8. For contaminated soil subject to LDRs as provided in under s. NR 668.49 (1), the constituents subject to treatment as described in under s. NR 668.49 (4), and the following statement: This contaminated soil [does/does not] contain listed hazardous waste and [does/does not] exhibit a characteristic of hazardous waste and [is subject to/complies with with] the soil treatment standards as provided by under s. NR 668.49 (3) or the universal treatment standards | ✓ | ✓ |
Technology code | Description of technology−based standards |
ADGAS: AMLGM: BIODG: CARBN: CHOXD: CHRED: CMBST: DEACT: FSUBS: HLVIT: IMERC: INCIN: LLEXT: MACRO: NEUTR: NLDBR: POLYM: PRECP: RBERY: RCGAS: RCORR: RLEAD: RMERC: RMETL: RORGS: RTHRM: RZINC: STABL: SSTRP: WETOX: WTRRX: | Venting of compressed gases into an absorbing or reacting media (i.e., solid or liquid)—venting can be accomplished through physical release utilizing valves or piping; physical penetration of the container; or penetration through detonation. Amalgamation of liquid, elemental mercury contaminated with radioactive materials utilizing inorganic reagents such as copper, zinc, nickel, gold, and sulfur that result in a nonliquid, semi−solid amalgam and thereby reducing potential emissions of elemental mercury vapors to the air. Biodegradation of organics or non−metallic inorganics (i.e., degradable inorganics that contain the elements of phosphorus, nitrogen, and sulfur) in units operated under either aerobic or anaerobic conditions such that a surrogate compound or indicator parameter has been substantially reduced in concentration in the residuals (e.g., total organic carbon can often be used as an indicator parameter for the biodegradation of many organic constituents that cannot be directly analyzed in wastewater residues). Carbon adsorption (granulated or powdered) of non−metallic inorganics, organo−metallics, or organic constituents, operated such that a surrogate compound or indicator parameter has not undergone breakthrough (e.g., total organic carbon can often be used as an indicator parameter for the adsorption of many organic constituents that cannot be directly analyzed in wastewater residues). Breakthrough occurs when the carbon has become saturated with the constituent (or indicator parameter) and substantial change in adsorption rate associated with that constituent occurs. Chemical or electrolytic oxidation utilizing the following oxidation reagents (or waste reagents) or combinations of reagents: (1) Hypochlorite (e.g., bleach); (2) chlorine; (3) chlorine dioxide; (4) ozone or UV (ultraviolet light) assisted ozone; (5) peroxides; (6) persulfates; (7) perchlorates; (8) permangantes; or (9) other oxidizing reagents of equivalent efficiency, performed in units operated such that a surrogate compound or indicator parameter has been substantially reduced in concentration in the residuals (e.g., total organic carbon can often be used as an indicator parameter for the oxidation of many organic constituents that cannot be directly analyzed in wastewater residues). Chemical oxidation specifically includes what is commonly referred to as alkaline