GB462630A - A process of refining hydrocarbon oils - Google Patents
A process of refining hydrocarbon oilsInfo
- Publication number
- GB462630A GB462630A GB8031/36A GB803136A GB462630A GB 462630 A GB462630 A GB 462630A GB 8031/36 A GB8031/36 A GB 8031/36A GB 803136 A GB803136 A GB 803136A GB 462630 A GB462630 A GB 462630A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solvent
- top product
- hydrocarbon
- fractions
- hydrocarbons
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/40—Extractive distillation
-
- 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
- C10G17/09—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acid salts
-
- 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
- C10G7/00—Distillation of hydrocarbon oils
- C10G7/08—Azeotropic or extractive distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Hydrocarbon fractions containing sulphur are rectified together with a selective solvent in a distillation zone, hydrocarbon fraction and solvent being continuously introduced, and a top product containing solvent and refined hydrocarbons and a bottom product containing the bulk of the sulphur compounds with or without solvent and hydrocarbons being continuously withdrawn. The hydrocarbon fractions may be gasoline, kerosene, naphthas, solar oils, and fuel oils, which may be either straight-run or cracked distillates, and may be derived from petroleum crudes, fractions of coal tar or brown coal tar, and mixtures obtained by the hydrogenation of carbonaceous substances. The solvent used must form one phase with the hydrocarbon fraction at the boiling temperature and have a boiling point low enough to cause a mixture of the said solvent and the highest boiling hydrocarbon in the fraction to boil at a lower temperature than the lowest boiling sulphur compound to be removed. The solvent may have a boiling point not substantially above the lower limit of the boiling range of the hydrocarbon fraction under treatment. There may be used as solvents organic compounds, either aliphatic, carbocyclic, or heterocyclic, containing one or more nitro, nitrile, thiocyanic, carboxyl, primary secondary or tertiary alcoholic, monochlor, amino, thiocarbonyl, carboxyl, or alkyl or aryl ether or ester groups. Examples are nitrobenzene, benzonitrile, monochloracetonitrile, phenyl-thiocyanate, phenolthiocyanate, formate of pyridine, benzaldehyde, acetone, furfuryl alcohol, chlorisopropyl alcohol, diacetone alcohol, methyl lactate, triacetin, di-acetin, methyl nitrobenzoate, formic acid, ethylene chlorhydrin, glycol monoacetate, glycol diacetate, lactic nitrile, toluidine, chlorpyridine, b b <1>-dichlordiethyl ether, chloraniline, quinoline, isoquinoline, pyridine, chlorphenol, sulphur dioxide, or preferably furfural, aniline methyl cyanide, ethylene diamine, nitromethane, or acetic anhydride, including isomers. It is preferable to fractionate in such a manner that the ratio of total hydrocarbons to the solvent in the rectified mixture withdrawn as a top product is maintained equal to the ratio thereof in the feed. This may be effected according to either of the following modes of operation: (a) the overhead mixture, or a portion thereof, is treated to withdraw therefrom a top product containing the solvent and the hydrocarbons in the same ratio as they occur in the feed, and the remaining portion of the overhead mixture is returned to the column; the top product may be withdrawn by chilling the portion of the overhead which is to be treated so as to cause it to separate into two liquid phases, or by adding water or another substance, e.g. methyl alcohol, to the overhead mixture or to the condensate, separating these phases, and withdrawing therefrom such quantities as are required to produce a top product of the desired composition; (b) the ratio of the solvent and the initial sulphur-bearing hydrocarbon fraction is so controlled as to produce a feed composition which contains the solvent and the hydrocarbons in the same ratio as they occur in the overhead mixture, which is then withdrawn as a top product. If it be impossible to keep the said ratios equal, it is preferable that the ratio of hydrocarbon to solvent be greater in the top product than in the feed. The initial hydrocarbon fraction may be first fractionated, preferably into fractions having a boiling point range of not more than 80 DEG C., and one or more of the fractions separately treated by the above process with or without the feature of adjusting the feed and top product compositions, e.g. those fractions difficult to de-sulphurize by ordinary methods may be so treated. The process is illustrated by a flow diagram (not shown). Specifications 324,350, [Class 2 (iii)], and 365,571 are referred to. The Specification as open to inspection under Sect. 91 refers also to batch processes. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12008A US2069329A (en) | 1935-03-20 | 1935-03-20 | Process of refining oils |
