EC Inventory
EC Inventory
Nested Applications
EC Inventory
The EC inventory published below is a copy as received from the JRC in 2008 on the founding of ECHA. It is comprised of the following lists:
- EINECS (European INventory of Existing Commercial chemical Substances) as published in O.J. C 146A, 15.6.1990. EINECS is an inventory of substances that were deemed to be on the European Community market between 1 January 1971 and 18 September 1981. EINECS was drawn up by the European Commission in the application of Article 13 of Directive 67/548/EEC, as amended by Directive 79/831/EEC, and in accordance with the detailed provisions of Commission Decision 81/437/EEC. Substances listed in EINECS are considered phase-in substances under the REACH Regulation.
- ELINCS (European LIst of Notified Chemical Substances) in support of Directive 92/32/EEC, the 7th amendment to Directive 67/548/EEC. ELINCS lists those substances which were notified under Directive 67/548/EEC, the Dangerous Substances Directive Notification of New Substances (NONS) that became commercially available after 18 September 1981.
- NLP (No-Longer Polymers). The definition of polymers was changed in April 1992 by Council Directive 92/32/EEC amending Directive 67/548/EEC, with the result that substances previously considered to be polymers were no longer excluded from regulation. Thus the No-longer Polymers (NLP) list was drawn up, consisting of such substances that were commercially available between 18 September 1981 and 31 October 1993.
Database contains 106212 unique substances/entries.
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The residue obtained from the sump phase hydrogenation of a residue from the thermal cracking of a residue obtained from the distillation of crude oil. It consists of coke from the brown coal coking or gasification added as a catalyst to the cracking residue and elemental metals boiling at greater than 360°C to greater than 500°C (680°F to 932°F).
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310-091-1
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102242-59-1
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The residue obtained from the sump phase hydrogenation of a residue from the thermal cracking of a residue obtained from the distillation of crude oil. It consists of coke from the brown coal coking or gasification added as a catalyst to the cracking residue and elemental metals boiling at greater than 360°C to greater than 500°C (680°F to 932°F).
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Details | |
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The residue obtained from the residual waters from hydrometallurgic cobalt manufacture.
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310-092-7
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102242-60-4
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The residue obtained from the residual waters from hydrometallurgic cobalt manufacture.
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Details | |
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The residue obtained from the recovery of crude benzene from aliphatic/naphthenic benzene absorbing oil boiling in the range of approximately 270°C to 380°C (518°F to 716°F) and used to absorb crude benzene from coal gas.
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302-655-0
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94114-21-3
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The residue obtained from the recovery of crude benzene from aliphatic/naphthenic benzene absorbing oil boiling in the range of approximately 270°C to 380°C (518°F to 716°F) and used to absorb crude benzene from coal gas.
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Details | |
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The residue obtained from the pyrolysis of polymer wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C20 through C28, sulfur- and nitrogen-containing heteroaromatics and inorganic components of the wastes.
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309-754-8
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100801-71-6
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The residue obtained from the pyrolysis of polymer wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C20 through C28, sulfur- and nitrogen-containing heteroaromatics and inorganic components of the wastes.
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Details | |
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The residue obtained from the distillation of polyester waste pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C16 through C28 and substituted aromatic hydrocarbons boiling in the range greater than 350°C (662°F).
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308-728-3
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98219-60-4
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The residue obtained from the distillation of polyester waste pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C16 through C28 and substituted aromatic hydrocarbons boiling in the range greater than 350°C (662°F).
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Details | |
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The residue obtained from the distillation of plastic waste pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C16 through C28 having a softening point of 25°C to 45°C (77°F to 113°F) according to DIN 52025.
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309-753-2
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100801-70-5
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The residue obtained from the distillation of plastic waste pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C16 through C28 having a softening point of 25°C to 45°C (77°F to 113°F) according to DIN 52025.
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Details | |
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The residue obtained from the carburizing of niobium and tantalum oxides.
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310-075-4
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102184-94-1
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The residue obtained from the carburizing of niobium and tantalum oxides.
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Details | |
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The residue obtained from roasting of an antimony concentrate or ore to remove volatile elements such as mercury or sulfur. Composed primarily of antimony but also containing other non-ferrous metals and gangue constituents.
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310-040-3
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102110-40-7
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The residue obtained from roasting of an antimony concentrate or ore to remove volatile elements such as mercury or sulfur. Composed primarily of antimony but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from roasting of a tin concentrate or ore to remove some of the volatile elements such as mercury or sulfur. Composed primarily of tin but also containing other non-ferrous metals and gangue constituents.
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310-068-6
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102110-66-7
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The residue obtained from roasting of a tin concentrate or ore to remove some of the volatile elements such as mercury or sulfur. Composed primarily of tin but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from roasting of a silver concentrate or ore to remove some of the volatile elements such as mercury or sulfur. Composed primarily of silver but also containing other non-ferrous metals and gangue constituents.
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310-059-7
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102110-57-6
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The residue obtained from roasting of a silver concentrate or ore to remove some of the volatile elements such as mercury or sulfur. Composed primarily of silver but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from magnetic separation of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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310-055-5
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102110-53-2
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The residue obtained from magnetic separation of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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Details | |
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The residue obtained from leaching of an antimony concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of antimony but also containing other non-ferrous metals and gangue constituents.
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310-039-8
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102110-39-4
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The residue obtained from leaching of an antimony concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of antimony but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from leaching of a tin concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of tin but also containing other non-ferrous metals and gangue constituents.
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310-067-0
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102110-65-6
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The residue obtained from leaching of a tin concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of tin but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from leaching of a silver concentrate or ore to remove some of the soluble elements such as arsenic or iron. Composed primarily of silver but also containing other non-ferrous metals and gangue constituents.
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310-058-1
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102110-56-5
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The residue obtained from leaching of a silver concentrate or ore to remove some of the soluble elements such as arsenic or iron. Composed primarily of silver but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from leaching of a lead concentrate or ore to remove some of the soluble elements such as arsenic or iron. Composed primarily of lead but also containing other non-ferrous metals and gangue constituents.
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310-049-2
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102110-48-5
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The residue obtained from leaching of a lead concentrate or ore to remove some of the soluble elements such as arsenic or iron. Composed primarily of lead but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from leaching of a copper concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of copper but also containing other non-ferrous metals and gangue constituents.
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310-042-4
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102110-42-9
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The residue obtained from leaching of a copper concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of copper but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from leaching of a bismuth concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of bismuth but also containing other non-ferrous metals and gangue constituents.
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310-041-9
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102110-41-8
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The residue obtained from leaching of a bismuth concentrate or ore to remove soluble elements such as arsenic or iron. Composed primarily of bismuth but also containing other non-ferrous metals and gangue constituents.
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Details | |
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The residue obtained from electrostatic separation of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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310-052-9
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102110-51-0
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The residue obtained from electrostatic separation of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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Details | |
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The residue obtained from coal tar oil by an alkaline wash such as aqueous sodium hydroxide after the removal of crude coal tar acids. Composed primarily of naphthalenes and aromatic nitrogen bases.
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266-021-4
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65996-87-4
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The residue obtained from coal tar oil by an alkaline wash such as aqueous sodium hydroxide after the removal of crude coal tar acids. Composed primarily of naphthalenes and aromatic nitrogen bases.
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Details | |
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The residue obtained from chemical oil extracted after the removal of naphthalene by distillation composed primarily of two to four membered condensed ring aromatic hydrocarbons and aromatic nitrogen bases.
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277-567-8
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73665-18-6
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The residue obtained from chemical oil extracted after the removal of naphthalene by distillation composed primarily of two to four membered condensed ring aromatic hydrocarbons and aromatic nitrogen bases.
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Details | |
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The residue obtained during the distillation of high boiling fractions from bituminous coal high temperature tar and/or pitch coke oil, with a softening point of 140° to 170°C (284°F to 392°F) according to DIN 52025. Composed primarily of tri- and polynuclear aromatic compounds which also contain heteroatoms.
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302-650-3
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94114-13-3
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The residue obtained during the distillation of high boiling fractions from bituminous coal high temperature tar and/or pitch coke oil, with a softening point of 140° to 170°C (284°F to 392°F) according to DIN 52025. Composed primarily of tri- and polynuclear aromatic compounds which also contain heteroatoms.
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Details | |
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The residue obtained during citric acid production by the treatment of the sugar of molasses by Aspergillis niger, separation of the fungus mycelium, precipitation of calcium citrate and separation of the citrate.
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305-978-5
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95371-10-1
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The residue obtained during citric acid production by the treatment of the sugar of molasses by Aspergillis niger, separation of the fungus mycelium, precipitation of calcium citrate and separation of the citrate.
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Details | |
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The residue obtained by zinc precipitation of the material obtained during the recovery of palladium and platinum from the anode sludges of silver electrolysis. Composed primarily of palladium, platinum, rhenium and the oxides of iron and zinc.
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309-641-3
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100656-52-8
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The residue obtained by zinc precipitation of the material obtained during the recovery of palladium and platinum from the anode sludges of silver electrolysis. Composed primarily of palladium, platinum, rhenium and the oxides of iron and zinc.
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Details | |
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The residue obtained by the vacuum distillation of the liquid phase obtained by the treatment of bituminous coal with hydrogen in a process-derived oil at high temperature and high pressure. The residue has a softening point in the approximate range of 90°C to 180°C (194°F to 356°F).
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295-504-2
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92061-91-1
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The residue obtained by the vacuum distillation of the liquid phase obtained by the treatment of bituminous coal with hydrogen in a process-derived oil at high temperature and high pressure. The residue has a softening point in the approximate range of 90°C to 180°C (194°F to 356°F).
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Details | |
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The residue obtained by solvent extraction of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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310-056-0
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102110-54-3
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The residue obtained by solvent extraction of ores, concentrates and secondary materials during manufacture of tungsten and its alloys. Composed primarily of iron, tin and tungsten.
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Details | |
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The residue from toluene extraction of dried brown coal.
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294-285-0
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91697-23-3
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The residue from toluene extraction of dried brown coal.
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Details | |
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The residue from the vacuum distillation of the products of coal treated with a hydrocarbon solvent in the presence of hydrogen. It solidifies at approximately 149°C (300°F). Composed primarily of carbon. May contain varying amounts of hydrogen, nitrogen, sulfur, oxygen, and ash.