chlorination. Chemical reduction utilizing the following reducing reagents (or waste reagents) or combinations of reagents: (1) Sulfur dioxide; (2) sodium, potassium, or alkali salts or sulfites, bisulfites, metabisulfites, and polyethylene glycols (e.g., NaPEG and KPEG); (3) sodium hydrosulfide; (4) ferrous salts; or (5) other reducing reagents of equivalent efficiency, performed in units operated such that a surrogate compound or indicator parameter has been substantially reduced in concentration in the residuals (e.g., total organic halogens can often be used as an indicator parameter for the reduction of many halogenated organic constituents that cannot be directly analyzed in wastewater residues). Chemical reduction is commonly used for the reduction of hexavalent chromium to the trivalent state. High temperature organic destruction technologies, such as combustion in incinerators, boilers, or industrial furnaces operated in accordance with the applicable requirements of subch. O of ch. NR 664 or 665, or subch. H of ch. NR 666, and in other units operated in accordance with applicable technical operating requirements; and certain non−combustive technologies, such as the catalytic extraction process. Deactivation to remove the hazardous characteristics of a waste due to its ignitability, corrosivity, or reactivity. Fuel substitution in units operated in accordance with applicable technical operating requirements. Vitrification of high level mixed radioactive wastes in units in compliance with all applicable radioactive protection requirements under control of the nuclear regulatory commission. Incineration of wastes containing organics and mercury in units operated according to the technical operating requirements of subch. O of ch. NR 664 and 665. All wastewater and nonwastewater residues derived from this process shall then comply with the corresponding treatment standards per waste code with consideration of any applicable subcategories (e.g., high or low mercury subcategories). Incineration in units operated in accordance with the technical operating requirements of subch. O of ch. NR 664 and 665. Liquid−liquid extraction (often referred to as solvent extraction) of organics from liquid wastes into an immiscible solvent for which the hazardous constituents have a greater solvent affinity, resulting in an extract high in organics that shall undergo either incineration, reuse as a fuel, or other recovery or reuse and a raffinate (extracted liquid waste) proportionately low in organics that shall undergo further treatment as specified in the standard. Macroencapsulation with surface coating materials such as polymeric organics (e.g., resins and plastics) or with a jacket of inert inorganic materials to substantially reduce surface exposure to potential leaching media. Macroencapsulation specifically does not include any material that would be classified as a tank or container according to s. NR 660.10. Neutralization with the following reagents (or waste reagents) or combinations of reagents: (1) acids; (2) bases; or (3) water (including wastewaters) resulting in a pH greater than 2 but