EU-MARINE_ENVIRONMENTAL_POLICY-ART_3_8
EU-MARINE_ENVIRONMENTAL_POLICY-ART_3_8
Marine Environmental Policy Framework Directive - Hazardous Substances
EU. Hazardous Substances for Purposes of Directive 2008/56/EC (Marine Strategy Framework Directive), 25 June 2008, amended by Directive 2017/845/EU, 18 May 2017
This list contains a non-exhaustive inventory of hazardous substances for purposes of the Marine Strategy Framework Directive, especially as it concerns Art. 3(8), and Annexes I and III. The listed substances meet the European Union's definitions as hazardous, as provided on: (1) Table 3 of Annex VI to the CLP Regulation (1272/2008/EC); (2) Annex III of Directive 2000/54/EC (Biological Agents); Candidate List of SVHCs; and REACH Annex XIV (Authorisation List).
Last updated 18 April 2024. Database contains 5402 unique substances/entries.
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A complex combination of hydrocarbons obtained as first runnings from the vacuum distillation of effluents from the treatment of a solvent-deasphalted short residue with hydrogen in the presence of a catalyst. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C17 through C30 and boiling in the range of approximately 300°C to 400°C (572°F to 752°F). It produces a finished oil having a viscosity of 4cSt at approximately 100°C (212°F).
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307-661-7
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97675-87-1
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yes |
|||
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A complex combination of hydrocarbons obtained as first runnings from the vacuum distillation of effluents from the catalytic hydrotreatment of a solvent deasphalted short residue having a viscosity of 8cSt at approximately 100°C (212°F). It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C17 through C40 and boiling in the range of approximately 300°C to 500°C (592°F to 932°F).
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307-755-8
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97722-06-0
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yes |
|||
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300-257-1
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93924-61-9
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yes |
||||
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A complex combination of hydrocarbons produced by treating dewaxed heavy paraffinic distillate with hydrogen in the presence of a catalyst. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C20 through C50.
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292-617-9
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90640-95-2
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yes |
|||
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308-289-8
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97926-70-0
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yes |
||||
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308-131-8
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97862-81-2
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yes |
||||
|
308-290-3
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97926-71-1
|
yes |
||||
|
308-287-7
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97926-68-6
|
yes |
||||
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308-133-9
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97862-83-4
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yes |
||||
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305-975-9
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95371-08-7
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yes |
||||
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305-974-3
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95371-07-6
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yes |
||||
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306-004-1
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95465-89-7
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yes |
||||
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A complex combination of hydrocarbons produced by the distillation of the products of a steam cracking process. It consists predominantly of hydrocarbons having a carbon number of C4, predominantly 1-butene and 2-butene, containing also butane and isobutene and boiling in the range of approximately minus 12°C to 5°C (10.4°F to 41°F).
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295-405-4
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92045-23-3
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yes |
|||
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A complex combination of hydrocarbons obtained from prehydrogenated cracked naphtha after distillative separation of benzene- and toluene-containing hydrocarbon cuts and a higher boiling fraction. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately 30°C to 205°C (86°F to 401°F).
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295-445-2
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92045-63-1
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yes |
|||
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A complex combination of hydrocarbons obtained by distillation from the product of a naphtha steam cracking process and subsequent catalytic selective hydrogenation of gum formers. It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C12 and boiling in the range of approximately 30°C to 230°C (86°F to 446°F).
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295-443-1
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92045-61-9
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yes |
|||
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A complex combination of hydrocarbons obtained as first runnings from the depentanizer column before hydrotreatment of the aromatic charges. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C4 through C6, predominantly pentanes and pentenes, and boiling in the range of approximately 25°C to 40°C (77°F to 104°F).
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295-298-4
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91995-38-9
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yes |
|||
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A complex combination of hydrocarbons obtained by separation from the platformate-containing fraction. It consists predominantly of nonaromatic hydrocarbons having carbon numbers predominantly in the range of C5 through C11 and boiling in the range of approximately 35°C to 125°C (94°F to 257°F), benzene and toluene.