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270-069-1
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68409-94-9
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The residue from the vacuum distillation of the products of coal treated with a hydrocarbon solvent in the presence of hydrogen. It solidifies at approximately 149°C (300°F). Composed primarily of carbon. May contain varying amounts of hydrogen, nitrogen, sulfur, oxygen, and ash.
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Details | |
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The residue from the vacuum distillation of the product from the treatment of coal with a solvent in the presence of hydrogen at high temperatures [above 426.7°C (800°F)] and removal of gaseous and light liquid products. Composed primarily of solvent-refined coal, unconverted coal, and mineral matter.
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272-748-8
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68910-58-7
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The residue from the vacuum distillation of the product from the treatment of coal with a solvent in the presence of hydrogen at high temperatures [above 426.7°C (800°F)] and removal of gaseous and light liquid products. Composed primarily of solvent-refined coal, unconverted coal, and mineral matter.
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Details | |
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The residue from the vacuum distillation of the hydrogenative liquefaction of coal. Composed primarily of organic material boiling above 450°C (842°F), mineral components of the liquefied coal and selective catalysts.
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302-654-5
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94114-20-2
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The residue from the vacuum distillation of the hydrogenative liquefaction of coal. Composed primarily of organic material boiling above 450°C (842°F), mineral components of the liquefied coal and selective catalysts.
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Details | |
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The residue from the joint distillation of brown coal tar and pyrolysis residual oil from ethylene plants. Composed primarily of polynuclear aromatic and naphthenic hydrocarbons which can be alkyl- and vinyl-substituted and can contain heteroatoms, paraffin hydrocarbons and high-boiling mono- and dinuclear phenols. It is a black solid with a softening point of 60°C (140°F) according to DIN 52025.
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309-605-7
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100403-59-6
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The residue from the joint distillation of brown coal tar and pyrolysis residual oil from ethylene plants. Composed primarily of polynuclear aromatic and naphthenic hydrocarbons which can be alkyl- and vinyl-substituted and can contain heteroatoms, paraffin hydrocarbons and high-boiling mono- and dinuclear phenols. It is a black solid with a softening point of 60°C (140°F) according to DIN 52025.
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Details | |
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The residue from the joint coking of acetylene soot with pyrolysis pitch from pyrolysis residual oil from ethylene plants. Composed primarily of carbon with lesser amounts of sulfur, nitrogen and ash formers.
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309-608-3
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100403-62-1
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The residue from the joint coking of acetylene soot with pyrolysis pitch from pyrolysis residual oil from ethylene plants. Composed primarily of carbon with lesser amounts of sulfur, nitrogen and ash formers.
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Details | |
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The residue from the joint carbonization of bituminous coal tar pitch with soot. Composed primarily of isotopic carbon with lesser amounts of sulfur and ash formers.
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309-564-5
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100403-22-3
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The residue from the joint carbonization of bituminous coal tar pitch with soot. Composed primarily of isotopic carbon with lesser amounts of sulfur and ash formers.
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Details | |
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The residue from the joint carbonization of bituminous coal tar pitch with pyrolysis pitch from pyrolysis residual oil from ethylene plants. Composed primarily of isotopic carbon with lesser amounts of sulfur and ash formers.
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309-565-0
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100403-23-4
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The residue from the joint carbonization of bituminous coal tar pitch with pyrolysis pitch from pyrolysis residual oil from ethylene plants. Composed primarily of isotopic carbon with lesser amounts of sulfur and ash formers.
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Details | |
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The residue from the fractional distillation of wash oil boiling in the approximate range of 270°C to 330°C (518°F to 626°F). It consists predominantly of dinuclear aromatic and heterocyclic hydrocarbons.
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295-506-3
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92061-93-3
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The residue from the fractional distillation of wash oil boiling in the approximate range of 270°C to 330°C (518°F to 626°F). It consists predominantly of dinuclear aromatic and heterocyclic hydrocarbons.
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Details | |
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The residue from the fraction distillation of crude anthracene boiling in the approximate range of 340°C to 400°C (644°F to 752°F). It consists predominantly of tri- and polynuclear aromatic and heterocyclic hydrocarbons.
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295-505-8
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92061-92-2
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The residue from the fraction distillation of crude anthracene boiling in the approximate range of 340°C to 400°C (644°F to 752°F). It consists predominantly of tri- and polynuclear aromatic and heterocyclic hydrocarbons.
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Details | |
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The residue from the distillation of vegetable oil fatty acids or saponified, acidulated vegetable oil fatty acids. Composed primarily of high boiling esters of the fatty acids, neutral materials of vegetable origin with lesser amounts of the free fatty acids.
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272-840-8
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68917-42-0
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The residue from the distillation of vegetable oil fatty acids or saponified, acidulated vegetable oil fatty acids. Composed primarily of high boiling esters of the fatty acids, neutral materials of vegetable origin with lesser amounts of the free fatty acids.
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Details | |
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The residue from the distillation of thermal cracked or steam-cracked residuum and/or catalytic cracked clarified oil with a softening point from 40°C to 180°C (104°F to 356°F). Composed primarily of a complex combination of three or more membered condensed ring aromatic hydrocarbons.
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269-110-6
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68187-58-6
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The residue from the distillation of thermal cracked or steam-cracked residuum and/or catalytic cracked clarified oil with a softening point from 40°C to 180°C (104°F to 356°F). Composed primarily of a complex combination of three or more membered condensed ring aromatic hydrocarbons.
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Details | |
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The residue from the distillation of tall oil. It contains primarily high-boiling esters of fatty acids and rosin. It may also contain neutral materials, free fatty acids and rosin acids.
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232-414-4
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8016-81-7
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The residue from the distillation of tall oil. It contains primarily high-boiling esters of fatty acids and rosin. It may also contain neutral materials, free fatty acids and rosin acids.
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Details | |
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The residue from the distillation of peat tar having a softening point of 105°C to 145°C. Composed primarily of high boiling and nonvolatile mono and divalent phenols and paraffin hydrocarbons.
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302-651-9
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94114-14-4
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The residue from the distillation of peat tar having a softening point of 105°C to 145°C. Composed primarily of high boiling and nonvolatile mono and divalent phenols and paraffin hydrocarbons.
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Details | |
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The residue from the distillation of old tire pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C20 through C28 having a softening point of 70°C to 110°C (158°F to 230°F).
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308-748-2
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98219-78-4
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The residue from the distillation of old tire pyrolysis oil. It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C20 through C28 having a softening point of 70°C to 110°C (158°F to 230°F).
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Details | |
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The residue from the distillation of high temperature coal tar. A black solid with an approximate softening point from 30°C to 180°C (86°F to 356°F). Composed primarily of a complex mixture of three or more membered condensed ring aromatic hydrocarbons.
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266-028-2
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65996-93-2
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The residue from the distillation of high temperature coal tar. A black solid with an approximate softening point from 30°C to 180°C (86°F to 356°F). Composed primarily of a complex mixture of three or more membered condensed ring aromatic hydrocarbons.
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Details | |
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The residue from the distillation of crude sulfur. It consists primarily of sulfur and solid carbon-sulfur compounds. It is commonly called boiler bottom sulfur.
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273-512-7
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68988-04-5
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The residue from the distillation of crude sulfur. It consists primarily of sulfur and solid carbon-sulfur compounds. It is commonly called boiler bottom sulfur.
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Details | |
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The residue from the distillation of brown coal tar formed by carbonization up to 1250°C (2282°F). Composed primarily of polynuclear aromatic and naphthenic hydrocarbons and heterocycles, paraffin hydrocarbons and high-boiling mono- and dinuclear phenols. It is a black solid with a softening point of 50°C to 120°C (122°F to 248°F) according to DIN 52025.
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309-604-1
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100403-58-5
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The residue from the distillation of brown coal tar formed by carbonization up to 1250°C (2282°F). Composed primarily of polynuclear aromatic and naphthenic hydrocarbons and heterocycles, paraffin hydrocarbons and high-boiling mono- and dinuclear phenols. It is a black solid with a softening point of 50°C to 120°C (122°F to 248°F) according to DIN 52025.
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Details | |
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The residue from the distillation of bituminus coal pressure gasification tar. A black solid with a softening point of greater than 60°C (140°F) according to DIN 52025 and composed primarily of a complex mixture of polynuclear aromatic and naphthenic hydrocarbons that may be alkyl substituted and may contain heteroatoms, high boiling aliphatic hydrocarbons and polynuclear phenols.
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302-649-8
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94114-12-2
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The residue from the distillation of bituminus coal pressure gasification tar. A black solid with a softening point of greater than 60°C (140°F) according to DIN 52025 and composed primarily of a complex mixture of polynuclear aromatic and naphthenic hydrocarbons that may be alkyl substituted and may contain heteroatoms, high boiling aliphatic hydrocarbons and polynuclear phenols.
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Details | |
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The residue from the distillation of alkali-washed naphthalene oil having an approximate distillation range of 220°C to 300°C (428°F to 572°F). Composed primarily of naphthalene, alkylnaphthalenes and aromatic nitrogen bases.
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292-628-9
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90641-05-7
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The residue from the distillation of alkali-washed naphthalene oil having an approximate distillation range of 220°C to 300°C (428°F to 572°F). Composed primarily of naphthalene, alkylnaphthalenes and aromatic nitrogen bases.
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Details | |
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The residue from the distillation of alkali-washed naphthalene oil from high temperature coal tar having an approximate distillation range of 220°C to 300°C (428°F to 572°F). Composed primarily of naphthalene, alkylnaphthalenes, and aromatic nitrogen bases.
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310-257-3
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140362-66-9
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The residue from the distillation of alkali-washed naphthalene oil from high temperature coal tar having an approximate distillation range of 220°C to 300°C (428°F to 572°F). Composed primarily of naphthalene, alkylnaphthalenes, and aromatic nitrogen bases.
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Details | |
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The residue from the distillation of a mixture of coal tar and aromatic petroleum streams. A solid with a softening point from 40°C to 180°C (104°F to 356°F). Composed primarily of a complex combination of three or more membered condensed ring aromatic hydrocarbons.
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269-109-0
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68187-57-5
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The residue from the distillation of a mixture of coal tar and aromatic petroleum streams. A solid with a softening point from 40°C to 180°C (104°F to 356°F). Composed primarily of a complex combination of three or more membered condensed ring aromatic hydrocarbons.
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Details | |
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The residue from the distillation of a complex reaction product, obtained by reaction of gases obtained by the dry distillation of bituminous coal with a distillate, consisting of di- and trinuclear aromatic hydrocarbons and their alkyl derivatives, with a softening point of 30°C to 50°C (86°F to 122°F). The residue consists predominantly of substituted aromatic di- and polynuclear hydrocarbons and sulfur-containing compounds.
