mass flow rate of total PSHAP and SHAP compounds emitted from the neutralization unit, kg/ hr QMGc = mass flow rate of total PSHAP and SHAP compounds emitted from the clarifier, kg/ hr ( )( ) ) 1 . Eq ( 100 QMW F QMG QMG QMG QMW E a bio c n e a ×       = 28 Fbio = Site specific fraction of PSHAP and SHAP compounds biodegraded in the biological treatment unit ( i) Include all PSHAP and SHAP compounds in both Group 1 and Group 2 wastewater streams from all MCPUs,

except you may exclude any compounds that meet the criteria specified in § 63.145( a)( 6)( ii) or ( iii).

( ii) Conduct the demonstration under representative process unit and treatment unit operating conditions in accordance with § 63.145( a)( 3) and ( 4).

( iii) Determine PSHAP and SHAP concentrations and the total wastewater flow rate at the inlet to the equalization unit in accordance with § 63.145( f)( 1) and ( 2). References in § 63.145( f)( 1) and ( 2) to RMR and AMR do not apply for the purposes of this section.

( iv) Determine Fbio for the activated sludge unit as specified in § 63.145( h), except as specified in paragraph ( n)( 2)( iv)( A) or ( B) of this section.

( A) If the biological treatment process meets both of the requirements specified in § 63.145( h)( 1)( i) and ( ii),

you may elect to replace the Fbio term in Equation 1 of this section with the numeral " 1."

( B) You may elect to assume fbio is zero for any compounds on List 2 of Table 36 in subpart G. 29 ( v) Determine QMGe, QMGn, and QMGc using EPA's WATER9 model or the most recent update to this model, and conduct testing or use other procedures to validate the modeling results.

( vi) Submit the data and results of your demonstration, including both a description of and the results of your WATER9 modeling validation procedures, in your notification of compliance status report as specified in § 63.2520( d)( 2)( ii).

( 3) As an alternative to the venting requirements in § 63.136( e)( 2)( ii)( A), a lift station with a volume larger than 10,000 gal may have openings necessary for proper venting of the lift station. The size and other design characteristics of these openings may be established based on manufacturer recommendations or engineering judgment for venting under normal operating conditions. You must describe the design of such openings and your supporting calculations and other rationale in your notification of compliance status report.

( 4) For any wastewater streams that are Group 1 for both PSHAP and SHAP, you may elect to meet the requirements specified in Table 7 to this subpart for the PSHAP and then comply with paragraphs ( n)( 1) through ( 3) of this section 30 for the SHAP in the wastewater system. You may determine the SHAP mass removal rate, in kg/ hr, in treatment units that are used to meet the requirements for PSHAP and add this amount to both the numerator and denominator in equation 1 of this section.

( o) Compliance records. For each CPMS used to monitor a nonflare control device for wastewater emissions,

you must keep records as specified in § 63.998( c)( 1) in addition to the records required in § 63.147( d).

11. Section 63.2495 is amended by revising paragraph ( b)( 1) to read as follows:

§ 63.2495 How do I comply with the alternative pollution prevention standard?

* * * * *

( b) * * *

( 1) You must comply with the emission limitations and work practice standards contained in Tables 1 through 7 of this subpart for all HAP that are generated in the MCPU and that are not included in consumption, as defined in § 63.2550. If any vent stream routed to the combustion control is a halogenated vent stream, as defined in § 63.2550, then hydrogen halides that are generated as a result of combustion control must be controlled according 31 to the requirements of § 63.994 and the requirements referenced therein.

* * * * *

12. Section 63.2520 is amended as follows:

a. Revising paragraph ( c)( 4);

b. Revising paragraph ( d)( 2)( i);

c. Revising paragraphs ( e)( 5) introductory text,

( e)( 5)( ii)( C), and ( e)( 5)( iii)( K) and adding new paragraph ( e)( 5)( iv);

d. Revising paragraph ( e)( 9); and e. Revising the first two sentences of paragraph ( e)( 10)( i) and paragraph ( e)( 10)( ii)( C).

§ 63.2520 What reports must I submit and when?

* * * * *

( c) * * *

( 4) Data and rationale used to support an engineering assessment to calculate uncontrolled emissions in accordance with § 63.1257( d)( 2)( ii). This requirement does not apply to calculations of hydrogen halide and halogen HAP emissions as specified in § 63.2465( b), to determinations that the total HAP concentration is less than 50 ppmv, or if you use previous test data to establish the uncontrolled emissions. 32 ( d) * * *

( 2) * * *

( i) The results of any applicability determinations,

emission calculations, or analyses used to identify and quantify HAP usage or HAP emissions from the affected source.

* * * * *

( ix) Records as specified in § 63.2535( l)( 1) through ( 3) of process units used to create a PUG and calculations of the initial primary product of the PUG.

( e) * * *

( 5) The compliance report must contain the information on deviations, as defined in § 63.2550,

according to paragraphs ( e)( 5)( i), ( ii), ( iii), and ( iv) of this section.

* * * * *

( ii) * * *

( C) Operating logs of processes with batch vents from batch operations for the day( s) during which the deviation occurred, except operating logs are not required for deviations of the work practice standards for equipment leaks.

( iii) * * * 33 ( K) Operating logs of processes with batch vents from batch operations for each day( s) during which the deviation occurred.

* * * * *

( iv) If you documented in your notification of compliance status report that an MCPU has Group 2 batch process vents because the non reactive HAP usage is less than 10,000 lb/ yr, the total uncontrolled organic HAP emissions from the batch process vents in an MCPU will be less than 1,000 lb/ yr for the anticipated number of standard batches, or total uncontrolled hydrogen halide and halogen HAP emissions from all batch process vents and continuous process vents in a process are less than 1,000 lb/ yr, include the records associated with each calculation required by § 63.2525( e) that exceeds an applicable HAP usage or emissions threshold.

* * * * *

( 9) Applicable records and information for periodic reports as specified in referenced subparts F, G, SS, UU,

WW, and GGG of this part and subpart F of 40 CFR part 65.

( 10) * * *

( i) Except as specified in paragraph ( e)( 10)( ii) of this section, whenever you make a process change, or change 34 any of the information submitted in the notification of compliance status report or a previous compliance report,

that is not within the scope of an existing operating scenario, you must document the change in your compliance report. A process change creates a new MCPU and does not include moving within a range of conditions identified in the standard batch, and a nonstandard batch does not constitute a process change.

* * *

( ii) * * *

( C) A change from Group 2 to Group 1 for any emission point except for batch process vents that meet the conditions specified in § 63.2460( b)( 6)( i).

13. Section 63.2525 is amended by revising paragraphs ( a), ( c), and ( e) to read as follows:

§ 63.2525 What records must I keep?

