EU-ACTIVE_INTELLIGENT_FCM-ART_5_2_c_i

Active and Intelligent Materials - CMR Substances not allowed for use

EU. Carcinogens, Mutagens and Reproductive substances Not Allowed for Use in Components of Active and Intelligent Materials and Articles (Article 5(2)(c)(i)), Regulation 450/2009/EC, 30 May 2009

This list contains a non-exhaustive list of Carcinogens, Mutagens and Reproductive substances (CMRs) that are not allowed for use in components of active and intelligent materials and articles per Art. 5(2)(c)(i) of Regulation 450/2009/EC. The list is derived from a subset of substances on Table 3 of Annex VI to the CLP Regulation (1272/2008/EC).

Last updated 18 lipnja 2024. Database contains 1679 unique substances/entries.
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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
649-326-00-0
Carc. 1B; Muta. 1B
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).
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
649-384-00-7
Carc. 1B; Muta. 1B
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).
307-035-3
97488-96-5
649-234-00-0
Carc. 1B
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).
295-430-0
92045-49-3
649-284-00-3
Carc. 1B; Muta. 1B
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).
295-432-1
92045-51-7
649-337-00-0
Carc. 1B; Muta. 1B
202-049-5
91-20-3
601-052-00-2
Carc. 2
300-094-6
93920-10-6
028-054-00-0
Carc. 1A; Muta. 2; Repr. 1B
300-093-0
93920-09-3
028-054-00-0
Carc. 1A; Muta. 2; Repr. 1B
202-716-0
98-95-3
609-003-00-7
Carc. 2; Repr. 1B
202-430-6
95-54-5
612-145-00-2
Carc. 2; Muta. 2
202-429-0
95-53-4
612-091-00-X
Carc. 1B
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
649-500-00-6
Carc. 1B
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.
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
648-053-00-4
Carc. 1B
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.
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
648-067-00-0
Carc. 1B
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.
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
648-052-00-9
Carc. 1B
A complex combination of hydrocarbons obtained by the treatment of lignite carbon ization 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.
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
648-066-00-5
Carc. 1B
A complex combination of hydrocarbons obtained from lignite carbonization tar by solvent crystallisation (solvent deoiling), by sweating or an adducting process treated with hydrogen in the presence of a catalyst. It consists predomi nantly of straight and branched chain saturated hydrocarbons having carbon numbers predominantly greater than C12.
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
648-065-00-X
Carc. 1B
A complex combination of hydrocarbons obtained from lignite 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.
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
649-258-00-1
Carc. 1B
A complex combination of hydrocarbons obtained by the treatment of petroleum petrolatum with activated carbon for the removal of trace polar constituents and impur ities. It consists predominantly of saturated hydrocarbons having carbon numbers predominantly greater than C20.
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
649-257-00-6
Carc. 1B
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.
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
649-259-00-7
Carc. 1B
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.
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
649-117-00-4
Carc. 1A; Muta. 1B
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.
293-435-2
91079-47-9
648-127-00-6
Carc. 1B; Muta. 1B
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
648-057-00-6
Carc. 1B
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 °C to 170 °C (284 °F to 392 °F) according to DIN 52025. Composed primarily of tri- and polynuclear aromatic compounds which also contain heteroatoms.
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
648-071-00-2
Carc. 1B
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.
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
648-070-00-7
Carc. 1B
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.
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
648-069-00-1
Carc. 1B
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.
202-051-6
91-22-5
613-281-00-5
Carc. 1B; Muta. 2
307-769-4
97722-19-5
649-119-00-5
Carc. 1A; Muta. 1B
294-843-3
91770-57-9
649-492-00-4
Carc. 1B
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
649-499-00-2
Carc. 1B
A complex combination of hydrocarbons produced by solvent removal of paraffins from the residue of the distil lation of acid-treated, hydrocracked heavy paraffins and boiling approximately above 380 °C (716 °F).
292-656-1
90669-74-2
649-491-00-9
Carc. 1B
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
649-045-00-3
Carc. 1B
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.
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
648-105-00-6
Carc. 1B; Muta. 1B
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.
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
648-080-00-1
Carc. 1B
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 predomi nantly of dinuclear aromatic and heterocyclic hydrocarbons.
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
648-058-00-1
Carc. 1B
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.
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
648-142-00-8
Carc. 1B
A cohesive powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a liquid solvent.
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
649-043-00-2
Carc. 1B
