Source: http://federal.elaws.us/fr/10/31/2019/2019-23616
Timestamp: 2020-06-05 22:07:28
Document Index: 757324381

Matched Legal Cases: ['art 2', 'art 63', 'art 60', 'art 63', 'art 60', 'art 63', 'art 63', 'art 60', 'art 63', 'art 60', 'art 63', 'art 60', '§\u200960', '§\u200960', '§\u200960', '§\u200960', '§\u200963', '§\u200963', '§\u200963', '§\u200963', '§\u200963', '§\u200963', '§\u200963', 'art 60', 'art 63', 'art 63', 'art 63']

2019-23616. National Emission Standards for Hazardous Air Pollutants for Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills; Standards of Performance for Kraft Pulp Mill Affected Sources for Which Construction, Reconstruction, or Modification Commenced After May 23, 2013, Federal Register
Home » 2019 Issues » 84 FR (10/31/2019) » 2019-23616. National Emission Standards for Hazardous Air Pollutants for Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills; Standards of Performance for Kraft Pulp Mill Affected Sources for Which ...
Comments. Comments must be received on or before December 30, 2019.
Public Hearing. If anyone contacts us requesting a public hearing on or before November 5, 2019, we will hold a hearing. Additional information about the hearing, if requested, will be published in a subsequent Federal Register document and posted at https://www.epa.gov/​stationary-sources-air-pollution/​kraft-soda-sulfite-and-stand-alone-semichemical-pulp-mills-mact-ii. See SUPPLEMENTARY INFORMATION for information on requesting and registering for a public hearing.
You may send comments, identified by Docket ID No. EPA-HQ-OAR-2014-0741, by any of the following methods:
Email: a-and-r-docket@epa.gov. Include Docket ID No. EPA-HQ-OAR-2014-0741 in the subject line of the message.
Fax: (202) 566-9744. Attention Docket ID No. EPA-HQ-OAR-2014-0741.
Mail: U.S. Environmental Protection Agency, EPA Docket Center, Docket ID No. EPA-HQ-OAR-2014-0741, Mail Code 28221T, 1200 Pennsylvania Avenue NW, Washington, DC 20460.
For questions about this proposed action, contact Dr. Kelley Spence, Sector Policies and Programs Division (E143-03), Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, Research Triangle Park, North Carolina 27711; telephone number: (919) 541-3158; fax number: (919) 541-0516; and email address: spence.kelley@epa.gov.
Public Hearing. Please contact Ms. Virginia Hunt at (919) 541-0832 or by email at hunt.virginia@epa.gov to request a hearing, to register to speak at the hearing, or to inquire as to whether a public hearing will be held.
Docket. The EPA has established a docket for this rulemaking under Docket ID No. EPA-HQ-OAR-2014-0741. All documents in the docket are listed in Regulations.gov. Although listed, some information is not publicly available, e.g., Confidential Business Information (CBI) or other information whose disclosure is restricted by statute. Certain other material, such as copyrighted material, is not placed on the internet and will be publicly available only in hard copy. Publicly Start Printed Page 58357available docket materials are available either electronically in Regulations.gov or in hard copy at the EPA Docket Center, Room 3334, EPA WJC West Building, 1301 Constitution Avenue NW, Washington, DC. The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday through Friday, excluding legal holidays. The telephone number for the Public Reading Room is (202) 566-1744, and the telephone number for the EPA Docket Center is (202) 566-1742.
Instructions. Direct your comments to Docket ID No. EPA-HQ-OAR-2014-0741. The EPA's policy is that all comments received will be included in the public docket without change and may be made available online at https://www.regulations.gov/​, including any personal information provided, unless the comment includes information claimed to be CBI or other information whose disclosure is restricted by statute. Do not submit information that you consider to be CBI or otherwise protected through https://www.regulations.gov/​ or email. This type of information should be submitted by mail as discussed below.