less than 12.5 as measured in the aqueous residuals. No land disposal based on recycling. Formation of complex high−molecular weight solids through polymerization of monomers in high−TOC D001 non−wastewaters which are chemical components in the manufacture of plastics. Chemical precipitation of metals and other inorganics as insoluble precipitates of oxides, hydroxides, carbonates, sulfides, sulfates, chlorides, fluorides, or phosphates. The following reagents (or waste reagents) are typically used alone or in combination: (1) lime (i.e., containing oxides or hydroxides of calcium or magnesium; (2) caustic (i.e., sodium or potassium hydroxides; (3) soda ash (i.e., sodium carbonate); (4) sodium sulfide; (5) ferric sulfate or ferric chloride; (6) alum; or (7) sodium sulfate. Additional floculating, coagulation or similar reagents or processes that enhance sludge dewatering characteristics are not precluded from use. Thermal recovery of beryllium. Recovery or reuse of compressed gases including techniques such as reprocessing of the gases for reuse or resale; filtering or adsorption of impurities; remixing for direct reuse or resale; and use of the gas as a fuel source. Recovery of acids or bases utilizing one or more of the following recovery technologies: (1) distillation (i.e., thermal concentration); (2) ion exchange; (3) resin or solid adsorption; (4) reverse osmosis; or (5) incineration for the recovery of acid—Note: this does not preclude the use of other physical phase separation or concentration techniques such as decantation, filtration (including ultrafiltration), and centrifugation, when used in conjunction with the above listed recovery technologies. Thermal recovery of lead in secondary lead smelters. Retorting or roasting in a thermal processing unit capable of volatilizing mercury and subsequently condensing the volatilized mercury for recovery. The retorting or roasting unit (or facility) shall be subject to one or more of the following: (a) a National Emissions Standard for Hazardous Air Pollutants (NESHAP) for mercury; (b) a Best Available Control Technology (BACT) or a Lowest Achievable Emission Rate (LAER) standard for mercury imposed pursuant to a Prevention of Significant Deterioration (PSD) permit; or (c) a state permit that establishes emission limitations (within meaning of section 302 of the Clean Air Act) for mercury. All wastewater and nonwastewater residues derived from this process shall then comply with the corresponding treatment standards per waste code with consideration of any applicable subcategories (e.g., high or low mercury subcategories). Recovery of metals or inorganics utilizing one or more of the following direct physical or removal technologies: (1) ion exchange; (2) resin or solid (i.e., zeolites) adsorption; (3) reverse osmosis; (4) chelation or solvent extraction; (5) freeze crystalization; (6) ultrafiltration and/or (7) simple precipitation (i.e., crystalization)—Note: This does not preclude the use of other physical phase separation or concentration techniques such as decantation, filtration (including ultrafiltration), and centrifugation, when