GB1204201A - Hydrocarbon conversion method - Google Patents
Hydrocarbon conversion methodInfo
- Publication number
- GB1204201A GB1204201A GB3398/68A GB339868A GB1204201A GB 1204201 A GB1204201 A GB 1204201A GB 3398/68 A GB3398/68 A GB 3398/68A GB 339868 A GB339868 A GB 339868A GB 1204201 A GB1204201 A GB 1204201A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction zone
- hydrogen
- hydrocarbons
- effluent
- refined
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
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)
Abstract
1,204,201. Hydrofining. UNIVERSAL OIL PRODUCTS CO. 23 Jan., 1968 [25 Jan., 1967], No. 3398/68. Heading C5E. A process for hydrorefining a full-boiling range hydrocarbon feedstock comprising a naphtha fraction and at least one contaminant selected from sulfurous compounds and nitrogenous compounds comprises: (a) reacting said feedstock with hydrogen in a first reaction zone containing hydrorefining catalyst; (b) separating the entire effluent from said first reaction zone in a first separation zone to provide a first gaseous phase comprising hydrogen and relatively light hydrocarbons, and a liquid phase comprising relatively heavy refined hydrocarbons; (c) reacting said first gaseous phase in the absence of added hydrogen in a second reaction zone maintained at a temperature lower than that at which said first reaction zone is maintained and containing hydrorefining catalyst; (d) withdrawing from said second reaction zone an effluent comprising hydrogen and relatively light, refined hydrocarbons; and (e) separating said second reaction zone effluent to provide a hydrogen-rich second gaseous stream and a refined, light hydrocarbon stream; and (f) recovering resulting refined hydrocarbons. In optional modifications, the second gaseous stream may be recycled to the first reaction stage; and the liquid phases from both zones may be combined.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US61159367A | 1967-01-25 | 1967-01-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1204201A true GB1204201A (en) | 1970-09-03 |
Family
ID=24449641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB3398/68A Expired GB1204201A (en) | 1967-01-25 | 1968-01-23 | Hydrocarbon conversion method |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US3481864A (en) |
| JP (1) | JPS4818081B1 (en) |
| DE (1) | DE1645830C3 (en) |
| ES (1) | ES349701A1 (en) |
| FR (1) | FR1560525A (en) |
| GB (1) | GB1204201A (en) |
| NL (1) | NL158839B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3668112A (en) * | 1968-12-06 | 1972-06-06 | Texaco Inc | Hydrodesulfurization process |
| US3969222A (en) * | 1974-02-15 | 1976-07-13 | Universal Oil Products Company | Hydrogenation and hydrodesulfurization of hydrocarbon distillate with a catalytic composite |
| JPS50117390A (en) * | 1974-02-18 | 1975-09-13 |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA612265A (en) * | 1961-01-10 | Sun Oil Company | Desulfurization of reformer charge | |
| US3119765A (en) * | 1959-10-19 | 1964-01-28 | Exxon Research Engineering Co | Catalytic treatment of crude oils |
| NL144659B (en) * | 1964-04-28 | 1975-01-15 | Shell Int Research | PROCESS FOR THE PREPARATION OF A KEROSINE WITH AN INCREASED SOOT POINT. |
-
1967
- 1967-01-25 US US611593A patent/US3481864A/en not_active Expired - Lifetime
-
1968
- 1968-01-23 GB GB3398/68A patent/GB1204201A/en not_active Expired
- 1968-01-24 DE DE1645830A patent/DE1645830C3/en not_active Expired
- 1968-01-24 ES ES349701A patent/ES349701A1/en not_active Expired
- 1968-01-24 JP JP43003844A patent/JPS4818081B1/ja active Pending
- 1968-01-25 NL NL6801126.A patent/NL158839B/en not_active IP Right Cessation
- 1968-01-25 FR FR1560525D patent/FR1560525A/fr not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE1645830B2 (en) | 1974-01-17 |
| NL158839B (en) | 1978-12-15 |
| ES349701A1 (en) | 1969-04-01 |
| US3481864A (en) | 1969-12-02 |
| DE1645830C3 (en) | 1974-08-15 |
| JPS4818081B1 (en) | 1973-06-04 |
| NL6801126A (en) | 1968-07-26 |
| FR1560525A (en) | 1969-03-21 |
| DE1645830A1 (en) | 1970-07-16 |
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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 |