GB1513267A - Ammonia synthesis - Google Patents
Ammonia synthesisInfo
- Publication number
- GB1513267A GB1513267A GB46946/75A GB4694675A GB1513267A GB 1513267 A GB1513267 A GB 1513267A GB 46946/75 A GB46946/75 A GB 46946/75A GB 4694675 A GB4694675 A GB 4694675A GB 1513267 A GB1513267 A GB 1513267A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mixture
- scrubbing
- hydrogen
- carbon monoxide
- zone
- 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
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title abstract 16
- 229910021529 ammonia Inorganic materials 0.000 title abstract 8
- 230000015572 biosynthetic process Effects 0.000 title abstract 8
- 238000003786 synthesis reaction Methods 0.000 title abstract 8
- 239000000203 mixture Substances 0.000 abstract 17
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 10
- 238000005201 scrubbing Methods 0.000 abstract 10
- 238000006243 chemical reaction Methods 0.000 abstract 9
- 239000007789 gas Substances 0.000 abstract 9
- 239000001257 hydrogen Substances 0.000 abstract 8
- 229910052739 hydrogen Inorganic materials 0.000 abstract 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 7
- 239000000243 solution Substances 0.000 abstract 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 6
- 239000003054 catalyst Substances 0.000 abstract 4
- 230000003197 catalytic effect Effects 0.000 abstract 4
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 3
- 239000001569 carbon dioxide Substances 0.000 abstract 3
- 238000010926 purge Methods 0.000 abstract 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- 238000010521 absorption reaction Methods 0.000 abstract 2
- 239000007864 aqueous solution Substances 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 abstract 2
- 230000008929 regeneration Effects 0.000 abstract 2
- 238000011069 regeneration method Methods 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 230000002745 absorbent Effects 0.000 abstract 1
- 239000002250 absorbent Substances 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000008246 gaseous mixture Substances 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 abstract 1
- 229910000027 potassium carbonate Inorganic materials 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 239000007858 starting material Substances 0.000 abstract 1
- 239000000126 substance 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
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/56—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids
- C01B3/58—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids including a catalytic reaction
- C01B3/586—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids including a catalytic reaction the reaction being a methanation reaction
-
- 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
- C01B3/025—Preparation or purification of gas mixtures for ammonia synthesis
-
- 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
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
- C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
-
- 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
- C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
-
- 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
- C01B2203/0415—Purification by absorption in liquids
-
- 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
- C01B2203/0435—Catalytic purification
- C01B2203/0445—Selective methanation
-
- 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
- C01B2203/047—Composition of the impurity the impurity being carbon monoxide
-
- 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
- C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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)
- Gas Separation By Absorption (AREA)
- Industrial Gases (AREA)
Abstract
1513267 Ammonia synthesis BENFIELD CORP 13 Nov 1975 46946/75 Heading C1A In the synthesis of ammonia from a hydrocarbon starting material involving the steps of generating under superatmospheric pressure a mixture comprising carbon monoxide and hydrogen from said hydrocarbon, converting the carbon monoxide in said mixture to hydrogen and CO 2 by reaction with water through catalytic shift conversion, removing said CO 2 from said mixture by absorption in a liquid scrubbing medium which is regenerated by steam-stripping, converting residual CO and CO 2 to methane by reaction with hydrogen contained in said mixture over a methanation catalyst, compressing the gaseous mixture so produced together with nitrogen contained in or added to said mixture in the molar ratio required for ammonia synthesis, passing said compressed mixture over an ammonia synthesis