( a) Each applicable record required by subpart A of this part 63 and in referenced subparts F, G, SS, UU, WW,

and GGG of this part 63 and in referenced subpart F of 40 CFR part 65.

* * * * *

( c) A schedule or log of operating scenarios for processes with batch vents from batch operations updated 35 each time a different operating scenario is put into effect.

* * * * *

( e) The information specified in paragraph ( e)( 2),

( 3), or ( 4) of this section, as applicable, for each process with Group 2 batch process vents or uncontrolled hydrogen halide and halogen HAP emissions from the sum of all batch and continuous process vents less than 1,000 lb/ yr. No records are required for situations described in paragraph ( e)( 1) of this section.

( 1) No records are required if you documented in your notification of compliance status report that the MCPU meets any of the situations described in paragraph ( e)( 1)( i), ( ii), or ( iii) of this section.

( i) The MCPU does not process, use, or generate HAP.

( ii) You control the Group 2 batch process vents using a flare that meets the requirements of § 63.987.

( iii) You control the Group 2 batch process vents using a control device for which your determination of worst case for initial compliance includes the contribution of all Group 2 batch process vents.

( 2) If you documented in your notification of compliance status report that an MCPU has Group 2 batch 36 process vents because the non reactive organic HAP usage is less than 10,000 lb/ yr, as specified in § 63.2460( b)( 7), you must keep records of the amount of HAP material used, and calculate the daily rolling annual sum of the amount used no less frequently than monthly. If a record indicates usage exceeds 10,000 lb/ yr, you must estimate emissions for the preceding 12 months based on the number of batches operated and the estimated emissions for a standard batch,

and you must begin recordkeeping as specified in paragraph ( e)( 4) of this section. After 1 year, you may revert to recording only usage if the usage during the year is less than 10,000 lb.

( 3) If you documented in your notification of compliance status report that total uncontrolled organic HAP emissions from the batch process vents in an MCPU will be less than 1,000 lb/ yr for the anticipated number of standard batches, then you must keep records of the number of batches operated and calculate a daily rolling annual sum of batches operated no less frequently than monthly.

If the number of batches operated results in organic HAP emissions that exceed 1,000 lb/ yr, you must estimate emissions for the preceding 12 months based on the number of batches operated and the estimated emissions for a 37 standard batch, and you must begin recordkeeping as specified in paragraph ( e)( 4) of this section. After one year, you may revert to recording only the number of batches if the number of batches operated during the year results in less than 1,000 lb of organic HAP emissions.

( 4) If you meet none of the conditions specified in paragraphs ( e)( 1) through ( 3) of this section, you must keep records of the information specified in paragraphs ( e)( 4)( i) through ( iv) of this section.

( i) A record of the day each batch was completed and/ or the operating hours per day for continuous operations with hydrogen halide and halogen emissions.

( ii) A record of whether each batch operated was considered a standard batch.

( iii) The estimated uncontrolled and controlled emissions for each batch that is considered to be a nonstandard batch.

( iv) Records of the daily 365 day rolling summations of emissions, or alternative records that correlate to the emissions ( e. g., number of batches), calculated no less frequently than monthly.

* * * * * 38 14. Section 63.2535 is amended by revising paragraphs ( a) and ( k) to read as follows:

§ 63.2535 What compliance options do I have if part of my plant is subject to both this subpart and another subpart?

( a) Compliance with other subparts of this part 63.

( 1) If you have an MCPU that includes a batch process vent that also is part of a CMPU as defined in subparts F and G of this part 63, you must comply with the emission limits;

operating limits; work practice standards; and the compliance, monitoring, reporting, and recordkeeping requirements for batch process vents in this subpart, and you must continue to comply with the requirements in subparts F, G, and H of this part 63 that are applicable to the CMPU and associated equipment.

( 2) After the compliance dates specified in § 63.2445,

at an offsite reloading or cleaning facility subject to § 63.1253( f), as referenced from § 63.2470( e), compliance with the monitoring, recordkeeping, and reporting provisions of any other subpart of this part 63 constitutes compliance with the provisions of § 63.1253( f)( 7)( ii) or ( iii). You must identify in your notification of compliance status report required by § 63.2520( d) the 39 subpart of this part 63 with which the owner or operator of the offsite reloading or cleaning facility complies.

* * * * *

( k) Compliance with 40 CFR part 60, subpart VV, and 40 CFR part 61, subpart V. After the compliance date specified in § 63.2445, if you have an affected source with equipment to which this subpart does not apply, but which is subject to the requirements of 40 CFR part 60, subpart VV, or 40 CFR part 61, subpart V, you may elect to apply this subpart to all such equipment. If you elect this method of compliance, you must consider all total organic compounds, minus methane and ethane, in such equipment for purposes of compliance with this subpart, as if they were organic HAP. Compliance with the provisions of this subpart, in the manner described in this paragraph ( k),

will constitute compliance with 40 VFR part 60, subpart VV and 40 CFR part 61, subpart V, as applicable.

* * * * *

15. Section 63.2550 is amended as follows:

a. Revising paragraph ( b);

b. Revising the last sentence in paragraph ( i)

introductory text; 40 c. Revising paragraph ( 8) in the definition of the term " batch process vent" in paragraph ( i);

d. Adding new paragraphs ( 6) and ( 7) to the definition of the term " continuous process vent" in paragraph ( i);

e. Revising the definition of the term " Group 1 continuous process vent" in paragraph ( i);

f. Revising the definition of the term " isolated intermediate" in paragraph ( i);

g. Adding new paragraph ( 6) to the definition of the term " miscellaneous organic chemical manufacturing process"

in paragraph ( i);

h. Revising the definition of the term " recovery device" in paragraph ( i);

i. Revising the definition of the term " surge control vessel" in paragraph ( i);

j. Revising the introductory text of the definition of the term " wastewater" in paragraph ( i); and k. Adding, in alphabetical order, new definitions for the terms " biofilter," " continuous operation," " emission point," " halogen atoms," " HAP metals," " point of determination," and " process condenser" in paragraph ( i).

§ 63.2550 What definitions apply to this subpart? 41 * * * * *

( b) For an affected source complying with the requirements in 40 CFR part 65, subpart F, the terms used in this subpart and in 40 CFR part 65, subpart F have the meaning given to them in § 65.2.

* * * * *

( i) * * * If a term is defined in § 63.2,

§ 63.101, § 63.111, § 63.981, § 63.1020, § 63.1061, § 63.1251, or § 65.2 and in this paragraph ( i), the definition in this paragraph ( i) applies for the purposes of this subpart.