Submitting CBI. Do not submit information containing CBI to the EPA through https://www.regulations.gov/​ or email. Clearly mark the part or all of the information that you claim to be CBI. For CBI information on any digital storage media that you mail to the EPA, mark the outside of the digital storage media as CBI and then identify electronically within the digital storage media the specific information that is claimed as CBI. In addition to one complete version of the comments that includes information claimed as CBI, you must submit a copy of the comments that does not contain the information claimed as CBI directly to the public docket through the procedures outlined in Instructions above. If you submit any digital storage media that does not contain CBI, mark the outside of the digital storage media clearly that it does not contain CBI. Information not marked as CBI will be included in the public docket and the EPA's electronic public docket without prior notice. Information marked as CBI will not be disclosed except in accordance with procedures set forth in 40 Code of Federal Regulations (CFR) part 2. Send or deliver information identified as CBI only to the following address: OAQPS Document Control Officer (C404-02), OAQPS, U.S. Environmental Protection Agency, Research Triangle Park, North Carolina 27711, Attention Docket ID No. EPA-HQ-OAR-2014-0741.
ADI Applicability Determination Index
PFLA percent full load amperage
RPM revolutions per minute
A. Why is the EPA issuing this proposed action?
A. What are the proposed amendments to the NESHAP?
B. What are the proposed amendments to the NSPS?
III. Summary of Cost, Environmental, and Economic Impacts
This document proposes to amend the National Emission Standards for Hazardous Air Pollutants for Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills (40 CFR part 63, subpart MM), and the Standards of Performance for Kraft Pulp Mill Affected Sources for Which Construction, Reconstruction, or Modification Commenced After May 23, 2013 (40 CFR part 60, subpart BBa). We are proposing this action to clarify how smelt dissolving tank (SDT) scrubber fan Start Printed Page 58358amperage limits should be determined and amend these rules to correct cross-reference errors. We explain our reasons for this action in this preamble.
Table 1 of this preamble lists the NESHAP, NSPS, and associated regulated industrial source categories that are the subject of this proposal. Table 1 is not intended to be exhaustive, but rather provides a guide for readers regarding the entities that this proposed action is likely to affect. The proposed amendments, once promulgated, will be directly applicable to the affected sources. Federal, state, local, and tribal government entities will not be affected by this proposed action. As defined in the Initial List of Categories of Sources Under Section 112(c)(1) of the Clean Air Act Amendments of 1990 (see 57 FR 31576, July 16, 1992) and Documentation for Developing the Initial Source Category List, Final Report (see EPA-450/3-91-030, July 1992), the Pulp and Paper Production source category is any facility engaged in the production of pulp and/or paper. This category includes, but is not limited to, integrated mills (where pulp alone or pulp and paper or paperboard are manufactured on-site), non-integrated mills (where paper or paperboard are manufactured, but no pulp is manufactured on-site), and secondary fiber mills (where waste paper is used as the primary raw material). Examples of pulping methods include kraft, soda, sulfite, semi-chemical, and mechanical. The pulp and paper production process units include operations such as pulping, bleaching, and chemical recovery. A kraft pulp mill is defined as a facility engaged in kraft pulping and includes digester systems, brown stock washer systems, multiple-effect evaporator systems, condensate stripper systems, recovery furnaces, SDTs, and lime kilns.
Table 1—Regulations and Industrial Source Categories Affected by This Proposed Action
Pulp and Paper Production Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills (40 CFR part 63, subpart MM) 32211, 32212, 32213
Kraft Pulp Mills Standards of Performance for Kraft Pulp Mill Affected Sources for Which Construction, Reconstruction, or Modification Commenced After May 23, 2013 (40 CFR part 60, subpart BBa) 3221
In addition to being available in the docket, an electronic copy of this action is available on the internet. Following signature by the EPA Administrator, the EPA will post a copy of this proposed action at https://www.epa.gov/​stationary-sources-air-pollution/​kraft-soda-sulfite-and-stand-alone-semichemical-pulp-mills-mact-ii and https://www.epa.gov/​stationary-sources-air-pollution/​kraft-pulp-mills-new-source-performance-standards-nsps-40-cfr-60. Following publication in the Federal Register, the EPA will post the Federal Register version of the proposal at this same website.
