GB491221A - Process for producing diesel oils - Google Patents
Process for producing diesel oilsInfo
- Publication number
- GB491221A GB491221A GB5877/37A GB587737A GB491221A GB 491221 A GB491221 A GB 491221A GB 5877/37 A GB5877/37 A GB 5877/37A GB 587737 A GB587737 A GB 587737A GB 491221 A GB491221 A GB 491221A
- Authority
- GB
- United Kingdom
- Prior art keywords
- density
- oil
- coal
- pit
- oils
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Diesel oils are obtained by mixing (a) the paraffinic oils prepared by catalytic conversion of carbon monoxide and hydrogen with (b) liquid or solid carbonaceous products poorer in hydrogen. Suitable fractions under (a) are those boiling above 200 DEG C.; suitable products under (b) are pit-coal tar oils, brown coal tar oils, low temperature distillation oils, shale oils, wood tar and the like obtained by high or low temperature coking of pit-coal, brown coal, shale, wood, peat and the like, extraction products of pit-coal and brown coal, products of mild hydrogenation, and solid hydrocarbons. If the last are insoluble in the paraffinic hydrocarbons they are brought into solution or suspension by means of dissolving agents. The hydrogen content of the products poor in hydrogen should not be so low as to cause excessive precipitation on addition of the paraffinic hydrocarbons; in some cases it is desirable, prior to mixing, to treat the product poor in hydrogen with a small quantity of gas oil to precipitate the insoluble substances which are then separated off. The substances so precipitated can be hydrogenated to useful oils. Also, in some cases the product from which the precipitate has been removed may be subjected to mild hydrogenation prior to mixture with the paraffinic hydrocarbons. The final mixture may be treated with fuller's earth and/or lye. The constituents are preferably mixed in such proportions as to give a Diesel oil of density 0,84-0,86 and a solidification point of about -20 DEG C. In the examples, Diesel oils are produced from (1) pit-coal tar oil of density 1,09, and a synthetic paraffinic oil of density 0,76 and initial B.P. 200 DEG C.; (2) brown coal tar of density 0,907 and B.P. 200-300 DEG C., and a synthetic oil of density 0,77 and B.P. 200-310 DEG C.; (3) a pit-coal distillate of density 1,07 and B.P. 215-360 DEG C. and the synthetic oil of example 2; (4) a pit-coal low temperature tar fraction of density 0,991 and B.P. 200-320 DEG C. and the synthetic oil of example 2; (5) a dephenolated pit-coal low temperature tar fraction of density 0,996 and B.P. 200-320 DEG C. and the synthetic oil of example 2; (6) an incompletely hydrogenated brown coal oil of density 0,901 and B.P. 200-300 DEG C. and the synthetic oil of example 1; (7) a pit-coal first stage hydrogenation oil of density 0,974 and B.P. 200-320 DEG C. and the synthetic oil of example 2; (8) a liquefied extract obtained by mild hydrogenation of pit-coal and having a density of 1,028 and B.P. 200-320 DEG C., and the synthetic oil of example 2; and (9) a heavy anthracene oil, first purified by treatment with gas oil, and a synthetic oil of B.P. 200-310 DEG C.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE491221X | 1936-03-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB491221A true GB491221A (en) | 1938-08-26 |
Family
ID=6544241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5877/37A Expired GB491221A (en) | 1936-03-04 | 1937-02-26 | Process for producing diesel oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB491221A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101619229A (en) * | 2008-07-04 | 2010-01-06 | 汉能科技有限公司 | Method for preparing diesel oil components with coal tar oil light ends |
-
1937
- 1937-02-26 GB GB5877/37A patent/GB491221A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101619229A (en) * | 2008-07-04 | 2010-01-06 | 汉能科技有限公司 | Method for preparing diesel oil components with coal tar oil light ends |
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