DE270192C - - Google Patents

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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
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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
Application number
DENDAT270192D
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German (de)
Publication of DE270192C publication Critical patent/DE270192C/de
Active legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0458Separation of NH3
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0458Separation of NH3
    • C01C1/0464Separation of NH3 by absorption in liquids, e.g. water
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • 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)

Patent-Ansprüche:Patent Claims: 1. Verfahren zur Abscheidung des synthetisch hergestellten Ammoniaks aus den unter Druck stehenden Gasgemischen mit Hilfe flüssiger Absorptionsmittel, darin bestehend, daß man das Gasgemisch und die Flüssigkeit im Gleichstrom durch Rohre hindurchführt.1. Process for separating the synthetically produced ammonia from the pressurized gas mixtures with the aid of liquid absorbents, consisting of that one passes the gas mixture and the liquid in cocurrent through pipes. 2. Ausführungsform des Verfahrens nach Anspruch 1, darin bestehend, daß man das Gasgemisch einer systematischen Behandlung mit Absorptionsmitteln von abnehmender Ammoniakkonzentration unterwirft. 2. Embodiment of the method according to claim 1, consisting in that the Gas mixture of a systematic treatment with absorbents of decreasing Subject to ammonia concentration. BERLIN. GEDRUCKT IN DER REICHSDRUCKEREI.BERLIN. PRINTED IN THE REICHSDRUCKEREI.
DENDAT270192D Active DE270192C (en)

Publications (1)

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