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297-466-2
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93572-36-2
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yes |
|||
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A complex combination of hydrocarbons obtained as solvents which have been subjected to hydrotreatment in order to convert aromatics to naphthenes by catalytic hydrogenation.
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297-852-0
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93763-33-8
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yes |
|||
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A complex combination of hydrocarbons obtained by the sorption of benzene from a catalytically fully hydrogenated benzene-rich hydrocarbon cut that was distillatively obtained from prehydrogenated cracked naphtha. It consists predominantly of paraffinic and naphthenic hydrocarbons having carbon numbers predominantly in the range of C6 through C7 and boiling in the range of approximately 70°C to 100°C (158°F to 212°F).
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295-446-8
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92045-64-2
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yes |
|||
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A complex combination of hydrocarbons obtained by separation from the platformate-containing fraction. It consists predominantly of nonaromatic hydrocarbons having carbon numbers predominantly in the range of C7 through C12 and boiling in the range of approximately 120°C to 210°C (248°F to 380°F) and C9 and higher aromatic hydrocarbons.
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297-465-7
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93572-35-1
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yes |
|||
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A complex combination of hydrocarbons obtained by distillation from prehydrogenated cracked naphtha. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C8 through C11 and boiling in the range of approximately 130°C to 205°C (266°F to 401°F).
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295-444-7
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92045-62-0
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yes |
|||
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A complex combination of hydrocarbons produced by the distillation of a cut from the catalytic cracking process, having undergone an alkaline washing. It consists predominantly of hydrocarbons having carbon numbers in the range of C8 through C12 and boiling in the range of approximately 130°C to 210°C (266°F to 410°F).
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295-794-0
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92128-94-4
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yes |
|||
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A complex combination of hydrocarbons obtained as solvents which have been subjected to hydrotreatment in order to convert aromatics to naphthenes by catalytic hydrogenation.
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297-853-6
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93763-34-9
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yes |
|||
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A complex combination of hydrocarbons obtained as solvents which have been subjected to hydrotreatment in order to convert aromatics to naphthenes by catalytic hydrogenation.
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297-854-1
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93763-35-0
|
yes |
|||
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297-857-8
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93763-38-3
|
yes |
||||
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A combination of hydrocarbons obtained from the distillation of hydrotreated naphtha followed by a solvent extraction and distillation process. It consists predominantly of saturated hydrocarbons boiling in the range of approximately 94°C to 99°C (201°F to 210°F).
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295-436-3
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92045-55-1
|
yes |
|||
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202-613-0
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97-86-9
|
yes |
||||
|
202-590-7
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97-54-1
|
yes |
||||
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307-033-2
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97488-94-3
|
yes |
||||
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A complex combination of hydrocarbons obtained from a petroleum stock by solvent refining and sweetening and boiling in the range of approximately 150°C to 260°C (302°F to 500°F).
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295-416-4
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92045-36-8
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yes |
|||
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A complex combination of hydrocarbons obtained as a wide cut hydrocarbon fuel cut from atmospheric distillation and boiling in the range of approximately 70°C to 220°C (158°F to 428°F).
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295-418-5
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92045-37-9
|
yes |
|||
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A complex combination of hydrocarbons obtained by subjecting a petroleum distillate to a sweetening process to convert mercaptans or to remove acidic impurities. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C9 through C16 and boiling in the range of 130°C to 290°C (266°F to 554°F).
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294-799-5
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91770-15-9
|
yes |
|||
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LAMBDA-CYHALOTHRIN
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415-130-7
|
91465-08-6
|
yes |
|||
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The volatile organic liquid condensed from the gas evolved in the low-temperature (less than 700°C (1292°F)) destructive distillation of coal. Composed primarily of C6-10 hydrocarbons.
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292-635-7
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90641-11-5
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yes |
|||
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BIS TRIFLUOROMETHANE SULFONIMIDE LITHIUM; FLUORAD BRAND LITHIUM TRIFLUOROMETHANESULPHONIMIDE HQ-115
|
415-300-0
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90076-65-6
|
yes |
|||
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A complex combination of hydrocarbons obtained by refining of crude oil. It consists predominantly of aromatics, naphthenics and paraffinics and produces a finished oil with a viscosity of 120 SUS at 100°F (23cSt at 40°C).