A redline version of the regulatory language that incorporates the proposed changes in this action is available in the docket (Docket ID No. EPA-HQ-OAR-2014-0741).
With this action, the EPA is proposing to clarify how SDT scrubber fan amperage operating limits should be determined. A technical-feasibility issue with implementing the residual risk and technology review amendments to 40 CFR part 63, subpart MM, published in 2017 (82 FR 47328, October 11, 2017) was brought to the EPA's attention through alternative monitoring requests the Agency received.
The 2017 NESHAP amendment that added the fan amperage [1] alternative parameter to 40 CFR 63.864(e)(10)(iii) was based on the EPA's review of alternative monitoring requests for SDTs available in the EPA's Applicability Determination Index (ADI) (81 FR 97074, December 30, 2016). In these previously approved alternative monitoring requests, the EPA acknowledged that pressure drop is not the best indicator of particulate matter (PM)/hazardous air pollutant (HAP) control device performance when the SDT scrubber is a low-energy entrainment scrubber or a dynamic scrubber that operates near atmospheric pressure. Low-energy entrainment scrubbers use the rotation of the fan blade to shatter the scrubbing liquid into fine droplets, while at the same time accelerating the particles into the airstream. The PM removal efficiency of these scrubbers is a function of the number of liquid droplets produced (to create a large contacting surface area) and the velocity of the particulates imparted by the fan blade, which in turn is a function of the amount of scrubbing liquid introduced and the tip speed of the fan blade. Therefore, the most important parameters to continuously monitor are the scrubbing liquid flow rate and the fan rotational speed (as indicated by the amperage of the fan motor or revolutions per minute (RPM)).
The 2017 NESHAP amendment also specified a method in 40 CFR 63.864(j)(5)(i)(A) for setting the fan motor amperage operating limit, requiring that the minimum fan amperage operating limit be set as the lowest of the 1-hour average fan amperage values associated with each run demonstrating compliance with the applicable emission limit. The intent of establishing the operating limit as the lowest 1-hour average fan amperage was to demonstrate that the scrubber was operating as intended and removing HAP accordingly, because fan amperage values can be correlated with fan speed. This seemed reasonable during the development of the 2017 NESHAP amendments because the fan on these units are constant speed fans and changes in the load to the fan motor (e.g., changes in gas density/pressure or fan belt issues) result in changes in the amperage needed to maintain the constant speed. For example, a scrubber operating without any scrubbing liquid or exhaust gas would pull a certain amount of amperage on the fan motor to maintain a constant speed. When the exhaust gas and scrubbing liquid are added, the fan motor amperage will increase to maintain that speed. Based on this concept, the basis for the fan motor amperage operating limit in the 2017 NESHAP amendments was that a drop in fan motor amperage below a certain point showed that the motor Start Printed Page 58359would no longer turn the fan properly (because, for example, the belt that connects the motor to the fan was slipping or broken), which in turn would mean the scrubber was not operating as well as it was during the emissions performance test.
As facilities began to plan their repeat performance test required by the 2017 NESHAP amendments and determine the appropriate operating parameters, they discovered that the method dictated to set the fan motor amperage did not accurately represent proper scrubber performance and submitted alternative monitoring requests. The alternative monitoring requests that EPA has received explained that setting the fan amperage operating limit as outlined in the 2017 NESHAP amendments at 40 CFR 63.864(j)(5)(i)(A) could result in a minimum limit that does not correlate with scrubber emissions-reduction performance and cannot be achieved at all times, leading to deviations of the amperage operating parameter even when the fan is turning as designed and the scrubber is operating properly to achieve the required HAP reduction. More details on these alternative monitoring requests are available in the memorandum titled Smelt Dissolving Tank Scrubber Operating Parameter Review, in the docket for this rulemaking (EPA Docket ID No. EPA-HQ-OAR-2014-0741).
