GB710972A - Process for refining petroleum and coal tar distillates - Google Patents
Process for refining petroleum and coal tar distillatesInfo
- Publication number
- GB710972A GB710972A GB2974251A GB2974251A GB710972A GB 710972 A GB710972 A GB 710972A GB 2974251 A GB2974251 A GB 2974251A GB 2974251 A GB2974251 A GB 2974251A GB 710972 A GB710972 A GB 710972A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- amino
- carbon atoms
- mercaptans
- hydroxy
- 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/06—Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Petroleum and coal tar distillates, such as benzene, which are substantially free from unsaturated hydrocarbons but contain both mercaptans and other organic sulphur compounds, are refined, first by extraction with aqueous alkali metal hydroxide solution in presence of a solutizer to remove the mercaptans, and then by treatment with sulphuric acid, oleum or a sulphonic acid, followed by removal of the acid. The refined distillates may further be washed with water and, if desired, with a small quantity of dilute aqueous alkali solution, but redistillation is unnecessary. When the crude distillate contains hydrogen sulphide, this may be removed by a preliminary wash with a small amount of dilute alkali metal hydroxide solution. Examples of solutizers are amino- and hydroxy-alkyl amines in which the alkyl groups contain 2-3 carbon atoms, glycols, amino-glycols and diamino-alcohols with 3-5 carbon atoms, diamino-, dihydroxy- or amino-hydroxy-dialkyl ethers or thioethers in which the alkyl groups have 2-3 carbon atoms, alkali (particularly potassium) salts of fatty acids (e.g. isobutyric acid) with 3-5 carbon-atoms or of hydroxy- or amino-fatty acids with 4-7 carbon atoms, or of phenyl acetic acid or hydroxy- or amino-phenyl acetic acids, or of alkyl phenols, or mixtures of two or more of the said compounds. Sulphonic acids mentioned are the lower alkyl (e.g. methyl, ethyl, propyl and isopropyl) sulphonic acids. In an example, extraction with aqueous caustic potash containing potassium cresolate and potassium picramate is followed by treatment with sulphuric acid.ALSO:Petroleum and coal tar distillates, which are substantially free from unsaturated hydrocarbons but contain both mercaptans and other organic sulphur compounds, are refined, first by extraction with aqueous alkali metal hydroxide solution in presence of a solutizer to remove the mercaptans, and then by treatment with sulphuric acid, oleum or a sulphonic acid, followed by removal of the acid. The refined distillates may further be washed with water and, if desired, with a small quantity of dilute aqueous alkali solution, but redistillation is unnecessary. When the crude distillate contains hydrogen sulphide, this may be removed by a preliminary wash with a small amount of dilute alkali metal hydroxide solution. Distillates mentioned are gasoline, kerosene and hydrogenation gasoline. Examples of solutizers are amino- and hydroxy-alkyl amines in which the alkyl groups contain 2-3 carbon atoms, glycols, amino-glycols and diamino-alcohols with 3-5 carbon atoms, diamino-, dihydroxy- or aminohydroxy-dialkyl ethers or thioethers in which the alkyl groups have 2-3 carbon atoms, alkali (particularly potassium) salts of fatty acids (e.g. isobutyric acid) with 3-5 carbon atoms or of hydroxy- or amino-fatty acids with 4-7 carbon atoms, or of phenyl acetic acid or hydroxy- or amino-phenyl acetic acids, or of alkyl phenols, or mixtures of two or more of the said compounds. Sulphonic acids mentioned are the lower alkyl (e.g. methyl, ethyl, propyl and isopropyl) sulphonic acids. The aqueous alkali metal hydroxide solution, which has been employed in extracting mercaptans according to the invention, may be regenerated for further use. Regeneration may be carried out by removing the absorbed mercaptans from the solution, for example with the aid of steam, or by oxidizing the mercaptans with an oxidant, such as air or another oxygen-containing gas, and separating the oxidation products or extracting the oxidation products with a hydrocarbon oil such as gasoline or kerosine. The oxidation of the mercaptans with an oxidant may be carried out in the presence of an oxidation catalyst, such as hydroxy- and aminophenols which may contain other substituents, for instance one or more carboxyl groups or nitro groups. Tannic acid, tannin and picramic acid are particularly suitable. In an example, straight run gasoline is extracted with aqueous caustic potash containing potassium cresolate and potassium picramate and then treated with sulphuric acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2974251A GB710972A (en) | 1951-12-19 | 1951-12-19 | Process for refining petroleum and coal tar distillates |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2974251A GB710972A (en) | 1951-12-19 | 1951-12-19 | Process for refining petroleum and coal tar distillates |
Publications (1)
Publication Number | Publication Date |
---|---|
GB710972A true GB710972A (en) | 1954-06-23 |
Family
ID=10296434
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2974251A Expired GB710972A (en) | 1951-12-19 | 1951-12-19 | Process for refining petroleum and coal tar distillates |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB710972A (en) |
-
1951
- 1951-12-19 GB GB2974251A patent/GB710972A/en not_active Expired
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