DE509582C - Process for the catalytic conversion of gases or vapors - Google Patents

Process for the catalytic conversion of gases or vapors

Info

Publication number
DE509582C
DE509582C DEI31811D DEI0031811D DE509582C DE 509582 C DE509582 C DE 509582C DE I31811 D DEI31811 D DE I31811D DE I0031811 D DEI0031811 D DE I0031811D DE 509582 C DE509582 C DE 509582C
Authority
DE
Germany
Prior art keywords
gases
vapors
pore
catalytic conversion
gel
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
DEI31811D
Other languages
German (de)
Inventor
Dr Hans Roetger
Dr Fritz Stoewener
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie AG
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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to DEI31811D priority Critical patent/DE509582C/en
Application granted granted Critical
Publication of DE509582C publication Critical patent/DE509582C/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)

Description

Verfahren zur katalytischen Umsetzung von Gasen oder Dämpfen Eine Reihe katalytischer Gasreaktionen wird bekanntlich durch die Verwendung oberflichenaktiver Kontaktmassen von hoher Porosität begünstigt.Process for the catalytic conversion of gases or vapors A number of catalytic gas reactions are known to become more active on the surface through the use of the surface Contact masses of high porosity are favored.

Es hat sich nun gezeigt, daß die Wirkung derartiger I Kontaktmassen, insbesondere bei gemäßigten Temperaturen, erhöht werden kann, wenn man die Gase oder Dämpfe durch Kontaktmassen von in Richtung der hindurchstreichenden Gase oder Dämpfe abnehmender Porenweite leitet. It has now been shown that the effect of such I contact masses, especially at moderate temperatures, can be increased if you turn off the gases or vapors through contact masses from in the direction of the passing gases or Conducts vapors of decreasing pore size.

Man kann z. B. ein weitporiges Aluminiumoxydgel mit einem engporigen Kieselgel kombinieren oder ein weitporiges und engporiges Kieselgel hintereinander anordnen. You can z. B. a wide pore aluminum oxide gel with a narrow pore Combine silica gel or a wide-pore and narrow-pore silica gel one after the other arrange.

Ferner können derartige oberflächenaktive Stoffe allein oder in Verbindung mit katalvtisch wirksamen Substanzen, z. B. mit Metalloxyden beladen, verwendet werden.Such surfactants can also be used alone or in combination with catalvic substances, e.g. B. loaded with metal oxides, used will.

Die Kontaktmassen können dabei in einem einzigen Kontaktraum untergebracht oder auf mehrere hintereinandergeschaltete Kontaktöfen verteilt werden. Sie können ferner auch bewegt und beispielsweise den Gasen im Gegenstrom entgegengeführt werden.The contact masses can be accommodated in a single contact space or distributed over several contact furnaces connected in series. You can furthermore, they can also be moved and, for example, fed in countercurrent to the gases.

Beispiel I Ein Gemisch von Acetvlen und Ammoniak s-irrl tlurch vier hintereinan4ergeschaltete, auf etwa 3500 geheizte Kontaktrohl-e geleitet. Die Kontaktmassen bestehen in allen Fällen aus Kieselgel mit darauf feinverteiltem Thoriumoxyd und Zinkoxyd, jedoch enthalten, im Sinne der Strömungsrichtung des Gasgemisches angeordnet, die beiden ersten Rohre weitporiges, das dritte Rohr ein Gemisch von gleichen Raumteilen weit- und engporiges und das vierte Rohr endlich nur engporiges Gel. Die Ausbeute an flüssigen Kondensationsprodukten beträgt etwa 8501, der Theorie im Gegensatz zu nur 57 bzw. 68"/1, bei Anwendung gleicher Volumina von nur weitporigem bzw. nur engporigem Gel. Example I A mixture of acetylene and ammonia by four cascaded contact tubes heated to around 3500. The contact masses consist in all cases of silica gel with finely divided thorium oxide and Zinc oxide, but contained, arranged in the sense of the direction of flow of the gas mixture, the first two tubes are wide-pored, the third tube is a mixture of identical spatial parts Wide and narrow pore and the fourth tube finally only narrow pore gel. The yield of liquid condensation products is about 8501, contrary to theory to only 57 or 68 "/ 1, when using the same volumes of only wide-pore or only narrow-pored gel.

