DE509582C - Process for the catalytic conversion of gases or vapors - Google Patents
Process for the catalytic conversion of gases or vaporsInfo
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; 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)
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)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE973776C (en) * | 1954-03-08 | 1960-06-02 | Power Gas Ltd | Process for producing flammable gases |
-
1927
- 1927-07-31 DE DEI31811D patent/DE509582C/en not_active Expired
Cited By (1)
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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