DE270192C - - Google Patents
Info
- Publication number
- DE270192C DE270192C DENDAT270192D DE270192DA DE270192C DE 270192 C DE270192 C DE 270192C DE NDAT270192 D DENDAT270192 D DE NDAT270192D DE 270192D A DE270192D A DE 270192DA DE 270192 C DE270192 C DE 270192C
- Authority
- DE
- Germany
- Prior art keywords
- ammonia
- liquid
- absorbents
- gas mixture
- gases
- 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.)
- Active
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 10
- 230000002745 absorbent Effects 0.000 claims description 8
- 239000002250 absorbent Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- 230000003247 decreasing Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
- C01C1/0458—Separation of NH3
-
- 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
- C01C1/0458—Separation of NH3
- C01C1/0464—Separation of NH3 by absorption in liquids, e.g. water
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
KAISERLICHESIMPERIAL
PATENTAMT.PATENT OFFICE.
PATENTSCHRIFTPATENT LETTERING
- M 270192 KLASSE 12 #. GRUPPE- M 270192 CLASS 12 #. GROUP
Patentiert im Deutschen Reiche vom 7. August 1912 ab.Patented in the German Empire on August 7, 1912.
Bei der Abscheidung von Ammoniak aus unter Druck stehenden Gasgemischen, z. B. solchen, wie sie bei der synthetischen Herstellung von Ammoniak aus seinen Elementen gewonnen werden, mittels flüssiger Absorptionsmittel tritt, besonders wenn es sich um große Gasmengen handelt, der Übelstand auf, daß bei Verwendung der- üblichen Absorptionsapparate (Türme, Wäschapparate usw.) ίο sehr umfangreiche Vorrichtungen nötig sind, die mit Rücksicht auf die erforderliche Druckbeständigkeit nur mit großen Kosten oder bei sehr hohen Drucken überhaupt kaum mehr zu beschaffen sind.When separating ammonia from pressurized gas mixtures, e.g. B. such as those used in the synthetic production of ammonia from its elements Be obtained by means of liquid absorbent occurs, especially if it is large amounts of gas are involved, the disadvantage that when using the usual absorption apparatus (Towers, washing machines, etc.) ίο very extensive devices are required, those with regard to the required pressure resistance only at great cost or at very high pressures can hardly be obtained at all.
ki5 Es hat sich nun gezeigt, daß man solche ammoniakhaltige, unter Druck stehende Gasgemische, die man als schwer kondensierbar bezeichnen kann, vorteilhaft in der Weise mit flüssigen Absorptionsmitteln, insbesondere Wasser, behandelt, daß man die Gase gemeinsam mit den Absorptionsmitteln im Gleichstrom durch Rohre hindurchführt. Die Absorption von Ammoniak, speziell auch unter Druck, ist bisher noch nicht mittels von außen eingeführter, flüssiger Absorptionsmittel im Gleichstrom bewirkt worden. Man hat vielmehr bisher lediglich bei einer unter gewöhnlichem Druck arbeitenden kombinierten Ammoniakdestillation und -konzentration die durch Kongo densation der wasserhaltigen Ammoniakdämpfe gebildete Flüssigkeit zur Absorption des nach-35 It has now been shown that such ammonia-containing, pressurized gas mixtures, which can be described as difficult to condense, are advantageously treated with liquid absorbents, especially water, that the gases are co-current with the absorbents through pipes leads through. The absorption of ammonia, especially under pressure, has not yet been brought about by means of liquid absorbents introduced from the outside in cocurrent. It has rather been only at an operating under ordinary pressure combined ammonia distillation and concentration by Congo-condensation of the hydrous ammonia vapors formed liquid to absorb the post-35
strömenden wasserdampfhaltigen Ammoniaks benutzt.flowing ammonia containing water vapor is used.
Man kann vorteilhaft, wenn es sich darum handelt, die Gase von Ammoniak zu befreien und gleichzeitig konzentrierte Ammoniaklösung zu erhalten, so verfahren, daß man die Gase in der beschriebenen Weise mehrmals mit dem Absorptionsmittel behandelt, derart, daß zunächst eine bereits angereicherte Lösung mit dem Gasstrom in Berührung gebracht wird, worauf man die Flüssigkeit vom Gas trennt und letzteres z. B. in einer zweiten oder eventuell noch weiteren Apparatur mit weniger konzentrierter Lösung bzw. frischem Absorptionsmittel behandelt.It can be advantageous when it comes to removing ammonia from the gases and at the same time to obtain concentrated ammonia solution, proceed in such a way that the gases treated in the manner described several times with the absorbent, such that initially an already enriched solution is brought into contact with the gas flow, whereupon the liquid is separated from the gas and the latter z. B. in a second or possibly still further equipment with less concentrated solution or fresh absorbent treated.
Claims (2)
Publications (1)
Publication Number | Publication Date |
---|---|
DE270192C true DE270192C (en) |
Family
ID=526965
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DENDAT270192D Active DE270192C (en) |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE270192C (en) |
-
0
- DE DENDAT270192D patent/DE270192C/de active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE1951751A1 (en) | Process for treating gases with an amine solution | |
DE2542705C2 (en) | Process and plant for the production of water enriched with deuterium in the production of hydrogen | |
DE270192C (en) | ||
DE2431531C2 (en) | Process for the selective absorption of ammonia from a gas mixture | |
DE1253686B (en) | Process for removing nitrogen oxides from industrial exhaust gases | |
DE1233836B (en) | Process for the production of ammonia gas | |
DE1544123C3 (en) | Process for removing acidic gases from gaseous mixtures | |
WO1997003920A1 (en) | Claus sulphur production process and installation | |
DE1544141B2 (en) | Process for removing gas or liquid residues from enriched solvents | |
DE502174C (en) | Denitration of waste acid | |
DE3935445C2 (en) | Water purification process | |
DE1768600C3 (en) | Process for recycling unconverted starting materials in urea synthesis | |
DE895497C (en) | Process for the removal and recovery of oxygen-containing compounds from synthetic and natural hydrocarbon mixtures | |
DE246712C (en) | ||
DE944848C (en) | Method for separating isotopes | |
DE526475C (en) | Process for the extraction of pure sulfur | |
DE925644C (en) | Process for the production of hydrogen cyanide | |
DE493777C (en) | Process for separating ammonia from the reaction gases under high pressure in the synthetic preparation of ammonia | |
DE373734C (en) | Process for the concentration of aqueous nitric acid using sulfuric acid | |
DE975924C (en) | Process for the processing of fluids that arise during the processing of coking and synthesis gases | |
DE440607C (en) | Method and device for the synthetic production of ammonia | |
DE174324C (en) | ||
DE931645C (en) | Process for the production of compressed, de-acidified ammonia water | |
DE481138C (en) | Process for liquefying and separating gas mixtures | |
DE925645C (en) | Process for the production of hydrogen cyanide |