Popis EZ-a
Popis EZ-a
Nested Applications
Popis EZ-a
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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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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