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297-474-6
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93572-43-1
|
yes |
|||
|
295-423-2
|
92045-42-6
|
yes |
||||
|
307-034-8
|
97488-95-4
|
yes |
||||
|
A complex combination of hydrocarbons obtained by solvent deparaffination of the distillation residue from hydrocracked petroleum. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C18 through C40 and boiling in the range of approximately 370°C to 550°C (698°F to 1022°F).
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305-594-8
|
94733-15-0
|
yes |
|||
|
A complex combination of hydrocarbons obtained by solvent deparaffination of the hydrogenated raffinate obtained by solvent extraction of a hydrotreated petroleum distillate. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C18 through C40 and boiling in the range of approximately 370°C to 550°C (698°F to 1022°F).
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305-595-3
|
94733-16-1
|
yes |
|||
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295-424-8
|
92045-43-7
|
yes |
||||
|
202-729-1
|
99-09-2
|
yes |
||||
|
202-360-6
|
94-74-6
|
yes |
||||
|
202-365-3
|
94-81-5
|
yes |
||||
|
213-447-3
|
950-10-7
|
yes |
||||
|
213-449-4
|
950-37-8
|
yes |
||||
|
DHPPME; MAK-ME; MEHPOPS; R-MAQ-ME
|
411-950-4
|
96562-58-2
|
yes |
|||
|
D,L-ESTER
|
411-040-7
|
97101-46-7
|
yes |
|||
|
431-720-7
|
90886-53-6
|
yes |
||||
|
202-500-6
|
96-33-3
|
yes |
||||
|
202-501-1
|
96-34-4
|
yes |
||||
|
CM 23-376; REOMET 30
|
401-280-0
|
91273-04-0
|
yes |
|||
|
202-088-8
|
91-66-7
|
yes |
||||
|
202-805-4
|
99-97-8
|
yes |
||||
|
213-103-2
|
924-42-5
|
yes |
yes |
|||
|
HSB-2115
|
414-740-0
|
96141-86-5
|
yes |
|||
|
427-880-2
|
90357-53-2
|
yes |
||||
|
202-615-1
|
97-88-1
|
yes |
||||
|
202-411-2
|
95-33-0
|
yes |
||||
|
FIDOL
|
418-790-4
|
93957-49-4
|
yes |
|||
|
The residue remaining from the distillation of recovered naphtha. Composed primarily of naphthalene and condensation products of indene and styrene.
|
292-636-2
|
90641-12-6
|
yes |
|||
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Fraction of the distillate obtained by hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 30°C to 180°C (86°F to 356°F). Composed primarily of aromatic, hydrogenated aromatic and naphthenic compounds, their alkyl derivatives and alkanes with carbon numbers predominantly in the range of C4 to C9. Nitrogen, sulfur and oxygen-containing aromatic and hydrogenated aromatic compounds are also present.
|
302-690-1
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94114-54-2
|
yes |
|||
|
A complex combination of hydrocarbons obtained by subjecting a catalytic cracked petroleum distillate to a sweetening process to convert mercaptans or to remove acidic impurities. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C6 through C12 and boiling in the range of approximately 60°C to 200°C (140°F to 392°F).
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295-431-6
|
92045-50-6
|
yes |
|||
|
A complex combination of hydrocarbons obtained from a catalytic hydrodesulfurization process. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately 30°C to 250°C (86°F to 482°F).
|
295-433-7
|
92045-52-8
|
yes |
|||
|
A complex combination of hydrocarbons obtained by distillation of hydrodesulfurized and dearomatized light petroleum fractions. It consists predominantly of C7 paraffins and cycloparaffins boiling in a range of approximately 90°C to 100°C (194°F to 212°F).
