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B.C. Reg. 214/2004, deposited May 14, 2004, pursuant to the WASTE MANAGEMENT ACT [Section 57]. Order in Council 467/2004, approved and ordered May 13, 2004.
On the recommendation of the undersigned, the Administrator, by and with the advice and consent of the Executive Council, orders that the Special Waste Regulation, B.C. Reg. 63/88, is amended as set out in the attached Schedule.
— B. BARISOFF, Minister of Water, Land and Air Protection; G. COLLINS, Presiding Member of the Executive Council.
Schedule
1 Section 1 of the Special Waste Regulation, B.C. Reg. 63/88, is amended
(a) by repealing the definition of "carrier" and substituting the following:
"carrier" means a person who, whether or not for hire or reward, has possession of special waste immediately before, during and immediately after the transport of the special waste;
(b) by repealing the definition of "consignee" and substituting the following:
"consignee" means a person to whom special waste is transported or is intended to be transported;
(c) by repealing the definition of "consignor" and substituting the following:
"consignor" means a person who has possession of special waste immediately before it is transported and who prepares the special waste for transportation to a consignee;
(d) by repealing the definition of "container" and substituting the following:
"container" means a portable receptacle in which waste is stored, transported, treated, disposed of, or otherwise handled;
(e) by repealing the definition of "dangerous goods" and substituting the following:
"dangerous goods" means dangerous goods as defined in section 2 of the federal Act and as regulated in the federal dangerous goods regulations, except for the exemption for dangerous goods within manufacturing or processing facilities under section 1.25 of the federal dangerous good regulations;
(f) by repealing the definition of "Federal Regulations";
(g) by adding the following definitions:
"federal Act" means the Transportation of Dangerous Goods Act, 1992 (Canada), as amended from time to time;
"federal dangerous goods regulations" means the Transportation of Dangerous Goods Regulations, SOR/2001-286, as amended from time to time;
"federal interprovincial movement regulations" means the Interprovincial Movement of Hazardous Waste Regulations, SOR/2002-301, as amended from time to time;
(h) by repealing the definition of "ignitable" and substituting the following:
"ignitable" means having the properties of
(a) gases in Class 2.1,
(b) flammable liquids in Class 3, or
(c) flammable solids, substances liable to spontaneous combustion or substances that on contact with water emit flammable gases in Class 4
of the federal dangerous goods regulations;
(i) by repealing the definition of "labpack" and substituting the following:
"labpack" means a drum or a barrel with a maximum capacity of 454 litres that
(a) is used to transport several containers of special waste for storage, recycle or disposal, and
(b) includes one or more inner linings that contain absorbent or cushioned packaging for safety of storage or transport of the containers of special waste;
(j) by repealing the definition of "leachable toxic waste" and substituting the following:
"leachable toxic waste" means waste when subject to the extraction procedure described in the US EPA Method 1311 produces an extract with a contaminant concentration greater than those prescribed in Table 1 of Schedule 4; ,
(k) in the definition of "reactive" by striking out "the Federal Regulations" in both places and substituting "the federal dangerous goods regulations",
(l) in the definition of "special waste" by repealing paragraphs (a), (n) and (o),
(m) in the definition of "special waste" by adding the following paragraph:
(i.1) waste designated in section 1.1.
2 Section 2 (14) is repealed.
3 The following section is added:
1.1 (1) The wastes listed in Schedule 7 are designated as special wastes.
(2) The following are designated as special wastes:
(a) dangerous goods that are no longer used for their original purpose if they are
(i) recycled, treated or disposed of, intended for recycle, treatment or disposal or in storage or transit before recycle, treatment or disposal, and
(ii) in Classes 2 to 6, 8 or 9 of the federal dangerous goods regulations;
(b) waste that is corrosive because it has a pH factor of less than 2.0 or greater than 12.5 measured directly when the waste is liquid or measured in a 50 per cent distilled water mixture or solution by mass when the waste is solid.
4 Section 6 (1) (a) is amended by striking out "as described in the Federal Regulations" and substituting "as described in the federal dangerous goods regulations".
5 Section 42 (3) is repealed and the following substituted:
(3) A waste containing a product is designated as a special waste if
(a) the waste fits the criteria for classes 3 to 6.1, 8 or 9 of the federal dangerous goods regulations, and
(b) the aquatic toxicity (the 96 hour LC50) of the waste is less than 500 mg/L as measured by methods that are approved in accordance with section 49.
