Popis EZ-a
Popis EZ-a
Nested Applications
Popis EZ-a
The EC inventory published below is a copy as received from the JRC in 2008 on the founding of ECHA. It is comprised of the following lists:
- EINECS (European INventory of Existing Commercial chemical Substances) as published in O.J. C 146A, 15.6.1990. EINECS is an inventory of substances that were deemed to be on the European Community market between 1 January 1971 and 18 September 1981. EINECS was drawn up by the European Commission in the application of Article 13 of Directive 67/548/EEC, as amended by Directive 79/831/EEC, and in accordance with the detailed provisions of Commission Decision 81/437/EEC. Substances listed in EINECS are considered phase-in substances under the REACH Regulation.
- ELINCS (European LIst of Notified Chemical Substances) in support of Directive 92/32/EEC, the 7th amendment to Directive 67/548/EEC. ELINCS lists those substances which were notified under Directive 67/548/EEC, the Dangerous Substances Directive Notification of New Substances (NONS) that became commercially available after 18 September 1981.
- NLP (No-Longer Polymers). The definition of polymers was changed in April 1992 by Council Directive 92/32/EEC amending Directive 67/548/EEC, with the result that substances previously considered to be polymers were no longer excluded from regulation. Thus the No-longer Polymers (NLP) list was drawn up, consisting of such substances that were commercially available between 18 September 1981 and 31 October 1993.
Database contains 106212 unique substances/entries.
Filter the list
The List does not contain any Substances.
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302-831-7
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94134-61-9
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C24H51N3O.CH2O2
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Details | ||
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302-830-1
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94134-60-8
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C19H22N2O.H3O4P
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Details | ||
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302-829-6
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94134-59-5
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C8H16O4
|
Details | ||
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302-828-0
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94134-58-4
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C8H10BrNO3S.C4H9NO
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Details | ||
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302-827-5
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94134-57-3
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C12H23N.C8H10BrNO3S
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Details | ||
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302-825-4
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94134-56-2
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C14H36O8Si2Sn
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Details | ||
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302-824-9
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94134-55-1
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C8H11NO2.1/2C4H6O6
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Details | ||
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302-823-3
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94134-54-0
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C14H10Cl2O2
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Details | ||
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302-822-8
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94134-53-9
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C49H54O27
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Details | ||
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302-821-2
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94134-52-8
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C26H20N4O8S2.4K
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Details | ||
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302-820-7
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94134-51-7
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C40H29N7O15S4.4Na
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Details | ||
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302-819-1
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94134-50-6
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C32H29N5O8S2.2C4H11NO2
|
Details | ||
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302-818-6
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94134-49-3
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C6H15O5P
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Details | ||
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302-817-0
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94134-48-2
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C6H8ClNO3S
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Details | ||
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302-816-5
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94134-47-1
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C12H14O4
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Details | ||
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302-814-4
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94134-46-0
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C13H22O2
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Details | ||
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302-813-9
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94134-45-9
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C14H24O2
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Details | ||
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302-812-3
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94134-44-8
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C22H42O4
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Details | ||
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302-811-8
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94134-43-7
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C17H24O2S2
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Details | ||
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302-810-2
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94134-42-6
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C24H26O3
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Details | ||
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302-809-7
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94134-41-5
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C12H14O7
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Details | ||
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302-808-1
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94134-40-4
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C18H36AlO6.3H
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Details | ||
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302-807-6
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94134-39-1
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C19H28O3
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Details | ||
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302-806-0
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94134-38-0
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C19H28O3
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Details | ||
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302-805-5
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94134-37-9
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C16H14N2O8S.Na
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Details | ||
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302-803-4
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94134-36-8
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C28H46N2O5S
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Details | ||
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302-802-9
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94134-35-7
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C12H13ClNS.Cl
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Details | ||
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302-801-3
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94134-34-6
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Details | |||
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302-800-8
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94134-32-4
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C15H22O2
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Details | ||
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302-799-4
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94134-31-3
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C9H19NO2
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Details | ||
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302-798-9
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94134-30-2
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C20H18N4O5S
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Details | ||
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302-797-3
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94134-29-9
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C29H52O12
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Details | ||
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302-796-8
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94134-28-8
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C18H36O2
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Details | ||
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302-795-2
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94134-27-7
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C43H48O8
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Details | ||
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302-794-7
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94134-26-6
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C3H4N2O2
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Details | ||
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302-793-1
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94134-25-5
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C13H22O2
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Details | ||
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302-792-6
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94134-24-4
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C13H30NO3.C7H7O3S
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Details | ||
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302-791-0
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94134-23-3
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C23H39N3O3
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Details | ||