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295-501-6
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92061-88-6
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The residue from the distillation of a complex reaction product, obtained by reaction of gases obtained by the dry distillation of bituminous coal with a distillate, consisting of di- and trinuclear aromatic hydrocarbons and their alkyl derivatives, with a softening point of 30°C to 50°C (86°F to 122°F). The residue consists predominantly of substituted aromatic di- and polynuclear hydrocarbons and sulfur-containing compounds.
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Details | |
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The residue from the distillation in the range of 235°C to 355°C (481°F to 697°F) of light carbolic oil.
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270-713-1
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68477-23-6
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The residue from the distillation in the range of 235°C to 355°C (481°F to 697°F) of light carbolic oil.
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Details | |
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The residue from the carbonization of reaction pitch from the joint distillation of brown coal tar and pyrolysis residual oil from ethylene plants. Composed primarily of carbon with lesser amounts of sulfur and ash formers.
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309-562-4
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100403-21-2
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The residue from the carbonization of reaction pitch from the joint distillation of brown coal tar and pyrolysis residual oil from ethylene plants. Composed primarily of carbon with lesser amounts of sulfur and ash formers.
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Details | |
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The residue from low temperature coal tar oils after an alkaline wash, such as aqueous sodium hydroxide, to remove crude coal tar acids. Composed primarily of hydrocarbons and aromatic nitrogen bases.
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310-191-5
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122384-78-5
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The residue from low temperature coal tar oils after an alkaline wash, such as aqueous sodium hydroxide, to remove crude coal tar acids. Composed primarily of hydrocarbons and aromatic nitrogen bases.
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Details | |
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The residue from fixed bed gasification of coal at 25-100 bar. Still contains ca. 5-10% coal dust and, depending on the origin of the coal, varying portions of mineral constituents, metal oxides and trace elements.
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295-500-0
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92061-87-5
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The residue from fixed bed gasification of coal at 25-100 bar. Still contains ca. 5-10% coal dust and, depending on the origin of the coal, varying portions of mineral constituents, metal oxides and trace elements.
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Details | |
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The residue from crude coal tar acids after removal of phenol, cresols, xylenols and any higher boiling phenols. A black solid with a melting point approximately 80°C (176°F). Composed primarily of polyalkylphenols, resin gums, and inorganic salts.
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271-418-0
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68555-24-8
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The residue from crude coal tar acids after removal of phenol, cresols, xylenols and any higher boiling phenols. A black solid with a melting point approximately 80°C (176°F). Composed primarily of polyalkylphenols, resin gums, and inorganic salts.
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Details | |
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The residue consisting mainly of rare earth chlorides and rare earth metals.
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284-897-6
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84989-08-2
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The residue consisting mainly of rare earth chlorides and rare earth metals.
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Details | |
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The residue after removal by distillation of the tar oils from pine tar.
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295-820-0
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92129-18-5
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The residue after removal by distillation of the tar oils from pine tar.
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Details | |
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The residue after extraction of animal glue or gelation. It consists of hair, hide, protein and leather scrap. It is processed by acidulation with sulfuric acid and water to remove grease and then digested under pressure and dried in a vacuum. It contains protein, nitrogen, moisture, fat and ash.
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270-343-0
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68425-25-2
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The residue after extraction of animal glue or gelation. It consists of hair, hide, protein and leather scrap. It is processed by acidulation with sulfuric acid and water to remove grease and then digested under pressure and dried in a vacuum. It contains protein, nitrogen, moisture, fat and ash.
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Details | |
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The residual product from the distillation of hydrocracked coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes. A black semi-solid composed primarily of condensed ring aromatic and hydrogenated aromatic compounds containing some sulfur, oxygen and nitrogen.
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302-684-9
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94114-49-5
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The residual product from the distillation of hydrocracked coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes. A black semi-solid composed primarily of condensed ring aromatic and hydrogenated aromatic compounds containing some sulfur, oxygen and nitrogen.
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Details | |
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The redistillate obtained from the fractional distillation of pitch distillate boiling in the range of approximately 350°C to 400°C (662°F to 752°F). Consists predominantly of tri- and polynuclear aromatics and heterocyclic hydrocarbons.
|
295-304-5
|
91995-42-5
|
The redistillate obtained from the fractional distillation of pitch distillate boiling in the range of approximately 350°C to 400°C (662°F to 752°F). Consists predominantly of tri- and polynuclear aromatics and heterocyclic hydrocarbons.
|
Details | |
|
The redistillate obtained from the fractional distillation of pitch distillate and boiling in the range of approximately 380°C to 410°C (716°F to 770°F). Composed primarily of tri- and polynuclear aromatic hydrocarbons and heterocyclic compounds.
|
295-313-4
|
91995-52-7
|
The redistillate obtained from the fractional distillation of pitch distillate and boiling in the range of approximately 380°C to 410°C (716°F to 770°F). Composed primarily of tri- and polynuclear aromatic hydrocarbons and heterocyclic compounds.
|
Details | |
|
The redistillate obtained from the fractional distillation of bituminous coal high temperature tar and pyrolysis residual oils and boiling in the range of approximately 190°C to 270°C (374°F to 518°F). Composed primarily of substituted dinuclear aromatics.
|
295-295-8
|
91995-35-6
|
The redistillate obtained from the fractional distillation of bituminous coal high temperature tar and pyrolysis residual oils and boiling in the range of approximately 190°C to 270°C (374°F to 518°F). Composed primarily of substituted dinuclear aromatics.
|
Details | |
|
The redistillate from the fractional distillation of dephenolated and debased methylnaphthalene oil obtained from bituminous coal high temperature tar and pyrolysis residual oils boiling in the approximate range of 220°C to 230°C (428°F to 446°F). It consists predominantly of unsubstituted and substituted dinuclear aromatic hydrocarbons.
|
295-329-1
|
91995-66-3
|
The redistillate from the fractional distillation of dephenolated and debased methylnaphthalene oil obtained from bituminous coal high temperature tar and pyrolysis residual oils boiling in the approximate range of 220°C to 230°C (428°F to 446°F). It consists predominantly of unsubstituted and substituted dinuclear aromatic hydrocarbons.
|
Details | |
|
The redistillate from the distillate, freed of tar acids and tar bases, from bituminous coal high temperature tar boiling in the approximate range of 90°C to 160°C (194°F to 320°F). It consists predominantly of benzene, toluene and xylenes.
|
295-323-9
|
91995-61-8
|
The redistillate from the distillate, freed of tar acids and tar bases, from bituminous coal high temperature tar boiling in the approximate range of 90°C to 160°C (194°F to 320°F). It consists predominantly of benzene, toluene and xylenes.
|
Details | |
|
The redistillate from the distillate, free of tar acids and tar bases, from bituminous coal high temperature tar boiling in the approximate range of 90°C to 160°C (194°F to 320°F). It consists predominantly of benzene, toluene and xylenes.
|
310-247-9
|
140362-56-7
|
The redistillate from the distillate, free of tar acids and tar bases, from bituminous coal high temperature tar boiling in the approximate range of 90°C to 160°C (194°F to 320°F). It consists predominantly of benzene, toluene and xylenes.
|
Details | |
|
The recovered oil obtained by skimming all plant oil-bearing water streams. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C7 through C10.
|
273-304-6
|
68956-48-9
|
The recovered oil obtained by skimming all plant oil-bearing water streams. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C7 through C10.
|
Details | |
|
The recovered oil obtained by skimming all plant oil bearing water streams. It consists predominantly of lubricating oil, oil additives and intermediates.
|
309-943-5
|
101631-18-9
|
The recovered oil obtained by skimming all plant oil bearing water streams. It consists predominantly of lubricating oil, oil additives and intermediates.
|
Details | |
|
The reaction product obtained by neutralizing the acidic extract of alkali-washed low-temperature coal tar middle oil with an alkaline solution, such as aqueous sodium hydroxide, to obtain the free bases. Composed primarily of a complex mixture of aromatic nitrogen bases.
|
310-294-5
|
141785-66-2
|
The reaction product obtained by neutralizing the acidic extract of alkali-washed low-temperature coal tar middle oil with an alkaline solution, such as aqueous sodium hydroxide, to obtain the free bases. Composed primarily of a complex mixture of aromatic nitrogen bases.
|
Details | |
|
The reaction product obtained by neutralizing the acid extract of alkali-washed carbolic oil and/or naphthalene oil with an alkaline solution, such as aqueous sodium hydroxide or ammonia to obtain the free bases. Composed primarily of pyridine, quinoline and their alkyl derivatives.
|
310-305-3
|
185323-44-8
|
The reaction product obtained by neutralizing the acid extract of alkali-washed carbolic oil and/or naphthalene oil with an alkaline solution, such as aqueous sodium hydroxide or ammonia to obtain the free bases. Composed primarily of pyridine, quinoline and their alkyl derivatives.
|
Details | |
|
The reaction product obtained by neutralizing low-temperature coal tar middle oil alkaline extract with an acidic solution, such as aqueous sulfuric acid, or an acidic gas, such as one containing carbon dioxide, to obtain the free acids. Composed primarily of phenols, cresols, xylenols, and higher-boiling phenols.
|
310-292-4
|
141785-63-9
|
The reaction product obtained by neutralizing low-temperature coal tar middle oil alkaline extract with an acidic solution, such as aqueous sulfuric acid, or an acidic gas, such as one containing carbon dioxide, to obtain the free acids. Composed primarily of phenols, cresols, xylenols, and higher-boiling phenols.
|
Details | |
|
The reaction product obtained by neutralizing coal tar oil alkaline extract with an acidic solution, such as aqueous sulfuric acid, or gaseous carbon dioxide, to obtain the free acids. Composed primarily of tar acids such as phenol, cresols, and xylenols.
|
266-019-3
|
65996-85-2
|
The reaction product obtained by neutralizing coal tar oil alkaline extract with an acidic solution, such as aqueous sulfuric acid, or gaseous carbon dioxide, to obtain the free acids. Composed primarily of tar acids such as phenol, cresols, and xylenols.
|
Details | |
|
The reaction product obtained by neutralizing coal tar base extract oil with an alkaline solution, such as aqueous sodium hydroxide, to obtain the free bases. Composed primarily of such organic bases as acridine, phenanthridine, pyridine, quinoline and their alkyl derivatives.
