GB739145A - Improvements in or relating to process and apparatus for recovery of ammonia from anammonia containing gas - Google Patents
Improvements in or relating to process and apparatus for recovery of ammonia from anammonia containing gasInfo
- Publication number
- GB739145A GB739145A GB31739/53A GB3173953A GB739145A GB 739145 A GB739145 A GB 739145A GB 31739/53 A GB31739/53 A GB 31739/53A GB 3173953 A GB3173953 A GB 3173953A GB 739145 A GB739145 A GB 739145A
- Authority
- GB
- United Kingdom
- Prior art keywords
- crystallizer
- absorber
- separator
- outlet
- pipe
- 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
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/24—Sulfates of ammonium
- C01C1/242—Preparation from ammonia and sulfuric acid or sulfur trioxide
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Gas Separation By Absorption (AREA)
Abstract
Apparatus for absorbing ammonia from coke oven gas in sulphuric acid and crystallizing ammonium sulphate comprises a crystallizer A, an absorber B, a mist precipitator C and a vacuum evaporator D all arranged about a <PICT:0739145/III/1> <PICT:0739145/III/2> common vertical axis. The absorber which surrounds the crystallizer has a gas inlet 22 and outlet 24 and a ring of spray heads 82 communicating through short pipes 80 with the top of the crystallizer. From the absorber, gas passes through a riser E and a tangential inlet 30 into the mist separator whence it flows through a central pipe 44 to an outlet 52. A pump P1 withdraws liquid collecting at the base of the absorber and from the evaporator through a pipe 58, returning it to the crystallizer from beneath and through a perforated deflector 70, whence it rises as a desupersaturated solution to an outlet 62 and thence past a throttling valve 65 to the evaporator. Supersaturation follows and on return to the crystallizer the current in rising clarifies the crystals, a slurry of the larger sizes being withdrawn through a suction head 76. Make-up acid is admitted through a pipe 95 into a tar skimmer 94 to which overflow from the absorber is directed through a pipe 90. Surplus liquid collecting in a tank 86 is drawn on to supply a spray head 106 in riser E. In one modification the absorber is disposed round the lower part of the mist separator and above the crystallizer; in another it extends below and surrounds the base of the crystallizer and the spray heads are downwardly inclined to direct liquid from an annular manifold on to the vessel walls. In a third embodiment the separator and evaporator are omitted but a centrifugal separator may be inserted in the outlet line. A further construction provides a trough round the separator outlet 44 with a pipe leading the moisture to the floor whence it drains to the absorber. Another arrangement locates the separator between the crystallizer situated above it and the absorber which surrounds its lower end.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US739145XA | 1953-02-24 | 1953-02-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB739145A true GB739145A (en) | 1955-10-26 |
Family
ID=22116548
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31739/53A Expired GB739145A (en) | 1953-02-24 | 1953-11-16 | Improvements in or relating to process and apparatus for recovery of ammonia from anammonia containing gas |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB739145A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1186839B (en) * | 1956-12-31 | 1965-02-11 | Dow Chemical Co | Continuous process for the production of ammonia and hydrocyanic acid |
US20180338391A1 (en) * | 2017-05-22 | 2018-11-22 | Pfannenberg Gmbh | Heat exchanger for cooling an electronic enclosure |
ES2958059A1 (en) * | 2022-07-01 | 2024-01-31 | Tkin Orma S L | EQUIPMENT THAT INCLUDES A VACUUM EVAPORATOR, AND A PROCESS TO RECOVER NITROGENATED NUTRIENTS AND WATER FROM WASTE FROM AGRIBUSINESS (Machine-translation by Google Translate, not legally binding) |
-
1953
- 1953-11-16 GB GB31739/53A patent/GB739145A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1186839B (en) * | 1956-12-31 | 1965-02-11 | Dow Chemical Co | Continuous process for the production of ammonia and hydrocyanic acid |
US20180338391A1 (en) * | 2017-05-22 | 2018-11-22 | Pfannenberg Gmbh | Heat exchanger for cooling an electronic enclosure |
ES2958059A1 (en) * | 2022-07-01 | 2024-01-31 | Tkin Orma S L | EQUIPMENT THAT INCLUDES A VACUUM EVAPORATOR, AND A PROCESS TO RECOVER NITROGENATED NUTRIENTS AND WATER FROM WASTE FROM AGRIBUSINESS (Machine-translation by Google Translate, not legally binding) |
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