Beispiel 2 Ein Gemisch von Acetvlen und Ammoniak wird bei 300° durch zwei hintereinanderheschaltete Kontaktrohre geleitet, von denen das erste (im Sinne der Strömungsrichtung) mit weitporigem Alumininmgel und das zweite mit gleichen Volumenteilen eines engporigen Aluminiumgels gefüllt ist. Pro Liter Kontaktmasse erhält man hierbei 43,7 ccm stickstoffhaltige Kondensationsprodukte, während man unter sonst gleichen Bedingungen bei Verwendung der gleichen Menge eines engporigen Aluminiumgels allein eine Ausbeute von I6,3 ccm und von nur 12,5 ccm bei alleiniger Verwendung eines weitporigen AIuminiumgels erzielt. Example 2 A mixture of acetylene and ammonia is passed through at 300 ° two contact tubes connected in series, of which the first (in the sense the direction of flow) with wide-pore aluminum deficiency and the second with the same Volume parts of a narrow-pored aluminum gel is filled. Per liter of contact mass 43.7 ccm of nitrogen-containing condensation products are obtained while all other things being equal, using the same amount of a narrow-pore Aluminum gels alone have a yield of 16.3 cc and only 12.5 cc when used alone use of a wide-pored aluminum gel.

Beispiel, 3 Ein Gemisch von 1 Teil Schwefeldioxyd mit g Teilen Luft wird bei 4750 über eine aus platiniertem Kieselgel bestehende Kontaktmasse geleitet, die durch Beladen von Kieselgel mit 6,25 g Platinchlorid pro Liter Trägersubstanz und anschließendes Reduzieren her- -gestellt wurde. Example 3 A mixture of 1 part sulfur dioxide with g parts air at 4750 is passed over a contact mass made of platinum-coated silica gel, by loading silica gel with 6.25 g of platinum chloride per liter of carrier substance and then reducing it was produced.

Bei Hintereinanderschalten gleicher Volumteile eines weitporigen und eines engporigen Kieselgels, das jeweils mit gleichen Mengen Platin pro Volumeneinheit beladen wurde, erreicht man eine Raumzeitausbeute. die um etwa 80 01o über der mit engpnrigem Gel allein und um etwa 45 °/0 über der ausschließlich mit weitporigem Gel erzielbaren liegt. If the same volume parts are connected in series, a wide-pored and a narrow-pore silica gel, each with equal amounts of platinum per unit volume has been loaded, a space-time yield is achieved. which is about 80 01o above the with narrow-pored gel alone and about 45% above that exclusively with wide-pored gel Gel achievable lies.

Claims (1)

PATENTANSPRUCH: Verfahren zur katalytischen Umsetzung von Gasen oder Dämpfen, dadurch gekennzeichnet, daß man diese durch hochporöse oberflächenaktive Kontaktmassen von in Richtung der hindurchstreichenden Gase oder Dämpfe abnehmender Porenweite leitet. PATENT CLAIM: Process for the catalytic conversion of gases or Steaming, characterized in that this is done by highly porous surface-active Contact masses of decreasing in the direction of the passing gases or vapors Pore size guides.
DEI31811D 1927-07-31 1927-07-31 Process for the catalytic conversion of gases or vapors Expired DE509582C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEI31811D DE509582C (en) 1927-07-31 1927-07-31 Process for the catalytic conversion of gases or vapors

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEI31811D DE509582C (en) 1927-07-31 1927-07-31 Process for the catalytic conversion of gases or vapors

Publications (1)

Publication Number Publication Date
DE509582C true DE509582C (en) 1930-10-10

Family

ID=7187974

Family Applications (1)

Application Number Title Priority Date Filing Date
DEI31811D Expired DE509582C (en) 1927-07-31 1927-07-31 Process for the catalytic conversion of gases or vapors

Country Status (1)

Country Link
DE (1) DE509582C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE973776C (en) * 1954-03-08 1960-06-02 Power Gas Ltd Process for producing flammable gases

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE973776C (en) * 1954-03-08 1960-06-02 Power Gas Ltd Process for producing flammable gases

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