GB1199097A - Hydrocarbon Separation Process - Google Patents
Hydrocarbon Separation ProcessInfo
- Publication number
- GB1199097A GB1199097A GB47552/68A GB4755268A GB1199097A GB 1199097 A GB1199097 A GB 1199097A GB 47552/68 A GB47552/68 A GB 47552/68A GB 4755268 A GB4755268 A GB 4755268A GB 1199097 A GB1199097 A GB 1199097A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fraction
- point
- zone
- butanes
- withdrawn
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/22—Separation of effluents
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,199,097. Separating hydrocarbons. UNIVERSAL OIL PRODUCTS CO. 8 Oct., 1968 [13 Oct., 1967], No. 47552/68. Heading C5E. In a process for separating in a zone 13 a hydro-cracked effluent 11 comprising butanes and normally liquid hydrocarbons to provide an intermediate fraction 18 having a predetermined end boiling point, a light fraction 15 comprising principally butanes, pentanes, and hexanes is withdrawn from a point above the point at which the fraction 18 is withdrawn and part at least of the fraction 15 is returned to the zone 13 at 24 to a point below the point of withdrawal of fraction 18. A feedstock having a B.R. of about 38 to 566 C. is catalytically hydrogenated at (5) with recycled H 2 from a separator (9) and fed at 11, 12 to the zone 13. An example is described in which the production of a jet fuel fraction having a B.R. of about 154 to 274 C. is maximized from a blend of vacuum tar reduced crude, gas oil and light and heavy cycle oils.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US67508967A | 1967-10-13 | 1967-10-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1199097A true GB1199097A (en) | 1970-07-15 |
Family
ID=24709009
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB47552/68A Expired GB1199097A (en) | 1967-10-13 | 1968-10-08 | Hydrocarbon Separation Process |
Country Status (8)
Country | Link |
---|---|
US (1) | US3455814A (en) |
JP (1) | JPS4933562B1 (en) |
BR (1) | BR6803038D0 (en) |
DE (1) | DE1802396A1 (en) |
ES (1) | ES359106A1 (en) |
FR (1) | FR1589035A (en) |
GB (1) | GB1199097A (en) |
NL (1) | NL158708B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2549892C1 (en) * | 2014-03-26 | 2015-05-10 | Открытое акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (ОАО "ВНИИ НП") | Method for producing rocketry hydrocarbon fuel |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3809157A1 (en) * | 1988-03-18 | 1989-09-28 | Schako Metallwarenfabrik | CEILING OUTLET |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2072456A (en) * | 1934-12-01 | 1937-03-02 | Gasoline Prod Co Inc | Process for the stabilization of hydrocarbon distillate |
US2952631A (en) * | 1957-11-26 | 1960-09-13 | Shell Oil Co | Distillation of lubricating oil |
US2995499A (en) * | 1958-12-11 | 1961-08-08 | Maloney Crawford Tank And Mfg | Apparatus for fractional distillation of multiple component mixtures |
US3368966A (en) * | 1966-12-27 | 1968-02-13 | Universal Oil Prod Co | Control of isobutane fractionating column |
-
1967
- 1967-10-13 US US675089A patent/US3455814A/en not_active Expired - Lifetime
-
1968
- 1968-10-08 GB GB47552/68A patent/GB1199097A/en not_active Expired
- 1968-10-10 NL NL6814497.A patent/NL158708B/en not_active IP Right Cessation
- 1968-10-10 DE DE19681802396 patent/DE1802396A1/en not_active Withdrawn
- 1968-10-11 ES ES359106A patent/ES359106A1/en not_active Expired
- 1968-10-11 BR BR203038/68A patent/BR6803038D0/en unknown
- 1968-10-11 FR FR1589035D patent/FR1589035A/fr not_active Expired
- 1968-10-14 JP JP43074288A patent/JPS4933562B1/ja active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2549892C1 (en) * | 2014-03-26 | 2015-05-10 | Открытое акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (ОАО "ВНИИ НП") | Method for producing rocketry hydrocarbon fuel |
Also Published As
Publication number | Publication date |
---|---|
FR1589035A (en) | 1970-03-16 |
DE1802396A1 (en) | 1969-05-29 |
US3455814A (en) | 1969-07-15 |
NL158708B (en) | 1978-12-15 |
BR6803038D0 (en) | 1973-01-04 |
NL6814497A (en) | 1969-04-15 |
ES359106A1 (en) | 1970-05-16 |
JPS4933562B1 (en) | 1974-09-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |