GB639137A - Improvements relating to the refining of naptha produced by the distillation of coaltar - Google Patents
Improvements relating to the refining of naptha produced by the distillation of coaltarInfo
- Publication number
- GB639137A GB639137A GB1102847A GB1102847A GB639137A GB 639137 A GB639137 A GB 639137A GB 1102847 A GB1102847 A GB 1102847A GB 1102847 A GB1102847 A GB 1102847A GB 639137 A GB639137 A GB 639137A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- acid
- washed
- naphtha
- oil
- 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/20—Refining by chemical means inorganic or organic compounds
-
- 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
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)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Coal tar naphtha which has been washed with strong sulphuric acid, is freed from acid-tar by sedimentation, agitated with aqueous alkali at a temperature between 90 DEG and 200 DEG C., and distilled. The hot alkali treatment, which may be carried out by boiling the naphtha and alkali together under a reflux condenser or by heating them together with agitation in a closed vessel under pressure, enables a distillate to be obtained having an acidity less than one-third of that given when cold alkali washing is employed. The treatment is preferably effected by agitating the naphtha with a solution of caustic soda, the amount of caustic soda being at least 0.3 per cent w : v of the naphtha, in a closed vessel at a temperature between 130 DEG and 200 DEG C. In an example, a naphtha fraction boiling between 100 DEG and 200 DEG C. was freed from tar acid and bases, and then agitated with 3 per cent by volume of 94.4 per cent sulphuric acid for 65 minutes at 40 DEG C. The mixture was allowed to settle for 15 minutes, as much acid-tar as possible was run off and the rest was, as far as possible, washed out with 20 per cent by volume of water. The oil was refluxed for 1 hour with 5 per cent by volume of a 50 per cent solution of caustic soda, and then distilled. The distillate had zero acidity. In another example, a naphtha fraction distilling up to 200 DEG C. was washed with 3 per cent of 94.6 per cent sulphuric acid for one hour at 40 DEG C. The acid-tar was separated and the oil washed twice with 20 per cent by volume of water. A portion of the oil was heated for one hour with 30 per cent by volume of a 2 per cent caustic soda solution under a pressure of 90 lbs. per square inch (about 146 DEG C.), and then distilled. The acidity of the distillate was about one-ninth of the distillate obtained from another portion of the acid-washed oil which was treated in the normal way, i.e. washed first with cold caustic soda solution and then with water until the water was neutral on leaving the oil.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1102847A GB639137A (en) | 1947-04-24 | 1947-04-24 | Improvements relating to the refining of naptha produced by the distillation of coaltar |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1102847A GB639137A (en) | 1947-04-24 | 1947-04-24 | Improvements relating to the refining of naptha produced by the distillation of coaltar |
Publications (1)
Publication Number | Publication Date |
---|---|
GB639137A true GB639137A (en) | 1950-06-21 |
Family
ID=9978726
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1102847A Expired GB639137A (en) | 1947-04-24 | 1947-04-24 | Improvements relating to the refining of naptha produced by the distillation of coaltar |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB639137A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2912374A (en) * | 1955-06-22 | 1959-11-10 | Shell Dev | Sulfuric acid sweetening of straight run petroleum distillates |
CN113004112A (en) * | 2021-03-04 | 2021-06-22 | 滁州市润达溶剂有限公司 | Isohexane preparation process |
-
1947
- 1947-04-24 GB GB1102847A patent/GB639137A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2912374A (en) * | 1955-06-22 | 1959-11-10 | Shell Dev | Sulfuric acid sweetening of straight run petroleum distillates |
CN113004112A (en) * | 2021-03-04 | 2021-06-22 | 滁州市润达溶剂有限公司 | Isohexane preparation process |
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