6 Section 42.4 (1) (a) is amended by striking out "Federal Regulations" and substituting "federal dangerous goods regulations".
7 Sections 46 (2) and (3) are repealed and the following substituted:
(2) Section 9 (1) (a) and (b), (2), and (3) (a) and (b) of the Act does not apply if special wastes are transported
(a) solely within the boundaries of property owned, leased or controlled by the person who generates or stores the special waste if the travelled distance between the shipping site and the receiving site is less than 100 km,
(b) on a public road for a distance of less than 3 km, or
(c) by a home owner from his or her home or a farmer from his or her farm directly to a facility operated by the government or a municipality, or directly to an agent of the government or a municipality.
(3) The prescribed form of the manifest and the prescribed manner of completing, distributing and keeping it are those referred to and set out in the federal interprovincial movement regulations.
8 Section 50 (6) (d) and (f) is amended by striking out "Federal Regulations" and substituting "federal dangerous goods regulations".
9 Schedule 4 is amended
(a) by repealing Part 1,
(b) by repealing Part 2 and Table 1 of Schedule 4 and substituting the following:
Part 2
Modified Leachate Extraction Procedure
1.1 For wastes with 0.5% solids weight by volume or greater, collect a sufficient amount of sample to provide approximately 100 g of solid material using techniques which ensure that the sample is representative of the waste.
1.2 If the waste has less than 0.5% solids weight by volume, collect at least 1 L of sample.
2.1 Sieve, 9.5 mm mesh opening, stainless steel or plastic material.
2.2 Stainless steel filtration unit, 142 mm diameter, minimum 1 L capacity, capable of sustaining a pressure of 5 kg/cm2 , applied to the material to be filtered.
2.3 Membrane filter, 142 mm diameter, 0.45 µm diameter pore size, made of synthetic organic material such as cellulose acetate, cellulose nitrate, nylon or polycarbonate and which is compatible with the leachate to be filtered. Teflon is recommended for organic constituents.
2.4 Glass fibre prefilter, 124 mm diameter 3 µm to 12 µm pore size range.
2.5 Vacuum filtration unit, 90 mm diameter.
2.6 Membrane filter 90 mm diameter as per Step 2.3.
2.7 Glass fibre filter 70 mm diameter as per Step 2.4.
2.8 Solid waste rotary extractor — a device that rotates the bottles end over end about a central axis through 360°, with a speed of 10 rpm. The dimensions of the box will depend on the needs of each laboratory
(Figure 1).
2.9 Structural Integrity Tester with a 3.18 cm diameter hammer weighing 0.33 kg and having a free fall of 15.24 cm
(Figure 2).
2.10 pH meter, with a readability of 0.01 pH unit and accuracy of ± 0.1 pH units.
2.11 Cylindrical bottles, wide mouth, 1 250 ml capacity, polyethylene or glass with Teflon-lined cap for inorganic constituents; glass with Teflon-lined cap or Teflon bottles for organic constituents.
2.12 Cleaning Procedure
All glassware and equipment that comes into contact with the sample should be cleaned in the following way before each use:
2.12.1 Wash with a non-phosphate detergent solution.
2.12.2 Rinse twice with tap water.
2.12.3 Rinse twice with reagent water.
2.12.4 Wash with 10% nitric acids.
2.12.5 Rinse several times with reagent water.
2.12.6 Store bottles filled with 10% nitric acids, until ready to use.
2.12.7 Rinse several times with reagent water before use.
2.12.8 Rinse clean oven dried bottles with methylene chloride, followed by methanol, for organic constituents.
3.1 Reagent water, Type IV (ASTM specification D1193).
3.2 Nitrogen gas, pre-purified, scrubbed through a molecular sieve.
If the sample is not a dry solid separate it into its component phases using the following procedure:
4.1 Determine the dry weight of the solids in the sample at 60°C, using a well homogenized sample. Use this weight to determine the amount of material to be filtered.
4.2 Assemble the filtration unit with a filter bed consisting of a 0.45 µm pore size membrane filter and a coarse glass fibre pre-filter upstream of the membrane filter (per manufacturer's instructions).