* * * * *

Batch process vent * * *

( 8) Emission streams from emission episodes that are undiluted and uncontrolled containing less than 50 ppmv HAP are not part of any batch process vent. A vent from a unit operation, or a vent from multiple unit operations that are manifolded together, from which total uncontrolled HAP emissions are less than 200 lb/ yr is not a batch process vent; emissions for all emission episodes associated with the unit operation( s) must be included in the determination of the total mass emitted. The HAP concentration or mass emission rate may be determined using any of the following:

process knowledge that no HAP are present in the emission 42 stream; an engineering assessment as discussed in § 63.1257( d)( 2)( ii), except that you do not need to demonstrate that the equations in § 63.1257( d)( 2)( i) do not apply, and the precompliance reporting requirements specified in § 63.1257( d)( 2)( ii)( E) do not apply for the purposes of this demonstration; equations specified in § 63.1257( d)( 2)( i), as applicable; test data using Method 18 of 40 CFR part 60, appendix A; or any other test method that has been validated according to the procedures in Method 301 of appendix A of this part.

* * * * *

Biofilter means an enclosed control system such as a tank or series of tanks with a fixed roof that contact emissions with a solid media ( such as bark) and use microbiological activity to transform organic pollutants in a process vent stream to innocuous compounds such as carbon dioxide, water, and inorganic salts. Wastewater treatment processes such as aeration lagoons or activated sludge systems are not considered to be biofilters.

* * * * *

Continuous process vent * * * 43 ( 6) The references to an " air oxidation reactor,

distillation unit, or reactor" in § 63.107 mean any continuous operation for the purposes of this subpart.

( 7) A separate determination is required for the emissions from each MCPU, even if emission streams from two or more MCPUs are combined prior to discharge to the atmosphere or to a control device.

* * * * *

Continuous operation means any operation that is not a batch operation.

* * * * *

Emission point means each continuous process vent,

batch process vent, storage tank, transfer rack, and wastewater stream.

* * * * *

Group 1 continuous process vent means a continuous process vent for which the flow rate is greater than or equal to 0.005 standard cubic meter per minute, and the total resource effectiveness index value, calculated according to § 63.2455( b), is less than or equal to 1.9 at an existing source and less than or equal to 5.0 at a new source.

* * * * * 44 Halogen atoms mean chlorine and fluorine.

HAP metals means the metal portion of antimony compounds, arsenic compounds, beryllium compounds, cadmium compounds, chromium compounds, cobalt compounds, lead compounds, manganese compounds, mercury compounds, nickel compounds, and selenium compounds.

* * * * *

Isolated intermediate means a product of a process that is stored before subsequent processing. An isolated intermediate is usually a product of a chemical synthesis,

fermentation, or biological extraction process. Storage of an isolated intermediate marks the end of a process.

Storage occurs at any time the intermediate is placed in equipment used solely for storage. The storage equipment is part of the MCPU that produces the isolated intermediate and is not assigned as specified in § 63.2445( d).

Miscellaneous organic chemical manufacturing process * * *

( 6) The end of a process that produces a solid material is either up to and including the dryer or, for a polymer production process without a dryer, up to and including the extruder, die plate, or solid state reactor,

except in two cases. If the dryer, extruder, die plate, or 45 solid state reactor is followed by an operation that is designed and operated to remove HAP solvent or residual HAP monomer from the solid, then the solvent removal operation is the last step in the process. If the dried solid is diluted or mixed with a HAP based solvent, then the solvent removal operation is the last step in the process.

* * * * *

Point of determination means each point where process wastewater exits the MCPU or control device.

Note to definition for point of determination: The regulation allows determination of the characteristics of a wastewater stream ( 1) at the point of determination or ( 2)

downstream of the point of determination if corrections are made for changes in flow rate and annual average concentration of soluble HAP and partially soluble HAP compounds as determined according to procedures in § 63.144 of subpart G in this part 63. Such changes include losses by air emissions; reduction of annual average concentration or changes in flow rate by mixing with other water or wastewater streams; and reduction in flow rate or annual average concentration by treating or otherwise handling the wastewater stream to remove or destroy HAP.

* * * * * 46 Process condenser means a condenser whose primary purpose is to recover material as an integral part of an MCPU. All condensers recovering condensate from an MCPU at or above the boiling point or all condensers in line prior to a vacuum source are considered process condensers.

Typically, a primary condenser or condensers in series are considered to be integral to the MCPU if they are capable of and normally used for the purpose of recovering chemicals for fuel value ( i. e., net positive heating value), use, reuse or for sale for fuel value, use, or reuse. This definition does not apply to a condenser that is used to remove materials that would hinder performance of a downstream recovery device as follows:

( 1) To remove water vapor that would cause icing in a downstream condenser, or ( 2) To remove water vapor that would negatively affect the adsorption capacity of carbon in a downstream carbon adsorber, or ( 3) To remove high molecular weight organic compounds or other organic compounds that would be difficult to remove during regeneration of a downstream carbon adsorber.

* * * * * 47 Recovery device means an individual unit of equipment used for the purpose of recovering chemicals from process vent streams and from wastewater streams for fuel value ( i. e., net positive heating value), use, reuse, or for sale for fuel value, use, or reuse. For the purposes of meeting requirements in Table 2 to this subpart, the recovery device must recover chemicals to be reused in a process at the affected source. Examples of equipment that may be recovery devices include absorbers, carbon adsorbers,

condensers, oil water separators or organic water separators, or organic removal devices such as decanters,

strippers, or thin film evaporation units. To be a recovery device for a wastewater stream, a decanter and any other equipment based on the operating principle of gravity separation must receive only multi phase liquid streams.

* * * * *

Surge control vessel means feed drums, recycle drums,

and intermediate vessels as part of any continuous operation. Surge control vessels are used within an MCPU when in process storage, mixing, or management of flowrates or volumes is needed to introduce material into continuous operations.

* * * * * 48 Wastewater means water that is discarded from an MCPU or control device through a POD and that contains either:

an annual average concentration of compounds in Tables 8 and 9 to this subpart of at least 5 ppmw and has an annual average flowrate of 0.02 liters per minute or greater; or an annual average concentration of compounds in Tables 8 and 9 to this subpart of at least 10,000 ppmw at any flowrate. Wastewater means process wastewater or maintenance wastewater. The following are not considered wastewater for the purposes of this subpart: * * *

* * * * *

16. Table 2 to subpart FFFF of part 63 is amended by revising entry 1 to read as follows:

TABLE 2 TO SUBPART FFFF OF PART 63. EMISSION LIMITS AND WORK PRACTICE STANDARDS FOR BATCH PROCESS VENTS For each . . . Then you must . . . And you must . . .