|
266-018-8
|
65996-84-1
|
The reaction product obtained by neutralizing coal tar base extract oil with an alkaline solution, such as aqueous sodium hydroxide, to obtain the free bases. Composed primarily of such organic bases as acridine, phenanthridine, pyridine, quinoline and their alkyl derivatives.
|
Details | |
|
The purified internal fat of the hog. It consists primarily of stearin, palmitin and olein.
|
263-100-5
|
61789-99-9
|
The purified internal fat of the hog. It consists primarily of stearin, palmitin and olein.
|
Details | |
|
The product of high temperature calcination (above 450°C (842°F)) of naturally occurring kaolin, a hydrated aluminum silicate, resulting in the evolution of water and the formation of new substances depending upon the calcination temperatures employed.
|
296-473-8
|
92704-41-1
|
The product of high temperature calcination (above 450°C (842°F)) of naturally occurring kaolin, a hydrated aluminum silicate, resulting in the evolution of water and the formation of new substances depending upon the calcination temperatures employed.
|
Details | |
|
The product of agglomerating iron ore fines, concentrates, iron sinter, and other iron-bearing materials. Includes pellets, nodules and briquettes.
|
265-996-3
|
65996-65-8
|
The product of agglomerating iron ore fines, concentrates, iron sinter, and other iron-bearing materials. Includes pellets, nodules and briquettes.
|
Details | |
|
The product obtained upon cleavage of the organic components of the acids during the burning of waste acid resins and waste acids.
|
308-698-1
|
98219-32-0
|
The product obtained upon cleavage of the organic components of the acids during the burning of waste acid resins and waste acids.
|
Details | |
|
The product obtained from wet dust-collecting equipment used in the casting of iron goods. Composed primarily of aluminum oxide, carbon, iron oxide and silicon dioxide.
|
310-064-4
|
102110-63-4
|
The product obtained from wet dust-collecting equipment used in the casting of iron goods. Composed primarily of aluminum oxide, carbon, iron oxide and silicon dioxide.
|
Details | |
|
The product obtained from the purification of waste waters from production and gas purification processes during non-ferrous metal production. Composed primarily of gypsum.
|
310-066-5
|
102110-64-5
|
The product obtained from the purification of waste waters from production and gas purification processes during non-ferrous metal production. Composed primarily of gypsum.
|
Details | |
|
The product obtained during production of castings with lost molds and cores. Composed primarily of quartz sand or chromium, olivine or zirconium ore sand that contains clay, coal dust constituents, synthetic resins and reaction products formed by thermal effects.
|
310-071-2
|
102110-69-0
|
The product obtained during production of castings with lost molds and cores. Composed primarily of quartz sand or chromium, olivine or zirconium ore sand that contains clay, coal dust constituents, synthetic resins and reaction products formed by thermal effects.
|
Details | |
|
The product obtained by treatment of coal tar oil alkaline extract with CO2 and CaO. Composed primarily of CaCO3, Ca(OH)2, Na2CO3 and other organic and inorganic impurities.
|
292-629-4
|
90641-06-8
|
The product obtained by treatment of coal tar oil alkaline extract with CO2 and CaO. Composed primarily of CaCO3, Ca(OH)2, Na2CO3 and other organic and inorganic impurities.
|
Details | |
|
The product obtained by treating cellulose with caustic soda, reacting this with carbon disulfide, dissolving this in a dilute alkali solution and extruding into an acid to form a continuous viscose tube.
|
270-493-7
|
68442-85-3
|
The product obtained by treating cellulose with caustic soda, reacting this with carbon disulfide, dissolving this in a dilute alkali solution and extruding into an acid to form a continuous viscose tube.
|
Details | |
|
The product obtained by the purification of copper-lead ore concentrate roasting offgas. Composed primarily of arsenic oxide (As2O3).
|
310-063-9
|
102110-62-3
|
The product obtained by the purification of copper-lead ore concentrate roasting offgas. Composed primarily of arsenic oxide (As2O3).
|
Details | |
|
The product obtained by the purification of copper ore concentrate roasting offgas. Composed primarily of lead, mercury and selenium.
|
310-062-3
|
102110-61-2
|
The product obtained by the purification of copper ore concentrate roasting offgas. Composed primarily of lead, mercury and selenium.
|
Details | |
|
The product obtained by oxidation of petroleum pitch in air at temperatures in the range of approximately 200°C to 300°C (392°F to 572°F).
|
307-353-2
|
97593-48-1
|
The product obtained by oxidation of petroleum pitch in air at temperatures in the range of approximately 200°C to 300°C (392°F to 572°F).
|
Details | |
|
The product obtained by filtration of coal mineral matter and undissolved coal from coal extract solution produced by digesting coal in a liquid solvent. A black, viscous, highly complex liquid combination composed primarily of aromatic and partly hydrogenated aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic and other aromatic oxygen compounds and their alkyl derivatives.
|
302-682-8
|
94114-47-3
|
The product obtained by filtration of coal mineral matter and undissolved coal from coal extract solution produced by digesting coal in a liquid solvent. A black, viscous, highly complex liquid combination composed primarily of aromatic and partly hydrogenated aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic and other aromatic oxygen compounds and their alkyl derivatives.
|
Details | |
|
The product obtained by air-blowing, at elevated temperature, low-temperature coal tar pitch. It has a softening-point within the approximate range of 70°C to 180°C (158°F to 356°F). Composed primarily of a complex mixture of hydrocarbons.
|
292-654-0
|
90669-59-3
|
The product obtained by air-blowing, at elevated temperature, low-temperature coal tar pitch. It has a softening-point within the approximate range of 70°C to 180°C (158°F to 356°F). Composed primarily of a complex mixture of hydrocarbons.
|
Details | |
|
The product obtained by acid leaching of copper speiss. Composed primarily of antimony, arsenic and lead with high precious metal content.
|
309-643-4
|
100656-54-0
|
The product obtained by acid leaching of copper speiss. Composed primarily of antimony, arsenic and lead with high precious metal content.
|
Details | |
|
The product obtained after alcoholic precipitation and treatment according to Cohn of the supernatant liquid obtained after sedimentation and centrifugation of bovine blood.
|
292-322-5
|
90604-29-8
|
The product obtained after alcoholic precipitation and treatment according to Cohn of the supernatant liquid obtained after sedimentation and centrifugation of bovine blood.
|
Details | |
|
The product formed by heating crushed and screened shale in a rotary kiln to a plastic state, cooling, crushing, and screening into the proper sized units. It contains, but is not limited to aluminium, calcium, iron, magnesium, oxygen, potassium, silicon, sodium, and sulfur.
|
269-827-4
|
68334-37-2
|
The product formed by heating crushed and screened shale in a rotary kiln to a plastic state, cooling, crushing, and screening into the proper sized units. It contains, but is not limited to aluminium, calcium, iron, magnesium, oxygen, potassium, silicon, sodium, and sulfur.
|
Details | |
|
The pregnant solution obtained when sulfuric acid is applied to copper oxide ores and the copper and other metals taken into solution.
|
266-963-6
|
67711-87-9
|
The pregnant solution obtained when sulfuric acid is applied to copper oxide ores and the copper and other metals taken into solution.
|
Details | |
|
The phenolic oil produced by the distillation of coal tar is distilled after dephenolation and debasing to obtain the indene fraction. This boils in the approximate range of 160°C to 190°C (320°F to 374°F). Contains primarily mesitylene, pseudocumene, coumarone, xylenes, hydrindene, and indene.
|
310-248-4
|
140362-58-9
|
The phenolic oil produced by the distillation of coal tar is distilled after dephenolation and debasing to obtain the indene fraction. This boils in the approximate range of 160°C to 190°C (320°F to 374°F). Contains primarily mesitylene, pseudocumene, coumarone, xylenes, hydrindene, and indene.
|
Details | |
|
The oxidized surface of steel produced during reheating, conditioning, hot rolling, and hot forming operations. This substance is usually removed by process waters used for descaling, roll and material cooling, and other purposes. It is subsequently recovered by gravity separation techniques. Composed primarily of high-purity iron oxides. May contain varying amounts of other oxides, elements, and trace compounds.
|
266-007-8
|
65996-74-9
|
The oxidized surface of steel produced during reheating, conditioning, hot rolling, and hot forming operations. This substance is usually removed by process waters used for descaling, roll and material cooling, and other purposes. It is subsequently recovered by gravity separation techniques. Composed primarily of high-purity iron oxides. May contain varying amounts of other oxides, elements, and trace compounds.
|
Details | |
|
The overhead middle cut from fractionation boiling in a range of approximately 446°C to 482°C (835°F to 900°F).
|
271-071-5
|
68515-29-7
|
The overhead middle cut from fractionation boiling in a range of approximately 446°C to 482°C (835°F to 900°F).
|
Details | |
|
The overhead light ends from fractionation boiling approximately below 446°C (835°F).
|
271-069-4
|
68515-28-6
|
The overhead light ends from fractionation boiling approximately below 446°C (835°F).
|
Details | |
|
The oil resulting from the alkali washing of carbolic oil from high temperature coal tar to remove phenolic compounds (tar acids). Composed primarily of indene, indan, and alkyl benzenes.
|
310-258-9
|
140362-67-0
|
The oil resulting from the alkali washing of carbolic oil from high temperature coal tar to remove phenolic compounds (tar acids). Composed primarily of indene, indan, and alkyl benzenes.
|
Details | |
|
The oil resulting from the acid washing of alkali-washed carbolic oil to remove the minor amounts of basic compounds (tar bases). Composed primarily of indene, indan and alkylbenzenes.
|
292-624-7
|
90641-01-3
|
The oil resulting from the acid washing of alkali-washed carbolic oil to remove the minor amounts of basic compounds (tar bases). Composed primarily of indene, indan and alkylbenzenes.
|
Details | |
|
The oil remaining after the removal, by a crystallization process, of an anthracene-rich solid (anthracene paste) from anthracene oil. It is composed primarily of two, three and four membered aromatic compounds.
|
292-604-8
|
90640-82-7
|
The oil remaining after the removal, by a crystallization process, of an anthracene-rich solid (anthracene paste) from anthracene oil. It is composed primarily of two, three and four membered aromatic compounds.
|
Details | |
|
The oil remaining after the removal of phenolic compounds (tar acids) from drained naphthalene oil by an alkali wash. Composed primarily of naphthalene and alkyl naphthalenes.
