GB332336A - Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight - Google Patents
Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weightInfo
- Publication number
- GB332336A GB332336A GB1520029A GB1520029A GB332336A GB 332336 A GB332336 A GB 332336A GB 1520029 A GB1520029 A GB 1520029A GB 1520029 A GB1520029 A GB 1520029A GB 332336 A GB332336 A GB 332336A
- Authority
- GB
- United Kingdom
- Prior art keywords
- adsorbent
- adsorbents
- catalyst
- treated
- molecular weight
- 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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
- C10G47/26—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries
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)
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
332,336. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). May 15, 1929. Hydrogenation, destructive. - In obtaining valuable hydrocarbon products from carbonaceous liquids containing substances of high molecular weight, the latter are removed from the liquids by adsorbents, and are destructively hydrogenated together with the adsorbents at elevated temperatures and pressures. The treatment with adsorbents may be carried out at ordinary or elevated temperatures, and the treated liquid mav be worked up further in any desired manner. Suitable adsorbents are silica gel and alumina gel; preferably the adsorbent should also be a destructive hydrogenation catalyst, such as molybdic acid, or alternatively should be impregnated with such a catalyst. The adsorbent may be used in a colloidal state. After the destructive hydrogenation the adsorbent may be regenerated and used again. In an example, a middle oil containing 7 per cent of constituents boiling between 325‹ C. and 350‹ C. and 5 per cent boiling above 350‹ C. is treated at 70-80 C‹. with a silica adsorbent which has been made catalytic by impregnation with a solution of the nitrates of molybdenum and zinc, followed by heat treatment. The middle oil is separated by centrifuging from the adsorbent and is destructively hydrogenated at 440-450‹ C. and under a pressure of 200 atmospheres of hydrogen in the presence of a catalyst containing molybdic and chromic acids. The activity of the catalyst remains practically unimpaired, whereas, without the preliminary treatment with adsorbent, poisoning occurs rapidly. The adsorbent and adsorbed substances are treated with hydrogen at 460‹ C. and 200 atmospheres. and the low-boiling products formed are returned to the main process. The adsorbent is preferably regenerated by heating for re-use.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1520029A GB332336A (en) | 1929-05-15 | 1929-05-15 | Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1520029A GB332336A (en) | 1929-05-15 | 1929-05-15 | Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight |
Publications (1)
Publication Number | Publication Date |
---|---|
GB332336A true GB332336A (en) | 1930-07-24 |
Family
ID=10054787
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1520029A Expired GB332336A (en) | 1929-05-15 | 1929-05-15 | Improvements in the working up of distillable carbonaceous liquids containing substances of high molecular weight |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB332336A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4071435A (en) * | 1977-06-06 | 1978-01-31 | Atlantic Richfield Company | Denitrogenation of syncrude |
GB2142930A (en) * | 1983-03-19 | 1985-01-30 | Asahi Chemical Ind | A process for cracking a heavy hydrocarbon |
FR2556000A1 (en) * | 1983-12-02 | 1985-06-07 | Asahi Chemical Ind | Process for converting a heavy hydrocarbon into a product of higher value or a lighter one |
-
1929
- 1929-05-15 GB GB1520029A patent/GB332336A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4071435A (en) * | 1977-06-06 | 1978-01-31 | Atlantic Richfield Company | Denitrogenation of syncrude |
GB2142930A (en) * | 1983-03-19 | 1985-01-30 | Asahi Chemical Ind | A process for cracking a heavy hydrocarbon |
US4770764A (en) * | 1983-03-19 | 1988-09-13 | Asahi Kasei Kogyo Kabushiki Kaisha | Process for converting heavy hydrocarbon into more valuable product |
FR2556000A1 (en) * | 1983-12-02 | 1985-06-07 | Asahi Chemical Ind | Process for converting a heavy hydrocarbon into a product of higher value or a lighter one |
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