4.3 Select one or more blank filters from each batch of filters. Filter 50 ml portions of reagent water through each test filter and analyze the filtrate for the analytical parameters of interest. Note the volume required to reduce the blank values to acceptable levels.
4.4 Wash each filter used in the leach procedure with at least this predetermined volume of water. Filter under pressure until no water flows through the filtrate outlet.
4.5 Remove the moist filter bed from the filtration unit and determine its weight to the nearest ± 0.01 g.
4.6 Re-assemble the filtration unit, replacing the filter beds, as before.
4.7 Comminute the sample, with a mortar and pestle, to a size that will pass through the opening of the filtration unit (less than 9.5 mm).
4.8 Agitate the sample by hand and pour a representative aliquot part of the solid and liquid phases into the opening of the filtration unit. Filter a sufficient amount of the sample to provide at least 60 g of dry solid material.
4.9 Pressurize the reservoir very slowly with nitrogen gas by means of the regulating valve on the nitrogen gas cylinder, until liquid begins to flow freely from the filtrate outlet.
4.10 Increase the pressure in increments of 0.5 kg/cm2 to a maximum of 5 kg/cm2, as the flow diminishes. Continue filtration until the liquid flow ceases or the pressurizing gas begins to exit from the filtrate outlet of the filter unit.
4.11 De-pressurize the filtration unit slowly using the release valve on the filtration unit. Remove and weigh the solid material together with the filter bed to ± 0.01 g. Record the weight of the solid material.
4.12 Measure and record the volume and pH of the liquid phase. Store the liquid at 4°C under nitrogen until required in Step 5.8.
4.13 Discard the solid portion, if the weight is less than 0.5% (w/v) of the aliquot part taken and proceed to step 5.9. If not, proceed to Step 5.1.
Note: For mixtures containing coarse grained solids, where separation can be performed without imposing a 5 kg/cm2 differential pressure, a vacuum filtration unit with a filter bed as per Step 4.2 may be used. Vacuum filtration must not be used if volatile organic compounds are to be analysed.
5.1 Prepare a solid sample for extraction by crushing, cutting or grinding, to pass through a 9.5 mm mesh sieve. If the original sample contains both liquid and solid phases, use the solid material from Step 4.13. The structural integrity procedure, Step 6, should be used for monolithic wastes which are expected to maintain their structural integrity in a landfill, (e.g. some slags and treated solidified wastes).
Note: Do not allow the solid waste material to dry prior to the extraction step.
5.2 Determine the moisture content of the de-watered sample, by drying a suitable aliquot part to constant weight at 60°C in an oven. Discard the dried solid material.
5.3 Place the equivalent of 50 g dry weight of the de-watered undried material into a 1 250 ml wide mouth cylindrical bottle. Use additional bottles if a larger volume of leachate is required for the analysis.
5.4 Add 800 ml (less the moisture content of the sample in ml) of reagent water to the bottle.
5.5 Cap the bottle and agitate it in the rotary extractor for 1 hour.
5.6 Add enough reagent water at the end of the extraction period so that the total volume of liquid is 1 000 ml.
5.7 Separate the material into its component liquid and solid phases as described under the Separation Procedure, Step 4. Discard the solid portion.
Note: It may be necessary to centrifuge the suspension at high speed before filtration, for leachates containing very fine grained particles.
5.8 Calculate the amount of free liquid from Step 4.12 corresponding to 50 g of the dry solid material. Add this amount to the leachate from Step 5.7.
Note: If the analysis is not performed immediately, store separate aliquot parts of the leachate at 4°C, after adding appropriate preservatives for the analytical parameters of interest.
5.9 If the weight of the solid portion in Step 4.1 was less than 0.5% (w/v), analyze the free liquid from Step 4.13; otherwise, analyze the combined solutions from Step 5.8 for contaminants listed in Table 1 of this Schedule that are likely to be present.
5.10 Report concentrations of contaminants in the combined leachate and the free liquid solution as mg/L.
6.1 This procedure may be required prior to extraction for some samples as indicated in Step 5.1. It may be omitted for wastes with known high structural integrity.
