GB1333979A - Process for the generation of synthesis gas from oil - Google Patents
Process for the generation of synthesis gas from oilInfo
- Publication number
- GB1333979A GB1333979A GB3666871A GB1333979DA GB1333979A GB 1333979 A GB1333979 A GB 1333979A GB 3666871 A GB3666871 A GB 3666871A GB 1333979D A GB1333979D A GB 1333979DA GB 1333979 A GB1333979 A GB 1333979A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- oil
- carbon
- water
- temperature
- 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
- 230000015572 biosynthetic process Effects 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 238000003786 synthesis reaction Methods 0.000 title 1
- 239000007789 gas Substances 0.000 abstract 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 4
- 229910052799 carbon Inorganic materials 0.000 abstract 4
- 229930195733 hydrocarbon Natural products 0.000 abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 abstract 3
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 2
- 238000002485 combustion reaction Methods 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 239000002737 fuel gas Substances 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 238000005201 scrubbing Methods 0.000 abstract 1
- 239000002002 slurry Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/10—Conditioning the gas to be cleaned
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/049—Composition of the impurity the impurity being carbon
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
1333979 Purifying fuel gas TEXACO DEVELOPMENT CORP 4 Aug 1971 36668/71 Heading C5E A gas containing H 2 and CO made by the partial combustion of liquid hydrocarbons with O 2 and steam at a temperature in the range 1800 to 3200 F. is purified of entrained carbon by cooling the gas to a temperature above the dew point of contained water vapour, e.g. by indirect heat exchange at 32, and contacting the cooled gas with a liquid hydrocarbon at a temperature above the dew point of water vapour in the gas, e.g. in a Venturi 39 or nozzle or plate orifice. The gas may be scrubbed with water in a similar contactor 62 to remove oil and residual carbon. The water scrubbing step may be performed at a temperature 50 F. below that of the oil contacting step, and may be in the range 100 to 500 F., and both steps may be carried out at the same pressure. The same hydrocarbon 45 may be used for purification and gasmaking, and circuits for recycling oil and carbon slurry to the gas generator 9 and to the Venturi 39, and for delivering water, oil and carbon to steam supply 77 through a heater 76 are illustrated in the Figure.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB3666871 | 1971-08-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1333979A true GB1333979A (en) | 1973-10-17 |
Family
ID=10390194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB3666871A Expired GB1333979A (en) | 1971-08-04 | 1971-08-04 | Process for the generation of synthesis gas from oil |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1333979A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4175929A (en) * | 1978-08-29 | 1979-11-27 | The United States Of America As Represented By The United States Department Of Energy | Process for control of pollutants generated during coal gasification |
| EP0133622A2 (en) * | 1983-08-08 | 1985-03-06 | Texaco Development Corporation | Simultaneous production of clean dewatered and clean saturated streams of synthesis gas |
-
1971
- 1971-08-04 GB GB3666871A patent/GB1333979A/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4175929A (en) * | 1978-08-29 | 1979-11-27 | The United States Of America As Represented By The United States Department Of Energy | Process for control of pollutants generated during coal gasification |
| EP0133622A2 (en) * | 1983-08-08 | 1985-03-06 | Texaco Development Corporation | Simultaneous production of clean dewatered and clean saturated streams of synthesis gas |
| EP0133622A3 (en) * | 1983-08-08 | 1985-04-03 | Texaco Development Corporation | Simultaneous production of clean dewatered and clean saturated streams of synthesis gas |
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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 |