|
292-612-1
|
90640-90-7
|
The oil remaining after the removal of phenolic compounds (tar acids) from drained naphthalene oil by an alkali wash. Composed primarily of naphthalene and alkyl naphthalenes.
|
Details | |
|
The oil remaining after the removal by a crystallization process of acenaphthene from acenaphthene oil from high temperature coal tar. Composed primarily of naphthene and alkyl naphthenes.
|
310-299-2
|
185323-41-5
|
The oil remaining after the removal by a crystallization process of acenaphthene from acenaphthene oil from high temperature coal tar. Composed primarily of naphthene and alkyl naphthenes.
|
Details | |
|
The oil remaining after removal by a crystallization process of most acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
|
310-223-8
|
140203-14-1
|
The oil remaining after removal by a crystallization process of most acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
|
Details | |
|
The oil remaining after removal by a crystallization process of acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
|
292-606-9
|
90640-85-0
|
The oil remaining after removal by a crystallization process of acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
|
Details | |
|
The oil obtained from the pyrolysis of textile wastes from a polyamide/polyester fiber mixture at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of benzene and naphthalene and their homologs, benzonitrile and other di- and polynuclear aromatic hydrocarbons.
|
309-762-1
|
100801-78-3
|
The oil obtained from the pyrolysis of textile wastes from a polyamide/polyester fiber mixture at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of benzene and naphthalene and their homologs, benzonitrile and other di- and polynuclear aromatic hydrocarbons.
|
Details | |
|
The oil obtained from the pyrolysis of polymer wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
309-755-3
|
100801-72-7
|
The oil obtained from the pyrolysis of polymer wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
Details | |
|
The oil obtained from the pyrolysis of polyamide wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C20 and other hydrocarbons boiling in the range of approximately 50°C to 400°C (122°F to 752°F).
|
308-724-1
|
98219-56-8
|
The oil obtained from the pyrolysis of polyamide wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C20 and other hydrocarbons boiling in the range of approximately 50°C to 400°C (122°F to 752°F).
|
Details | |
|
The oil obtained from the pyrolysis of old tires at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
308-747-7
|
98219-77-3
|
The oil obtained from the pyrolysis of old tires at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
Details | |
|
The oil obtained from the pyrolysis of old electric cables at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
308-700-0
|
98219-34-2
|
The oil obtained from the pyrolysis of old electric cables at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
Details | |
|
The oil obtained from the pyrolysis of automobile shredder wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C28, substituted aromatic hydrocarbons, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
309-847-3
|
101227-24-1
|
The oil obtained from the pyrolysis of automobile shredder wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C28, substituted aromatic hydrocarbons, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
Details | |
|
The oil obtained from the pyrolysis of acid sludge at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
308-739-3
|
98219-70-6
|
The oil obtained from the pyrolysis of acid sludge at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C28, heteroaromatics and other organic compounds boiling in the range of approximately 50°C to 500°C (122°F to 932°F).
|
Details | |
|
The oil obtained from the heat treatment of polystyrene with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of approximately 70°C to 210°C (158°F to 410°F).
|
309-749-0
|
100801-66-9
|
The oil obtained from the heat treatment of polystyrene with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of approximately 70°C to 210°C (158°F to 410°F).
|
Details | |
|
The oil obtained from the heat treatment of polystyrene with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
309-836-3
|
101227-13-8
|
The oil obtained from the heat treatment of polystyrene with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
Details | |
|
The oil obtained from the heat treatment of polyethylene with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of 70°C to 120°C (158°F to 248°F).
|
309-748-5
|
100801-65-8
|
The oil obtained from the heat treatment of polyethylene with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of 70°C to 120°C (158°F to 248°F).
|
Details | |
|
The oil obtained from the heat treatment of polyethylene with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
309-837-9
|
101227-14-9
|
The oil obtained from the heat treatment of polyethylene with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
Details | |
|
The oil obtained from the heat treatment of a polyethylene/polypropylene mixture with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of approximately 70°C to 120°C (158°F to 248°F).
|
309-745-9
|
100801-63-6
|
The oil obtained from the heat treatment of a polyethylene/polypropylene mixture with coal tar pitch or aromatic oils. It consists predominantly of benzene and its homologs boiling in a range of approximately 70°C to 120°C (158°F to 248°F).
|
Details | |
|
The oil obtained from the heat treatment of a polyethylene/polypropylene mixture with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
309-746-4
|
100801-64-7
|
The oil obtained from the heat treatment of a polyethylene/polypropylene mixture with aromatic oils. It consists predominantly of naphthalene and its homologs, 1,3-diphenylpropane and other polynuclear aromatic hydrocarbons boiling in a range of approximately 200°C to 400°C (392°F to 752°F).
|
Details | |
|
The oil obtained from pyrolysis of polyester wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C20 and substituted aromatic hydrocarbons boiling in the range of approximately 50°C to 400°C (122°F to 752°F).
|
308-727-8
|
98219-59-1
|
The oil obtained from pyrolysis of polyester wastes at 600°C to 800°C (1112°F to 1472°F). It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C6 through C20 and substituted aromatic hydrocarbons boiling in the range of approximately 50°C to 400°C (122°F to 752°F).
|
Details | |
|
The oil obtained from condensation of the vapors from the heat treatment of pitch. Composed primarily of two- to four-ring aromatic compounds boiling in the range of 200°C to greater than 400°C (392°F to greater than 752°F).
|
309-855-7
|
101316-49-8
|
The oil obtained from condensation of the vapors from the heat treatment of pitch. Composed primarily of two- to four-ring aromatic compounds boiling in the range of 200°C to greater than 400°C (392°F to greater than 752°F).
|
Details | |
|
The off-gases from the zinc/lead blast furnace. Consists primarily of carbon monoxide, carbon dioxide and nitrogen.
|
298-735-7
|
93821-47-7
|
The off-gases from the zinc/lead blast furnace. Consists primarily of carbon monoxide, carbon dioxide and nitrogen.
|
Details | |
|
The off gas from the blast furnaces. Composed primarily of carbon monoxide, carbon dioxide, nitrogen, and hydrogen.
|
266-001-5
|
65996-68-1
|
The off gas from the blast furnaces. Composed primarily of carbon monoxide, carbon dioxide, nitrogen, and hydrogen.
|
Details | |
|
The non-volatile, high-boiling residue from the distillation of products from cumene-phenol process. It consists predominantly of substituted phenyl groups crosslinked by carbon-oxygen bonds and phenylaliphatic bonds.
|
269-798-8
|
68333-89-1
|
The non-volatile, high-boiling residue from the distillation of products from cumene-phenol process. It consists predominantly of substituted phenyl groups crosslinked by carbon-oxygen bonds and phenylaliphatic bonds.
|
Details | |
|
The neutral oil obtained by debasing annd dephenolating the light oil obtained by the high pressure hydrogenation of bituminous coal. Composed primarily of partially hydrogenated substituted mononuclear aromatic compounds.
|
295-326-5
|
91995-63-0
|
The neutral oil obtained by debasing annd dephenolating the light oil obtained by the high pressure hydrogenation of bituminous coal. Composed primarily of partially hydrogenated substituted mononuclear aromatic compounds.
|
Details | |
|
The neutral oil obtained by debasing and dephenolating the middle oil from the low temperature carbonization of bituminous coal. Composed primarily of a mixture of mono- and polynuclear, substituted and unsubstituted aromatic and naphthenic hydrocarbons and heterocycles as well as paraffinic hydrocarbons.
|
302-630-4
|
94113-95-8
|
The neutral oil obtained by debasing and dephenolating the middle oil from the low temperature carbonization of bituminous coal. Composed primarily of a mixture of mono- and polynuclear, substituted and unsubstituted aromatic and naphthenic hydrocarbons and heterocycles as well as paraffinic hydrocarbons.
|
Details | |
|
The neutral oil obtained by debasing and dephenolating the heavy oil from the high pressure hydrogenation of bituminous coal. Composed primarily of unsubstituted and alkyl-substituted aromatic polynuclear hydrocarbons that are partially hydrogenated and may contain heteroatoms.
|
302-632-5
|
94113-96-9
|
The neutral oil obtained by debasing and dephenolating the heavy oil from the high pressure hydrogenation of bituminous coal. Composed primarily of unsubstituted and alkyl-substituted aromatic polynuclear hydrocarbons that are partially hydrogenated and may contain heteroatoms.
|
Details | |
|
The neutral oil obtained by debasing and dephenolating the condensate from the pressure gasification of bituminous coal. Composed primarily of substituted and unsubstituted mono-to tetranuclear aromatic hydrocarbons and heterocyclic compounds.
|
295-324-4
|
91995-62-9
|
The neutral oil obtained by debasing and dephenolating the condensate from the pressure gasification of bituminous coal. Composed primarily of substituted and unsubstituted mono-to tetranuclear aromatic hydrocarbons and heterocyclic compounds.
|
Details | |
|
The neutral oil obtained by debasing and dehenolating the middle oil obtained by the high pressure hydrogenation of bituminous coal. Composed primarily of partially hydrogenated unsubstituted and alkyl-substituted di- and trinuclear aromatic hydrocarbons and heterocyclic compounds.
|
295-327-0
|
91995-64-1
|
The neutral oil obtained by debasing and dehenolating the middle oil obtained by the high pressure hydrogenation of bituminous coal. Composed primarily of partially hydrogenated unsubstituted and alkyl-substituted di- and trinuclear aromatic hydrocarbons and heterocyclic compounds.
|
Details | |
|
The mother liquors obtained during the hydrolysis of a sulfuric acid solution of titanyl sulfate in the manufacture of TiO2 by the sulfate process. They are separated by filtration or decantation.
|
292-634-1
|
90641-10-4
|
The mother liquors obtained during the hydrolysis of a sulfuric acid solution of titanyl sulfate in the manufacture of TiO2 by the sulfate process. They are separated by filtration or decantation.
|
Details | |
|
The mixed vegetable oils reclaimed from various food processing steps.
|
273-618-3
|
68990-65-8
|
The mixed vegetable oils reclaimed from various food processing steps.
|
Details | |
|
The middle oil from the atmospheric distillation of coal oil obtained from the hydrogenation of coal and coal-derived products. Composed primarily of aromatic hydrocarbons and naphthenes boiling in the range of approximately 200°C to 350°C (392°F to 662°F). The product contains phenols, organic sulfur compounds and organic nitrogen bases.