6.2 Fill the sample holder with the material to be tested. If the sample of the waste is a large monolithic block, cut a portion from the block measuring 3.3 cm in diameter by 7.1 cm in length. For a treated waste (e.g. solidified waste) samples may be cast in a form with the above dimensions for the purposes of conducting this test. In such cases, the waste should be allowed to cure for 30 days prior to further testing.
6.3 Place the sample holder in the structural integrity tester, then raise the hammer to its maximum height and allow it to fall. Repeat this procedure 14 times.
6.4 Remove the material from the sample holder, and proceed to Step 5.2. If the sample has not disintegrated, it may be sectioned; alternatively use the entire sample (after weighing) and a sufficiently large bottle as the extraction vessel. The volume of reagent water to be initially added is 16 ml/g of dry sample weight. The maximum amount of 0.5 N acetic acid to be added is 4 ml/g of dry sample weight. The final volume of the leachate should be 20 ml/g of dry sample weight.
Table 1
Leachate Quality Standards
The item column gives sequential item numbers for the entries in this Table.
Item | Column 1 Contaminant |
Column 2 Concentration in Waste Extract (mg/L) |
---|---|---|
1 | Aldicarb | 0.9 |
2 | Aldrin + Dieldrin (the concentration shown in column 2 is for aldrin and dieldrin together) | 0.07 |
3 | Arsenic | 2.5 |
4 | Atrazine + N-dealkylated metabolites (the concentration shown in column 2 is for atrazine and N-dealkylated metabolites together) | 0.5 |
5 | Azinphos-methyl | 2.0 |
6 | Barium | 100.0 |
7 | Bendiocarb | 4.0 |
8 | Benzene | 0.5 |
9 | Benzo(a)pyrene | 0.001 |
10 | Boron | 500.0 |
11 | Bromoxynil | 0.5 |
12 | Cadmium | 0.5 |
13 | Carbaryl/1-Naphthyl-N-methyl carbamate | 9.0 |
14 | Carbofuran | 9.0 |
15 | Carbon tetrachloride | 0.5 |
16 | Chloramines | 300.0 |
17 | Chlordane | 0.7 |
18 | Chlorobenzene | 8.0 |
19 | Chlorpyrifos | 9.0 |
20 | Chromium | 5.0 |
21 | Copper | 100 |
22 | Cresols (total of all isomers) | 200.0 |
23 | Cyanazine | 1.0 |
24 | Cyanide | 20.0 |
25 | DDT (total of all isomers) | 3.0 |
26 | Diazinon | 2.0 |
27 | Dicamba | 12.0 |
28 | 1,2-Dichlorobenzene | 20.0 |
29 | 1,4-Dichlorobenzene | 0.5 |
30 | 1,2-Dichloroethane | 0.5 |
31 | 1,1-Dichloroethylene | 1.4 |
32 | Dichloromethane | 5.0 |
33 | 2,4-Dichlorophenol | 90.0 |
34 | 2,4-Dichlorophenoxyacetic acid | 10.0 |
35 | Diclofop-methyl | 0.9 |
36 | Dimethoate | 2.0 |
37 | 2,4-Dinitrotoluene | 0.13 |
38 | Dinoseb | 1.0 |
39 | Diquat | 7.0 |
40 | Diuron | 15.0 |
41 | Endrin | 0.02 |
42 | Ethyl benzene | 0.24 |
43 | Ethyl methyl ketone | 200.0 |
44 | Fluoride | 150.0 |
45 | Glyphosate | 28.0 |
46 | Heptachlor + Heptachlor epoxide (the concentration shown in column 2 is for Heptachlor and Heptachlor epoxide together) | 0.3 |
47 | Hexachlorobenzene | 0.13 |
48 | Hexachlorobutadiene | 0.5 |
49 | Hexachloroethane | 3.0 |
50 | Lead | 5.0 |
51 | Lindane | 0.4 |
52 | Malathion | 19.0 |
53 | Mercury | 0.1 |
54 | Methoxychlor | 90.0 |
55 | Metolachlor | 5.0 |
56 | Metribuzin | 8.0 |
57 | 1-Naphthyl-N-methyl carbamate | 9.0 |
58 | Nitrate | 4500.0 |
59 | Nitrate + Nitrite (the concentration shown in column 2 is for Nitrate and Nitrite together) | 1000.0 |
60 | Nitrilotriacetic acid | 40 |
61 | Nitrite | 320.0 |
62 | Nitrobenzene | 2.0 |
63 | Paraquat | 1.0 |
64 | Parathion | 5.0 |
65 | Parathion-methyl | 0.7 |
66 | Pentachlorophenol | 6.0 |
67 | Phorate | 0.2 |
68 | Picloram | 19.0 |
69 | Pyridine | 5.0 |
70 | Selenium | 1.0 |
71 | Silver | 5.0 |
72 | Simazine | 1.0 |
73 | Temephos | 28.0 |
74 | Terbufos | 0.1 |
75 | Tetrachloroethylene | 3.0 |
76 | Tetrachloromethane | 0.5 |
77 | 2,3,4,6-Tetrachlorophenol | 10.0 |
78 | Toluene | 2.4 |
79 | Toxaphene | 0.5 |
80 | Triallate | 23.0 |
81 | Trichloroethylene | 5.0 |
82 | 1,1,1-Trichloro-2,2-bis(p-methoxyphenyl) ethane | 90.0 |
83 | 2,4,5-Trichlorophenol | 400.0 |
84 | 2,4,6-Trichlorophenol | 0.5 |
85 | 2,4,5-Trichlorophenoxyacetic acid | 28.0 |