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302-790-5
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94134-22-2
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C17H36NO5Si.Cl
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Details | ||
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302-788-4
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94134-21-1
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C27H60NO3Si.Cl
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Details | ||
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302-787-9
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94134-20-0
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C10H15NO.C5H8O3
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Details | ||
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302-786-3
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94134-19-7
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C6H8O7.C4H11N5
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Details | ||
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302-785-8
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94134-18-6
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C14H16O
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Details | ||
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302-784-2
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94134-17-5
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C9H22N6.ClH
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Details | ||
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302-783-7
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94134-16-4
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C8H21N2O4P
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Details | ||
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302-782-1
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94134-15-3
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C6H17N2O4P
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Details | ||
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302-781-6
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94134-14-2
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C10H14N4O4
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Details | ||
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302-780-0
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94134-13-1
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C14H22N4O4
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Details | ||
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302-779-5
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94134-12-0
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C12H18N4O4
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Details | ||
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302-777-4
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94134-11-9
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C18H30N4O4
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Details | ||
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302-776-9
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94134-10-8
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C16H26N4O4
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Details | ||
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302-775-3
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94134-09-5
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C13H17NO8S
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Details | ||
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302-774-8
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94134-08-4
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C12H14O7S
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Details | ||
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302-773-2
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94134-07-3
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C9H10O6S
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Details | ||
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302-772-7
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94134-06-2
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C12H15NO6S
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Details | ||
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302-771-1
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94134-05-1
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C15H19Cl2NO3
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Details | ||
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302-770-6
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94134-04-0
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C18H27NO2
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Details | ||
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302-769-0
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94134-03-9
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C11H20O2
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Details | ||
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302-768-5
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94134-02-8
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C4H7N3O
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Details | ||
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302-766-4
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94134-01-7
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C6H9NO6.3C2H7NO
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Details | ||
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302-765-9
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94134-00-6
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C13H19NO4S.K
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Details | ||
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302-764-3
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94133-99-0
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C63H87O16P
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Details | ||
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302-763-8
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94133-98-9
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C9H16ClN4.Cl
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Details | ||
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302-762-2
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94133-97-8
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C16H30O7
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Details | ||
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302-761-7
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94133-96-7
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C3H6O3.xC2H8N2
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Details | ||
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302-760-1
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94133-95-6
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C13H12O8S2
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Details | ||
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302-759-6
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94133-94-5
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C22H47N3O.xC2H6O4S
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Details | ||
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302-758-0
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94133-93-4
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C24H49NO3
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Details | ||
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302-757-5
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94133-92-3
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C13H24O2
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Details | ||
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302-755-4
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94133-91-2
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C18H24F17N2O7S2Na
|
Details | ||
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302-754-9
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94133-90-1
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C16H19F17N2O6S2.Na
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Details | ||
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302-753-3
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94133-89-8
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C33H24N8O14S4.xNa
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Details | ||
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302-752-8
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94133-88-7
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C22H28N5.C2H3O2
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Details | ||
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302-751-2
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94133-87-6
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C16H11Cl3N4O4S.Na
|
Details | ||
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302-750-7
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94133-86-5
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C27H52O2
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Details | ||
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302-749-1
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94133-85-4
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C13H16N2.H3O4P
|
Details | ||
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302-748-6
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94133-84-3
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C10H13NO2.Na
|
Details | ||
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302-747-0
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94133-83-2
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C10H21N2O.HO4S
|
Details | ||
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302-746-5
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94133-82-1
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C3H5NO4.C2H5NO2.2Na
|
Details | ||
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302-744-4
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94133-81-0
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C16H20
|
Details | ||
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302-743-9
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94133-80-9
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C16H20
|
Details | ||
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302-742-3
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94133-79-6
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C16H20
|
Details | ||
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302-741-8
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94133-78-5
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C33H69O3P
|
Details | ||
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302-740-2
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94133-77-4