After reviewing how the SDT scrubbers in question operate, the EPA agrees that use of the average fan motor amperage measured during the performance test to establish the fan amperage limit as dictated in 40 CFR 63.864(j)(5)(i)(A) of the 2017 NESHAP amendments can be problematic because it does not necessarily correlate with proper operation of the scrubber. The EPA's intent with adding the fan motor amperage alternative as part of the 2017 NESHAP amendments was to add regulatory flexibility while ensuring proper scrubber operation, not to arbitrarily set an operating limit that may not be met, even while the SDT scrubber is operating properly. The requirement for determining the fan motor amperage during the performance test to set the minimum limit was included in the 2017 NESHAP (40 CFR part 63, subpart MM) amendments for new and existing sources and in the NSPS (40 CFR part 60, subpart BBa) promulgated in 2014 (79 FR 18952, April 4, 2014) which applies to new sources only. The issue was not identified in public comments on either rule but was discovered as existing sources began to implement the 2017 NESHAP amendments.
Upon further review of the EPA's responses to historical alternative monitoring requests included in the ADI, recent requests for alternative monitoring and other available information, we recognize that the requirement to monitor fan amperage directly and establish a minimum fan amperage limit based on the average amperage measured during the performance test may result in deviations even when the scrubber is properly operating. Some facilities were approved by the EPA to use indicators of fan operation closely related to fan amperage (e.g., RPM) and engineering design considerations when setting the site-specific fan amperage limit indicative of proper scrubber operation. For more details, see the memorandum titled Smelt Dissolving Tank Scrubber Operating Parameter Review, in the docket for this rulemaking (EPA Docket ID No. EPA-HQ-OAR-2014-0741).
To continue with our original intent to measure scrubber performance with an alternative method in these rules, this action is proposing to modify the language at 40 CFR 63.864(e)(10)(iii) and (j)(5)(i) to clarify how wet scrubber parameter limits are to be established and that fan amperage or RPM can be used to demonstrate compliance for the SDT scrubbers in question. Specifically, we are proposing to replace 40 CFR 63.864(j)(5)(i)(A) with a requirement to set the minimum scrubbing liquid flow rate operating limit as the lowest of the 1-hour average scrubbing liquid flow rate values associated with each test run demonstrating compliance with the applicable emission limit. This requirement was inadvertently left out of the 2017 NESHAP amendment but was required by other sections of the rule. Additionally, we are proposing to add a new subsection, 40 CFR 63.864(j)(5)(i)(B) to clarify how wet scrubber fan amperage operating limits should be established.
The proposed text in 40 CFR 63.864(j)(5)(i)(B) would have the same requirements that were previously in the 40 CFR 63.864(j)(5)(i) introductory paragraph, which states the scrubber pressure drop operating limit must be set as the lowest of the 1-hour average pressure drop values associated with each test run demonstrating compliance with the applicable emission limit and provides alternatives for determining parameters for dynamic or low energy entrainment scrubbers. The proposed new 40 CFR 63.864(j)(5)(i)(B)(1) would clarify that, for SDT dynamic wet scrubbers operating at ambient pressure or for low energy entrainment scrubbers where fan speed does not vary, the minimum fan amperage operating limit must be set as the midpoint between the lowest of the 1-hour average fan amperage values associated with each test run demonstrating compliance with the applicable emission limit and the no-load amperage value. Additionally, the proposed regulatory text specifies that the no-load amperage value must be determined using manufacturers specifications or by performing a no-load test of the fan motor, and that it must be verified that the scrubber fan is operating within 5 percent of the design RPM during the emissions performance test. The proposed 40 CFR 63.864(j)(5)(i)(B)(2) would allow for the use of percent full load amperage (PFLA) to demonstrate compliance. The minimum PFLA to the fan motor must be set as the percent of full load amps under no-load, plus 10 percent. Because the no-load value represents the amperage pulled by the motor without a fan belt (i.e., the fan is not engaged), the additional 10 percent will ensure that the belt has not broken and the fan is engaged during operation. This proposed subsection also would require verification that the scrubber fan is operating within 5 percent of the design RPM during the emissions performance test. Further, we are proposing 40 CFR 63.864(j)(5)(i)(B)(3) to allow the use of RPM to demonstrate compliance. The minimum RPM must be set at 95 percent of the design RPM. Finally, we are proposing a conforming amendment in 40 CFR 63.867(c)(3)(iii)(C)(1) to incorporate this language.
