DE337153C - Process for the catalytic production of hydrogen - Google Patents

Process for the catalytic production of hydrogen

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Publication number
DE337153C
DE337153C DE1915337153D DE337153DD DE337153C DE 337153 C DE337153 C DE 337153C DE 1915337153 D DE1915337153 D DE 1915337153D DE 337153D D DE337153D D DE 337153DD DE 337153 C DE337153 C DE 337153C
Authority
DE
Germany
Prior art keywords
water
hydrogen
catalytic production
contact
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.)
Expired
Application number
DE1915337153D
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German (de)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Application granted granted Critical
Publication of DE337153C publication Critical patent/DE337153C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06Production 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
    • C01B3/12Production 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
    • C01B3/16Production 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

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Description

Nachstehend ist ein Verfahren beschrieben, welches die katalytische Darstellung von Wasserstoff aus Kohlenoxyd und Wasserdampf in technisch besonders vorteilhafter S Weise ermöglicht.The following is a description of a method which catalyzes the preparation of Enables hydrogen from carbon oxide and water vapor in a technically particularly advantageous manner.

Das Verfahren besteht darin, daß man in das den Kontaktraum verlassende, in der Regel schon zur Vorwärmung der eintretenden Gase verwendete aber noch heiße Gasgemisch kaltes Wasser einführt und das so erhaltene heiße Wasser zur Aufwärmung und Wasserdampfbeladung neuen kalten, dem Kontaktofen zuzuführenden kohlenoxydhaltigen Gases verwendet. Hierdurch wird ein großer Teil des für das Verfahren nötigen Frischdampfes in einfacher Weise geliefert, indem insbesondere die latente -Kondensationswärme des in den abziehenden Gasen noch enthaltenen Wasserdampfes nutzbar gemacht wird.The method consists in that one leaves the contact space in the Usually already used to preheat the incoming gases but still hot gas mixture introduces cold water and the hot water obtained in this way for heating and water vapor loading new cold, the Contact furnace to be supplied carbon oxide-containing gas used. This becomes a large part of the live steam required for the process is supplied in a simple manner, in particular by the latent heat of condensation in the withdrawing gases still contained water vapor is made usable.

Man verfährt dabei z. B. in der Weise, daß man die aus den Kontaktöfen abziehenden Gase in Einspritzkühlern im Gegenstrom mit einer zur Kondensation der Hauptmenge des Wasserdampfes und zur Abkühlung der Gase ausreichenden Kühlwassermenge zusammenbringt und das aus dem Kühler ablaufende Wasser, das die Summe des eingespritzten und kondensierten Wassers darstellt, nun in einem anderen Apparat, dem Verdunster, im Gegenstrom mit dem frischen, noch nicht mit Dampf versetzten Wassergas ο. dgl. zusammenbringt, so daß sich dieses bei der Temperatur des heißen Wassers mit Wasserdampf sättigt. Die Menge des einzuspritzenden Kühlwassers wird zweckmäßig so bemessen, daß die Temperatur des austretenden Wassers möglichst hoch und gleichzeitig diejenige der austretenden Gase möglichst niedrig ist. Wechselnde Betriebsverhältnisse, wechselnde Belastung der Kontaktöfen usw. bedingen also jeweils eine andere Einstellung der Kühlwassermenge.One proceeds z. B. in such a way that one withdraws from the contact furnaces Gases in injection coolers in countercurrent with a condensation of the bulk of the Brings together water vapor and sufficient cooling water to cool the gases and the water draining from the cooler, which is the sum of the injected and condensed water, now in another device, the evaporator, in countercurrent with the fresh one, not yet with Steam added water gas ο. Like. Brings together, so that this is at the temperature of the hot water is saturated with water vapor. The amount to be injected Cooling water is expediently dimensioned so that the temperature of the exiting water as high as possible and at the same time that of the escaping gases is as low as possible. Changing operating conditions, changing loads on the contact furnaces, etc. so a different setting of the cooling water quantity in each case.

Es wurde weiter gefunden, daß es vielfach zweckmäßig ist, die Kondensation und Abkühlung und gegebenenfalls auch die Aufwärmung der Gase in zwei oder mehreren Stufen durchzuführen.It has also been found that it is often expedient to use the condensation and cooling and optionally also the warming up of the gases in two or more To carry out stages.

Mittels des beschriebenen Verfahrens gelingt es leicht, 50 Prozent oder mehr von dem für die Reaktion erforderlichen Wasser als Dampf zu erhalten.Using the method described, it is easy to achieve 50 percent or more of to obtain the water required for the reaction as steam.

Claims (1)

Patent-Anspruch:Patent claim: Verfahren zur katalytischen Herstellung von Wasserstoff aus Kohlenoxyd und Wasserdampf, dadurch gekennzeichnet, daß man in das den Kontaktraum verlassende, in der Regel schon zur Vorwärmung der eintretenden Gase verwendete aber noch heiße Gasgemisch kaltes Wasser einführt und das so erhaltene heiße Wasser zur Aufwärmung und Wasserdampfbeladung neuen kalten, dem Kontaktofen zuzuführenden kohlenoxydhaltigen Gases verwendet.Process for the catalytic production of hydrogen from carbon oxide and steam, characterized in that one enters the one leaving the contact space, usually already for preheating of the incoming gases but still used cold gas mixture that was still hot Introduces water and the hot water thus obtained for heating and water vapor loading new cold, carbon-oxide-containing gas to be supplied to the contact furnace is used.
DE1915337153D 1915-12-24 1915-12-24 Process for the catalytic production of hydrogen Expired DE337153C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE337153T 1915-12-24

Publications (1)

Publication Number Publication Date
DE337153C true DE337153C (en) 1921-05-21

Family

ID=33459919

Family Applications (1)

Application Number Title Priority Date Filing Date
DE1915337153D Expired DE337153C (en) 1915-12-24 1915-12-24 Process for the catalytic production of hydrogen

Country Status (2)

Country Link
DE (1) DE337153C (en)
FR (1) FR514101A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE940726C (en) * 1952-04-26 1956-03-22 Basf Ag Method for operating an oil processing plant
DE1083966B (en) * 1955-12-05 1960-06-23 Scholven Chemie Ag Process for the catalytic pressure refining of hydrocarbon oils such as raw benzene or raw gasoline

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE940726C (en) * 1952-04-26 1956-03-22 Basf Ag Method for operating an oil processing plant
DE1083966B (en) * 1955-12-05 1960-06-23 Scholven Chemie Ag Process for the catalytic pressure refining of hydrocarbon oils such as raw benzene or raw gasoline

Also Published As

Publication number Publication date
FR514101A (en) 1921-03-03

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