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C10H11ClO3.1/2Ca
|
Details | ||
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302-739-7
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94133-76-3
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C9H9ClO3.CH5N
|
Details | ||
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302-738-1
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94133-75-2
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C10H11ClO3.CH5N
|
Details | ||
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302-737-6
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94133-74-1
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C16H16N2O6S
|
Details | ||
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302-736-0
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94133-73-0
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C5H3Cl2FN2O.K
|
Details | ||
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302-735-5
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94133-72-9
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C16H10Cl2F3NO2.Na
|
Details | ||
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302-733-4
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94133-71-8
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C15H22N2O4
|
Details | ||
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302-732-9
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94133-70-7
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C26H28Cl2F3NO2
|
Details | ||
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302-731-3
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94133-69-4
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C26H30Cl2F3NO2
|
Details | ||
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302-730-8
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94133-68-3
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C17H9Cl2F3O
|
Details | ||
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302-729-2
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94133-67-2
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C16H6Cl3F3O
|
Details | ||
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302-728-7
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94133-66-1
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C16H9Cl2F3
|
Details | ||
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302-727-1
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94133-65-0
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C17H9Cl2F3O2
|
Details | ||
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302-726-6
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94133-64-9
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C16H10Cl2F3NO2
|
Details | ||
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302-725-0
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94133-63-8
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C26H30Cl2F3NO.C2H2O4
|
Details | ||
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302-724-5
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94133-62-7
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C5H3Cl2FN2O
|
Details | ||
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302-722-4
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94133-61-6
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C8H13BrO4
|
Details | ||
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302-721-9
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94133-60-5
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C10H13NO4
|
Details | ||
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302-720-3
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94133-59-2
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C12H14O
|
Details | ||
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302-719-8
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94133-58-1
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C11H20O2
|
Details | ||
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302-718-2
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94133-57-0
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C14H24O2
|
Details | ||
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302-717-7
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94133-56-9
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C10H18O2
|
Details | ||
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302-716-1
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94133-55-8
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C13H26O2
|
Details | ||
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302-715-6
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94133-54-7
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C12H22O
|
Details | ||
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302-714-0
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94133-53-6
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C11H16O2
|
Details | ||
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302-713-5
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94133-52-5
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C6H12O2S
|
Details | ||
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302-711-4
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94133-51-4
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C30H65N3O2.2Cl
|
Details | ||
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302-710-9
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94133-50-3
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C8H18O4S.C4H11N
|
Details | ||
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302-709-3
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94133-49-0
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C36H18Cl6N12O17S5
|
Details | ||
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302-708-8
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94133-48-9
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C28H17N3O10S2
|
Details | ||
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302-707-2
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94133-47-8
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C36H18Cl6N12O20S6
|
Details | ||
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302-706-7
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94133-46-7
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C35H28O6S2
|
Details | ||
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302-705-1
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94133-45-6
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C28H17N3O7S
|
Details | ||
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302-704-6
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94133-44-5
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C29H20ClN7O11S3.3Na
|
Details | ||
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302-703-0
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94133-43-4
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C14H26O2
|
Details | ||
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302-702-5
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94133-42-3
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C10H14ClN.ClH
|
Details | ||
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302-700-4
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94133-41-2
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C12H22O3
|
Details | ||
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302-699-0
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94132-59-9
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C14H24O
|
Details | ||
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302-698-5
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94131-37-0
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C30H54O8
|
Details | ||
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302-696-4
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94131-36-9
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C18H30O3S.Na
|
Details | ||
|
Diesel engine fuel produced by the hydrogenation of the middle distillate fraction of the products of hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 200°C to 280°C (392°F to 536°F). Composed primarily of hydrogenated two-ring hydrocarbons and their alkyl derivatives having carbon numbers predominantly in the range of C11 through C14.
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302-695-9
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94114-59-7
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Diesel engine fuel produced by the hydrogenation of the middle distillate fraction of the products of hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 200°C to 280°C (392°F to 536°F). Composed primarily of hydrogenated two-ring hydrocarbons and their alkyl derivatives having carbon numbers predominantly in the range of C11 through C14.
|
Details | |
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Jet engine fuel produced by hydrogenation of the middle distillate fraction of the products of hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 225°C (356°F to 473°F). Composed primarily of hydrogenated two-ring hydrocarbons and their alkyl derivatives having carbon numbers predominantly in the range of C10 through C12.
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302-694-3
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94114-58-6
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Jet engine fuel produced by hydrogenation of the middle distillate fraction of the products of hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 225°C (356°F to 473°F). Composed primarily of hydrogenated two-ring hydrocarbons and their alkyl derivatives having carbon numbers predominantly in the range of C10 through C12.
|
Details | |
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Distillate from the hydrogenation of hydrocracked middle distillate from coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 280°C (356°F to 536°F). Composed primarily of hydrogenated two- ring carbon compounds and their alkyl derivatives having carbon numbers predominantly in the range of C9 through C14.
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302-693-8
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94114-57-5
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Distillate from the hydrogenation of hydrocracked middle distillate from coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 280°C (356°F to 536°F). Composed primarily of hydrogenated two- ring carbon compounds and their alkyl derivatives having carbon numbers predominantly in the range of C9 through C14.
|
Details | |
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Distillate obtained from the hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 300°C (356°F to 572°F. Composed primarily of two-ring aromatic, hydrogenated aromatic and naphthenic compounds, their alkyl derivatives and alkanes having carbon numbers predominantly in the range of C9 through C14. Nitrogen, sulfur and oxygen-containing compounds are also present.