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295-434-2
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92045-53-9
|
yes |
|||
|
A complex combination of hydrocarbons obtained by treating a petroleum fraction, derived from a pyrolysis process, with hydrogen in the presence of a catalyst. It consists predominantly of unsaturated hydrocarbons having carbon numbers predominantly in the range of C5 through C11 and boiling in the range of approximately 35°C to 190°C (95°F to 374°F).
|
295-438-4
|
92045-57-3
|
yes |
|||
|
A complex combination of hydrocarbons obtained by distillation of a gasoline which has been catalytically isomerized. It consists predominantly of hexane isomers boiling in the range of approximately 60°C to 66°C (140°F to 151°F).
|
295-440-5
|
92045-58-4
|
yes |
|||
|
A complex combination of hydrocarbons obtained by subjecting naphtha from a catalytic cracking process to a sweetening process to convert mercaptans or to remove acidic impurities. It consists predominantly of hydrocarbons boiling in a range of approximately 35°C to 210°C (95°F to 410°F).
|
295-441-0
|
92045-59-5
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the fractionation of steam cracked naphtha after recovery from a heat soaking process. It consists predominantly of hydrocarbons having a carbon number predominantly in the range of C4 through C6 and boiling in the range of approximately 0°C to 80°C (32°F to 176°F).
|
296-028-8
|
92201-97-3
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment and distillation of debenzenized light steam-cracked petroleum naphtha. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C7 through C12 and boiling in the range of approximately 95°C to 200°C (203°F to 392°F).
|
308-713-1
|
98219-46-6
|
yes |
|||
|
A complex combination of hydrocarbons produced from the separation and subsequent hydrogenation of the products of a steam-cracking process to produce ethylene. It consists predominantly of saturated and unsaturated paraffins, cyclic paraffins and cyclic aromatic hydrocarbons having carbon numbers predominantly in the range of C4 through C10 and boiling in the range of approximately 50°C to 200°C (122°F to 392°F). The proportion of benzene hydrocarbons may vary up to 30 wt. % and the stream may also contain small amounts of sulphur and oxygenated compounds.
|
296-942-7
|
93165-55-0
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment and distillation of light steam-cracked petroleum naphtha. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C5 through C6 and boiling in the range of approximately 35°C to 80°C (95°F to 176°F).
|
308-714-7
|
98219-47-7
|
yes |
|||
|
A complex combination of hydrocarbons obtained by subjecting a petroleum distillate from the high temperature thermal cracking of heavy oil fractions to a sweetening process to convert mercaptans. It consists predominantly of aromatics, olefins and saturated hydrocarbons boiling in the range of approximately 20°C to 100°C (68°F to 212°F).
|
295-447-3
|
92045-65-3
|
yes |
|||
|
A complex combination of hydrocarbons obtained by subjecting a petroleum naphtha to a sweetening process to convert mercaptans or to remove acidic impurities. It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C5, predominantly C5, and boiling in the range of approximately minus 10°C to 35°C (14°F to 95°F).
|
295-442-6
|
92045-60-8
|
yes |
|||
|
307-035-3
|
97488-96-5
|
yes |
||||
|
A complex combination of hydrocarbons produced by the distillation of the products from a steam cracking process thereafter treated with hydrogen in the presence of a catalyst. It consists predominantly of aromatic hydrocarbons having carbon numbers in the range of C9 through C10 and boiling in the range of approximately 140°C to 200°C (284°F to 392°F).
|
292-637-8
|
90641-13-7
|
yes |
|||
|
A complex combination of hydrocarbons obtained by alkylation of butanes. It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C4 through C12, rich in isooctane, and boiling in the range of approximately 35°C to 210°C (95°F to 410°F).