1. Process with Group 1 batch process vents. a. Reduce collective uncontrolled organic HAP emissions from the sum of all batch process vents within the process by   98 percent by weight by venting emissions from a sufficient number of the vents through one or more closed vent systems to any combination of control devices ( except a flare); or Not applicable. 49 b. Reduce collective uncontrolled organic HAP emissions from the sum of all batch process vents within the process by   95 percent by weight by venting emissions from a sufficient number of the vents through one or more closed vent systems to any combination of recovery devices or a biofilter, except you may elect to comply with the requirements of subpart WW of this part for any process tank; or Not applicable.

c. Reduce uncontrolled organic HAP emissions from one or more batch process vents within the process by venting through a closed vent system to a flare or by venting through one or more closed vent systems to any combination of control devices ( excluding a flare) that reduce organic HAP to an outlet concentration   20 ppmv as TOC or total organic HAP. For all other batch process vents within the process, reduce collective organic HAP emissions as specified in item 1. a and/ or item 1. b of this table.

* * * * * * *

17. Table 3 to subpart FFFF of part 63 is revised to read as follows: 50 TABLE 3 TO SUBPART FFFF OF PART 63. EMISSION LIMITS FOR HYDROGEN HALIDE AND HALOGEN HAP EMISSIONS OR HAP METALS EMISSIONS FROM PROCESS VENTS For each . . . You must . . .

1. Process with uncontrolled hydrogen halide and halogen HAP emissions from process vents   1,000 lb/ yr a. Reduce collective hydrogen halide and halogen HAP emissions by   99 percent by weight or to an outlet concentration   20 ppmv by venting through one or more closed vent systems to any combination of control devices, or b. Reduce the halogen atom mass emission rate from the sum of all batch process vents and each individual continuous process vent to   0.45 kg/ hr by venting through one or more closed vent systems to a halogen reduction device.

2. Process at a new source with uncontrolled emissions from process vents   150 lb/ yr of HAP metals. Reduce overall emissions of HAP metals by   97 percent by weight.

18. Table 4 to subpart FFFF of part 63 is amended by revising entry 1 to read as follows: 51 TABLE 4 TO SUBPART FFFF OF PART 63. EMISSION LIMITS FOR STORAGE TANKS For each . . . For which . . . Then you must . . .

1. Group 1 storage tank a. The maximum true vapor pressure of total HAP at the storage temperature is   76.6 kilopascals i. Reduce total HAP emissions by   95 percent by weight or to   20 ppmv of TOC or organic HAP and   20 ppmv of hydrogen halide and halogen HAP by venting emissions through a closed vent system to any combination of control devices ( excluding a flare); or ii. Reduce total organic HAP emissions by venting emissions through a closed vent system to a flare; or iii. Reduce total HAP emissions by venting emissions to a fuel gas system or process in accordance with § 63.982( d) and the requirements referenced therein.

b. The maximum true vapor pressure of total HAP at the storage temperature is < 76.6 kilopascals i. Comply with the requirements of subpart WW of this part, except as specified in § 63.2470; or ii. Reduce total HAP emissions by   95 percent by weight or to   20 ppmv of TOC or organic HAP and   20 ppmv of hydrogen halide and halogen HAP by venting emissions through a closed vent system to any combination of control devices ( excluding a flare); or iii. Reduce total organic HAP emissions by venting emissions through a closed vent system to a flare; or 52 iv. Reduce total HAP emissions by venting emissions to a fuel gas system or process in accordance with § 63.982( d) and the requirements referenced therein.

* * * * * * *

19. Table 5 to subpart FFFF of part 63 is amended by revising entry 1 to read as follows:

TABLE 5 TO SUBPART FFFF OF PART 63. EMISSION LIMITS AND WORK PRACTICE STANDARDS FOR TRANSFER RACKS For each . . . You must . . .

1. Group 1 transfer rack a. Reduce emissions of total organic HAP by   98 percent by weight or to an outlet concentration   20 ppmv as organic HAP or TOC by venting emissions through a closed vent system to any combination of control devices ( except a flare); or b. Reduce emissions of total organic HAP by venting emissions through a closedvent system to a flare; or c. Reduce emissions of total organic HAP by venting emissions to a fuel gas system or process in accordance with § 63.982( d) and the requirements referenced therein; or d. Use a vapor balancing system designed and operated to collect organic HAP vapors displaced from tank trucks and railcars during loading and route the collected HAP vapors to the storage tank from which the liquid being loaded originated or to another storage tank connected by a common header.

* * * * * * * 53 20. Table 6 to subpart FFFF of part 63 is revised to read as follows:

TABLE 6 TO SUBPART FFFF OF PART 63. REQUIREMENTS FOR EQUIPMENT LEAKS For all . . . You must . . .

1. Equipment that is in organic HAP service a. Comply with the requirements of subpart UU of this part 63 and the requirements referenced therein, except as specified in § 63.2480( b) and ( d); or b. Comply with the requirements of subpart H of this part 63 and the requirements referenced therein, except as specified in § 63.2480( b) and ( d); or c. Comply with the requirements of 40 CFR part 65, subpart F and the requirements referenced therein, except as specified in § 63.2480( c) and ( d).

21. Table 8 to subpart FFFF of part 63 is revised by deleting entry 10 and redesignating entries 11 through 61 as entries 10 through 60.

22. Table 12 to subpart FFFF of part 63 is amended as follows:

a. Removing the entries for § § 63.8( c)( 4)( i)( ii) and 63.10( e)( 1)( 2);

b. Adding new entries for § § 63.8( c)( 4)( i),

63.8( c)( 4)( ii), 63.10( e)( 1), 63.10( e)( 2)( i), and 63.10( e)( 2)( ii); and 54 c. Revising the entries for § § 63.8( c)( 4), 63.8( c)( 6),

63.8( c)( 7)( 8), 63.8( d), 63.8( e), 63.9( g),

63.10( b)( 2)( xiii), and 63.10( c)( 1)( 6), ( 7)( 15). 55 TABLE 12 TO SUBPART FFFF OF PART 63. APPLICABILITY OF GENERAL PROVISIONS TO SUBPART FFFF Citation Subject Explanation * * * * * * *

§ 63.8( c)( 4) CMS Requirements Only for CEMS. Requirements for CPMS are specified in referenced subparts G and SS of part 63. Requirements for COMS do not apply because subpart FFFF does not require COMS.

§ 63.8( c)( 4) ( i) COMS Measurement and Recording Frequency No; subpart FFFF does not require COMS.

§ 63.8( c)( 4) ( ii) CEMS Measurement and Recording Frequency Yes.

* * * * * * *

§ 63.8( c)( 6) CMS Requirements Only for CEMS; requirements for CPMS are specified in referenced subparts G and SS of this part 63. Requirements for COMS do not apply because subpart FFFF does not require COMS.