In addition to clarifying how to set SDT fan amperage operating limits, the EPA is also proposing to correct the following cross-reference errors in the promulgated Combustion Source NESHAP (40 CFR part 63, subpart MM):
An incorrect paragraph reference in the definition of “modification” in 40 CFR 63.861;
An incorrect paragraph reference in 40 CFR 63.864(e)(10)(iii), referring to 40 CFR 63.864(e)(3)(i) instead of 40 CFR 63.864(e)(10)(i) as intended;
Incorrect paragraph references in 40 CFR 63.864(j)(1), (3), and (5) which cross-referenced requirements that were proposed (81 FR 97046, December 30, 2016) but not finalized for establishing site-specific electrostatic precipitator (ESP) operating limits. Instead, the EPA finalized a requirement to maintain proper operation of the ESP's automatic voltage control (82 FR 47328, October 11, 2017), but inadvertently kept the cross-references to the proposed requirements in the final rule; and
Omission of reference to wet scrubber liquid flow rate in 40 CFR 63.864(j)(5) which specifies how to establish operating limits.Start Printed Page 58360
With this action, the EPA is proposing similar amendments to the fan amperage requirements as discussed in section II.A of this preamble to 40 CFR 60.284a(b)(2)(iii), (c)(4), and (d)(4)(ii) and 40 CFR 60.287(b)(4)(i) for consistency between the two rules that apply to the same scrubbers. Additionally, the EPA is also proposing to correct a cross-reference error in the promulgated Kraft Pulp Mills NSPS (40 CFR part 60, subpart BBa). Specifically, the EPA is proposing to amend incorrect paragraph references in 40 CFR 60.285a(b)(1) and 60.285a(d)(1) intended to cross-reference the rule's oxygen correction equation.
The sources affected by this proposal are chemical pulp mills that use SDTs equipped with low-energy entrainment scrubbers or dynamic scrubbers that operate near atmospheric pressure. We estimate that there are 54 facilities that utilize these types of scrubbers.
There are no air quality impacts associated with the proposed amendments.
No cost impacts are estimated to be associated with this proposed action because the proposal serves only to provide regulatory clarity. This proposed action reduces the likelihood that facilities will choose to submit site-specific alternative monitoring requests but does not change the scope of any regulatory requirements.
There are no economic impacts associated with the proposed amendments.
Because these proposed amendments are not considered economically significant, as defined by Executive Order 12866, and because we did not estimate any emission reductions associated with the proposal, we did not estimate any benefits from reducing emissions.
We solicit comments on this proposed action. In addition to general comments on this action, we are also interested in any additional SDT scrubber performance data that may improve the parameter calculations needed to determine compliance. Such data should include supporting documentation in sufficient detail to allow characterization of the quality and representativeness of the data or information.
This action does not impose any new information collection burden under the PRA. OMB has previously approved the information collection activities contained in the existing regulation (40 CFR part 63, subpart MM) and has assigned OMB control number 2060-0377. This action does not change the information collection requirements.
I certify that this action will not have a significant economic impact on a substantial number of small entities under the RFA. This action will not impose any requirements on small entities. This action does not create any new requirements or burdens, and no costs are associated with this proposed action.
This action does not have tribal implications, as specified in Executive Order 13175. The EPA does not know of any pulp mills owned or operated by Indian tribal governments or located within tribal lands. Thus, Executive Order 13175 does not apply to this action.