catalyst, recycling unconverted synthesis gas to the ammonia synthesis catalyst, and purging sufficient gas from the recycle stream to maintain a desired concentration of methane and other inerts in such stream, hydrogen losses in the methanation step and hydrogen and ammonia losses in the purge step are minimized while at the same time minimizing the steam required by such CO 2 removal and CO shift conversion steps which comprise the steps of: (a) converting from 90% to 99% of the carbon monoxide in said carbon monoxide-hydrogen mixture to hydrogen and CO 2 by reaction of said carbon monoxide with water in at least two successive catalytic shift conversion zones, the first of which is a high-temperature shift conversion zone and the last of which utilizes a lowtemperature shift conversion catalyst; (b) removing carbon dioxide from the mixture produced in step (a) in a first CO 2 scrubbing zone to provide a gas mixture containing not more than 2% and not less than 01% CO 2 , the CO 2 removal in said first zone being carried out by contacting said mixture with a scrubbing solution comprising an aqueous solution of potassium carbonate, wherein at least the major portion of said scrubbing is carried out at a scrubbing solution temperature in the vicinity of the atmospheric boiling temperature of said solution, and wherein the regeneration of said scrubbing solution is carried out at a reduced pressure in the vicinity of atmospheric pressure by steam-stripping thereof, whereby the bulk of said CO 2 is removed with a minimum consumption of stripping steam; (c) subjecting the gas mixture produced in step (b) to low-temperature catalytic shift conversion to convert residual carbon monoxide to hydrogen and carbon dioxide to produce a gas stream containing not more than 0À1% residual carbon monoxide; (d) removing CO 2 from the gas mixture produced in step (c) in a second CO 2 scrubbing zone to provide a mixture containing not more than 200 ppm of residual CO 2 , on an anhydrous basis, the CO 2 removal in said second zone being carried out by contacting said gas mixture with a scrubbing solution comprising an aqueous solution of an alkaline chemical absorbent wherein said scrubbing is carried out at an absorption temperature substantially below the atmospheric boiling temperature of the solution, permitting the reduction of residual CO 2 in said mixture to a low level and wherein the regeneration of such scrubbing solution is carried out by steam-stripping thereof; (e) converting the residual carbon monoxide and carbon dioxide in the gas mixture from step (d) to methane in a catalytic methanation zone, and thereafter introducing said gas mixture into an ammonia synthesis loop including a purge for preventing the buildup of inert gases in said loop.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB46946/75A GB1513267A (en) | 1975-11-13 | 1975-11-13 | Ammonia synthesis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB46946/75A GB1513267A (en) | 1975-11-13 | 1975-11-13 | Ammonia synthesis |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1513267A true GB1513267A (en) | 1978-06-07 |
Family
ID=10443170
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB46946/75A Expired GB1513267A (en) | 1975-11-13 | 1975-11-13 | Ammonia synthesis |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1513267A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121775A (en) * | 1979-04-24 | 1984-01-04 | Foster Wheeler Ltd | Synthesis gas for ammonia production |
EP1174486A1 (en) * | 1999-03-05 | 2002-01-23 | Osaka Gas Co., Ltd. | System for removing carbon monoxide and method for removing carbon monoxide |
CN112520695A (en) * | 2020-12-14 | 2021-03-19 | 河南骏化发展股份有限公司 | Process for improving catalyst activity and saving steam by adjusting steam drum pressure |
-
1975
- 1975-11-13 GB GB46946/75A patent/GB1513267A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121775A (en) * | 1979-04-24 | 1984-01-04 | Foster Wheeler Ltd | Synthesis gas for ammonia production |
EP1174486A1 (en) * | 1999-03-05 | 2002-01-23 | Osaka Gas Co., Ltd. | System for removing carbon monoxide and method for removing carbon monoxide |
EP1174486A4 (en) * | 1999-03-05 | 2002-07-24 | Osaka Gas Co Ltd | System for removing carbon monoxide and method for removing carbon monoxide |
CN112520695A (en) * | 2020-12-14 | 2021-03-19 | 河南骏化发展股份有限公司 | Process for improving catalyst activity and saving steam by adjusting steam drum pressure |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
732 | Registration of transactions, instruments or events in the register (sect. 32/1977) | ||
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19921113 |