|
295-289-5
|
91995-27-6
|
The middle oil from the atmospheric distillation of coal oil obtained from the hydrogenation of coal and coal-derived products. Composed primarily of aromatic hydrocarbons and naphthenes boiling in the range of approximately 200°C to 350°C (392°F to 662°F). The product contains phenols, organic sulfur compounds and organic nitrogen bases.
|
Details | |
|
The methylnaphthalene fraction obtained from the fractional distillation of high temperature coal tar is debased using sulfuric acid. The crude bases are subsequently distilled to provide the tar bases. Contains chiefly isoquinoline, indole, quinaldine, methylquinoline, isoquinoline, and higher boiling bases.
|
310-243-7
|
140203-32-3
|
The methylnaphthalene fraction obtained from the fractional distillation of high temperature coal tar is debased using sulfuric acid. The crude bases are subsequently distilled to provide the tar bases. Contains chiefly isoquinoline, indole, quinaldine, methylquinoline, isoquinoline, and higher boiling bases.
|
Details | |
|
The metallic substance produced in a blast furnace or direct reduction furnace which contains over 90% iron.
|
265-998-4
|
65996-67-0
|
The metallic substance produced in a blast furnace or direct reduction furnace which contains over 90% iron.
|
Details | |
|
The metallic salts, primarily of iron and tin, which precipitate during the coating of steel by the halogen tin plating process.
|
273-741-2
|
69012-42-6
|
The metallic salts, primarily of iron and tin, which precipitate during the coating of steel by the halogen tin plating process.
|
Details | |
|
The metallic salts and oxides removed from the molten metals used to coat steel by dip processes. Composed primarily of salts and oxides of aluminum, lead, tin, and zinc.
|
266-009-9
|
65996-76-1
|
The metallic salts and oxides removed from the molten metals used to coat steel by dip processes. Composed primarily of salts and oxides of aluminum, lead, tin, and zinc.
|
Details | |
|
The material obtained by biological degradation of wastewater from industrial processes by aerobic or anaerobic paths. This material is thickened, treated with additives, compacted and dried.
|
309-613-0
|
100403-66-5
|
The material obtained by biological degradation of wastewater from industrial processes by aerobic or anaerobic paths. This material is thickened, treated with additives, compacted and dried.
|
Details | |
|
The material obtained after the production of glutin glue from chrome leather fold shavings.
|
295-732-2
|
92128-38-6
|
The material obtained after the production of glutin glue from chrome leather fold shavings.
|
Details | |
|
The material having low solids concentration in water obtained by biological oxidation of wastewater from rosin derivative manufacturing by aerobic or anaerobic paths.
|
309-843-1
|
101227-19-4
|
The material having low solids concentration in water obtained by biological oxidation of wastewater from rosin derivative manufacturing by aerobic or anaerobic paths.
|
Details | |
|
The material having low solids concentration in water obtained by biological oxidation of wastewater from hydroxyethylcellulose manufacturing by aerobic or anaerobic paths.
|
309-842-6
|
101227-18-3
|
The material having low solids concentration in water obtained by biological oxidation of wastewater from hydroxyethylcellulose manufacturing by aerobic or anaerobic paths.
|
Details | |
|
The low-boiling fraction obtained by the distillation of rosin. Contains decarboxylated rosin, decarboxylated resin acids, resin acids, terpenes and hydrocarbons derived from decarboxylated fatty acids.
|
270-333-6
|
68425-08-1
|
The low-boiling fraction obtained by the distillation of rosin. Contains decarboxylated rosin, decarboxylated resin acids, resin acids, terpenes and hydrocarbons derived from decarboxylated fatty acids.
|
Details | |
|
The low-boiling distillation fraction obtained from the high temperature carbonization of bituminous coal, which is further refined to remove excess crystalline salts. It consists primarily of creosote oil with some of the normal polynuclear aromatic salts, which are components of coal tar distillate, removed. It is crystal free at approximately 38°C (100°F).
|
274-566-4
|
70321-80-1
|
The low-boiling distillation fraction obtained from the high temperature carbonization of bituminous coal, which is further refined to remove excess crystalline salts. It consists primarily of creosote oil with some of the normal polynuclear aromatic salts, which are components of coal tar distillate, removed. It is crystal free at approximately 38°C (100°F).
|
Details | |
|
The low boiling fraction obtained by the distillation of tall oil. Contains fatty acids such as palmitic, stearic, oleic and linoleic as well as neutral materials.
|
266-039-2
|
65997-03-7
|
The low boiling fraction obtained by the distillation of tall oil. Contains fatty acids such as palmitic, stearic, oleic and linoleic as well as neutral materials.
|
Details | |
|
The liquid used to form the solvent slurry for treating coal in the presence of hydrogen at high temperatures (over 427°C (800°F)). It boils in a range of approximately 249°C to 454°C (480°F to 850°F).
|
270-079-6
|
68410-08-2
|
The liquid used to form the solvent slurry for treating coal in the presence of hydrogen at high temperatures (over 427°C (800°F)). It boils in a range of approximately 249°C to 454°C (480°F to 850°F).
|
Details | |
|
The liquid product of condensation of vapors emitted during the digestion of coal in a liquid solvent and boiling in the range of approximately 30°C to 300°C (86°F to 572°F). Composed primarily of partly hydrogenated condensed-ring aromatic hydrocarbons, aromatic compounds containing nitrogen, oxygen and sulfur, and their alkyl derivatives having carbon numbers predominantly in the range of C4 through C14.
|
302-688-0
|
94114-52-0
|
The liquid product of condensation of vapors emitted during the digestion of coal in a liquid solvent and boiling in the range of approximately 30°C to 300°C (86°F to 572°F). Composed primarily of partly hydrogenated condensed-ring aromatic hydrocarbons, aromatic compounds containing nitrogen, oxygen and sulfur, and their alkyl derivatives having carbon numbers predominantly in the range of C4 through C14.
|
Details | |
|
The liquid product from various refinery streams, usually residues. The composition is complex and varies with the source of the crude oil.
|
270-675-6
|
68476-33-5
|
The liquid product from various refinery streams, usually residues. The composition is complex and varies with the source of the crude oil.
|
Details | |
|
The lining of the cathodic portion of aluminum electrolysis cells consists of a carbon mass which, for the purpose of thermal isolation, is embedded in a layer of fireproof masses (SiO2 + Al2O3) in a steel vat. Flux and aluminum penetrate these masses during the furnace operation.
|
306-253-6
|
96690-57-2
|
The lining of the cathodic portion of aluminum electrolysis cells consists of a carbon mass which, for the purpose of thermal isolation, is embedded in a layer of fireproof masses (SiO2 + Al2O3) in a steel vat. Flux and aluminum penetrate these masses during the furnace operation.
|
Details | |
|
The light terpene fraction separated from pseudomethylionone during distillation. It consists primarily of methylheptanone and linalool with trace amounts of citral and pseudomethylionone.
|
273-055-3
|
68937-18-8
|
The light terpene fraction separated from pseudomethylionone during distillation. It consists primarily of methylheptanone and linalool with trace amounts of citral and pseudomethylionone.
|
Details | |
|
The light terpene fraction separated from pseudoionone during distillation. It consists primarily of methylheptanone, linalool and citral with trace amounts of pseudoionone.
|
273-073-1
|
68937-52-0
|
The light terpene fraction separated from pseudoionone during distillation. It consists primarily of methylheptanone, linalool and citral with trace amounts of pseudoionone.
|
Details | |
|
The light oil obtained by the distillation of coal tar is dephenolated with caustic soda, and debased with sulfuric acid. The crude base is obtained on subsequent neutralization. It boils in the approximate range of 110°C to 240°C (230°F to 464°F), and consists primarily of pyridine, picoline, lutidine, collidine, aniline, xylidine, quinoline, isoquinoline, and quinaldine.
|
310-244-2
|
140203-33-4
|
The light oil obtained by the distillation of coal tar is dephenolated with caustic soda, and debased with sulfuric acid. The crude base is obtained on subsequent neutralization. It boils in the approximate range of 110°C to 240°C (230°F to 464°F), and consists primarily of pyridine, picoline, lutidine, collidine, aniline, xylidine, quinoline, isoquinoline, and quinaldine.
|
Details | |
|
The light ends from fractionation bottoms boiling in the range of approximately 332°C to 393°C (630°F to 740°F).
|
271-076-2
|
68515-35-5
|
The light ends from fractionation bottoms boiling in the range of approximately 332°C to 393°C (630°F to 740°F).
|
Details | |
|
The light ends from fractionation bottoms boiling in a range of approximately 360°C to 427°C (680°F to 800°F).
|
271-077-8
|
68515-36-6
|
The light ends from fractionation bottoms boiling in a range of approximately 360°C to 427°C (680°F to 800°F).
|
Details | |
|
The light end distillation fraction boiling approximately below 82.5°C.
|
271-788-3
|
68608-59-3
|
The light end distillation fraction boiling approximately below 82.5°C.
|
Details | |
|
The insoluble protein formed from fibrinogen by the proteolytic action of thrombin during normal clotting of blood.
|
232-597-0
|
9001-31-4
|
The insoluble protein formed from fibrinogen by the proteolytic action of thrombin during normal clotting of blood.
|
Details | |
|
The hydrocarbon fraction distilled from oil of turpentine. Contains greater than 80% α-pinene, the remainder being other terpene hydrocarbons.
|
266-031-9
|
65996-96-5
|
The hydrocarbon fraction distilled from oil of turpentine. Contains greater than 80% α-pinene, the remainder being other terpene hydrocarbons.
|
Details | |
|
The hydrocarbon fraction distilled from oil of turpentine or produced by the isomerization of α-pinene. Contains greater than 70% β-pinene. Other major components being limonene, α-pinene, camphene, myrcene. May contain other acyclic, monocyclic, and bicyclic terpenes.
|
266-032-4
|
65996-97-6
|
The hydrocarbon fraction distilled from oil of turpentine or produced by the isomerization of α-pinene. Contains greater than 70% β-pinene. Other major components being limonene, α-pinene, camphene, myrcene. May contain other acyclic, monocyclic, and bicyclic terpenes.
|
Details | |
|
The hot gases obtained by the roasting of raw zinc concentrate are cooled and cleaned from dust by passing through a spray of dilute sulfuric acid and/or water. This acid and/or water is filtered; the solid residue contains most of the volatile components of the concentrates to be roasted.