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295-430-0
|
92045-49-3
|
yes |
|||
|
295-432-1
|
92045-51-7
|
yes |
||||
|
202-049-5
|
91-20-3
|
yes |
||||
|
300-094-6
|
93920-10-6
|
yes |
||||
|
300-093-0
|
93920-09-3
|
yes |
||||
|
202-716-0
|
98-95-3
|
yes |
yes |
|||
|
213-589-6
|
991-42-4
|
yes |
||||
|
202-423-8
|
95-48-7
|
yes |
||||
|
202-430-6
|
95-54-5
|
yes |
||||
|
202-429-0
|
95-53-4
|
yes |
yes |
|||
|
202-422-2
|
95-47-6
|
yes |
||||
|
202-464-1
|
95-92-1
|
yes |
||||
|
202-795-1
|
99-86-5
|
yes |
||||
|
232-627-2
|
9001-73-4
|
yes |
||||
|
A complex combination of hydrocarbons obtained from sulfur-containing paraffinic crude oil. It consists predominantly of a solvent refined deparaffinated lubricating oil with a viscosity of 65cSt at 50°C.
|
295-810-6
|
92129-09-4
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of lignite carbonization tar with bentonite for removal of trace constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-297-1
|
97926-77-7
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of lignite carbonization tar with silicic acid for removal of trace constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-298-7
|
97926-78-8
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of lignite carbonization tar with activated carbon for removal of trace constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-296-6
|
97926-76-6
|
yes |
|||
|
A complex combination of hydrocarbons obtained from liqnite carbonization tar by solvent crystallisation (solvent deoiling), by sweating or an adducting process treated with hydrogen in the presence of a catalyst. It consists predominantly of straight and branched chain saturated hydrocarbons having carbon numbers predominantly greater than C12.
|
295-455-7
|
92045-72-2
|
yes |
|||
|
A complex combination of hydrocarbons obtained from liqnite carbonization tar by solvent crystallisation (solvent deoiling), by sweating or an adducting process. It consists predominantly of straight and branched chain saturated hydrocarbons having carbon numbers predominantly greater than C12.
|
295-454-1
|
92045-71-1
|
yes |
|||
|
307-202-0
|
97553-43-0
|
yes |
||||
|
202-490-3
|
96-22-0
|
yes |
||||
|
301-312-2
|
93983-23-4
|
yes |
||||
|
232-629-3
|
9001-75-6
|
yes |
||||
|
A complex combination of hydrocarbons obtained by the treatment of petroleum petrolatum with activated carbon for the removal of trace polar constituents and impurities. It consists predominantly of saturated hydrocarbons having carbon numbers predominantly greater than C20.
|
308-149-6
|
97862-97-0
|
yes |
|||
|
A complex combination of hydrocarbons obtained as a semi-solid from dewaxed paraffinic residual oil treated with hydrogen in the presence of a catalyst. It consists predominantly of saturated microcrystalline and liquid hydrocarbons having carbon numbers predominantly greater than C20.
|
295-459-9
|
92045-77-7
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of petroleum petrolatum with silicic acid for the removal of trace polar constituents and impurities. It consists predominantly of saturated hydrocarbons having carbon numbers predominantly greater than C20.
|
308-150-1
|
97862-98-1
|
yes |
|||
|
A complex combination of hydrocarbons obtained by subjecting a liquified petroleum gas mix to a sweetening process to oxidize mercaptans or to remove acidic impurities. It consists predominantly of C4 saturated and unsaturated hydrocarbons.
|
295-463-0
|
92045-80-2
|
yes |
|||
|
291-844-0
|
90481-04-2
|
yes |
||||
|
293-435-2
|
91079-47-9
|
yes |
||||
|
213-423-2
|
947-02-4
|
yes |
||||
|
CYANINE BLEUE NO. 150
|
413-650-9
|
93971-95-0
|
yes |
|||
|
202-128-4
|
92-13-7
|
yes |
||||
|
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.
|
302-650-3
|
94114-13-3
|
yes |
|||
|
A complex black solid obtained by the heat treatment of low temperature coal tar pitch. It has a softening point within the approximate range of 50°C to 140°C (122°F to 284°F). Composed primarily of a complex mixture of aromatic compounds.
|
292-653-5
|
90669-58-2
|
yes |
|||
|
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
|
yes |
|||
|
A complex black solid or semi-solid obtained from the distillation of a low temperature coal tar. It has a softening point within the approximate range of 40°C to 180°C (104°F to 356°F). Composed primarily of a complex mixture of hydrocarbons.