used in conjunction with the above listed recovery technologies. Recovery of organics utilizing one or more of the following technologies: (1) distillation; (2) thin film evaporation; (3) steam stripping; (4) carbon adsorption; (5) critical fluid extraction; (6) liquid−liquid extraction; (7) precipitation or crystallization (including freeze crystallization); or (8) chemical phase separation techniques (i.e., addition of acids, bases, demulsifiers, or similar chemicals);—Note: this does not preclude the use of other physical phase separation techniques such as a decantation, filtration (including ultrafiltration), and centrifugation, when used in conjunction with the above listed recovery technologies. Thermal recovery of metals or inorganics from nonwastewaters in units identified as industrial furnaces according to s. NR 660.10 (a), (f), (g), (k) and (L) under the definition of “industrial furnaces”. Resmelting in high temperature metal recovery units for the purpose of recovery of zinc. Stabilization with the following reagents (or waste reagents) or combinations of reagents: (1) Portland cement; or (2) lime/pozzolans (e.g., fly ash and cement kiln dust)—this does not preclude the addition of reagents (e.g., iron salts, silicates, and clays) designed to enhance the set/cure time or compressive strength, or to overall reduce the leachability of the metal or inorganic. Steam stripping of organics from liquid wastes utilizing direct application of steam to the wastes operated such in a manner that liquid and vapor flow rates, as well as, temperature and pressure ranges have been optimized, monitored, and maintained. These operating parameters are dependent upon the design parameters of the unit, such as, the number of separation stages and the internal column design. Thus, thus, resulting in a condensed extract high in organics that shall undergo either incineration, reuse as a fuel, or other recovery or reuse and an extracted wastewater that shall undergo further treatment as specified in the standard. Wet air oxidation performed in units operated such that a surrogate compound or indicator parameter has been substantially reduced in concentration in the residuals (e.g., total organic carbon can often be used as an indicator parameter for the oxidation of many organic constituents that cannot be directly analyzed in wastewater residues). Controlled reaction with water for highly reactive inorganic or organic chemicals with precautionary controls for protection of workers from potential violent reactions as well as precautionary controls for potential emissions of toxic or ignitable levels of gases released during the reaction. |
Technology description | Performance and/or design and operating standard | Contaminant restrictions2 |
B. Destruction Technologies: |
2. Chemical Destruction |