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302-692-2
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94114-56-4
|
Distillate obtained from the hydrocracking of coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes and boiling in the range of approximately 180°C to 300°C (356°F to 572°F. Composed primarily of two-ring aromatic, hydrogenated aromatic and naphthenic compounds, their alkyl derivatives and alkanes having carbon numbers predominantly in the range of C9 through C14. Nitrogen, sulfur and oxygen-containing compounds are also present.
|
Details | |
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Motor fuel produced by the reforming of the refined naphtha fraction of the products of 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 and naphthenic hydrocarbons, their alkyl derivatives and alkyl hydrocarbons having carbon numbers in the range of C4 through C9.
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302-691-7
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94114-55-3
|
Motor fuel produced by the reforming of the refined naphtha fraction of the products of 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 and naphthenic hydrocarbons, their alkyl derivatives and alkyl hydrocarbons having carbon numbers in the range of C4 through C9.
|
Details | |
|
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
|
94114-54-2
|
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.
|
Details | |
|
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 300°C (86°F to 572°F). Composed primarily of aromatic, hydrogenated aromatic and naphthenic compounds, their alkyl derivatives and alkanes with carbon numbers predominantly in the range of C4 through C14. Nitrogen, sulfur and oxygen-containing aromatic and hydrogenated aromatic compounds are also present.
|
302-689-6
|
94114-53-1
|
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 300°C (86°F to 572°F). Composed primarily of aromatic, hydrogenated aromatic and naphthenic compounds, their alkyl derivatives and alkanes with carbon numbers predominantly in the range of C4 through C14. Nitrogen, sulfur and oxygen-containing aromatic and hydrogenated aromatic compounds are also present.
|
Details | |
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The liquid product of condensation of vapors emitted during the digestion of coal in a liquid solvent and boiling in the range of approximately 30°C to 300°C (86°F to 572°F). Composed primarily of partly hydrogenated condensed-ring aromatic hydrocarbons, aromatic compounds containing nitrogen, oxygen and sulfur, and their alkyl derivatives having carbon numbers predominantly in the range of C4 through C14.
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302-688-0
|
94114-52-0
|
The liquid product of condensation of vapors emitted during the digestion of coal in a liquid solvent and boiling in the range of approximately 30°C to 300°C (86°F to 572°F). Composed primarily of partly hydrogenated condensed-ring aromatic hydrocarbons, aromatic compounds containing nitrogen, oxygen and sulfur, and their alkyl derivatives having carbon numbers predominantly in the range of C4 through C14.
|
Details | |
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Coke produced by calcination of green coke produced by delayed coking of coal extract from the liquid solvent extraction or supercritical gas extraction processes, or of the pitch fraction remaining after distillation of the products of hydrocracking of those extracts. A black porous solid composed primarily of highly condensed aromatic carbon rings with a very low hydrogen to carbon ratio containing some nitrogen, oxygen and sulfur compounds.
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302-687-5
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94114-51-9
|
Coke produced by calcination of green coke produced by delayed coking of coal extract from the liquid solvent extraction or supercritical gas extraction processes, or of the pitch fraction remaining after distillation of the products of hydrocracking of those extracts. A black porous solid composed primarily of highly condensed aromatic carbon rings with a very low hydrogen to carbon ratio containing some nitrogen, oxygen and sulfur compounds.
|
Details | |
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Coke produced by delayed coking of coal extract from the liquid solvent extraction or supercritical gas extraction processes or of the pitch fraction remaining after distillation of the products of hydrocracking of these extracts. A black porous solid composed primarily of highly condensed aromatic carbon rings with a low hydrogen to carbon ratio containing some nitrogen, oxygen and sulfur compounds.
|
302-685-4
|
94114-50-8
|
Coke produced by delayed coking of coal extract from the liquid solvent extraction or supercritical gas extraction processes or of the pitch fraction remaining after distillation of the products of hydrocracking of these extracts. A black porous solid composed primarily of highly condensed aromatic carbon rings with a low hydrogen to carbon ratio containing some nitrogen, oxygen and sulfur compounds.
|
Details | |
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The residual product from the distillation of hydrocracked coal extract or solution produced by the liquid solvent extraction or supercritical gas extraction processes. A black semi-solid composed primarily of condensed ring aromatic and hydrogenated aromatic compounds containing some sulfur, oxygen and nitrogen.
|
302-684-9
|
94114-49-5
|
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.
|
Details | |
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The substantially solvent-free product obtained by the distillation of the solvent from filtered coal extract solution produced by digesting coal in a liquid solvent. A black semi-solid, composed primarily of a complex combination of condensed-ring aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic compounds and other aromatic oxygen compounds, and their alkyl derivatives.
|
302-683-3
|
94114-48-4
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The substantially solvent-free product obtained by the distillation of the solvent from filtered coal extract solution produced by digesting coal in a liquid solvent. A black semi-solid, composed primarily of a complex combination of condensed-ring aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic compounds and other aromatic oxygen compounds, and their alkyl derivatives.
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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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A cohesive powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a liquid solvent.