|
292-651-4
|
90669-57-1
|
yes |
|||
|
618-541-1
|
9036-19-5
|
yes |
||||
|
500-024-6
|
9016-45-9
|
yes |
||||
|
500-024-6
|
9016-45-9
|
yes |
||||
|
500-024-6
|
9016-45-9
|
yes |
||||
|
AZYLACID-POTASSIUMSALT
|
401-630-2
|
96566-70-0
|
yes |
|||
|
213-029-0
|
917-58-8
|
yes |
||||
|
POTASSIUM-P-TOLYLSULFIMIDE
|
406-650-5
|
97888-41-0
|
yes |
|||
|
620-365-5
|
9016-72-2
|
yes |
||||
|
619-000-2
|
94125-34-5
|
yes |
||||
|
232-966-6
|
9068-59-1
|
yes |
||||
|
PYRIDABEN
|
405-700-3
|
96489-71-3
|
yes |
|||
|
202-051-6
|
91-22-5
|
yes |
||||
|
307-769-4
|
97722-19-5
|
yes |
||||
|
425-530-3
|
98769-75-6
|
yes |
||||
|
VITALIDE
|
414-870-8
|
96792-67-5
|
yes |
|||
|
426-970-9
|
94400-98-3
|
yes |
||||
|
DOW CORNING (R) 4-2920 INTERMEDIATE
|
406-930-7
|
96-29-7
|
yes |
|||
|
REACTIVE RED 180 (HYDROLYSED)
|
423-200-3
|
98114-32-0
|
yes |
|||
|
232-645-0
|
9001-98-3
|
yes |
||||
|
294-843-3
|
91770-57-9
|
yes |
||||
|
A complex combination of hydrocarbons produced by solvent removal of paraffins from the residue of the distillation of acid-treated, hydrocracked heavy paraffins and boiling approximately above 380°C (716°F).
|
295-499-7
|
92061-86-4
|
yes |
|||
|
292-656-1
|
90669-74-2
|
yes |
||||
|
A complex combination of hydrocarbons, sulfur compounds and metal-containing organic compounds obtained as the residue from refinery fractionation cracking processes. It produces a finished oil with a viscosity above 2cSt. at 100°C.
|
298-754-0
|
93821-66-0
|
yes |
|||
|
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.
|
295-505-8
|
92061-92-2
|
yes |
|||
|
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.
|
295-506-3
|
92061-93-3
|
yes |
|||
|
Residue from the fractional distillation of pitch distillate boiling in the range of approximately 400°C to 470°C (752°F to 846°F). Composed primarily of polynuclear aromatic hydrocarbons, and heterocyclic compounds.
|
295-507-9
|
92061-94-4
|
yes |
|||
|
A cohesive powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a liquid solvent.
|
302-681-2
|
94114-46-2
|
yes |
|||
|
A complex combination of hydrocarbons produced as the residual fraction from the distillation of the products from a catalytic cracking process. It consists predominantly of hydrocarbons having carbon numbers predominantly greater than C11 and boiling above approximately 200°C (392°F).
|
295-511-0
|
92061-97-7
|
yes |
|||
|
A complex combination of hydrocarbons obtained as a residual fraction from the distillation of hydrotreated steam-cracked naphtha. It consists predominantly of hydrocarbons boiling in the range of approximately 200°C to 350°C (32°F to 662°F).
|
295-514-7
|
92062-00-5
|
yes |
|||
|
A complex combination of hydrocarbons obtained as residue from the distillation of steam cracked heat soaked naphtha and boiling in the range of approximately 150°C to 350°C (302°F to 662°F).
|
297-905-8
|
93763-85-0
|
yes |
|||
|
A complex combination of hydrocarbons obtained as a column bottom from the separation of effluents from steam cracking naphtha at a high temperature. It boils in the range of approximately 147°C to 300°C (297°F to 572°F) and produces a finished oil having a viscosity of 18cSt at 50°C.
