GB1137065A - Improvements in or relating to the manufacture of ammonia - Google Patents
Improvements in or relating to the manufacture of ammoniaInfo
- Publication number
- GB1137065A GB1137065A GB3414/65A GB341465A GB1137065A GB 1137065 A GB1137065 A GB 1137065A GB 3414/65 A GB3414/65 A GB 3414/65A GB 341465 A GB341465 A GB 341465A GB 1137065 A GB1137065 A GB 1137065A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- mixture
- converter
- ammonia
- proportion
- 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
- 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
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0476—Purge gas treatment, e.g. for removal of inert gases or recovery of H2
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,137,065. Ammonia. HUMPHREYS & GLASGOW Ltd. 18 Jan., 1966 [26 Jan., 1965; 9 April, 19651, Nos. 3414/65 and 15275/65. Heading C1A. [Also in Division B1] In the catalytic synthesis of NH 3 , the mixture of H 2 and N 2 is partially purified from inert gaseous components such as CH 4 and argon by dissolving at least part of the mixture under pressure in liquid ammonia, additional NH 3 being introduced for this purpose, and thereafter cooling the liquid NH 3 so as to release a proportion of the dissolved gases for use in the synthesis reaction whereby the proportion of the inert impurities in the H 2 /N 2 mixture is reduced. Preferably after the liquid NH 3 is cooled it is subjected to a reduction of pressure to release a further proportion of dissolved gases from solution. The liquid ammonia used for dissolving the gaseous mixture may be at a temperature of 65-74‹ C. Preferably the H 2 /N 2 mixture is derived in part from the gases leaving the converter and is washed under pressure with liquid NH 3 drawn from the product of the converter in an absorber. The gases released from solution in liquid NH 3 may be subjected to a second washing with liquid NH 3 and then recycled to the converter. The liquid NH 3 when freed of dissolved gases may be returned to the product stream before the initial separation of the liquid and gaseous components and before the heat exchangers for cooling the converter product.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3414/65A GB1137065A (en) | 1965-01-26 | 1965-01-26 | Improvements in or relating to the manufacture of ammonia |
NL6600954A NL6600954A (en) | 1965-01-26 | 1966-01-25 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3414/65A GB1137065A (en) | 1965-01-26 | 1965-01-26 | Improvements in or relating to the manufacture of ammonia |
GB1527565 | 1965-04-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1137065A true GB1137065A (en) | 1968-12-18 |
Family
ID=26238284
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3414/65A Expired GB1137065A (en) | 1965-01-26 | 1965-01-26 | Improvements in or relating to the manufacture of ammonia |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB1137065A (en) |
NL (1) | NL6600954A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3805536A (en) * | 1970-12-16 | 1974-04-23 | Univ Cal | Removal of methane and argon from ammonia synthesis gas |
WO1981002985A1 (en) * | 1980-04-14 | 1981-10-29 | L Silberring | Method for the separation of mixture by means of exchange of materials at different temperatures or pressures |
-
1965
- 1965-01-26 GB GB3414/65A patent/GB1137065A/en not_active Expired
-
1966
- 1966-01-25 NL NL6600954A patent/NL6600954A/xx unknown
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3805536A (en) * | 1970-12-16 | 1974-04-23 | Univ Cal | Removal of methane and argon from ammonia synthesis gas |
WO1981002985A1 (en) * | 1980-04-14 | 1981-10-29 | L Silberring | Method for the separation of mixture by means of exchange of materials at different temperatures or pressures |
Also Published As
Publication number | Publication date |
---|---|
NL6600954A (en) | 1966-03-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1203103A (en) | A process for removing hydrogen sulphide and carbon dioxide from fuel gas or synthesis gas containing the same | |
GB1467027A (en) | Removal of impurities from gaseous mixtures and the regeneratio of absorbent solutions used therefor | |
GB1275140A (en) | Improvements in or relating to a process for the purification of gaseous mixtures | |
ES391122A1 (en) | Process for separating and recovering acid gases from gaseous mixtures | |
GB1185944A (en) | Process for the Synthesis of Urea | |
GB1237780A (en) | Processing offgas from the synthesis of melamine | |
GB977969A (en) | Hydrogen recovery | |
GB1306581A (en) | Process for the production of nitric acid with a concentration of over 70percent by weight | |
GB1137065A (en) | Improvements in or relating to the manufacture of ammonia | |
GB1239957A (en) | Process for the separation of acrylonitrile and acetonitrile | |
GB1288309A (en) | ||
GB1259945A (en) | Methanol production | |
GB1392337A (en) | Process for the production of hydroxylamino-and aminoanthra- quinones | |
GB1240499A (en) | Separating ammonia from offgas obtained in the synthesis of melamine | |
GB952335A (en) | Process for the production of deuterium enriched ammonia | |
ES386315A1 (en) | Process for separating off melamine from a hot synthesis gas mixture which contains melamine vapor | |
GB1003277A (en) | Process and apparatus for the production and separation of melamine | |
ES260137A1 (en) | Acrylonitrile recovery process | |
GB1175774A (en) | Process for the Preparation of Sulphur Hexafluoride | |
GB1198955A (en) | Process for the Production of Oxalic Acid | |
ES400511A1 (en) | Recovery of hydrogen fluoride | |
GB1129939A (en) | Process for the separation and recovery of ammonia and carbon dioxide from an ammoniacal ammonium carbonate solution | |
GB1140339A (en) | Treatment of gases | |
ES298518A1 (en) | A continuous procedure to separate urea from a contaminated urea solution with biuret (Machine-translation by Google Translate, not legally binding) | |
GB1158195A (en) | Process for obtaining a Low Biuret Urea |