a. Chemical Oxidation: Chemical or electolytic electrolytic oxidation utilizing the following oxidation reagents (,or waste reagents), or combination of reagents—(1) hypochlorite (e.g., bleach); (2) chlorine; (3) chlorine dioxide; (4) ozone or UV (ultraviolet light) assisted ozone; (5) peroxides; (6) persulfates; (7) perchlorates; (8) permanganates; or (9) other oxidizing reagents of equivalent destruction efficiency4. Chemical oxidation specifically includes what is referred to as alkaline chlorination. | All Debris: Obtain an “Equivalent Technology” approval under s. NR 668.42 (2)8; treated debris shall be separated from treatment residuals using simple physical or mechanical means9, and, prior to further treatment, the residue shall meet the waste−specific treatment standards for organic compounds in the waste contaminating the debris. Brick, Cloth, Concrete, Paper, Pavement, Rock, Wood: Debris shall be no more than 1.2 cm (½ inch) in one dimension (i.e., thickness limit)5, except that this thickness limit may be waived under the “Equivalent Technology” approval. | All Debris: Metal contaminants. |
Regulated constituent common name Organic Constituents | CAS1 Number | Wastewater Standard | Nonwastewater Standard |
Concentration2 in mg/ L2mg/L | Concentration3 in mg/kg3mg/kg unless noted as “mg/L TCLP” |
Acenaphthylene | 208−96−8 | 0.059 | 3.4 |
Acenaphthene | 83−32−9 | 0.059 | 3.4 |
Acetone | 67−64−1 | 0.28 | 160 |
Acetonitrile | 75−05−8 | 5.6 | 38 |
Acetophenone | 96−86−2 | 0.010 | 9.7 |
2−Acetylaminofluorene | 53−96−3 | 0.059 | 140 |
Acrolein | 107−02−8 | 0.29 | NA |
Acrylamide | 79−06−1 | 19 | 23 |
Acrylonitrile | 107−13−1 | 0.24 | 84 |
Aldrin | 309−00−2 | 0.021 | 0.066 |
4−Aminobiphenyl | 92−67−1 | 0.13 | NA |
Aniline | 62−53−3 | 0.81 | 14 |
o−Anisidine (2−methoxyaniline) | 90−04−0 | 0.010 | 0.66 |
Anthracene | 120−12−7 | 0.059 | 3.4 |
Aramite | 140−57−8 | 0.36 | NA |
alpha−BHC | 319−84−6 | 0.00014 | 0.066 |
beta−BHC | 319−85−7 | 0.00014 | 0.066 |
delta−BHC | 319−86−8 | 0.023 | 0.066 |
gamma−BHC | 58−89−9 | 0.0017 | 0.066 |
Benzene | 71−43−2 | 0.14 | 10 |
Benz(a)anthracene | 56−55−3 | 0.059 | 3.4 |
Benzal chloride | 98−87−3 | 0.055 | 6.0 |
Benzo(b)fluoranthene (difficult to distinguish from benzo(k)fluoranthene) | 205−99−2 | 0.11 | 6.8 |
Benzo(k)fluoranthene (difficult to distinguish from benzo(b)fluoranthene) | 207−08−9 | 0.11 | 6.8 |
Benzo(g,h,i)perylene | 191−24−2 | 0.0055 | 1.8 |
Benzo(a)pyrene | 50−32−8 | 0.061 | 3.4 |
Bromodichloromethane | 75−27−4 | 0.35 | 15 |
Bromomethane/Methyl bromide | 74−83−9 | 0.11 | 15 |
4−Bromophenyl phenyl ether | 101−55−3 | 0.055 | 15 |
n−Butyl alcohol | 71−36−3 | 5.6 | 2.6 |
Butyl benzyl phthalate | 85−68−7 | 0.017 | 28 |
2−sec−Butyl−4,6−dinitrophenol/Dinoseb | 88−85−7 | 0.066 | 2.5 |
Carbon disulfide | 75−15−0 | 3.8 | 4.8 mg/L TCLP |
Carbon tetrachloride | 56−23−5 | 0.057 | 6.0 |
Chlordane (alpha and gamma isomers) | 57−74−9 | 0.0033 | 0.26 |
p−Chloroaniline | 106−47−8 | 0.46 | 16 |
Chlorobenzene | 108−90−7 | 0.057 | 6.0 |
Chlorobenzilate | 510−15−6 | 0.10 | NA |
2−Chloro−1,3−butadiene | 126−99−8 | 0.057 | 0.28 |
Chlorodibromomethane | 124−48−1 | 0.057 | 15 |
Chloroethane | 75−00−3 | 0.27 | 6.0 |
bis(2−Chloroethoxy)methane | 111−91−1 | 0.036 | 7.2 |
bis(2−Chloroethyl)ether | 111−44−4 | 0.033 | 6.0 |
Chloroform | 67−66−3 | 0.046 | 6.0 |
bis(2−Chloroisopropyl)ether | 39638−32−9 | 0.055 | 7.2 |
p−Chloro−m−cresol | 59−50−7 | 0.018 | 14 |