|
295-517-3
|
92062-04-9
|
yes |
|||
|
A complex combination of hydrocarbons obtained during the production of refined petroleum tar by the distillation of steam cracked tar. It consists predominantly of aromatic and other hydrocarbons and organic sulfur compounds.
|
292-657-7
|
90669-75-3
|
yes |
|||
|
A complex residuum from the vacuum distillation of the residuum from atmospheric distillation of crude oil. It consists predominantly of hydrocarbons having carbon numbers predominantly greater than C24 and boiling above approximately 390°C (734°F).
|
292-658-2
|
90669-76-4
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment and distillation of raw steam-cracked naphtha. It consists predominantly of unsaturated hydrocarbons boiling in the range above approximately 180°C (356°F).
|
308-733-0
|
98219-64-8
|
yes |
|||
|
-
|
953-17-3
|
yes |
||||
|
202-345-4
|
94-59-7
|
yes |
||||
|
213-104-8
|
924-43-6
|
yes |
||||
|
A complex combination of hydrocarbons obtained as a raffinate by treatment of a petroleum slack wax fraction with sulfuric acid treating process. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C20.
|
292-659-8
|
90669-77-5
|
yes |
|||
|
A complex combination of hydrocarbons obtained by treatment of a petroleum slack wax fraction with natural or modified clay in either a contacting or percolation process. It consists predominantly of saturated straight and branched hydrocarbons having carbon numbers predominantly greater than C20.
|
292-660-3
|
90669-78-6
|
yes |
|||
|
A complex combination of hydrocarbons obtained by treating slack wax with hydrogen in the presence of a catalyst. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C20.
|
295-523-6
|
92062-09-4
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of low-melting slack wax with activated carbon for the removal of trace polar constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-155-9
|
97863-04-2
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of low-melting petroleum slack wax with bentonite for removal of trace polar constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-156-4
|
97863-05-3
|
yes |
|||
|
A complex combination of hydrocarbons obtained by treatment of low-melting petroleum slack wax with hydrogen in the presence of a catalyst. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
295-525-7
|
92062-11-8
|
yes |
|||
|
A complex combination of hydrocarbons obtained by the treatment of low-melting petroleum slack wax with silicic acid for the removal of trace polar constituents and impurities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
308-158-5
|
97863-06-4
|
yes |
|||
|
A complex combination of hydrocarbons obtained from a petroleum fraction by solvent deparaffination. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
|
295-524-1
|
92062-10-7
|
yes |
|||
|
Substance obtained as a powdery cathodic precipitate during the electrolytic decoppering stage of copper refining electrolysis. Consists primarily of copper with antimony, arsenic, lead and nickel in metallic form as well as oxides and sulfates.
|
305-433-1
|
94551-87-8
|
yes |
|||
|
Product obtained from recycling of the end electrolyte of copper refining electrolysis followed by evaporation to separate the residual sulfuric acid. Consists primarily of nickel and iron sulfates with small amounts of the sulfates of zinc, alkali earths and alkali metals.
|
295-859-3
|
92129-57-2
|
yes |
|||
|
434-360-9
|
91125-43-8
|
yes |
||||
|
BENZTRIAZOL UV ABSORBER BUK 4499; BUK 4499; UV ABSORBER BUK 4499
|
403-080-9
|
92484-48-5
|
yes |
|||
|
ACTIZONE; PG 85; PHENOLESTER C; PHENOLESTER C/S
|
400-030-8
|
94612-91-6
|
yes |
|||
|
213-030-6
|
917-61-3
|
yes |
||||
|
A complex combination of hydrocarbons obtained by treating a petroleum fraction with hydrogen in the presence of a catalyst. It consists predominantly of cycloparaffinic hydrocarbons having carbon numbers predominantly in the range of C6 through C7 and boiling in the range of approximately 73°C to 85°C (163°F to 185°F).