§ 63.8( c)( 7) ( 8) CMS Requirements Only for CEMS. Requirements for CPMS are specified in referenced subparts G and SS of part 63. Requirements for COMS do not apply 56 because subpart FFFF does not require COMS.

§ 63.8( d) CMS Quality Control Only for CEMS.

§ 63.8( e) CMS Performance Evaluation Only for CEMS. Section 63.8( e)( 5)( ii) does not apply because subpart FFFF does not require COMS.

* * * * * * *

§ 63.9( g) Additional Notifications When Using CMS Only for CEMS. Section 63.9( g)( 2) does not apply because subpart FFFF does not require COMS.

* * * * * * *

§ 63.10( b)( 2) ( xiii) Records Only for CEMS.

* * * * * * *

§ 63.10( c)( 1) ( 6),( 9) ( 15) Records Only for CEMS. Recordkeeping requirements for CPMS are specified in referenced subparts G and SS of this part 63.

* * * * * * *

§ 63.10( e)( 1) Additional CEMS Reports Yes.

§ 63.10( e)( 2) ( i) Additional CMS Reports Only for CEMS.

§ 63.10( e)( 2) ( ii) Additional COMS Reports No. Subpart FFFF does not require COMS.

* * * * * * *


[Federal Register Volume 86, Number 89 (Tuesday, May 11, 2021)]
[Notices]
[Page 25856]
[FR Doc No: 2021-09928]

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DEPARTMENT OF ENERGY

Federal Energy Regulatory Commission

[Docket No. ER21-1814-000]

Yellow Pine Energy Center II, LLC; Supplemental Notice That
Initial Market-Based Rate Filing Includes Request for Blanket Section
204 Authorization

    This is a supplemental notice in the above-referenced proceeding of
Yellow Pine Energy Center II, LLC's application for market-based rate
authority, with an accompanying rate tariff, noting that such
application includes a request for blanket authorization, under 18 CFR
part 34, of future issuances of securities and assumptions of
liability.
    Any person desiring to intervene or to protest should file with the
Federal Energy Regulatory Commission, 888 First Street NE, Washington,
DC 20426, in accordance with Rules 211 and 214 of the Commission's
Rules of Practice and Procedure (18 CFR 385.211 and 385.214). Anyone
filing a motion to intervene or protest must serve a copy of that
document on the Applicant.
    Notice is hereby given that the deadline for filing protests with
regard to the applicant's request for blanket authorization, under 18
CFR part 34, of future issuances of securities and assumptions of
liability, is May 25, 2021.
    The Commission encourages electronic submission of protests and
interventions in lieu of paper, using the FERC Online links at http://www.ferc.gov. To facilitate electronic service, persons with internet
access who will eFile a document and/or be listed as a contact for an
intervenor must create and validate an eRegistration account using the
eRegistration link. Select the eFiling link to log on and submit the
intervention or protests.
    Persons unable to file electronically may mail similar pleadings to
the Federal Energy Regulatory Commission, 888 First Street NE,
Washington, DC 20426. Hand delivered submissions in docketed
proceedings should be delivered to Health and Human Services, 12225
Wilkins Avenue, Rockville, Maryland 20852.
    In addition to publishing the full text of this document in the
Federal Register, the Commission provides all interested persons an
opportunity to view and/or print the contents of this document via the
internet through the Commission's Home Page (http://www.ferc.gov) using
the ``eLibrary'' link. Enter the docket number excluding the last three
digits in the docket number field to access the document. At this time,
the Commission has suspended access to the Commission's Public
Reference Room, due to the proclamation declaring a National Emergency
concerning the Novel Coronavirus Disease (COVID-19), issued by the
President on March 13, 2020. For assistance, contact the Federal Energy
Regulatory Commission at<EMAIL_ADDRESS>or call toll-free,
(886) 208-3676 or TYY,<PHONE_NUMBER>.

    Dated: May 5, 2021.
Kimberly D. Bose,
Secretary.
[FR Doc. 2021-09928 Filed 5-10-21; 8:45 am]
BILLING CODE 6717-01-P


[Federal Register Volume 80, Number 199 (Thursday, October 15, 2015)]
[Notices]
[Pages 62065-62067]
[FR Doc No: 2015-26185]

-----------------------------------------------------------------------

DEPARTMENT OF ENERGY

Federal Energy Regulatory Commission

[Docket No. CP15-527-000]

Transcontinental Gas Pipe Line Company, LLC; Notice of Intent To
Prepare an Environmental Assessment for the Proposed New York Bay
Expansion Project and Request for Comments on Environmental Issues

    The staff of the Federal Energy Regulatory Commission (FERC or
Commission) will prepare an environmental assessment (EA) that will
discuss the environmental impacts of the New York Bay Expansion Project
involving construction and operation of facilities by Transcontinental
Gas Pipe Line Company, LLC (Transco) in Chester, Pennsylvania; Essex
and Middlesex, New Jersey; and Richmond, New York. The Commission will
use this EA in its decision-making process to determine whether the
project is in the public convenience and necessity
    This notice announces the opening of the scoping process the
Commission will use to gather input from the public and interested
agencies on the project. You can make a difference by providing us with
your specific comments or concerns about the project. Your comments
should focus on the potential environmental effects, reasonable
alternatives, and measures to avoid or lessen environmental impacts.
Your input will help the Commission staff determine what issues they
need to evaluate in the EA. To ensure that your comments are timely and
properly recorded, please send your comments so that the Commission
receives them in Washington, DC on or before November 8, 2015.
    If you sent comments on this project to the Commission before the
opening of this docket on July 8, 2015, you will need to file those
comments in Docket No. CP15-527 to ensure they are considered as part
of this proceeding.
    This notice is being sent to the Commission's current environmental
mailing list for this project. State and local government
representatives should notify their constituents of this proposed
project and encourage them to comment on their areas of concern.
    If you are a landowner receiving this notice, a pipeline company
representative may contact you about the acquisition of an easement to
construct, operate, and maintain the proposed facilities. The company
would seek to negotiate a mutually acceptable agreement. However, if
the Commission approves the project, that approval conveys with it the
right of eminent domain. Therefore, if easement negotiations fail to
produce an agreement, the pipeline company could initiate condemnation
proceedings where compensation would be determined in accordance with
state law.
    Transco provided landowners with a fact sheet prepared by the FERC
entitled ``An Interstate Natural Gas Facility On My Land? What Do I
Need To Know?'' This fact sheet addresses a number of typically asked
questions, including the use of eminent domain and how to

participate in the Commission's proceedings. It is also available for
viewing on the FERC Web site (www.ferc.gov).

