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NR 279.54(5)(b) (b) If contaminated runoff is commingled or treated with process wastewater, or if wastewater consisting solely of contaminated runoff which exceeds 15 mg/l oil and grease is not commingled or treated with any other type of wastewater, the quantity of pollutants discharged may not exceed the quantity determined by multiplying the flow of contaminated runoff as determined by the department times the concentrations listed in the following table: - See PDF for table PDF
NR 279.54 Note 1 Within the range of 6.0 to 9.0.
NR 279.54 History History: Cr. Register, October, 1986, No. 370, eff. 11-1-86.
NR 279.55 NR 279.55Pretreatment standards for existing sources (PSES). Except as provided in 40 CFR 403.7 and 403.13 any existing source subject to this subcategory which introduces pollutants into a publicly owned treatment works shall comply with 40 CFR Part 403 and achieve the following pretreatment standards for existing sources (PSES). The following standards apply to the total refinery flow contribution to the POTW: - See PDF for table PDF
NR 279.55 Note 1 Where the discharge to the POTW consists solely of sour waters, the owner or operator has the option of complying with this limit or the daily maximum mass limitation for ammonia set forth in s. NR 279.53 (1) and (2).
NR 279.55 History History: Cr. Register, October, 1986, No. 370, eff. 11-1-86.
NR 279.56 NR 279.56Standards of performance for new sources (NSPS).
NR 279.56(1)(1) Any new source subject to this subcategory shall achieve the following new source performance standards (NSPS): - See PDF for table PDF
NR 279.56(2) (2) The limits set forth in sub. (1) shall be multiplied by the following factors to calculate the maximum for any one day and maximum average of daily values for 30 consecutive days. 
NR 279.56(2)(b) (b) Process factor. - See PDF for table PDF
NR 279.56 Note Note: See the comprehensive example in s. NR 279.42 (2) (c).
NR 279.56(3) (3) The provisions of s. NR 279.16 (3) apply to discharges of process wastewater pollutants attributable to ballast water by a point source subject to the provisions of this subcategory.
NR 279.56(4) (4) The quantity and quality of pollutants or pollutant properties controlled by this subsection, attributable to once-through cooling water, are excluded from the discharge allowed by sub. (2). Once-through cooling water may be discharged with a total organic carbon concentration not to exceed 5 mg/l. 
NR 279.56 History History: Cr. Register, October, 1986, No. 370, eff. 11-1-86.
NR 279.57 NR 279.57Pretreatment standards for new sources (PSNS). Except as provided in 40 CFR 403.7 any existing [new] source subject to this subcategory which introduces pollutants into a publicly owned treatment works shall comply with 40 CFR Part 403 and achieve the following pretreatment standards for new sources (PSNS).
NR 279.57(1) (1) The following standards apply to the total refinery flow contribution to the POTW: - See PDF for table PDF
NR 279.57 Note 1 Where the discharge to the POTW consists solely of sour waters, the owner or operator has the option of complying with this limit or the daily maximum mass limitation for ammonia set forth in s. NR 279.53 (1) and (2).
NR 279.57(2) (2) The following standard is applied to the cooling tower discharge part of the total refinery flow to the POTW by multiplying:
NR 279.57(2)(a) (a) The standards;
NR 279.57(2)(b) (b) By the total refinery flow to the POTW; and
NR 279.57(2)(c) (c) By the ratio of the cooling tower discharge flow to the total refinery flow. - See PDF for table PDF
NR 279.57 History History: Cr. Register, October, 1986, No. 370, eff. 11-1-86.
NR 279.60 NR 279.60Cross-reference. The federal citations in this chapter correspond to provisions of the Wisconsin administrative code and Wisconsin statutes. The federal citations may be cross-referenced in the following table: - See PDF for table PDF
NR 279.60 History History: Cr. Register, October, 1986, No. 370, eff. 11-1-86.
Appendix A
Processes Included in the Determination of BAT Effluent Limitations for Total Chromium, Hexavalent Chromium, and Phenolic Compounds (4AAP)
Crude Processes:
1. Atmospheric Crude Distillation
2. Crude Desalting
3. Vacuum Crude Distillation
Cracking and Coking Processes:
4. Visbreaking
5. Thermal Cracking
6. Fluid Catalytic Cracking
7. Moving Bed Catalytic Cracking
10. Hydrocracking
15. Delayed Coking
16. Fluid Coking
54. Hydrotreating
Asphalt Processes:
18. Asphalt Production
32. 200°F Softening Point Unfluxed Asphalt
43. Asphalt Oxidizing
89. Asphalt Emulsifying
Lube Processes:
21. Hydrofining, Hydrofinishing, Lube Hydrofining
22. White Oil Manufacture
23. Propane Dewaxing, Propane Deasphalting, Propane Fractioning, Propane Deresining
24. Duo Sol, Solvent Treating, Solvent Extraction, Duotreating, Solvent Dewaxing, Solvent Deasphalting
25. Lube Vac Twr, Oil Fractionation, Batch Still (Naphtha Strip), Bright Stock Treating
26. Centrifuge & Chilling
27. MEK Dewaxing, Ketone Dewaxing, MEK-Toluene Dewaxing
28. Deoiling (wax)
29. Naphthenic Lubes Production
30. SO2 Extraction
34. Wax Pressing
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Published under s. 35.93, Stats. Updated on the first day of each month. Entire code is always current. The Register date on each page is the date the chapter was last published.