[Code of Federal Regulations]
[Title 40, Volume 28]
[Revised as of July 1, 2006]
From the U.S. Government Printing Office via GPO Access
[CITE: 40CFR419.57]
[Page 385-386]
TITLE 40--PROTECTION OF ENVIRONMENT
CHAPTER I--ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)
PART 419_PETROLEUM REFINING POINT SOURCE CATEGORY--Table of Contents
Subpart E_Integrated Subcategory
Sec. 419.57 Pretreatment standards for new sources (PSNS).
Except as provided in 40 CFR 403.7, any new source subject to this
subpart
[[Page 386]]
which introduces pollutants into a publicly owned treatment works must
comply with 40 CFR part 403 and achieve the following pretreatment
standards for new sources (PSNS).
(a) The following standards apply to the total refinery flow
contribution to the POTW:
------------------------------------------------------------------------
Pretreatment
standards for
Pollutant or pollutant property new sources--
maximum for any
1 day
------------------------------------------------------------------------
Milligrams per
liter (mg/l)
---------------
Oil and grease........................................ 100
Ammonia (as N)........................................ \1\ 100
------------------------------------------------------------------------
\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 Sec. 419.56
(a) and (b).
(b) The following standard is applied to the cooling tower discharge
part of the total refinery flow to the POTW by multiplying: (1) The
standards; (2) by the total refinery flow to the POTW; and (3) by the
ratio of the cooling tower discharge flow to the total refinery flow.
------------------------------------------------------------------------
Pretreatment
standards for
Pollutant or pollutant property new sources--
maximum for any
1 day
------------------------------------------------------------------------
Milligrams per
liter (mg/1)
---------------
Total chromium........................................ 1
------------------------------------------------------------------------
Appendix A to Part 419--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[deg] 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 and Chilling
27. MEK Dewaxing, Ketone Dewaxing, MEK-Toluene Dewaxing
28. Deoiling (wax)
29. Naphthenic Lubes Production
30. SO2 Extraction
34. Wax Pressing
35. Wax Plant (with Neutral Separation)
36. Furfural Extraction
37. Clay Contacting--Percolation
38. Wax Sweating
39. Acid Treating
40. Phenol Extraction
Reforming and Alkylation Processes
8. H2SO4 Alkylation
12. Catalytic Reforming
[50 FR 28528, July 12, 1985; 50 FR 32414, Aug. 12, 1985]