86 | 2-(2,4,5-Trichlorophenoxy) propionic acid | 1.0 |
87 | Trifluralin | 4.5 |
88 | Trihalomethanes (Total) | 10.0 |
89 | Uranium | 10.0 |
90 | Vinyl chloride | 0.2 |
91 | Xylenes | 30.0 |
92 | Zinc | 500.0 |
10 Schedule 6 is amended
(a) by repealing items 1, 5, 6, 8, 18 and 19 in Table 1,
(b) in item 7 of Column I of Table 1 by striking out "3.2" and substituting "3",
(c) in item 17 of Column I of Table 1 by repealing "9.1" and substituting "9"
(d) by adding the following to Table 1:
Item | Column I Waste Classification or Name |
Column II Registration Quantity (kg or L as appropriate) |
Column III Storage Permit Quantities (kg or L as appropriate) |
---|---|---|---|
29. | waste listed in Schedule 7 | 100 | 1 000 |
30. | waste referred to in section 1.1 (2) (b) | 100 | 1 000 |
, and
(e) by adding the following at the bottom of Table 1:
The Waste Classification or Name in Column I refers to the classification of dangerous goods in Part 2 of the federal dangerous goods regulations.
11 The attached Schedule 7 is added.
Schedule 7
(s. 1.1 (1))
Wastes
Description | |
---|---|
Type 1 | The following spent halogenated solvents used in degreasing: tetrachloroethylene, trichloroethylene, methylene chloride, 1,1,1-trichloroethane, carbon tetrachloride, and chlorinated fluorocarbons; and sludges from the recovery of these solvents in degreasing operations |
Type 2 | The following spent halogenated solvents: tetrachloroethylene, methylene chloride, trichloroethylene, 1,1,1-trichloroethane, chlorobenzene, 1,1,2-trichloro-1,2,2-trifluoroethane, ortho-dichlorobenzene, and trichlorofluoromethane; and the still bottoms from the recovery of these solvents |
Type 3 | The following spent non-halogenated solvents: xylene, acetone, ethyl acetate, ethyl benzene, ethyl ether, methyl isobutyl ketone, n-butyl alcohol, cyclohexanone; and methanol; and the still bottoms from the recovery of these solvents |
Type 4 | The following spent non-halogenated solvents: cresols and cresylic acid, nitrobenzene; and the still bottoms from the recovery of these solvents |
Type 5 | The following spent non-halogenated solvents: toluene, methyl ethyl ketone, carbon disulphide, isobutanol, and pyridine; and the still bottoms from the recovery of these solvents |
Type 6 | Wastewater treatment sludges from electroplating operations except for the following processes: (1) sulphuric acid anodizing of aluminum; (2) tin plating on carbon steel; (3) zinc plating (on a segregated basis) on carbon steel; (4) aluminum or aluminum- zinc plating on carbon steel; (5) cleaning, stripping associated with tin, zinc, and aluminum plating on carbon steel; and (6) chemical etching and milling of aluminum |
Type 7 | Wastewater treatment sludges from the chemical conversion coating of aluminum |
Type 8 | Spent cyanide plating bath solutions from non-precious metal electroplating operations |
Type 9 | Plating bath sludges from the bottom of plating baths from electroplating operations where cyanides are used in the process |
Type 10 | Spent stripping and cleaning bath solutions from non-precious metal electroplating operations where cyanides are used in the process |
Type 11 | Quenching bath sludge from oil baths from non-precious metal heat treating operations where cyanides are used in the process |
Type 12 | Spent cyanide solutions from salt bath pot cleaning from non-precious metal heat treating operations |
Type 13 | Quenching wastewater treatment sludges from non-precious metal heat treating operations where cyanides are used in the process |
Type 14 | Cyanidation wastewater treatment tailing pond sediment from mineral metals recovery operations |
Type 15 | Spent cyanide bath solutions from mineral metal recovery operations |
Type 16 | Bottom sediment sludge from the treatment of wastewaters from wood preserving processes that use creosote or pentachlorophenol |
Type 17 | Wastewater treatment sludge from the production of chrome yellow and orange pigments |