|
295-529-9
|
92062-15-2
|
yes |
|||
|
293-901-5
|
91648-39-4
|
yes |
||||
|
202-476-7
|
96-09-3
|
yes |
||||
|
232-752-2
|
9014-01-1
|
yes |
||||
|
619-394-6
|
99105-77-8
|
yes |
||||
|
202-388-9
|
95-06-7
|
yes |
||||
|
807-366-8
|
946578-00-3
|
yes |
||||
|
The distillate from the acidification of alkaline washed lignite tar distillate boiling in the range of approximately 200°C to 230°C (392°F to 446°F). Composed primarily of m- and p-ethylphenol as well as cresols and xylenols.
|
302-662-9
|
94114-29-1
|
yes |
|||
|
A complex combination of organic compounds obtained from brown coal gasification. Composed primarily of C6-10 hydroxy aromatic phenols and their homologs.
|
295-536-7
|
92062-22-1
|
yes |
|||
|
A complex combination of organic compounds obtained from brown coal and boiling in the range of approximately 200°C to 230°C (392°F to 446°F). It contains chiefly phenols and pyridine bases.
|
295-540-9
|
92062-26-5
|
yes |
|||
|
A residue from the distillation of crude phenol from coal. It consists predominantly of phenols having carbon numbers in the range of C8 through C10 with a softening point of 60°C to 80°C (140°F to 176°F).
|
306-251-5
|
96690-55-0
|
yes |
|||
|
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.
|
295-541-4
|
92062-27-6
|
yes |
|||
|
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.
|
295-543-5
|
92062-28-7
|
yes |
|||
|
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.
|
295-544-0
|
92062-29-8
|
yes |
|||
|
293-766-2
|
91082-52-9
|
yes |
||||
|
Pyridine bases boiling in the range of approximately 125°C to 160°C (257°F 320°F) obtained by distillation of neutralized acid extract of the base-containing tar fraction obtained by the distillation of bituminous coal tars. Composed chiefly of lutidines and picolines.
|
295-548-2
|
92062-33-4
|
yes |
|||
|
293-767-8
|
91082-53-0
|
yes |
||||
|
The distillate from lignite tar boiling in the range of approximately 80°C to 250°C (176°F to 482°F). Composed primarily of aliphatic and aromatic hydrocarbons and monobasic phenols.
|
302-674-4
|
94114-40-6
|
yes |
|||
|
Coke- and ash-containing solid residues that separate on distillation and thermal treatment of bituminous coal high temperature tar in distillation installations and storage vessels. Consists predominantly of carbon and contains a small quantity of hetero compounds as well as ash components.
|
295-535-1
|
92062-20-9
|
yes |
|||
|
The deposit removed from crude coal tar storages. Composed primarily of coal tar and carbonaceous particulate matter.
|
293-764-1
|
91082-50-7
|
yes |
|||
|
425-420-5
|
98737-29-2
|
yes |
||||
|
202-625-6
|
97-99-4
|
yes |
||||
|
428-070-1
|
91788-83-9
|
yes |
||||
|
202-605-7
|
97-74-5
|
yes |
||||
|
C.I. REACTIVE BROWN 44
|
400-430-2
|
95078-21-0
|
yes |
|||
|
202-272-8
|
93-75-4
|
yes |
||||
|
SQ28,646
|
419-160-1
|
90657-55-9
|
yes |
|||
|
SQ 27,616
|
416-020-1
|
96314-26-0
|
yes |
|||
|
213-608-8
|
993-16-8
|
yes |
||||
|
680-302-2
|
95266-40-3
|
yes |
||||
|
403-670-6
|
92408-46-3
|
yes |
||||
|
ACID BLUE 349; AZO-METALCOMPLEX-BLUE AP 1149; BLEU ACIDE 349; C.I. ACID BLUE 349; SELLASET BLEU H; SELLASET BLUE H
|
402-870-0
|
93952-24-0
|
yes |
|||
|
232-650-8
|
9002-07-7
|
yes |
||||
|
424-390-0
|
93280-40-1
|
yes |
||||
|
The combination of wastes formed by the coking of bituminous coal tar pitch. It consists predominantly of carbon.
|
295-549-8
|
92062-34-5
|
yes |
|||
|
202-634-5
|
98-07-7
|
yes |
||||