ES206563A2 - Combination crude distillation and oil refining process - Google Patents
Combination crude distillation and oil refining processInfo
- Publication number
- ES206563A2 ES206563A2 ES0206563A ES206563A ES206563A2 ES 206563 A2 ES206563 A2 ES 206563A2 ES 0206563 A ES0206563 A ES 0206563A ES 206563 A ES206563 A ES 206563A ES 206563 A2 ES206563 A2 ES 206563A2
- Authority
- ES
- Spain
- Prior art keywords
- fraction
- fractionator
- crude
- crude oil
- decayed
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
Abstract
Improvement or modification of the combined process of distillation and conversion to refine petroleum oils to obtain high quality petroleum products that boil in the range of engine fuel described and claimed in our patent no. 197,062, according to which the quantity of the products subjected to cracking of the craking stage fed to the fractionation zone and therefore the quantity of the fraction of diesel coming from said fractionator fed to the cracking zone are expressed by the equation ** (see formula) ** where f is the total feed to the cracking stage expressed as% volume on the distilled material of the fraction of crude oil decapitated or reduced in the fractionation zone: t is the cut-off point of the initial temperature inºf. Of the fraction of crude or decayed crude oil charged to the fractionator on the basis of the true boiling point; the conversion of distilled material to the fraction of crude or decayed crude oil in the fractionator defined as 100 less than the final yield of cycle diesel boiling above 221ºc. (actual boiling point) in% volumes or distilled material from the fraction of crude or decayed crude oil in the fractionator. (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US259654A US2777801A (en) | 1951-12-03 | 1951-12-03 | Combination crude distillation and oil refining process |
Publications (1)
Publication Number | Publication Date |
---|---|
ES206563A2 true ES206563A2 (en) | 1954-04-16 |
Family
ID=22985816
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES0206563A Expired ES206563A2 (en) | 1951-12-03 | 1952-12-01 | Combination crude distillation and oil refining process |
Country Status (2)
Country | Link |
---|---|
US (1) | US2777801A (en) |
ES (1) | ES206563A2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2935462A (en) * | 1954-08-02 | 1960-05-03 | Exxon Research Engineering Co | Selective segregation of hydrocarbon constituents in a combination crude distillation process |
US2950241A (en) * | 1957-12-09 | 1960-08-23 | Exxon Research Engineering Co | Combination crude distillation and olefin production process |
US3159565A (en) * | 1961-09-26 | 1964-12-01 | Exxon Research Engineering Co | Hydrocarbon conversion process to obtain gasoline with the use of a single distillation zone |
GB1050558A (en) * | 1964-09-04 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2174858A (en) * | 1937-07-22 | 1939-10-03 | Gasoline Prod Co Inc | Process of treating hydrocarbon oil |
US2294126A (en) * | 1938-09-12 | 1942-08-25 | Ernest A Ocon | Method of treating a plurality of hydrocarbon oils for subsequent cracking |
US2378542A (en) * | 1941-08-30 | 1945-06-19 | Standard Oil Co | Method and apparatus for catalytic processes |
-
1951
- 1951-12-03 US US259654A patent/US2777801A/en not_active Expired - Lifetime
-
1952
- 1952-12-01 ES ES0206563A patent/ES206563A2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US2777801A (en) | 1957-01-15 |
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