Type 18 | Wastewater treatment sludge from the production of molybdate orange pigments |
Type 19 | Wastewater treatment sludge from the production of zinc yellow pigments |
Type 20 | Wastewater treatment sludge from the production of chrome green pigments |
Type 21 | Wastewater treatment sludge from the production of chromeoxide green pigments (anhydrous and hydrated) |
Type 22 | Wastewater treatment sludge from the production of iron blue pigments |
Type 23 | Oven residue from the production of chrome oxide green pigments |
Type 24 | Distillation bottoms from the production of acetaldehyde from ethylene |
Type 25 | Distillation side cuts from the production of acetaldehyde from ethylene |
Type 26 | Bottom stream from the wastewater stripper in the production of acrylonitrile |
Type 27 | Bottom stream from the acetonitrile column in the production of acrylonitrile |
Type 28 | Bottoms from the acetonitrile purification column in the production of acrylonitrile |
Type 29 | Still bottoms from the distillation of benzylchloride |
Type 30 | Heavy ends or distillation residues from the production of carbon tetrachloride |
Type 31 | Heavy ends (still bottoms) from the purification column in the production of epichlorohydrin |
Type 32 | Heavy ends from the fractionation column in ethyl chloride production |
Type 33 | Heavy ends from the distillation of ethylene dichloride in ethylene dichloride production |
Type 34 | Heavy ends from the distillation of vinyl chloride in vinyl chloride monomer production |
Type 35 | Aqueous spent antimony catalyst waste from fluoromethanes production |
Type 36 | Distillation bottom tars from the production of phenol or acetone from cumene |
Type 37 | Distillation light ends from the production of phthalic anhydride from naphthalene |
Type 38 | Distillation bottoms from the production of phthalic anhydride from naphthalene |
Type 39 | Distillation light ends from the production of phthalic anhydride from ortho-xylene |
Type 40 | Distillation bottoms from the production of phthalic anhydride from ortho-xylene |
Type 41 | Distillation bottoms from the production of nitrobenzene by the nitration of benzene |
Type 42 | Stripping still tails from the production of methyl ethyl pyridines |
Type 43 | Centrifuge and distillation residues from toluene diisocyanate production |
Type 44 | Spent catalyst from the hydrochlorinator reactor in the production of 1,1,1-trichloroethane |
Type 45 | Waste from the product stream stripper in the production of 1,1,1-trichloroethane |
Type 46 | Distillation bottoms from the production of 1,1,1-trichloroethane |
Type 47 | Heavy ends from the heavy ends columns from the production of 1,1,1-trichloroethane |
Type 48 | Column bottoms or heavy ends from the combined production of trichloroethylene and perchloroethylene |
Type 49 | Distillation bottoms from aniline production |
Type 50 | Process residues from aniline extraction from the production of aniline |
Type 51 | Combined wastewater streams generated from nitrobenzene or aniline production |
Type 52 | Distillation or fractionating column bottoms from the production of chlorobenzenes |
Type 53 | Separated aqueous stream from the reactor product washing step in the production of chlorobenzene |
Type 54 | By-product salts generated in the production of MSMA and cacodylic acid |
Type 55 | Wastewater treatment sludge from the production of chlordane |
Type 56 | Wastewater and scrub water from the chlorination of cyclopentadiene in the production of chlordane |
Type 57 | Filter solids from the filtration of hexachlorocyclopentadiene in the production of chlordane |
Type 58 | Vacuum stripper discharge from the chlordane chlorinator in the production of chlordane |
Type 59 | Wastewater treatment sludges generated in the production of creosote |
Type 60 | Still bottoms from toluene reclamation distillation in the production of disulfoton |
Type 61 | Wastewater treatment sludges from the production of disulfoton |
Type 62 | Wastewater from the washing and stripping of phorate production |