Public Participation

    For your convenience, there are three methods you can use to submit
your comments to the Commission. The Commission encourages electronic
filing of comments and has expert staff available to assist you at
(202) 502-8258 or<EMAIL_ADDRESS>Please carefully follow these
instructions so that your comments are properly recorded.
    (1) You can file your comments electronically using the eComment
feature on the Commission's Web site (www.ferc.gov) under the link to
Documents and Filings. This is an easy method for submitting brief,
text-only comments on a project;
    (2) You can file your comments electronically by using the eFiling
feature on the Commission's Web site (www.ferc.gov) under the link to
Documents and Filings. With eFiling, you can provide comments in a
variety of formats by attaching them as a file with your submission.
New eFiling users must first create an account by clicking on
``eRegister.'' If you are filing a comment on a particular project,
please select ``Comment on a Filing'' as the filing type; or
    (3) You can file a paper copy of your comments by mailing them to
the following address. Be sure to reference the project docket number
(CP15-527-000) with your submission:
    Kimberly D. Bose, Secretary, Federal Energy Regulatory Commission,
888 First Street NE., Room 1A, Washington, DC 20426.

Summary of the Proposed Project

    Transco proposes the New York Bay Expansion Project to modify
existing facilities and replace existing pipeline to provide an
additional 115,000 dekatherms per day of firm transportation service to
National Grid New York to meet 2017-2018 winter heating season needs.
The project would involve the following activities at existing
aboveground facilities in the specified towns and municipalities:
     Uprate Compressor Station 200 from 30,860 horsepower (hp)
to 33,000 hp (East Whiteland Township, Chester, Pennsylvania);
     uprate a unit of Compressor Station 303 from 25,000 hp to
27,500 hp (Roseland Borough, Essex, New Jersey);
     add 11,000 hp of electric-driven compression to Compressor
Station 207 (Old Bridge Township, Middlesex, New Jersey); and
     install various appurtenances and modifications at three
meter and regulation stations in East Brandywine Township (Chester,
Pennsylvania), Sayreville Borough (Middlesex, New Jersey), and Staten
Island Borough (Richmond, New York).
    In addition, Transco proposes to replace three segments of its 42-
inch-diameter Lower New York Bay Lateral pipeline, totaling 0.25 mile,
and uprate the lateral pipeline's operating pressure from 960 to 1000
pounds per square inch in Middlesex County, NJ.
    The general location of the project facilities is shown in appendix
1.\1\
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    \1\ The appendices referenced in this notice will not appear in
the Federal Register. Copies of appendices were sent to all those
receiving this notice in the mail and are available at www.ferc.gov
using the link called ``eLibrary'' or from the Commission's Public
Reference Room, 888 First Street NE., Washington, DC 20426, or call
(202) 502-8371. For instructions on connecting to eLibrary, refer to
the last page of this notice.
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Land Requirements for Construction

    Construction of the project would disturb about 56.70 acres of land
for the aboveground facilities and 14.05 acres of land for the pipe
replacement; these acres would be restored by Transco and revert to
former uses. The permanent footprint for Compressor Stations 200 and
303 would remain unchanged. The permanent footprint of Compressor
Station 207 would expand by 0.59 acre, and the three existing meter and
regulation stations would expand by combined total of 0.8 acre. No new
acreage would be required for the replacement pipe as Transco would
replace the pipeline in the same permanent right-of-way.

The EA Process

    The National Environmental Policy Act (NEPA) requires the
Commission to take into account the environmental impacts that could
result from an action whenever it considers the issuance of a
Certificate of Public Convenience and Necessity. NEPA also requires us
\2\ to discover and address concerns the public may have about
proposals. This process is referred to as ``scoping.'' The main goal of
the scoping process is to focus the analysis in the EA on the important
environmental issues. By this notice, the Commission requests public
comments on the scope of the issues to address in the EA. We will
consider all filed comments during the preparation of the EA.
---------------------------------------------------------------------------

    \2\ ``We,'' ``us,'' and ``our'' refer to the environmental staff
of the Commission's Office of Energy Projects.
---------------------------------------------------------------------------

    In the EA we will discuss impacts that could occur as a result of
the construction and operation of the proposed project under these
general headings:
     Geology and soils;
     land use;
     water resources, fisheries, and wetlands;
     cultural resources;
     vegetation and wildlife;
     air quality and noise;
     endangered and threatened species;
     public safety; and
     cumulative impacts
    We will also evaluate reasonable alternatives to the proposed
project or portions of the project, and make recommendations on how to
lessen or avoid impacts on the various resource areas.
    The EA will present our independent analysis of the issues. The EA
will be available in the public record through eLibrary. Depending on
the comments received during the scoping process, we may also publish
and distribute the EA to the public for an allotted comment period. We
will consider all comments on the EA before making our recommendations
to the Commission. To ensure we have the opportunity to consider and
address your comments, please carefully follow the instructions in the
Public Participation section, on page 2.
    With this notice, we are asking agencies with jurisdiction by law
and/or special expertise with respect to the environmental issues of
this project to formally cooperate with us in the preparation of the
EA.\3\ Agencies that would like to request cooperating agency status
should follow the instructions for filing comments provided under the
Public Participation section of this notice.
---------------------------------------------------------------------------

    \3\ The Council on Environmental Quality regulations addressing
cooperating agency responsibilities are at title 40, Code of Federal
Regulations, part 1501.6.
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Consultations Under Section 106 of the National Historic Preservation
Act

    In accordance with the Advisory Council on Historic Preservation's
implementing regulations for section 106 of the National Historic
Preservation Act, we are using this notice to initiate consultation
with the applicable State Historic Preservation Offices (SHPO), and to
solicit their views and those of other government agencies, interested
Indian tribes, and the public on the project's potential effects on
historic properties.\4\ We will

define the project-specific Area of Potential Effects (APE) in
consultation with the SHPOs as the project develops. On natural gas
facility projects, the APE at a minimum encompasses all areas subject
to ground disturbance (examples include construction right-of-way,
contractor/pipe storage yards, compressor stations, and access roads).
Our EA for this project will document our findings on the impacts on
historic properties and summarize the status of consultations under
section 106.
---------------------------------------------------------------------------

    \4\ The Advisory Council on Historic Preservation's regulations
are at title 36, Code of Federal Regulations, part 800. Those
regulations define historic properties as any prehistoric or
historic district, site, building, structure, or object included in
or eligible for inclusion in the National Register of Historic
Places.
---------------------------------------------------------------------------

Environmental Mailing List

    The environmental mailing list includes: Federal, state, and local
government representatives and agencies; elected officials; Native
American Tribes; other interested parties; and local libraries and
newspapers. This list also includes all affected landowners (as defined
in the Commission's regulations) who are potential right-of-way
grantors, whose property may be used temporarily for project purposes,
or who own homes within certain distances of aboveground facilities,
and anyone who submits comments on the project. We will update the
environmental mailing list as the analysis proceeds to ensure that we
send the information related to this environmental review to all
individuals, organizations, and government entities interested in and/
or potentially affected by the proposed project.
    If we publish and distribute the EA, copies will be sent to the
environmental mailing list for public review and comment. If you would
prefer to receive a paper copy of the document instead of the CD
version or would like to remove your name from the mailing list, please
return the attached Information Request (appendix 2).

