GB1310176A - Hydrogenation of hydrocarbons and reactor therefore - Google Patents
Hydrogenation of hydrocarbons and reactor thereforeInfo
- Publication number
- GB1310176A GB1310176A GB1310176DA GB1310176A GB 1310176 A GB1310176 A GB 1310176A GB 1310176D A GB1310176D A GB 1310176DA GB 1310176 A GB1310176 A GB 1310176A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- catalyst
- reaction vessel
- hydrocarbons
- reactor
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/14—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles
- C10G45/16—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles suspended in the oil, e.g. slurries
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1310176 Catalytic hydrogenation reactor; liquid/gas separation HYDROCARBON RESEARCH Inc 19 June 1970 29967/70 Headings B1F and B1M A process for liquid phase hydrogenation of hydrocarbons with improved separation of gas and liquid products comprises passing the hydrocarbons together with hydrogen upwardly through a mass of particulate catalyst in reactor 2 under conditions of high temperature and pressure such that a continuous liquid phase exists in the reaction vessel and at a velocity such as to bring the catalyst into an abullated state in the liquid phase in the reaction vessel an interface 12 between an upper zone in which the catalyst density is relatively low and a lower zone in which the catalyst density is relatively high and such that the catalyst is retained in the reaction vessel, separately removing vapourous and liquid effluents from the reaction vessel, and passing the liquid across baffles 4 after the liquid has passed through the zone of relatively high catalyst density but prior to separation of the vapourous and liquid effluents, the baffles 4 being of a metal resistant to the reaction conditions and inert to the reaction taking place.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2996770 | 1970-06-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1310176A true GB1310176A (en) | 1973-03-14 |
Family
ID=10300115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1310176D Expired GB1310176A (en) | 1970-06-19 | 1970-06-19 | Hydrogenation of hydrocarbons and reactor therefore |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1310176A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108554323A (en) * | 2018-06-28 | 2018-09-21 | 钦州学院 | Duct type liquid-phase catalysis reaction unit |
-
1970
- 1970-06-19 GB GB1310176D patent/GB1310176A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108554323A (en) * | 2018-06-28 | 2018-09-21 | 钦州学院 | Duct type liquid-phase catalysis reaction unit |
| CN108554323B (en) * | 2018-06-28 | 2024-05-28 | 钦州学院 | Pipeline type liquid phase catalytic reaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed | ||
| PLNP | Patent lapsed through nonpayment of renewal fees |