2−Chloroethyl vinyl ether | 110−75−8 | 0.062 | NA |
Chloromethane/Methyl chloride | 74−87−3 | 0.19 | 30 |
2−Chloronaphthalene | 91−58−7 | 0.055 | 5.6 |
2−Chlorophenol | 95−57−8 | 0.044 | 5.7 |
3−Chloropropylene | 107−05−1 | 0.036 | 30 |
Chrysene | 218−01−9 | 0.059 | 3.4 |
p−Cresidine | 120−71−8 | 0.010 | 0.66 |
o−Cresol | 95−48−7 | 0.11 | 5.6 |
m−Cresol (difficult to distinguish from p−cresol) | 108−39−4 | 0.77 | 5.6 |
p−Cresol (difficult to distinguish from m−cresol) | 106−44−5 | 0.77 | 5.6 |
Cyclohexanone | 108−94−1 | 0.36 | 0.75 mg/L TCLP |
o,p’−DDD | 53−19−0 | 0.023 | 0.087 |
p,p’−DDD | 72−54−8 | 0.023 | 0.087 |
o,p’−DDE | 3424−82−6 | 0.031 | 0.087 |
p,p’−DDE | 72−55−9 | 0.031 | 0.087 |
o,p’−DDT | 789−02−6 | 0.0039 | 0.087 |
p,p’−DDT | 50−29−3 | 0.0039 | 0.087 |
Dibenz(a,h)anthracene | 53−70−3 | 0.055 | 8.2 |
Dibenz(a,e)pyrene | 192−65−4 | 0.061 | NA |
1,2−Dibromo−3−chloropropane | 96−12−8 | 0.11 | 15 |
1,2−Dibromoethane/Ethylene dibromide | 106−93−4 | 0.028 | 15 |
Dibromomethane | 74−95−3 | 0.11 | 15 |
m−Dichlorobenzene | 541−73−1 | 0.036 | 6.0 |
o−Dichlorobenzene | 95−50−1 | 0.088 | 6.0 |
p−Dichlorobenzene | 106−46−7 | 0.090 | 6.0 |
Dichlorodifluoromethane | 75−71−8 | 0.23 | 7.2 |
1,1−Dichloroethane | 75−34−3 | 0.059 | 6.0 |
1,2−Dichloroethane | 107−06−2 | 0.21 | 6.0 |
1,1−Dichloroethylene | 75−35−4 | 0.025 | 6.0 |
trans−1,2−Dichloroethylene | 156−60−5 | 0.054 | 30 |
2,4−Dichlorophenol | 120−83−2 | 0.044 | 14 |
2,6−Dichlorophenol | 87−65−0 | 0.044 | 14 |
2,4−Dichlorophenoxyacetic acid/2,4−D | 94−75−7 | 0.72 | 10 |
1,2−Dichloropropane | 78−87−5 | 0.85 | 18 |
cis−1,3−Dichloropropylene | 10061−01−5 | 0.036 | 18 |
trans−1,3−Dichloropropylene | 10061−02−6 | 0.036 | 18 |
Dieldrin | 60−57−1 | 0.017 | 0.13 |
Diethyl phthalate | 84−66−2 | 0.20 | 28 |
p−Dimethylaminoazobenzene | 60−11−7 | 0.13 | NA |
2,4−Dimethylanaline (2,4−xylidine) | 95−68−1 | 0.010 | 0.66 |
2−4−Dimethyl phenol | 105−67−9 | 0.036 | 14 |
Dimethyl phthalate | 131−11−3 | 0.047 | 28 |
Di−n−butyl phthalate | 84−74−2 | 0.057 | 28 |
1,4−Dinitrobenzene | 100−25−4 | 0.32 | 2.3 |
4,6−Dinitro−o−cresol | 534−52−1 | 0.28 | 160 |
2,4−Dinitrophenol | 51−28−5 | 0.12 | 160 |
2,4−Dinitrotoluene | 121−14−2 | 0.32 | 140 |
2,6−Dinitrotoluene | 606−20−2 | 0.55 | 28 |
Di−n−octyl phthalate | 117−84−0 | 0.017 | 28 |
Di−n−propylnitrosamine | 621−64−7 | 0.40 | 14 |
1,4−Dioxane | 123−91−1 | 12.0 | 170 |
Diphenylamine (difficult to distinguish from diphenylnitrosamine) | 122−39−4 | 0.92 | 13 |
Diphenylnitrosamine (difficult to distinguish from diphenylamine) | 86−30−6 | 0.92 | 13 |
1,2−Diphenylhydrazine | 122−66−7 | 0.087 | NA |
Disulfoton | 298−04−4 | 0.017 | 6.2 |
Endosulfan I | 959−98−8 | 0.023 | 0.066 |
Endosulfan II | 33213−65−9 | 0.029 | 0.13 |
Endosulfan sulfate | 1031−07−8 | 0.029 | 0.13 |
Endrin | 72−20−8 | 0.0028 | 0.13 |
Endrin aldehyde | 7421−93−4 | 0.025 | 0.13 |
Ethyl acetate | 141−78−6 | 0.34 | 33 |
Ethyl benzene | 100−41−4 | 0.057 | 10 |
Ethyl cyanide/Propanenitrile | 107−12−0 | 0.24 | 360 |
Ethyl ether | 60−29−7 | 0.12 | 160 |
bis(2−Ethylhexyl)phthalate | 117−81−7 | 0.28 | 28 |
Ethyl methacrylate | 97−63−2 | 0.14 | 160 |
Ethylene oxide | 75−21−8 | 0.12 | NA |