Type 63 | Filter cake from the filtration of diethylphosphorodithioic acid in the production of phorate |
Type 64 | Wastewater treatment sludge from the production of phorate |
Type 65 | Wastewater treatment sludge from the production of toxaphene |
Type 66 | Untreated process wastewater from the production of toxaphene |
Type 67 | Heavy ends or distillation residues from the distillation of tetrachlorobenzene in the production of 2,4,5-T |
Type 68 | 2,6-Dichlorophenol waste from the production of 2,4-D |
Type 69 | Untreated wastewater from the production of 2,4-D |
Type 70 | Wastewater treatment sludges from the manufacturing and processing of explosives |
Type 71 | Spent carbon from the treatment of wastewater containing explosives |
Type 72 | Wastewater treatment sludges from the manufacturing, formulation, and loading of lead-based initiating compounds |
Type 73 | Pink or red water from TNT operations |
Type 74 | Dissolved air flotation (DAF) float from the petroleum refining industry |
Type 75 | Slop oil emulsion solids from the petroleum refining industry |
Type 76 | Heat exchanger bundle cleaning sludge from the petroleum refining industry |
Type 77 | API separator sludge from the petroleum refining industry |
Type 78 | Tanks bottoms (leaded) from the petroleum refining industry |
Type 79 | Ammonia still lime sludge from coking operations |
Type 80 | Emission control dust or sludge from the primary production of steel in electric furnaces |
Type 81 | Spent pickle liquor from steel finishing operations |
Type 82 | Sludge from lime treatment of spent pickle liquor from steel finishing operations |
Type 83 | Acid plant blowdown slurry or sludge resulting from the thickening of blowdown slurry from primary copper production |
Type 84 | Surface impoundment solids contained in and dredged from surface impoundments at primary lead smelting facilities |
Type 85 | Sludge from treatment of process wastewater or acid plant blowdown from primary zinc production |
Type 86 | Electrolytic anode slime or sludge from primary zinc production |
Type 87 | Cadmium plant leach residue (iron oxide) from primary zinc production |
Type 88 | Emission control dust or sludge from secondary lead smelting |
Type 89 | Waste leaching solution from acid leaching of emission control dust or sludge from secondary lead smelting use TOXIC LIQUID, CORROSIVE, INORGANIC, N.O.S. |
Type 90 | Brine purification muds from the mercury cell process in chlorine production where separately prepurified brine is not used |
Type 91 | Chlorinated hydrocarbon wastes from the purification step of the diaphragm cell process using graphite anodes in chlorine production |
Type 92 | Wastewater treatment sludge from the mercury cell process in chlorine production |
Type 93 | Solvent washes and sludges, caustic washes and sludges, or water washes and sludges from cleaning tubs and equipment used in the formulation of ink from pigments, driers, soaps, and stabilizers containing chromium and lead |
Type 94 | Wastewater treatment sludges generated during the production of veterinary pharmaceuticals from arsenic or organo-arsenic compounds |
Type 95 | Distillation tar residues from the distillation of aniline-based compounds in the production of veterinary pharmaceuticals from arsenic or organo-arsenic compounds |
Type 96 | Residue from the use of activated carbon for decolourization in the production of veterinary pharmaceuticals from arsenic or organo-arsenic compounds |
Type 97 | Decanter tank tar sludge from coking operations |
Type 99 | Wastes that on contact with water or air, emit toxic gases, vapours or fumes in sufficient quantity to present danger to human health or the environment |
Type 100 | Any cyanide or sulphide bearing waste liable, when exposed to pH conditions of not less than 2 and not greater than 12.5, to generate toxic gases in sufficient quantity to present danger to human health or the environment |
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