CSR 45-21-50. Disposition of Rule; Severability

§45-21-50. Disposition of Rule; Severability. 50.1. In the event the U.S. EPA’s June 12, 2015 “State Implementation Plans: Response to Petition for Rulemaking; Restatement and Update of EPA’s SSM Policy Applicable to SIPs; Finding of Substantial Inadequacy; and SIP Calls to Amend Provisions Applying to Excess Emissions During Periods of Startup, Shutdown and Malfunction,” at 80 Fed. Reg. 33840 (2015 SSM SIP Call) is withdrawn by the U.S. EPA, is invalidated by a court of competent jurisdiction, and/or is invalidated by an act of the West Virginia Legislature or United States Congress, the Secretary may terminate any permit or section of an existing permit issued pursuant to this rule. 50.2. In the event the U.S. EPA’s April 17, 2023 “Air Plan Disapproval; West Virginia; Revision to the West Virginia State Implementation Plan To Add the Startup, Shutdown, Maintenance Rule 45CSR1—Alternative Emission Limitations During Startup, Shutdown, and Maintenance Operations,” at 88 Fed. Reg. 23356 (45CSR1 2023 Disapproval) is withdrawn by the U.S. EPA, is invalidated by a court of competent jurisdiction, and/or is invalidated by an act of the West Virginia Legislature or United States Congress, the Secretary may terminate any permit or section of an existing permit issued pursuant to this rule. 50.3. In the event the U.S. EPA’s April 17, 2023 “West Virginia; Finding of Failure To Submit State Implementation Plan Revision in Response to the 2015 Findings of Substantial Inadequacy and SIP Calls To Amend Provisions Applying to Excess Emissions During Periods of Startup, Shutdown, and Malfunction,” at 88 Fed. Reg. 23353 (2023 FFS) is withdrawn by the U.S. EPA, is invalidated by a court of competent jurisdiction, and/or is invalidated by an act of the West Virginia Legislature or United States Congress, the Secretary may terminate any permit or section of an existing permit issued pursuant to this rule. 50.4. In the event the 2015 SSM SIP Call, 45CSR1 2023 Disapproval, and/or the 2023 FFS is withdrawn by the U.S. EPA, is invalidated by a court of competent jurisdiction, and/or is invalidated by an act of the West Virginia Legislature or United States Congress, the Secretary may sever requirements § 45-21-3.8 and revert to the May 1, 1996 requirements found at § 45-21-9.3. Emission Limit kg/L lb/gala Sheet basecoat and sheet overvarnish 0.34 2.8 Exterior basecoat and overvarnish (two-piece can) 0.34 2.8 Interior body spray coat 0.51 4.2 Two-piece can exterior end coat 0.51 4.2 Side seam spray coat 0.66 5.5 End sealing compound coat 0.44 3.7 Emission Limit kg/La lb/gala Clear coating 0.52 4.3 Steel pail & drum interior coating 0.52 4.3 Air-dried coating 0.42 3.5 Extreme performance coating 0.42 3.5 All other coatings 0.36 3.0 Emission limit kg/100 m2a lb/1,000 ft2a Printed interior panels 2.9 6.0 Natural finish hardwood plywood panels 5.8 12.0 Class II finish on hardwood panels 4.8 10.0 Allowable condenser outlet gas temperature, °C VOC vapor pressure at 20° C VOC vapor pressure at 20° C Allowable condenser outlet gas temperature, °C (kPa) (psi) -25 >40.01 5.8 -15 >20.0 2.9 0 >10.0 1.5 10 >7.0 1.0 25 >3.5 0.5 Production Process Process Section Uncontrolled Emission Rate, megagram of product per year (Mg/yr) High density polyethylene, liquid-phase slurry process. material recovery section 7 High density polyethylene, liquid-phase slurry process product finishing section 19 Polypropylene, liquid-phase process polymerization reaction section 7 Polypropylene, liquid-phase process material recovery section 8 Polypropylene, liquid-phase process product finishing section 36 Polystyrene, continuous process material recovery section 7 Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation Table 45-21F. Coefficients of the total resource effectiveness (TRE)index equation A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: A1. For chlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 3.5: FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 48.73 0 0.404 -0.1632 0 0 13.5 < FL ≤ 700 42.35 0.624 0.404 -0.1632 0 0.0245 700 < FL ≤ 1,400 84.38 0.678 0.404 -0.1632 0 0.0346 1,400 < FL≤ 2,100 126.41 0.712 0.404 -0.1632 0 0.0424 2,100 < FL ≤ 2,800 168.44 0.747 0.404 -0.1632 0 0.0490 2,800 < FL ≤ 3,500 210.47 0.758 0.404 -0.1632 0 0.0548 A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): A2. For chlorinated process vent streams, if 3.5 < net heating value (MJ/scm): FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 47.76 0 -0.292 0 0 0 13.5 < FL ≤ 700 41.58 0.605 -0.292 0 0 0.0245 700 < FL ≤ 1,400 82.84 0.658 -0.292 0 0 0.0346 1,400 < FL ≤ 2,100 123.10 0.691 -0.292 0 0 0.0424 2,100 < FL ≤ 2,800 165.36 0.715 -0.292 0 0 0.0490 2,800 < FL ≤ 3,500 206.62 0.734 -0.292 0 0 0.0548 B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: B. For nonchlorinated process vent streams, if 0 ≤ net heating value (MJ/scm) ≤ 0.48: FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 19.05 0 0.113 -0.214 0 0 13.5 < FL ≤ 1,350 16.61 0.239 0.113 -0.214 0 0.0245 1,350 < FL ≤ 2,700 32.91 0.260 0.113 -0.214 0 0.0346 2,700 < FL ≤ 3,500 49.21 0.273 0.113 -0.214 0 0.0424 C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: C. For nonchlorinated process vent streams, if 0.48 < net hearing value (MJ/scm) ≤ 1.9: FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 19.74 0 0.400 -0.202 0 0 13.5 < FL ≤ 1,350 18.30 0.138 0.400 -0.202 0 0.0245 1,350 < FL ≤ 2,700 36.28 0.150 0.400 -0.202 0 0.0346 2,700 < FL ≤ 4,050 54.26 0.158 0.400 -0.202 0 0.0424 D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: D. For nonchlorinated process vent streams, if 1.9 < net heating value (MJ/scm) ≤ 3.6: FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 15.24 0 0.033 0 0 0 13.5 < FL ≤ 1,190 13.63 0.157 0.033 0 0 0.0245 1,190 < FL ≤ 2,380 26.95 0.171 0.033 0 0 0.0346 2,380 < FL ≤ 3,570 40.27 0.179 0.033 0 0 0.0424 E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): E. For nonchlorinated process vent streams, if 3.6 < net heating value (MJ/scm): FL = vent stream flow rate (scm/min) a b c d e f FL ≤ 13.5 15.24 0 0 0.0090 0 0 13.5 < FL ≤ 1,190 13.63 0 0 0.0090 0.0503 0.0245 1,190 < FL ≤ 2,380 26.95 0 0 0.0090 0.0546 0.0346 2,380 < FL ≤ 3,570 40.27 0 0 0.0090 0.0573 0.0424