US95385A US2114852A (en) | 1935-03-20 | 1936-08-11 | Process for desulphurizing mineral oil distillates |
Publications (1)
Publication Number | Publication Date |
---|---|
GB462630A true GB462630A (en) | 1937-03-12 |
Family
ID=26683040
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8031/36A Expired GB462630A (en) | 1935-03-20 | 1936-03-17 | A process of refining hydrocarbon oils |
Country Status (4)
Country | Link |
---|---|
US (2) | US2069329A (en) |
FR (2) | FR804488A (en) |
GB (1) | GB462630A (en) |
NL (1) | NL43587C (en) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE747402C (en) * | 1941-09-26 | 1944-09-27 | Edeleanu Gmbh | Process for the production of oil-free paraffin from tars or tar distillates |
US2428611A (en) * | 1941-11-17 | 1947-10-07 | Union Oil Co | Recovery of azeotrope former in azeotropic distillation of hydrocarbons |
US2433751A (en) * | 1943-09-30 | 1947-12-30 | Universal Oil Prod Co | Separation of organic compounds |
US2422341A (en) * | 1944-12-26 | 1947-06-17 | Phillips Petroleum Co | Solvent extraction |
US2636883A (en) * | 1945-01-31 | 1953-04-28 | Union Oil Co | Thienyl ketones |
US2522752A (en) * | 1945-02-17 | 1950-09-19 | Union Oil Co | Thiophene acylation with catalyst of sulfuric acid-carboxylic acid complex |
US2427988A (en) * | 1945-04-24 | 1947-09-23 | Carnegie Illinois Steel Corp | Process for removing sulphur compounds from hydrocarbons |
US2567174A (en) * | 1949-01-24 | 1951-09-11 | Standard Oil Dev Co | Process for improving stability and engine cleanliness characteristics of petroleum fractions |
US2662843A (en) * | 1951-05-25 | 1953-12-15 | Shell Dev | Shale oil refining |
US2666794A (en) * | 1951-06-08 | 1954-01-19 | Phillips Petroleum Co | Desulfurization of hydrocarbons by extraction with phenylacetonitrile |
US2671047A (en) * | 1951-09-29 | 1954-03-02 | Standard Oil Co | Refining hydrocarbon materials with so2 and bf3 |
US2698278A (en) * | 1952-06-20 | 1954-12-28 | Socony Vacuum Oil Co Inc | Solvent extraction |
US2813918A (en) * | 1953-06-05 | 1957-11-19 | Phillips Petroleum Co | Solvent extraction with the operation of the uppermost portion of the extractor as a vapor liquid fractionation zone |
US2852436A (en) * | 1955-03-28 | 1958-09-16 | Gulf Research Development Co | Process for removal of elemental sulfur from crude petroleum oils with an aliphatic diamine and an adsorbent |
DE1117249B (en) * | 1959-03-13 | 1961-11-16 | Dr Georg Kowalski | Process for the extraction of mineral oils by treatment with nitriles |
FR1302375A (en) * | 1960-10-05 | 1962-08-31 | Houilleres Bassin Du Nord | Aromatic hydrocarbon refining process |
NL276254A (en) * | 1961-03-25 | |||
US3205164A (en) * | 1962-09-24 | 1965-09-07 | Universal Oil Prod Co | Hydrogen sulfide removal |
US3424673A (en) * | 1966-03-07 | 1969-01-28 | Sun Oil Co | Process for hydrodesulfurizing the lower boiling fraction of a cracked gas oil blend |
US3919402A (en) * | 1973-08-06 | 1975-11-11 | Kvb Inc | Petroleum oil desulfurization process |
US3957625A (en) * | 1975-02-07 | 1976-05-18 | Mobil Oil Corporation | Method for reducing the sulfur level of gasoline product |
US4485007A (en) * | 1982-06-15 | 1984-11-27 | Environmental Research And Technology Inc. | Process for purifying hydrocarbonaceous oils |
US4455221A (en) * | 1983-02-09 | 1984-06-19 | Intevep | Process for upgrading heavy hydrocarbons employing a diluent |
DE3602240A1 (en) * | 1986-01-25 | 1987-07-30 | Krupp Koppers Gmbh | METHOD FOR SEPARATING AROMATES FROM HYDROCARBON MIXTURES OF ANY AROMATE CONTENT |
GB8602320D0 (en) * | 1986-01-30 | 1986-03-05 | British Petroleum Co | Removing hydrogen sulphide from crude oil |
US5599441A (en) * | 1995-05-31 | 1997-02-04 | Mobil Oil Corporation | Alkylation process for desulfurization of gasoline |
US6802959B1 (en) * | 2000-06-23 | 2004-10-12 | Conocophillips Company | Separation of olefinic hydrocarbons from sulfur-containing hydrocarbons by use of a solvent |
ES2652032T3 (en) | 2011-07-29 | 2018-01-31 | Saudi Arabian Oil Company | Selective hydrotreatment procedure of medium distillates |
CN103965078B (en) * | 2014-05-05 | 2015-07-29 | 大连理工大学 | A kind of method of removal phenol carbolic oil cyanobenzene and clean fuel |
-
1935
- 1935-03-20 US US12008A patent/US2069329A/en not_active Expired - Lifetime
-
1936
- 1936-03-17 GB GB8031/36A patent/GB462630A/en not_active Expired
- 1936-03-19 NL NL77051A patent/NL43587C/xx active
- 1936-03-20 FR FR804488D patent/FR804488A/en not_active Expired
- 1936-08-11 US US95385A patent/US2114852A/en not_active Expired - Lifetime
-
1937
- 1937-07-09 FR FR824157D patent/FR824157A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US2114852A (en) | 1938-04-19 |
FR804488A (en) | 1936-10-24 |
US2069329A (en) | 1937-02-02 |
FR824157A (en) | 1938-02-02 |
NL43587C (en) | 1938-07-15 |
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