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302-681-2
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94114-46-2
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A cohesive powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a liquid solvent.
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The substantially solvent-free product of the extraction of coal by a supercritical fluid solvent. A black or brown semi-solid, composed primarily of a complex combination of condensed-ring aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic compounds and other aromatic oxygen compounds, and their alkyl derivatives.
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302-680-7
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94114-45-1
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The substantially solvent-free product of the extraction of coal by a supercritical fluid solvent. A black or brown semi-solid, composed primarily of a complex combination of condensed-ring aromatic hydrocarbons, aromatic nitrogen compounds, aromatic sulfur compounds, phenolic compounds and other aromatic oxygen compounds, and their alkyl derivatives.
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A powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a supercritical fluid solvent.
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302-679-1
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94114-44-0
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A powder composed of coal mineral matter and undissolved coal remaining after extraction of coal by a supercritical fluid solvent.
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A complex combination of organic compounds obtained from the thermal decomposition of wood.
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302-678-6
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94114-43-9
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A complex combination of organic compounds obtained from the thermal decomposition of wood.
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Grinding material residues obtained during the production of magnets. Consists primarily of aluminum, cobalt, copper, iron, nickel, titanium and rare earth metals.
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302-677-0
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94114-42-8
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Grinding material residues obtained during the production of magnets. Consists primarily of aluminum, cobalt, copper, iron, nickel, titanium and rare earth metals.
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Substance resulting from the treatment of copper-manufacturing effluent with calcium hydroxide and subsequent filtration. Consists primarily of calcium and copper hydroxide and carbonates, oxides or sulfates of calcium, copper and other metals.
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302-676-5
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94114-41-7
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Substance resulting from the treatment of copper-manufacturing effluent with calcium hydroxide and subsequent filtration. Consists primarily of calcium and copper hydroxide and carbonates, oxides or sulfates of calcium, copper and other metals.
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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.
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302-674-4
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94114-40-6
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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.
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302-673-9
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94114-39-3
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302-672-3
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94114-38-2
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302-671-8
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94114-37-1
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302-670-2
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94114-36-0
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302-669-7
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94114-35-9
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302-668-1
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94114-34-8
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302-667-6
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94114-33-7
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302-666-0
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94114-32-6
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302-665-5
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94114-31-5
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302-663-4
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94114-30-4
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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.
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302-662-9
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94114-29-1
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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.
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302-661-3
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94114-27-9
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A complex combination of primary and biological sludge obtained from treatment of the effluent from a wood treatment plant.
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302-660-8
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94114-26-8
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A complex combination of primary and biological sludge obtained from treatment of the effluent from a wood treatment plant.
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Filter sludge formed during the treatment of surface water for cooling purposes in a power plant operation followed by removal of hydrogen carbonates. Composed primarily of calcium carbonate, with the addition of iron and/or aluminium oxides, chlorides, sulfates and fluorides of the alkali and alkaline earth elements and organic components from the raw water.
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302-659-2
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94114-25-7
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Filter sludge formed during the treatment of surface water for cooling purposes in a power plant operation followed by removal of hydrogen carbonates. Composed primarily of calcium carbonate, with the addition of iron and/or aluminium oxides, chlorides, sulfates and fluorides of the alkali and alkaline earth elements and organic components from the raw water.
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302-658-7
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94114-24-6
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302-657-1
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94114-23-5
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A complex combination of hydrocarbons obtained as the residue from the molecular distillation of a dewaxed heavy paraffinic distillate. It consists of hydrocarbons having carbon numbers predominantly greater than C80 and boiling above approximately 450°C (842°F).
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302-656-6
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94114-22-4
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A complex combination of hydrocarbons obtained as the residue from the molecular distillation of a dewaxed heavy paraffinic distillate. It consists of hydrocarbons having carbon numbers predominantly greater than C80 and boiling above approximately 450°C (842°F).
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The residue obtained from the recovery of crude benzene from aliphatic/naphthenic benzene absorbing oil boiling in the range of approximately 270°C to 380°C (518°F to 716°F) and used to absorb crude benzene from coal gas.
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302-655-0
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94114-21-3
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The residue obtained from the recovery of crude benzene from aliphatic/naphthenic benzene absorbing oil boiling in the range of approximately 270°C to 380°C (518°F to 716°F) and used to absorb crude benzene from coal gas.
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The residue from the vacuum distillation of the hydrogenative liquefaction of coal. Composed primarily of organic material boiling above 450°C (842°F), mineral components of the liquefied coal and selective catalysts.
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302-654-5
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94114-20-2
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The residue from the vacuum distillation of the hydrogenative liquefaction of coal. Composed primarily of organic material boiling above 450°C (842°F), mineral components of the liquefied coal and selective catalysts.