|
309-609-9
|
100403-63-2
|
The hot gases obtained by the roasting of raw zinc concentrate are cooled and cleaned from dust by passing through a spray of dilute sulfuric acid and/or water. This acid and/or water is filtered; the solid residue contains most of the volatile components of the concentrates to be roasted.
|
Details | |
|
The high-boiling fraction separated by distillation from the products obtained from the reaction of nitric acid with cyclododecanol and cyclododecanone. Composed primarily of dodecanedioic acid, undecanedioic acid, and sebacic acid.
|
276-431-5
|
72162-23-3
|
The high-boiling fraction separated by distillation from the products obtained from the reaction of nitric acid with cyclododecanol and cyclododecanone. Composed primarily of dodecanedioic acid, undecanedioic acid, and sebacic acid.
|
Details | |
|
The high-boiling distillation fraction obtained from the high temperature carbonization of bituminous coal which is further refined to remove excess crystalline salts. It consists primarily of creosote oil with some of the normal polynuclear aromatic salts, which are components of coal tar distillates, removed. It is crystal free at approximately 5°C (41°F).
|
274-565-9
|
70321-79-8
|
The high-boiling distillation fraction obtained from the high temperature carbonization of bituminous coal which is further refined to remove excess crystalline salts. It consists primarily of creosote oil with some of the normal polynuclear aromatic salts, which are components of coal tar distillates, removed. It is crystal free at approximately 5°C (41°F).
|
Details | |
|
The high boiling residuum from the distillation of C7-11 alcohols.
|
271-230-9
|
68526-82-9
|
The high boiling residuum from the distillation of C7-11 alcohols.
|
Details | |
|
The heavy oil obtained by the high pressure hydrogenation of bituminous coal is subjected to acid extraction and then neutralized. The crude bases thus obtained contain polynuclear nitrogen aromatics such as quinoline, acridine, and phenanthridine.
|
310-245-8
|
140203-34-5
|
The heavy oil obtained by the high pressure hydrogenation of bituminous coal is subjected to acid extraction and then neutralized. The crude bases thus obtained contain polynuclear nitrogen aromatics such as quinoline, acridine, and phenanthridine.
|
Details | |
|
The heavy oil obtained by distillation in the range of approximately 300°C to 550°C (572°F to 1022°F) of coal oil from the catalytic hydrogenation of coal and coal- derived products. Composed primarily of polynuclear aromatics and naphthenes. The product contains sulfur, oxygen and nitrogen compounds.
|
295-286-9
|
91995-25-4
|
The heavy oil obtained by distillation in the range of approximately 300°C to 550°C (572°F to 1022°F) of coal oil from the catalytic hydrogenation of coal and coal- derived products. Composed primarily of polynuclear aromatics and naphthenes. The product contains sulfur, oxygen and nitrogen compounds.
|
Details | |
|
The heavy ends of fractionation bottoms boiling approximately above 393°C (740°F).
|
271-074-1
|
68515-33-3
|
The heavy ends of fractionation bottoms boiling approximately above 393°C (740°F).
|
Details | |
|
The heavy ends from fractionation bottoms boiling approximately above 427°C (800°F).
|
271-075-7
|
68515-34-4
|
The heavy ends from fractionation bottoms boiling approximately above 427°C (800°F).
|
Details | |
|
The heat-treated residue from the distillation of thermal cracked residuum and/or catalytic cracked clarified oil with a softening point from 50°C to 140°C (122°F to 284°F). Composed primarily of a complex combination of aromatic and other hydrocarbons and organic sulfur compounds.
|
310-173-7
|
122070-82-0
|
The heat-treated residue from the distillation of thermal cracked residuum and/or catalytic cracked clarified oil with a softening point from 50°C to 140°C (122°F to 284°F). Composed primarily of a complex combination of aromatic and other hydrocarbons and organic sulfur compounds.
|
Details | |
|
The heat treated residue from the distillation of high temperature coal tar. A black solid with an approximate softening point from 80°C to 180°C (176°F to 356°F). Composed primarily of a complex mixture of three or more membered condensed ring aromatic hydrocarbons.
|
310-162-7
|
121575-60-8
|
The heat treated residue from the distillation of high temperature coal tar. A black solid with an approximate softening point from 80°C to 180°C (176°F to 356°F). Composed primarily of a complex mixture of three or more membered condensed ring aromatic hydrocarbons.
|
Details | |
|
The gas produced by the reaction of oxygen with natural gas to obtain acetylene. It consists primarily of hydrogen, carbon monoxide, carbon dioxide, natural components of air and hydrocarbons having carbon numbers predominantly in the range of C1 through C2.
|
270-745-6
|
68477-64-5
|
The gas produced by the reaction of oxygen with natural gas to obtain acetylene. It consists primarily of hydrogen, carbon monoxide, carbon dioxide, natural components of air and hydrocarbons having carbon numbers predominantly in the range of C1 through C2.
|
Details | |
|
The gas evolved from the treatment of coal with a solvent in the presence of hydrogen at high temperatures (above 427°C (800°F)). Composed primarily of hydrocarbons having carbon numbers predominantly in the range of C1 through C5.
|
270-677-7
|
68476-35-7
|
The gas evolved from the treatment of coal with a solvent in the presence of hydrogen at high temperatures (above 427°C (800°F)). Composed primarily of hydrocarbons having carbon numbers predominantly in the range of C1 through C5.
|
Details | |
|
The gas evolved from the high temperature (greater than 700°C (1292°F)) destructive distillation of coal after the removal of high temperature coal tar, coke oven light oil, and ammonia liquor. Composed primarily of hydrogen and methane. May contain ammonia, hydrogen sulfide, and low molecular weight hydrocarbons.
|
266-015-1
|
65996-81-8
|
The gas evolved from the high temperature (greater than 700°C (1292°F)) destructive distillation of coal after the removal of high temperature coal tar, coke oven light oil, and ammonia liquor. Composed primarily of hydrogen and methane. May contain ammonia, hydrogen sulfide, and low molecular weight hydrocarbons.
|
Details | |
|
The fused substance formed by the action of a flux upon the gangue of the iron-bearing materials charged to a blast furnace and upon the oxidized impurities in the iron produced. Depending upon the particular blast furnace operation, the slag is composed primarily of sulfur and oxides of aluminum, calcium, magnesium, and silicon.
|
266-002-0
|
65996-69-2
|
The fused substance formed by the action of a flux upon the gangue of the iron-bearing materials charged to a blast furnace and upon the oxidized impurities in the iron produced. Depending upon the particular blast furnace operation, the slag is composed primarily of sulfur and oxides of aluminum, calcium, magnesium, and silicon.
|
Details | |
|
The fused substance formed by the action of a flux upon the gangue of iron-bearing materials charged to a steelmaking furnace and upon the oxidized impurities in the steel produced. Depending upon the particular steelmaking operation, the slag is composed primarily of sulfur and oxides of aluminum, calcium, iron, magnesium, manganese, phosphorus, and silicon.
|
266-004-1
|
65996-71-6
|
The fused substance formed by the action of a flux upon the gangue of iron-bearing materials charged to a steelmaking furnace and upon the oxidized impurities in the steel produced. Depending upon the particular steelmaking operation, the slag is composed primarily of sulfur and oxides of aluminum, calcium, iron, magnesium, manganese, phosphorus, and silicon.
|
Details | |
|
The fumes obtained from the concentration of ores and/or preconcentrates of tin by volatilization. Composed primarily of oxides of lead, tin, zinc and other volatile metals.
|
310-105-6
|
102423-87-0
|
The fumes obtained from the concentration of ores and/or preconcentrates of tin by volatilization. Composed primarily of oxides of lead, tin, zinc and other volatile metals.
|
Details | |
|
The fraction of tar acids, rich in 3- and 4-ethylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
284-891-3
|
84989-03-7
|
The fraction of tar acids, rich in 3- and 4-ethylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
Details | |
|
The fraction of tar acids, rich in 3,5-dimethylphenol, recovered by distillation of low-temperature coal tar acids.
|
284-896-0
|
84989-07-1
|
The fraction of tar acids, rich in 3,5-dimethylphenol, recovered by distillation of low-temperature coal tar acids.
|
Details | |
|
The fraction of tar acids, rich in 2,4- and 2,5-dimethylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
284-895-5
|
84989-06-0
|
The fraction of tar acids, rich in 2,4- and 2,5-dimethylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
Details | |
|
The fraction of tar acids, recovered by distillation of low-temperature coal tar crude tar acids, having an approximate boiling range of 225°C to 320°C (437°F to 608°F). Composed primarily of polyalkylphenols.
|
284-893-4
|
84989-05-9
|
The fraction of tar acids, recovered by distillation of low-temperature coal tar crude tar acids, having an approximate boiling range of 225°C to 320°C (437°F to 608°F). Composed primarily of polyalkylphenols.
|
Details | |
|
The fraction of tar acid rich in 3- and 4-methylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
284-892-9
|
84989-04-8
|
The fraction of tar acid rich in 3- and 4-methylphenol, recovered by distillation of low-temperature coal tar crude tar acids.
|
Details | |
|
The fraction from the distillation of bituminous coal pressure gasification tar boiling in the range of approximately 280°C to 400°C (536°F to 752°F). Composed primarily of anthracene, fluorene, phenanthrene and homologs, tetranuclear aromatic hydrocarbons, hetero compounds and aliphatic and naphthenic hydrocarbons.
|
302-615-2
|
94113-81-2
|
The fraction from the distillation of bituminous coal pressure gasification tar boiling in the range of approximately 280°C to 400°C (536°F to 752°F). Composed primarily of anthracene, fluorene, phenanthrene and homologs, tetranuclear aromatic hydrocarbons, hetero compounds and aliphatic and naphthenic hydrocarbons.
|
Details | |
|
The fossil resins extracted from coal seams by subjecting crushed coal to a flotation and hexane extraction process.
|
270-090-6
|
68410-73-1
|
The fossil resins extracted from coal seams by subjecting crushed coal to a flotation and hexane extraction process.
|
Details | |
|
The first fraction from the distillation of aromatic hydrocarbons, coumarone, naphthalene and indene rich prefractionator bottoms or washed carbolic oil boiling substantially below 145°C (293°F). Composed primarily of C7 and C8 aliphatic and aromatic hydrocarbons.
|
292-625-2
|
90641-02-4
|
The first fraction from the distillation of aromatic hydrocarbons, coumarone, naphthalene and indene rich prefractionator bottoms or washed carbolic oil boiling substantially below 145°C (293°F). Composed primarily of C7 and C8 aliphatic and aromatic hydrocarbons.