For the reasons set forth in the preamble, the Environmental Protection Agency proposes to amend 40 CFR part 60 and 63 as follows:
2. Section 60.284a is amended by revising paragraphs (b)(2)(iii), (c)(3)(i), (c)(4), and (d)(4)(ii) to read as follows:
(iii) As an alternative to pressure drop measurement under paragraph (b)(2)(i) of this section, a monitoring device for measurement of fan amperage or revolutions per minute (RPM) may be used for smelt dissolving tank dynamic scrubbers that operate at ambient pressure or for low-energy entrainment scrubbers where the fan speed does not vary.
(i) Calculate 12-hour block averages from the recorded measurements of wet scrubber pressure drop (or smelt dissolving tank scrubber fan amperage or RPM) and liquid flow rate (or liquid supply pressure), as applicable.
(4) During the initial performance test required in § 60.285a, the owner or operator must establish site-specific operating limits for the monitoring parameters in paragraphs (b)(2) through (4) of this section by continuously monitoring the parameters and determining the arithmetic average value of each parameter during the performance test. The arithmetic average of the measured values for the three test runs establishes your minimum site-specific operating limit for each wet scrubber or ESP parameter (except for smelt dissolving tank scrubber fan amperage or RPM). For smelt dissolving tank scrubber fan amperage, see 40 CFR 63.864(j)(5)(i)(B). For smelt dissolving tank scrubber RPM, the minimum RPM must be set as 5 percent lower than the design RPM. Multiple performance tests may be conducted to establish a range of parameter values. The owner or operator may establish replacement operating limits for the monitoring parameters during subsequent performance tests using the test methods in § 60.285a.
(ii) All 12-hour block average scrubber pressure drop (or fan amperage or RPM, if used as an alternative under paragraph (b)(2)(iii) of this section) measurements below the minimum site-specific limit established during performance testing during times when BLS or lime mud is fired (as applicable), except during startup and shutdown.
3. Section 60.285a is amended by revising paragraphs (b)(1) and (d)(1) to read as follows:
(1) Method 5 of appendix A-3 of this part must be used to determine the filterable particulate matter concentration. The sampling time and sample volume for each run must be at least 60 minutes and 0.90 dscm (31.8 dscf). Water must be used as the cleanup solvent instead of acetone in the sample recovery procedure. The particulate concentration must be corrected to the appropriate oxygen concentration according to § 60.284a(c)(1)(iii).
(1) Method 16 of appendix A-6 of this part must be used to determine the TRS concentration. The TRS concentration must be corrected to the appropriate oxygen concentration using the procedure in § 60.284a(c)(1)(iii). The sampling time must be at least 3 hours, but no longer than 6 hours.
4. Section 60.287a is amended by revising paragraph (b)(4)(i) to read as follows:
(i) Records of the pressure drop of the gas stream through the control equipment (or smelt dissolving tank scrubber fan amperage or RPM), and
6. Section 63.861 is amended by revising the definition of “modification” and adding in alphabetical order the definition of “no-load fan amperage” to read as follows:
Modification means, for the purposes of § 63.862(a)(1)(ii)(D)(1), any physical change (excluding any routine part replacement or maintenance) or operational change that is made to the air pollution control device that could result in an increase in PM emissions.
No-load fan amperage means, for purposes of this subpart, the amperage pulled by the fan motor when the fan is operating under no-load, specifically the amperage value the motor would use if the fan belt was removed.
7. Section 63.864 is amended by revising paragraphs (e)(10)(iii), (j)(1), (3), and (5) to read as follows:
(iii) As an alternative to pressure drop measurement under paragraph (e)(10)(i) of this section, a monitoring device for measurement of fan amperage or fan revolutions per minute (RPM) may be used for smelt dissolving tank dynamic scrubbers that operate at ambient pressure or for low-energy entrainment scrubbers where the fan speed does not vary.