Famphur | 52−85−7 | 0.017 | 15 |
Fluoranthene | 206−44−0 | 0.068 | 3.4 |
Fluorene | 86−73−7 | 0.059 | 3.4 |
Heptachlor | 76−44−8 | 0.0012 | 0.066 |
Heptachlor epoxide | 1024−57−3 | 0.016 | 0.066 |
1,2,3,4,6,7,8−Heptachlorodibenzo−p−dioxin(1,2,3,4,6,7,8−HpCDD) | 35822−46−9 | 0.000035 | 0.0025 |
1,2,3,4,6,7,8−Heptachlorodibenzofuran (1,2,3,4,6,7,8−HpCDF) | 67562−39−4 | 0.000035 | 0.0025 |
1,2,3,4,7,8,9−Heptachlorodibenzofuran (1,2,3,4,7,8,9−HpCDF) | 55673−89−7 | 0.000035 | 0.0025 |
Hexachlorobenzene | 118−74−1 | 0.055 | 10 |
Hexachlorobutadiene | 87−68−3 | 0.055 | 5.6 |
Hexachlorocyclopentadiene | 77−47−4 | 0.057 | 2.4 |
HxCDDs (All Hexachlorodibenzo−p−dioxins) | NA | 0.000063 | 0.001 |
HxCDFs (All Hexachlorodibenzofurans) | NA | 0.000063 | 0.001 |
Hexachloroethane | 67−72−1 | 0.055 | 30 |
Hexachloropropylene | 1888−71−7 | 0.035 | 30 |
Indeno (1,2,3−c,d) pyrene | 193−39−5 | 0.0055 | 3.4 |
Iodomethane | 74−88−4 | 0.19 | 65 |
Isobutyl alcohol | 78−83−1 | 5.6 | 170 |
Isodrin | 465−73−6 | 0.021 | 0.066 |
Isosafrole | 120−58−1 | 0.081 | 2.6 |
Kepone | 143−50−0 | 0.0011 | 0.13 |
Methacrylonitrile | 126−98−7 | 0.24 | 84 |
Methanol | 67−56−1 | 5.6 | 0.75 mg/L TCLP |
Methapyrilene | 91−80−5 | 0.081 | 1.5 |
Methoxychlor | 72−43−5 | 0.25 | 0.18 |
3−Methylcholanthrene | 56−49−5 | 0.0055 | 15 |
4,4−Methylene bis(2−chloroaniline) | 101−14−4 | 0.50 | 30 |
Methylene chloride | 75−09−2 | 0.089 | 30 |
Methyl ethyl ketone | 78−93−3 | 0.28 | 36 |
Methyl isobutyl ketone | 108−10−1 | 0.14 | 33 |
Methyl methacrylate | 80−62−6 | 0.14 | 160 |
Methyl methansulfonate | 66−27−3 | 0.018 | NA |
Methyl parathion | 298−00−0 | 0.014 | 4.6 |
Naphthalene | 91−20−3 | 0.059 | 5.6 |
2−Naphthylamine | 91−59−8 | 0.52 | NA |
o−Nitroaniline | 88−74−4 | 0.27 | 14 |
p−Nitroaniline | 100−01−6 | 0.028 | 28 |
Nitrobenzene | 98−95−3 | 0.068 | 14 |
5−Nitro−o−toluidine | 99−55−8 | 0.32 | 28 |
o−Nitrophenol | 88−75−5 | 0.028 | 13 |
p−Nitrophenol | 100−02−7 | 0.12 | 29 |
N−Nitrosodiethylamine | 55−18−5 | 0.40 | 28 |
N−Nitrosodimethylamine | 62−75−9 | 0.40 | 2.3 |
N−Nitroso−di−n−butylamine | 924−16−3 | 0.40 | 17 |
N−Nitrosomethylethylamine | 10595−95−6 | 0.40 | 2.3 |
N−Nitrosomorpholine | 59−89−2 | 0.40 | 2.3 |
N−Nitrosopiperidine | 100−75−4 | 0.013 | 35 |
N−Nitrosopyrrolidine | 930−55−2 | 0.013 | 35 |
1,2,3,4,6,7,8,9−Octachlorodibenzo−p−dioxin (OCDD) | 3268−87−9 | 0.000063 | 0.005 |
1,2,3,4,6,7,8,9−Octachlorodibenzofuran (OCDF) | 39001−02−0 | 0.000063 | 0.005 |
Parathion | 56−38−2 | 0.014 | 4.6 |
Total PCBs (sum of all PCB isomers, or all Aroclors)8 | 1336−36−3 | 0.10 | 10 |
Pentachlorobenzene | 608−93−5 | 0.055 | 10 |
PeCDDs (All Pentachlorodibenzo−p−dioxins) | NA | 0.000063 | 0.001 |
PeCDFs (All Pentachlorodibenzofurans) | NA | 0.000035 | 0.001 |
Pentachloroethane | 76−01−7 | 0.055 | 6.0 |
Pentachloronitrobenzene | 82−68−8 | 0.055 | 4.8 |
Pentachlorophenol | 87−86−5 | 0.089 | 7.4 |
Phenacetin | 62−44−2 | 0.081 | 16 |
Phenanthrene | 85−01−8 | 0.059 | 5.6 |
Phenol | 108−95−2 | 0.039 | 6.2 |
1,3−Phenylenediamine | 108−45−2 | 0.010 | 0.66 |
Phorate | 298−02−2 | 0.021 | 4.6 |
Phthalic acid | 100−21−0 | 0.055 | 28 |
Phthalic anhydride | 85−44−9 | 0.055 | 28 |
