Inventario CE
Inventario CE
Applicazioni nidificate
Inventario CE
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 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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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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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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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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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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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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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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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.
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295-304-5
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91995-42-5
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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.
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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.
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295-313-4
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91995-52-7
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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.
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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.
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295-295-8
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91995-35-6
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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.
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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.
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295-329-1
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91995-66-3
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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.
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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.
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295-323-9
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91995-61-8
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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.
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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.
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310-247-9
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140362-56-7
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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.
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Details | |
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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.
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273-304-6
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68956-48-9
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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.
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The recovered oil obtained by skimming all plant oil bearing water streams. It consists predominantly of lubricating oil, oil additives and intermediates.
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309-943-5
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101631-18-9
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The recovered oil obtained by skimming all plant oil bearing water streams. It consists predominantly of lubricating oil, oil additives and intermediates.
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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.
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310-294-5
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141785-66-2
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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.
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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.
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310-305-3
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185323-44-8
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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.
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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.
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310-292-4
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141785-63-9
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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.
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Details | |
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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.
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266-019-3
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65996-85-2
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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.
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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.
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266-018-8
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65996-84-1
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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.
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The purified internal fat of the hog. It consists primarily of stearin, palmitin and olein.
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263-100-5
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61789-99-9
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The purified internal fat of the hog. It consists primarily of stearin, palmitin and olein.
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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.
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296-473-8
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92704-41-1
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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.
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The product of agglomerating iron ore fines, concentrates, iron sinter, and other iron-bearing materials. Includes pellets, nodules and briquettes.
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265-996-3
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65996-65-8
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The product of agglomerating iron ore fines, concentrates, iron sinter, and other iron-bearing materials. Includes pellets, nodules and briquettes.
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The product obtained upon cleavage of the organic components of the acids during the burning of waste acid resins and waste acids.
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308-698-1
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98219-32-0
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The product obtained upon cleavage of the organic components of the acids during the burning of waste acid resins and waste acids.
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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.
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310-064-4
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102110-63-4
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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.
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The product obtained from the purification of waste waters from production and gas purification processes during non-ferrous metal production. Composed primarily of gypsum.
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310-066-5
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102110-64-5
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The product obtained from the purification of waste waters from production and gas purification processes during non-ferrous metal production. Composed primarily of gypsum.
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Details | |
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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.
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310-071-2
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102110-69-0
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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.
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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.
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292-629-4
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90641-06-8
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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.
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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.
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270-493-7
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68442-85-3
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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.
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Details | |
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The product obtained by the purification of copper-lead ore concentrate roasting offgas. Composed primarily of arsenic oxide (As2O3).
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310-063-9
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102110-62-3
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The product obtained by the purification of copper-lead ore concentrate roasting offgas. Composed primarily of arsenic oxide (As2O3).
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The product obtained by the purification of copper ore concentrate roasting offgas. Composed primarily of lead, mercury and selenium.
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310-062-3
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102110-61-2
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The product obtained by the purification of copper ore concentrate roasting offgas. Composed primarily of lead, mercury and selenium.
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Details | |
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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).
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307-353-2
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97593-48-1
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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).
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Details | |
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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.
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302-682-8
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94114-47-3
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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.
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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.
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292-654-0
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90669-59-3
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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.
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The product obtained by acid leaching of copper speiss. Composed primarily of antimony, arsenic and lead with high precious metal content.
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309-643-4
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100656-54-0
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The product obtained by acid leaching of copper speiss. Composed primarily of antimony, arsenic and lead with high precious metal content.
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The product obtained after alcoholic precipitation and treatment according to Cohn of the supernatant liquid obtained after sedimentation and centrifugation of bovine blood.
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292-322-5
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90604-29-8
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The product obtained after alcoholic precipitation and treatment according to Cohn of the supernatant liquid obtained after sedimentation and centrifugation of bovine blood.
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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.
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269-827-4
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68334-37-2
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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.
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Details | |
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The pregnant solution obtained when sulfuric acid is applied to copper oxide ores and the copper and other metals taken into solution.
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266-963-6
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67711-87-9
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The pregnant solution obtained when sulfuric acid is applied to copper oxide ores and the copper and other metals taken into solution.
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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.
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310-248-4
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140362-58-9
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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.
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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.
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266-007-8
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65996-74-9
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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.
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The overhead middle cut from fractionation boiling in a range of approximately 446°C to 482°C (835°F to 900°F).
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271-071-5
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68515-29-7
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The overhead middle cut from fractionation boiling in a range of approximately 446°C to 482°C (835°F to 900°F).
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The overhead light ends from fractionation boiling approximately below 446°C (835°F).
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271-069-4
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68515-28-6
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The overhead light ends from fractionation boiling approximately below 446°C (835°F).
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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.
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310-258-9
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140362-67-0
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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.
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Details | |
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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.
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292-624-7
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90641-01-3
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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.
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Details | |
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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.
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292-604-8
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90640-82-7
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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.
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Details | |
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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.
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292-612-1
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90640-90-7
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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.
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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.
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310-299-2
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185323-41-5
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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.
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Details | |
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The oil remaining after removal by a crystallization process of most acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
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310-223-8
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140203-14-1
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The oil remaining after removal by a crystallization process of most acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
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Details | |
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The oil remaining after removal by a crystallization process of acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
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292-606-9
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90640-85-0
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The oil remaining after removal by a crystallization process of acenaphthene from acenaphthene oil from coal tar. Composed primarily of naphthalene and alkylnaphthalenes.
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Details | |
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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.
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309-762-1
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100801-78-3
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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.
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Details | |