(1) During the initial or periodic performance test required in § 63.865, the owner or operator of any affected source or process unit must establish operating limits for the monitoring parameters in paragraphs (e)(2) and (10) Start Printed Page 58362through (14) of this section, as appropriate; or
(3) The owner or operator of an affected source or process unit may establish expanded or replacement operating limits for the monitoring parameters listed in paragraphs (e)(2) and (10) through (14) of this section and established in paragraph (j)(1) or (2) of this section during subsequent performance tests using the test methods in § 63.865.
(5) New, expanded, or replacement operating limits for the monitoring parameter values listed in paragraphs (e)(2) and (10) through (14) of this section should be determined as described in paragraphs (j)(5)(i) and (ii) of this section.
(i) The owner or operator of an affected source or process unit that uses a wet scrubber must set minimum operating limits as described in paragraph (j)(5)(i)(A) and (B) of this section.
(A) Set the minimum scrubbing liquid flow rate operating limit as the lowest of the 1-hour average scrubbing liquid flow rate values associated with each test run demonstrating compliance with the applicable emission limit in § 63.862.
(B) Set the minimum scrubber pressure drop operating limit as the lowest of the 1-hour average pressure drop values associated with each test run demonstrating compliance with the applicable emission limit in § 63.862; or for a smelt dissolving tank dynamic wet scrubber operating at ambient pressure or for low energy entrainment scrubbers where fan speed does not vary, set the minimum operating limit using one of the methods in paragraph (j)(5)(i)(B)(1) through (3) of this section.
(1) The minimum fan amperage operating limit must be set as the midpoint between the lowest of the 1-hour average fan amperage values associated with each test run demonstrating compliance with the applicable emission limit in § 63.862 and the no-load amperage value. The no-load amperage value must be determined using manufacturers specifications, or by performing a no-load test of the fan motor for each smelt dissolving tank scrubber. It must be verified that the scrubber fan is operating within 5 percent of the design RPM during the emissions performance test; or
(2) The minimum percent full load amperage (PFLA) to the fan motor must be set as the percent of full load amps under no-load, plus 10 percent. The PFLA is calculated by dividing the no-load amperage value by the highest of the 1-hour average fan amperage values associated with each test run demonstrating compliance with the applicable emission limit in § 63.862 multiplied by 100. The no-load amperage value must be determined using manufacturers specifications, or by performing a no-load test of the fan motor for each smelt dissolving tank scrubber. It must be verified that the scrubber fan is operating within 5 percent of the design RPM during the emissions performance test; or
(3) The minimum RPM must be set as 95 percent of the design RPM.
8. Section 63.867 is amended by revising paragraph (c)(3)(iii)(C)( 1) to read as follows:
(1) The operating limits established during the performance test for scrubbing liquid flow rate and pressure drop across the scrubber (or alternatively, fan amperage or RPM if used for smelt dissolving tank scrubbers).
1. Fan amperage refers to the amperage delivered to the fan motor.
[FR Doc. 2019-23616 Filed 10-30-19; 8:45 am]
2019-23616
58356-58362 (7 pages)
EPA-HQ-OAR-2014-0741, FRL-10001-62-OAR
2060-AU53
60.284a,60.285a,63.864,63.867
2019-23616.pdf
» Redline: 40 CFR Part 60 Subpart BBa
» Redline: 40 CFR Part 63 Subpart MM
» Smelt Dissolving Tank Scrubber Operating Parameter Review
» Petition for Reconsideration from EarthJustice
» EPA's Response to the Petition for Reconsideration from EarthJustice
» May 2016 National Industry-Specific Occupational Employment and Wage Estimates: NAICS 322100 - Pulp, Paper, and Paperboard Mills
» NESHAP for Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills (40 CFR Part 63, Subpart MM) RTR, Final Amendments: Response to Public Comments on December 30, 2016 Proposal
» Tax Incidence
» Redline Version of 40 CFR Part 63, Subpart MM Showing Final Changes Made as a Result of the Residual Risk and Technology Review