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Residue rich in calcium sulfate obtained during the desulfurization of flue gases of bituminous coal or oil-fired boilers of power plants. Composed primarily of calcium sulfate with chlorides, fluorides, trace element oxides as well as pure gas dust components from the combustion process.
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302-652-4
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94114-19-9
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Residue rich in calcium sulfate obtained during the desulfurization of flue gases of bituminous coal or oil-fired boilers of power plants. Composed primarily of calcium sulfate with chlorides, fluorides, trace element oxides as well as pure gas dust components from the combustion process.
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The residue from the distillation of peat tar having a softening point of 105°C to 145°C. Composed primarily of high boiling and nonvolatile mono and divalent phenols and paraffin hydrocarbons.
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302-651-9
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94114-14-4
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The residue from the distillation of peat tar having a softening point of 105°C to 145°C. Composed primarily of high boiling and nonvolatile mono and divalent phenols and paraffin hydrocarbons.
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The residue obtained during the distillation of high boiling fractions from bituminous coal high temperature tar and/or pitch coke oil, with a softening point of 140° to 170°C (284°F to 392°F) according to DIN 52025. Composed primarily of tri- and polynuclear aromatic compounds which also contain heteroatoms.
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302-650-3
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94114-13-3
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The residue obtained during the distillation of high boiling fractions from bituminous coal high temperature tar and/or pitch coke oil, with a softening point of 140° to 170°C (284°F to 392°F) according to DIN 52025. Composed primarily of tri- and polynuclear aromatic compounds which also contain heteroatoms.
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The residue from the distillation of bituminus coal pressure gasification tar. A black solid with a softening point of greater than 60°C (140°F) according to DIN 52025 and composed primarily of a complex mixture of polynuclear aromatic and naphthenic hydrocarbons that may be alkyl substituted and may contain heteroatoms, high boiling aliphatic hydrocarbons and polynuclear phenols.
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302-649-8
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94114-12-2
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The residue from the distillation of bituminus coal pressure gasification tar. A black solid with a softening point of greater than 60°C (140°F) according to DIN 52025 and composed primarily of a complex mixture of polynuclear aromatic and naphthenic hydrocarbons that may be alkyl substituted and may contain heteroatoms, high boiling aliphatic hydrocarbons and polynuclear phenols.
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302-648-2
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94114-11-1
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302-647-7
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94114-10-0
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A complex combination of organic compounds obtained as the low boiling fraction of the residues from the manufacture of acetic acid by the air oxidation of naphtha. It consists predominantly of mono- and di-carboxylic acids, esters, ketones and lactones having carbon numbers predominantly in the range C3 through C10 and boiling in the range of approximately 140°C to 250°C (284°F to 482°F).
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302-646-1
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94114-09-7
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A complex combination of organic compounds obtained as the low boiling fraction of the residues from the manufacture of acetic acid by the air oxidation of naphtha. It consists predominantly of mono- and di-carboxylic acids, esters, ketones and lactones having carbon numbers predominantly in the range C3 through C10 and boiling in the range of approximately 140°C to 250°C (284°F to 482°F).
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A complex combination of organic compounds obtained as the residual fraction from the distillation of a mixture of acetic, formic and propionic acids produced by the air oxidation of naphtha. It consists predominantly of carboxylic acids having carbon numbers predominantly in the range of C3 through C10 and boiling in the range of approximately 140°C to 200°C (284°F to 392°F).
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302-645-6
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94114-08-6
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A complex combination of organic compounds obtained as the residual fraction from the distillation of a mixture of acetic, formic and propionic acids produced by the air oxidation of naphtha. It consists predominantly of carboxylic acids having carbon numbers predominantly in the range of C3 through C10 and boiling in the range of approximately 140°C to 200°C (284°F to 392°F).
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Substance produced by drying and treating the residue obtained after the distillative removal of alcohol from the product of the yeast fermentation of molasses. Composed primarily of carbohydrate, protein, minerals and trace elements.
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302-644-0
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94114-07-5
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Substance produced by drying and treating the residue obtained after the distillative removal of alcohol from the product of the yeast fermentation of molasses. Composed primarily of carbohydrate, protein, minerals and trace elements.
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302-643-5
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94114-06-4
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302-641-4
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94114-05-3
|
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A distillation fraction from the distillation of a pyrolysis oil from polyamide waste. It consists predominantly of cyclopentadiene, benzene and homologs, indan and indene homologs and naphthalene and boils in the range of approximately 40°C to 200°C (104°F to 392°F).
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302-640-9
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94114-04-2
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A distillation fraction from the distillation of a pyrolysis oil from polyamide waste. It consists predominantly of cyclopentadiene, benzene and homologs, indan and indene homologs and naphthalene and boils in the range of approximately 40°C to 200°C (104°F to 392°F).