Becoming an Intervenor

    In addition to involvement in the EA scoping process, you may want
to become an ``intervenor'' which is an official party to the
Commission's proceeding. Intervenors play a more formal role in the
process and are able to file briefs, appear at hearings, and be heard
by the courts if they choose to appeal the Commission's final ruling.
An intervenor formally participates in the proceeding by filing a
request to intervene. Instructions for becoming an intervenor are in
the ``Document-less Intervention Guide'' under the ``e-filing'' link on
the Commission's Web site. Motions to intervene are more fully
described at http://www.ferc.gov/resources/guides/how-to/intervene.asp.

Additional Information

    Additional information about the project is available from the
Commission's Office of External Affairs, at (866) 208-FERC, or on the
FERC Web site at www.ferc.gov using the ``eLibrary'' link. Click on the
eLibrary link, click on ``General Search'' and enter the docket number,
excluding the last three digits in the Docket Number field (i.e., CP15-
527). Be sure you have selected an appropriate date range. For
assistance, please contact FERC Online Support at
<EMAIL_ADDRESS>or toll free at<PHONE_NUMBER>, or for TTY,
contact<PHONE_NUMBER>. The eLibrary link also provides access to the
texts of formal documents issued by the Commission, such as orders,
notices, and rulemakings.
    In addition, the Commission offers a free service called
eSubscription which allows you to keep track of all formal issuances
and submittals in specific dockets. This can reduce the amount of time
you spend researching proceedings by automatically providing you with
notification of these filings, document summaries, and direct links to
the documents. Go to www.ferc.gov/docs-filing/esubscription.asp.
    Finally, public meetings or site visits will be posted on the
Commission's calendar located at www.ferc.gov/EventCalendar/EventsList.aspx along with other related information.

    Dated: October 8, 2015.
Kimberly D. Bose,
Secretary.
[FR Doc. 2015-26185 Filed 10-14-15; 8:45 am]
 BILLING CODE 6717-01-P


[Federal Register Volume 80, Number 149 (Tuesday, August 4, 2015)]
[Notices]
[Pages 46368-46369]
[FR Doc No: 2015-18887]

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SECURITIES AND EXCHANGE COMMISSION

Proposed Collection; Comment Request

Upon Written Request, Copy Available From: Securities and Exchange
Commission, Office of FOIA Services, 100 F Street NE., Washington, DC
20549-2736.

Extension:
    Form N-8A. SEC File No. 270-135, OMB Control No. 3235-0175.

    Notice is hereby given that, pursuant to the Paperwork Reduction
Act of 1995 (44 U.S.C. 3501 et seq.), the Securities and Exchange
Commission (the ``Commission'') is soliciting comments on the
collection of information summarized below. The Commission plans to
submit this existing collection of information to the Office of
Management and Budget (``OMB'') for extension and approval.
    The Investment Company Act of 1940 (``Investment Company Act'') (15
U.S.C. 80a-1 et seq.) requires investment companies to register with
the Commission before they conduct any business in interstate commerce.
Section 8(a) of the Investment Company Act provides that an investment
company shall be deemed to be registered upon receipt by the Commission
of a notification of

registration in such form as the Commission prescribes. Form N-8A (17
CFR 274.10) is the form for notification of registration that the
Commission has adopted under section 8(a). The purpose of such
notification of registration provided on Form N-8A is to notify the
Commission of the existence of investment companies required to be
registered under the Investment Company Act and to enable the
Commission to administer the provisions of the Investment Company Act
with respect to those companies. After an investment company has filed
its notification of registration under section 8(a), the company is
then subject to the provisions of the Investment Company Act which
govern certain aspects of its organization and activities, such as the
composition of its board of directors and the issuance of senior
securities. Form N-8A requires an investment company to provide its
name, state of organization, form of organization, classification, the
name and address of each investment adviser of the investment company,
the current value of its total assets, and certain other information
readily available to the investment company. If the investment company
is filing a registration statement as required by Section 8(b) of the
Investment Company Act concurrently with its notification of
registration, Form N-8A requires only that the registrant file the
cover page (giving its name, address, and agent for service of process)
and sign the form in order to effect registration.
    Based on recent filings of notifications of registration on Form N-
8A, we estimate that about 92 investment companies file such
notifications each year. An investment company must only file a
notification of registration on Form N-8A once. The currently approved
average hour burden per investment company of preparing and filing a
notification of registration on Form N-8A is one hour. Based on the
Commission staff's experience with the requirements of Form N-8A and
with disclosure documents generally--and considering that investment
companies that are filing notifications of registration on Form N-8A
simultaneously with the registration statement under the Investment
Company Act are only required by Form N-8A to file a signed cover
page--we continue to believe that this estimate is appropriate.
Therefore, we estimate that the total annual hour burden to prepare and
file notifications of registration on Form N-8A is 92 hours. The
currently approved cost burden of Form N-8A is $443 per filing. We are
updating the estimated cost burden to $449 to account for the effects
of inflation. Therefore, we estimate that the total annual cost burden
to associated with preparing and filing notifications of registration
on Form N-8A is about $41,308.
    Estimates of average burden hours and costs are made solely for the
purposes of the Paperwork Reduction Act, and are not derived from a
comprehensive or even representative survey or study of the costs of
Commission rules and forms. Compliance with the collection of
information requirements of Form N-8A is mandatory. Responses to the
collection of information will not be kept confidential. An agency may
not conduct or sponsor, and a person is not required to respond to, a
collection of information unless it displays a currently valid OMB
control number.
    Written comments are invited on: (a) Whether the collection of
information is necessary for the proper performance of the functions of
the Commission, including whether the information has practical
utility; (b) the accuracy of the Commission's estimate of the burden of
the collection of information; (c) ways to enhance the quality,
utility, and clarity of the information collected; and (d) ways to
minimize the burden of the collection of information on respondents,
including through the use of automated collection techniques or other
forms of information technology. Consideration will be given to
comments and suggestions submitted in writing within 60 days of this
publication.
    Please direct your written comments to Pamela Dyson, Director/Chief
Information Officer, Securities and Exchange Commission, C/O Remi
Pavlik-Simon, 100 F Street NE., Washington, DC 20549; or send an email
to<EMAIL_ADDRESS>
    Dated: July 28, 2015.
Robert W. Errett,
Deputy Secretary.
[FR Doc. 2015-18887 Filed 8-3-15; 8:45 am]
BILLING CODE 8011-01-P


[Federal Register Volume 81, Number 209 (Friday, October 28, 2016)]
[Notices]
[Page 75186]
[FR Doc No: 2016-26090]

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DEPARTMENT OF TRANSPORTATION

Federal Aviation Administration

Notice of Availability of the Record of Decision for the Proposed
Airport, Angoon, Alaska

AGENCY: Federal Aviation Administration (FAA), DOT.