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).
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
649-445-00-8
Carc. 1B
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).
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
649-448-00-4
Carc. 1B
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).
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
649-446-00-3
Carc. 1B
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.
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
649-040-00-6
Carc. 1B
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.
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
649-041-00-1
Carc. 1B
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).
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
649-046-00-9
Carc. 1B
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).
202-345-4
94-59-7
605-020-00-9
Carc. 1B; Muta. 2
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
649-245-00-0
Carc. 1B
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.
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
649-246-00-6
Carc. 1B
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 predomi nantly of saturated straight and branched hydrocarbons having carbon numbers predominantly greater than C20.
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
649-247-00-1
Carc. 1B
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.
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
649-250-00-8
Carc. 1B
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.
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
649-251-00-3
Carc. 1B
A complex combination of hydrocarbons obtained by the treatment of low-melting petroleum slack wax with bentonite for removal of trace polar constituents and impur ities. It consists predominantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
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
649-249-00-2
Carc. 1B
A complex combination of hydrocarbons obtained by treatment of low-melting petroleum slack wax with hydrogen in the presence of a catalyst. It consists predomi nantly of saturated straight and branched chain hydrocarbons having carbon numbers predominantly greater than C12.
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
649-252-00-9
Carc. 1B
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.
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
649-248-00-7
Carc. 1B
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.
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
028-015-00-8
Carc. 1A; Muta. 2; Repr. 1A
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
028-014-00-2
Carc. 1A; Muta. 2; Repr. 1B
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
649-341-00-2
Carc. 1B; Muta. 1B
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 approxi mately 73 °C to 85 °C (163 °F to 185 °F).
293-901-5
91648-39-4
050-031-00-9
Repr. 1B
202-476-7
96-09-3
603-084-00-2
Carc. 1B
619-394-6
99105-77-8
606-145-00-1
Repr. 2
202-388-9
95-06-7
006-038-00-4
Carc. 1B
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
648-129-00-7
Carc. 1B; Muta. 1B
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.
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
648-118-00-7
Carc. 1B; Muta. 1B
A complex combination of organic compounds obtained from brown coal gasification. Composed primarily of C6-10 hydroxy aromatic phenols and their homologs.
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
648-128-00-1
Carc. 1B; Muta. 1B
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.
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
648-119-00-2
Carc. 1B; Muta. 1B
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).
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
648-034-00-0
Carc. 1B; Muta. 1B
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.
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
648-033-00-5
Carc. 1B; Muta. 1B
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.
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
648-133-00-9
Carc. 1B; Muta. 1B
The distillation residue remaining after the distillation of the neutralized, acid-extracted base-containing tar fractions obtained by the distillation of oal tars. I contains chiefly aniline, collidines, quinoline and quinoline derivatives and toluidines.
293-766-2
91082-52-9
648-031-00-4
Carc. 1B; Muta. 1B
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
648-030-00-9
Carc. 1B; Muta. 1B
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.
293-767-8
91082-53-0
648-035-00-6
Carc. 1B; Muta. 1B
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
648-002-00-6
Carc. 1B; Muta. 1B
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.
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
648-059-00-7
Carc. 1B
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.
The deposit removed from crude coal tar storages. Composed primarily of coal tar and carbonaceous particulate matter.
293-764-1
91082-50-7
648-060-00-2
Carc. 1B
The deposit removed from crude coal tar storages. Composed primarily of coal tar and carbonaceous particulate matter.
202-625-6
97-99-4
603-061-00-7
Repr. 1B
SQ28,646
419-160-1
90657-55-9
607-377-00-6
Repr. 2
SQ 27,616
416-020-1
96314-26-0
607-413-00-0
Repr. 2
213-608-8
993-16-8
050-025-00-6
Repr. 2
The combination of wastes formed by the coking of bituminous coal tar pitch. It consists predominantly of carbon.
295-549-8
92062-34-5
648-063-00-9
Carc. 1B
The combination of wastes formed by the coking of bituminous coal tar pitch. It consists predominantly of carbon.
202-634-5
98-07-7
602-038-00-9
Carc. 1B
202-709-2
98-87-3
602-058-00-8
Carc. 2

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