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A distillation fraction from the hydrogenation of pyrolysis gasoline boiling in the range of approximately 20°C to 200°C (68°F to 392°F).
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302-639-3
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94114-03-1
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A distillation fraction from the hydrogenation of pyrolysis gasoline boiling in the range of approximately 20°C to 200°C (68°F to 392°F).
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A residue from the distillation of pyrolysis gasoline. It consists predominantly of unsaturated hydrocarbons and multi-nuclear aromatic hydrocarbons.
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302-638-8
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94114-02-0
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A residue from the distillation of pyrolysis gasoline. It consists predominantly of unsaturated hydrocarbons and multi-nuclear aromatic hydrocarbons.
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Material obtained during the production of ferrosilicon. Consists primarily of SiO2 with lesser amounts of metal oxides.
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302-637-2
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94114-01-9
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Material obtained during the production of ferrosilicon. Consists primarily of SiO2 with lesser amounts of metal oxides.
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Dusts from the production of cast iron with spheroidal graphite. Consists primarily of magnesium oxide.
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302-636-7
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94114-00-8
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Dusts from the production of cast iron with spheroidal graphite. Consists primarily of magnesium oxide.
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Substance obtained from an electrostatic precipitator during alumina production. Consists primarily of borates, fluorides, hydroxides and oxides of aluminium, calcium, magnesium and sodium and their reaction products.
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302-635-1
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94113-99-2
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Substance obtained from an electrostatic precipitator during alumina production. Consists primarily of borates, fluorides, hydroxides and oxides of aluminium, calcium, magnesium and sodium and their reaction products.
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Insoluble reaction product obtained by addition of a picric acid solution to the solvent extract of a bituminous coal tar pitch. Composed primarily of polycyclic aromatic hydrocarbons.
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302-634-6
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94113-98-1
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Insoluble reaction product obtained by addition of a picric acid solution to the solvent extract of a bituminous coal tar pitch. Composed primarily of polycyclic aromatic hydrocarbons.
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Extract obtained by adding an iodine solution to the solvent extract of a bituminous coal tar pitch. Composed primarily of polycyclic aromatic hydrocarbons.
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302-633-0
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94113-97-0
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Extract obtained by adding an iodine solution to the solvent extract of a bituminous coal tar pitch. Composed primarily of polycyclic aromatic hydrocarbons.
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Details | |
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The neutral oil obtained by debasing and dephenolating the heavy oil from the high pressure hydrogenation of bituminous coal. Composed primarily of unsubstituted and alkyl-substituted aromatic polynuclear hydrocarbons that are partially hydrogenated and may contain heteroatoms.
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302-632-5
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94113-96-9
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The neutral oil obtained by debasing and dephenolating the heavy oil from the high pressure hydrogenation of bituminous coal. Composed primarily of unsubstituted and alkyl-substituted aromatic polynuclear hydrocarbons that are partially hydrogenated and may contain heteroatoms.
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The neutral oil obtained by debasing and dephenolating the middle oil from the low temperature carbonization of bituminous coal. Composed primarily of a mixture of mono- and polynuclear, substituted and unsubstituted aromatic and naphthenic hydrocarbons and heterocycles as well as paraffinic hydrocarbons.
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302-630-4
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94113-95-8
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The neutral oil obtained by debasing and dephenolating the middle oil from the low temperature carbonization of bituminous coal. Composed primarily of a mixture of mono- and polynuclear, substituted and unsubstituted aromatic and naphthenic hydrocarbons and heterocycles as well as paraffinic hydrocarbons.
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Details | |
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A product obtained by addition of slate to a composition of coal tar pitch and coal.
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302-629-9
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94113-94-7
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A product obtained by addition of slate to a composition of coal tar pitch and coal.
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The distillate of peat tar with a boiling range of approximately 175°C to 360°C. Composed primarily of paraffin hydrocarbons as well as mono and divalent phenols and phenol ethers.
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302-628-3
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94113-93-6
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The distillate of peat tar with a boiling range of approximately 175°C to 360°C. Composed primarily of paraffin hydrocarbons as well as mono and divalent phenols and phenol ethers.
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A distillate obtained from bituminous coal pressure gasification tar and boiling in the range of approximately 170°C to 240°C (338°F to 464°F). Composed primarily of indene/indan homologs, naphthalene and homologs, aliphatic and naphthenic hydrocarbons, as well as phenol and homologs.
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302-627-8
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94113-92-5
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A distillate obtained from bituminous coal pressure gasification tar and boiling in the range of approximately 170°C to 240°C (338°F to 464°F). Composed primarily of indene/indan homologs, naphthalene and homologs, aliphatic and naphthenic hydrocarbons, as well as phenol and homologs.
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A carbon-containing residue from the coking of air blown pitch coke oil and/or pitch distillate. Composed primarily of isotropic carbon , it contains small amounts of sulfur and ash constituents.