|
Details | |
|
The final, unpurified mother liquor in the beet or cane sugar industry from which no more sugar can be crystallized by factory methods.
|
232-487-2
|
8052-35-5
|
The final, unpurified mother liquor in the beet or cane sugar industry from which no more sugar can be crystallized by factory methods.
|
Details | |
|
The final cut residuum boiling at approximately 503°C (938°F).
|
273-491-4
|
68987-40-6
|
The final cut residuum boiling at approximately 503°C (938°F).
|
Details | |
|
The fibrous substance obtained from the treatment of lignocellulosic substances (wood or other agricultural fiber sources) with one or more aqueous solutions of pulping and/or bleaching chemicals. Composed of cellulose, hemi-cellulose, lignin, and other minor components. The relative amounts of these components depend on the extent of the pulping and bleaching processes.
|
265-995-8
|
65996-61-4
|
The fibrous substance obtained from the treatment of lignocellulosic substances (wood or other agricultural fiber sources) with one or more aqueous solutions of pulping and/or bleaching chemicals. Composed of cellulose, hemi-cellulose, lignin, and other minor components. The relative amounts of these components depend on the extent of the pulping and bleaching processes.
|
Details | |
|
The fibrous residue obtained from the separation of wort from a mash of malted barley and wheat flour in approximately equal proportions.
|
307-527-8
|
97660-18-9
|
The fibrous residue obtained from the separation of wort from a mash of malted barley and wheat flour in approximately equal proportions.
|
Details | |
|
The feed gas to the amine system for removal of hydrogen sulfide. It consists of hydrogen. Carbon monoxide, carbon dioxide, hydrogen sulfide and aliphatic hydrocarbons having carbon numbers predominantly in the range of C1 through C5 may also be present.
|
270-746-1
|
68477-65-6
|
The feed gas to the amine system for removal of hydrogen sulfide. It consists of hydrogen. Carbon monoxide, carbon dioxide, hydrogen sulfide and aliphatic hydrocarbons having carbon numbers predominantly in the range of C1 through C5 may also be present.
|
Details | |
|
The extract produced by the acidic extraction of bases from crude coal tar aromatic oils, neutralization, and distillation of the bases. Composed primarily of collidines, aniline, toluidines, lutidines, xylidines.
|
273-077-3
|
68937-63-3
|
The extract produced by the acidic extraction of bases from crude coal tar aromatic oils, neutralization, and distillation of the bases. Composed primarily of collidines, aniline, toluidines, lutidines, xylidines.
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Details | |
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from low-temperature coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove most of the tar bases present. Composed primarily of alkylnaphthalenes.
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310-246-3
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140362-54-5
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from low-temperature coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove most of the tar bases present. Composed primarily of alkylnaphthalenes.
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid. Composed primarily of hydrocarbons.
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310-285-6
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141785-65-1
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid. Composed primarily of hydrocarbons.
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove tar bases. Composed primarily of alkylnaphthalenes.
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284-901-6
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84989-12-8
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The extract oil boiling in the range of approximately 220°C to 265°C (428°F to 509°F) from coal tar alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove tar bases. Composed primarily of alkylnaphthalenes.
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The extract obtained by treating the pulp from the various pulping processes with hot caustic. It contains the soluble compound in the pulp remaining after the pulping process and the compounds solubilized by bleaching.
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270-323-1
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68424-83-9
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The extract obtained by treating the pulp from the various pulping processes with hot caustic. It contains the soluble compound in the pulp remaining after the pulping process and the compounds solubilized by bleaching.
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The extract from coal tar oil produced by an alkaline wash such as aqueous sodium hydroxide. Composed primarily of the alkali salts of various phenolic compounds.
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266-017-2
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65996-83-0
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The extract from coal tar oil produced by an alkaline wash such as aqueous sodium hydroxide. Composed primarily of the alkali salts of various phenolic compounds.
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The extract from coal tar oil alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove naphthalene. Composed primarily of the acid salts of various aromatic nitrogen bases including pyridine, quinoline, and their alkyl derivatives.
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266-020-9
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65996-86-3
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The extract from coal tar oil alkaline extract residue produced by an acidic wash such as aqueous sulfuric acid after distillation to remove naphthalene. Composed primarily of the acid salts of various aromatic nitrogen bases including pyridine, quinoline, and their alkyl derivatives.
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The dusts from an electrostatic filter obtained during the combustion of waste substances from the preparation of acrylonitrile according to the Sohio process. Composed primarily of carbonates and sulfates of antimony and molybdenum.
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309-961-3
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101794-79-0
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The dusts from an electrostatic filter obtained during the combustion of waste substances from the preparation of acrylonitrile according to the Sohio process. Composed primarily of carbonates and sulfates of antimony and molybdenum.
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The dust produced from a fume cleaning process used to remove solids from the gas stream from a steelmaking desulfurizing plant using injected calcium carbide composed of iron oxide, calcium sulfide and calcium carbide.
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305-413-2
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94551-65-2
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The dust produced from a fume cleaning process used to remove solids from the gas stream from a steelmaking desulfurizing plant using injected calcium carbide composed of iron oxide, calcium sulfide and calcium carbide.
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The dust obtained from the refining of materials from primary and secondary sources containing gold, iridium, osmium, palladium, platinum, rhenium, ruthenium and silver. Composed primarily of lead with traces of other metals.
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308-496-3
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98072-44-7
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The dust obtained from the refining of materials from primary and secondary sources containing gold, iridium, osmium, palladium, platinum, rhenium, ruthenium and silver. Composed primarily of lead with traces of other metals.
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The dust generated from the initial cleaning of off gases from a blast furnace. Composed primarily of iron and carbon. May contain varying amounts of other elements, oxides, and trace compounds.
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266-003-6
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65996-70-5
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The dust generated from the initial cleaning of off gases from a blast furnace. Composed primarily of iron and carbon. May contain varying amounts of other elements, oxides, and trace compounds.
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The dust generated during the charging, operation, and tapping of a steelmaking furnace and from steel conditioning, including that which is recovered through the use of pollution abatement equipment. Composed primarily of iron oxides. May contain varying amounts of other metallic oxides and trace compounds.
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266-005-7
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65996-72-7
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The dust generated during the charging, operation, and tapping of a steelmaking furnace and from steel conditioning, including that which is recovered through the use of pollution abatement equipment. Composed primarily of iron oxides. May contain varying amounts of other metallic oxides and trace compounds.
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The dried, mixed culture of microorganisms from a waste treatment process of pulping and papermaking liquid wastes. Contains ammonia and phosphoric acid.
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269-143-6
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68188-15-8
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The dried, mixed culture of microorganisms from a waste treatment process of pulping and papermaking liquid wastes. Contains ammonia and phosphoric acid.
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The dried residue from corn after the removal of the larger part of the starch and germ and the separation of the bran in the wet-milling manufacture of corn starch or syrup, or by enzymatic treatment of the endosperm.
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266-116-0
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66071-96-3
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The dried residue from corn after the removal of the larger part of the starch and germ and the separation of the bran in the wet-milling manufacture of corn starch or syrup, or by enzymatic treatment of the endosperm.
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The dregs removed by liquid recovery from the oxidation of spent pulping liquor. It consists primarily of sodium carbonate, calcium carbonate and sand with trace amounts of Fe2O3.
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273-165-1
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68952-32-9
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The dregs removed by liquid recovery from the oxidation of spent pulping liquor. It consists primarily of sodium carbonate, calcium carbonate and sand with trace amounts of Fe2O3.
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The distillation residue remaining after the distillation of the neutralized, acid-extracted base-containing tar fractions obtained by the distillation of coal tars. It contains chiefly aniline, collidines, quinoline and quinoline derivatives and toluidines.
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295-544-0
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92062-29-8
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The distillation residue remaining after the distillation of the neutralized, acid-extracted base-containing tar fractions obtained by the distillation of coal tars. It contains chiefly aniline, collidines, quinoline and quinoline derivatives and toluidines.
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The distillation fraction boiling in the range of approximately 181°C to 186°C (356°F to 367°F) from the crude bases obtained from the neutralized, acid-extracted base-containing tar fractions obtained by the distillation of bituminous coal tar. It contains chiefly aniline and collidines.
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295-543-5
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92062-28-7
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The distillation fraction boiling in the range of approximately 181°C to 186°C (356°F to 367°F) from the crude bases obtained from the neutralized, acid-extracted base-containing tar fractions obtained by the distillation of bituminous coal tar. It contains chiefly aniline and collidines.
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The distillation fraction boiling in the range of approximately 180°C to 200°C (356°F to 392°F) from the crude bases obtained by dephenolating and debasing the carbolated oil from the distillation of coal tar. It contains chiefly aniline, collidines, lutidines and toluidines.
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295-541-4
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92062-27-6
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The distillation fraction boiling in the range of approximately 180°C to 200°C (356°F to 392°F) from the crude bases obtained by dephenolating and debasing the carbolated oil from the distillation of coal tar. It contains chiefly aniline, collidines, lutidines and toluidines.
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The distillation bottoms boiling above approximately 84.5°C.
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271-821-1
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68609-22-3
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The distillation bottoms boiling above approximately 84.5°C.
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The distillate of peat tar with a boiling range of approximately 175°C to 360°C. Composed primarily of paraffin hydrocarbons as well as mono and divalent phenols and phenol ethers.
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302-628-3
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94113-93-6
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The distillate of peat tar with a boiling range of approximately 175°C to 360°C. Composed primarily of paraffin hydrocarbons as well as mono and divalent phenols and phenol ethers.
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The distillate of coal tar produced by the high temperature carbonization of bituminous coal. It consists primarily of aromatic hydrocarbons, tar acids and tar bases.
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232-287-5
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8001-58-9
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The distillate of coal tar produced by the high temperature carbonization of bituminous coal. It consists primarily of aromatic hydrocarbons, tar acids and tar bases.
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The distillate obtained during the heat treatment of pitch obtained from coal gasification tar having an approximate distillation range of 100°C to 400°C (212°F to 752°F). Composed primarily of aromatic and other hydrocarbons, phenolic compounds and aromatic nitrogen compounds.
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310-230-6
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140203-20-9
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The distillate obtained during the heat treatment of pitch obtained from coal gasification tar having an approximate distillation range of 100°C to 400°C (212°F to 752°F). Composed primarily of aromatic and other hydrocarbons, phenolic compounds and aromatic nitrogen compounds.
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