Pronamide | 23950−58−5 | 0.093 | 1.5 |
Pyrene | 129−00−0 | 0.067 | 8.2 |
Pyridine | 110−86−1 | 0.014 | 16 |
Safrole | 94−59−7 | 0.081 | 22 |
Silvex/2,4,5−TP | 93−72−1 | 0.72 | 7.9 |
1,2,4,5−Tetrachlorobenzene | 95−94−3 | 0.055 | 14 |
TCDDs (All Tetrachlorodibenzo−p−dioxins) | NA | 0.000063 | 0.001 |
TCDFs (All Tetrachlorodibenzofurans) | NA | 0.000063 | 0.001 |
1,1,1,2−Tetrachloroethane | 630−20−6 | 0.057 | 6.0 |
1,1,2,2−Tetrachloroethane | 79−34−5 | 0.057 | 6.0 |
Tetrachloroethylene | 127−18−4 | 0.056 | 6.0 |
2,3,4,6−Tetrachlorophenol | 58−90−2 | 0.030 | 7.4 |
Toluene | 108−88−3 | 0.080 | 10 |
Toxaphene | 8001−35−2 | 0.0095 | 2.6 |
Tribromomethane/Bromoform | 75−25−2 | 0.63 | 15 |
1,2,4−Trichlorobenzene | 120−82−1 | 0.055 | 19 |
1,1,1−Trichloroethane | 71−55−6 | 0.054 | 6.0 |
1,1,2−Trichloroethane | 79−00−5 | 0.054 | 6.0 |
Trichloroethylene | 79−01−6 | 0.054 | 6.0 |
Trichloromonofluoromethane | 75−69−4 | 0.020 | 30 |
2,4,5−Trichlorophenol | 95−95−4 | 0.18 | 7.4 |
2,4,6−Trichlorophenol | 88−06−2 | 0.035 | 7.4 |
2,4,5−Trichlorophenoxyacetic acid/2,4,5−T | 93−76−5 | 0.72 | 7.9 |
1,2,3−Trichloropropane | 96−18−4 | 0.85 | 30 |
1,1,2−Trichloro−1,2,2−trifluoroethane | 76−13−1 | 0.057 | 30 |
tris−(2,3−Dibromopropyl) phosphate | 126−72−7 | 0.11 | 0.10 |
Vinyl chloride | 75−01−4 | 0.27 | 6.0 |
Xylenes−mixed isomers (sum of o−, m−, and p−xylene concentrations) | 1330−20−7 | 0.32 | 30 |
Inorganic Constituents |
Antimony | 7440−36−0 | 1.9 | 1.15 mg/L TCLP |
Arsenic | 7440−38−2 | 1.4 | 5.0 mg/L TCLP |
Barium | 7440−39−3 | 1.2 | 21 mg/L TCLP |
Beryllium | 7440−41−7 | 0.82 | 1.22 mg/L TCLP |
Cadmium | 7440−43−9 | 0.69 | 0.11 mg/L TCLP |
Chromium (Total) | 7440−47−3 | 2.77 | 0.60 mg/L TCLP |
Cyanides (Total)4 | 57−12−5 | 1.2 | 590 |
Cyanides (Amenable)4 | 57−12−5 | 0.86 | 30 |
Fluoride5 | 16984−48−8 | 35 | NA |
Lead | 7439−92−1 | 0.69 | 0.75 mg/L TCLP |
Mercury − Nonwastewater from Retort | 7439−97−6 | NA | 0.20 mg/L TCLP |
Mercury − All Others | 7439−97−6 | 0.15 | 0.025 mg/L TCLP |
Nickel | 7440−02−0 | 3.98 | 11. mg/L TCLP |
Selenium7 | 7782−49−2 | 0.82 | 5.7 mg/L TCLP |
Silver | 7440−22−4 | 0.43 | 0.14 mg/L TCLP |
Sulfide5 | 18496−25−8 | 14 | NA |
Thallium | 7440−28−0 | 1.4 | 0.20 mg/L TCLP |
Vanadium5 | 7440−62−2 | 4.3 | 1.6 mg/L TCLP |
Zinc5 | 7440−66−6 | 2.61 | 4.3 mg/L TCLP |
Modifications | Class |
L. Incinerators, Boilers and Industrial Furnaces: |
9. Changes to hazardous waste license provisions needed to support transition to 40 CFR part 63 (Subpart EEE—National Emission Standards for Hazardous Air Pollutants from Hazardous Waste Combustors), provided the procedures of under s. NR 670.042 (11) are followed. | 11 1-1 |
O. Burden Reduction: |
1. Development of one contingency plan based on Integrated Contingency Plan Guidance pursuant to s. NR 664.0052 (2) | 11 1-1 |
Constituent or property | Allowable level |
Arsenic . . . . . . . . . . . . . . Cadmium . . . . . . . . . . . Chromium . . . . . . . . . . . . Lead . . . . . . . . . . . . . . . Flash point . . . . . . . . . . Total halogens | 5 ppm maximum 2 ppm maximum 10 ppm maximum 100 ppm maximum 100 0F minimum 4,000 ppm maximum2 |