ACTION: Notice of Availability (NOA), Record of Decision (ROD).

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SUMMARY: In accordance with the National Environmental Policy Act of
1969 (NEPA; 42 U.S.C. 4321 et seq.) and Council on Environmental
Quality (CEQ) regulations, the FAA issues this notice to advise the
public that the FAA has issued the Record of Decision (ROD) for the
Final Environmental Impact Statement (FEIS) that evaluated the effects
of a proposed airport in Angoon Alaska. The ROD constitutes the final
decision of the FAA and summarizes the FEIS analyses and selected
mitigation measures.

SUPPLEMENTARY INFORMATION: In the ROD, the FAA selected the following
alternative for implementation:

    Airport 12a with Access 12a which involves the construction of a
land-based airport consisting of a paved, 3,300-foot-long and 75-
foot-wide runway and associated access road. The project will be
located on lands owned or managed by private landowners;
Kootznoowoo, Inc.; and the City of Angoon.

    The FAA has included determinations on the project based upon
evidence set forth in the FEIS, public input, and the supporting
administrative record.

ADDRESSES: Copies of the ROD are available at the following locations.
Paper copies may be viewed during regular business hours.

1. Online at www.angoonairporteis.com
2. Online at http://www.faa.gov/airports/environmental/records_decision/ under FAA Region: Alaskan
3. Juneau Public Library
     Downtown Branch, 292 Marine Way, Juneau, AK 99801
     Douglas Branch, 1016 3rd Street, Douglas, AK 99824
     Mendenhall Mall Branch, 9109 Mendenhall Mall Road, Juneau,
AK 99801
4. U.S. Forest Service, Admiralty Island National Monument Office, 8510
Mendenhall Loop Road, Juneau, AK 99801
5. Angoon Community Association Building, 315 Heendae Road, Angoon, AK
99820
6. Angoon City Government Office, 700 Aan Deina Aat Street, Angoon, AK
99820
7. Angoon Senior Center, 812 Xootz Road, Angoon, AK 99820
8. The FAA Airports Division in Anchorage, AK. Please contact Leslie
Grey at<PHONE_NUMBER> to schedule.

FOR FURTHER INFORMATION CONTACT: Leslie Grey, AAL-611, Federal Aviation
Administration, Alaskan Region, Airports Division, 222 W. 7th Avenue
Box #14, Anchorage, AK 99513. Ms. Grey may be contacted during business
hours at<PHONE_NUMBER> (telephone) and<PHONE_NUMBER> (fax), or by
email at<EMAIL_ADDRESS>
    Issued in Anchorage, Alaska, on October 21, 2016.
Kristi A. Warden,
Deputy Division Manager, Airports Division, AAL-600.
[FR Doc. 2016-26090 Filed 10-27-16; 8:45 am]
 BILLING CODE 4910-13-P


[Federal Register Volume 83, Number 245 (Friday, December 21, 2018)]
[Notices]
[Page 65670]
[FR Doc No: 2018-27711]

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ENVIRONMENTAL PROTECTION AGENCY

[ER-FRL-9042-9]

Environmental Impact Statements; Notice of Availability

    Responsible Agency: Office of Federal Activities, General
Information<PHONE_NUMBER> or https://www.epa.gov/nepa/.

Weekly receipt of Environmental Impact Statements
Filed 12/10/2018 Through 12/14/2018
Pursuant to 40 CFR 1506.9.

Notice

    Section 309(a) of the Clean Air Act requires that EPA make public
its comments on EISs issued by other Federal agencies. EPA's comment
letters on EISs are available at: https://cdxnodengn.epa.gov/cdx-enepa-public/action/eis/search.

EIS No. 20180312, Draft, USACE, CO, Cherry Creek Dam Safety
Modification Study, Comment Period Ends: 02/04/2019, Contact: John
Palensky<PHONE_NUMBER>
EIS No. 20180313, Draft, USFS, ID, John Wood Forest Management Project,
Comment Period Ends: 02/04/2019, Contact: Bryan Fuell<PHONE_NUMBER>
EIS No. 20180314, Final, NPS, TN, Big South Fork National River and
Recreation Area Final Contaminated Mine Drainage Mitigation and
Treatment Programmatic and Site Specific Environmental Impact
Statement, Review Period Ends: 01/22/2019, Contact: Michael Edwards
303-969-2694
EIS No. 20180316, Draft Supplement, USFS, SC, AP Loblolly Pine Removal
and Restoration Project, Comment Period Ends: 02/04/2019, Contact:
Victor Wyant<PHONE_NUMBER>
EIS No. 20180317, Draft, FERC, TX, Annova LNG Brownville Project,
Comment Period Ends: 02/04/2019, Contact: Office of External Affairs
866-208-3372
EIS No. 20180318, Final, NMFS, NAT, Amendment 11 to the 2006
Consolidated Atlantic Highly Migratory Species Fishery Management Plan,
Review Period Ends: 01/22/2019, Contact: Guy DuBeck<PHONE_NUMBER>
EIS No. 20180319, Draft, NMFS, AL, State Management Program for
Recreational Red Snapper Amendment 50A to the Fishery Management Plan
for the Reef Fish Resources of the Gulf of Mexico, Comment Period Ends:
02/04/2019, Contact: Lauren Waters<PHONE_NUMBER>

Amended Notices

EIS No. 20180282, Final, USACE, IL, The Great Lakes and Mississippi
River Interbasin Study--Brandon Road Integrated Feasibility Study and
Environmental Impact Statement--Will County, Illinois, Review Period
Ends: 01/07/2019, Contact: Andrew Leichty<PHONE_NUMBER> Revision to FR
Notice Published 11/23/2018; Extending the Comment Period from 12/24/
2018 to 01/07/2019.

    Dated: December 18, 2018.
Kelly Knight,
Acting Director, Office of Federal Activities.
[FR Doc. 2018-27711 Filed 12-20-18; 8:45 am]
 BILLING CODE 6560-50-P