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302-626-2
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94113-91-4
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A carbon-containing residue from the coking of air blown pitch coke oil and/or pitch distillate. Composed primarily of isotropic carbon , it contains small amounts of sulfur and ash constituents.
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The solid material resulting from high temperature (greater than 700°C (1292°F)) carbonization of a pitch bound coal briquette. Composed primarily of carbon, it may contain varying amounts of ash, sulfur, volatile material and moisture.
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302-625-7
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94113-90-3
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The solid material resulting from high temperature (greater than 700°C (1292°F)) carbonization of a pitch bound coal briquette. Composed primarily of carbon, it may contain varying amounts of ash, sulfur, volatile material and moisture.
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A carbon-containing residue from the carbonization of lignite tar pitch with a volatile content up to 10%. Composed primarily of carbon, it may contain varying amounts of ash, sulfur, volatile material and moisture.
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302-624-1
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94113-89-0
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A carbon-containing residue from the carbonization of lignite tar pitch with a volatile content up to 10%. Composed primarily of carbon, it may contain varying amounts of ash, sulfur, volatile material and moisture.
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302-623-6
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94113-88-9
|
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A distillation fraction from the distillation of a pyrolysis oil from polyester wastes. It consists predominantly of benzene, toluene and styrene as well as other mono- and dinuclear aromatic hydrocarbons boiling in the range of approximately 40°C to 200°C (104°F to 392°F).
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302-622-0
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94113-87-8
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A distillation fraction from the distillation of a pyrolysis oil from polyester wastes. It consists predominantly of benzene, toluene and styrene as well as other mono- and dinuclear aromatic hydrocarbons boiling in the range of approximately 40°C to 200°C (104°F to 392°F).
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Details | |
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A distillation fraction from the distillation of a pyrolysis oil from polyester wastes. It consists predominantly of biphenyl, naphthalene and other mono- to tetranuclear aromatic hydrocarbons boiling in the range of approximately 200°C to 350°C (392°F to 662°F).
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302-621-5
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94113-86-7
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A distillation fraction from the distillation of a pyrolysis oil from polyester wastes. It consists predominantly of biphenyl, naphthalene and other mono- to tetranuclear aromatic hydrocarbons boiling in the range of approximately 200°C to 350°C (392°F to 662°F).
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Details | |
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A complex combination of organic compounds obtained by addition of a picric acid solution to the solvent extract of a bituminous coal tar pitch and decomposition of the precipitated pitch-picric acid reaction product with bases. Composed primarily of high molecular weight polycyclic aromatic compounds.
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302-619-4
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94113-85-6
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A complex combination of organic compounds obtained by addition of a picric acid solution to the solvent extract of a bituminous coal tar pitch and decomposition of the precipitated pitch-picric acid reaction product with bases. Composed primarily of high molecular weight polycyclic aromatic compounds.
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Details | |
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A complex combination of organic compounds obtained by addition of iodine solution to the solvent extract of a bituminous coal tar pitch and decomposition of the precipitated pitch iodine reaction products. Composed primarily of high molecular weight polycyclic aromatic compounds.
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302-618-9
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94113-84-5
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A complex combination of organic compounds obtained by addition of iodine solution to the solvent extract of a bituminous coal tar pitch and decomposition of the precipitated pitch iodine reaction products. Composed primarily of high molecular weight polycyclic aromatic compounds.
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A complex combination of hydrocarbons obtained by distillation of pyrolysis oil that was obtained by thermal cleavage of hydrocarbons. It consists predominantly of C8-10 aromatic hydrocarbons with a high portion of naphthalene.
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302-617-3
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94113-83-4
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A complex combination of hydrocarbons obtained by distillation of pyrolysis oil that was obtained by thermal cleavage of hydrocarbons. It consists predominantly of C8-10 aromatic hydrocarbons with a high portion of naphthalene.
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302-616-8
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94113-82-3
|
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The fraction from the distillation of bituminous coal pressure gasification tar boiling in the range of approximately 280°C to 400°C (536°F to 752°F). Composed primarily of anthracene, fluorene, phenanthrene and homologs, tetranuclear aromatic hydrocarbons, hetero compounds and aliphatic and naphthenic hydrocarbons.
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302-615-2
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94113-81-2
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The fraction from the distillation of bituminous coal pressure gasification tar boiling in the range of approximately 280°C to 400°C (536°F to 752°F). Composed primarily of anthracene, fluorene, phenanthrene and homologs, tetranuclear aromatic hydrocarbons, hetero compounds and aliphatic and naphthenic hydrocarbons.
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Details | |
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302-614-7
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94113-80-1
|
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302-613-1
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94113-79-8
|
Details | |||
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302-612-6
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94113-78-7
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C8H19O6P
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Details | ||