DE706826C - Process for making shaped catalysts - Google Patents
Process for making shaped catalystsInfo
- Publication number
- DE706826C DE706826C DEI48851D DEI0048851D DE706826C DE 706826 C DE706826 C DE 706826C DE I48851 D DEI48851 D DE I48851D DE I0048851 D DEI0048851 D DE I0048851D DE 706826 C DE706826 C DE 706826C
- Authority
- DE
- Germany
- Prior art keywords
- catalysts
- mass
- water
- different
- ground
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
Description
Zur Ausführung katalytischer ReaktionenFor carrying out catalytic reactions
ist es vielfach erwünscht, einen geformten Katalysator zu verwenden, der hohe Aktivität aufweist und unter den ArbeitsbedingungenIt is often desired to use a shaped catalyst which has high activity has and under the working conditions
S seine Form behält.S retains its shape.
Erfindungsgemäß lassen sich derartige Katalysatoren leicht erhalten, wenn man katalytisch wirkende Metallverbindungen in Pulverform mit Wasser, wäßrigen Lösungen oderAccording to the invention, such catalysts can easily be obtained if one is catalytically acting metal compounds in powder form with water, aqueous solutions or
ίο niedrigsiedenden organischen Flüssigkeiten, wie Benzin und Benzol, verrührt, die feuchte Masse durch Austreiben von Flüssigkeit unter Erhitzen in mahlbare Form überführt, dann vermahlt und nach Zugabe der gleichen oder einer anderen Metallverbindung in nicht derart vorbehandeltem Zustand und gegebenenfalls einer Flüssigkeit der genannten Art in Stücke bestimmter Form preßt. Die Katalysatoren können einer aktivierenden Nachbehandlung unterzogen werden.ίο low-boiling organic liquids, like gasoline and benzene, mixed together, the moist mass by expelling liquid underneath Heating converted into grindable form, then ground and after adding the same or another metal compound in a state that has not been pretreated in this way and, if applicable presses a liquid of the type mentioned into pieces of a certain shape. The catalysts can be subjected to an activating post-treatment.
Zur Herstellung der Katalysatoren können beliebige Metallverbindungen, ζ. B. die Oxyde, Sulfide, Carbonate, Phosphate von Metallen, insbesondere von Molybdän, Wolfram, Chrom, Titan, Vanadin, Mangan, Eisen, Kobalt, Nickel u. dgl., verwendet werden. Diese werden zerkleinert, zweckmäßig bis zu einer Korngröße von V3 bis Vio ram.> un(i sodann mit einer Flüssigkeit, z. B. Wasser, einige Zeit verrührt oder geknetet. Man wählt hierbei eine Flüssigkeitsmenge von mindestens 20 0/0, vorteilhaft 3 ο 0/0, bezogen auf die Metall verbindung; im allgemeinen geht man nicht über 100 0/0 hinaus. Als Flüssigkeiten können außer Wasser wäßrige Metallsalzlösungen, verdünnte Säuren oder organische Flüssigkeiten, wie Benzin, Benzol u. dgl., verwendet werden. Die so hergestellte breiförmige oder feuchte Masse wird dann einer erhöhten Temperatur, je, nach dem Siedepunkt der vorhandenen Flüssigkeit, ausgesetzt, bis diese vollständig oder teilweise, z. B. bis zu einer Menge von 2 bis 10%, entfernt ist. Die verbleibende Masse wird dann vermählen, z. B. bis zu einer Korngröße von V3 mm, und vorteilhaft nochmais mit· einer Flüssigkeit versetzt. Die Menge der Flüssigkeit wird hierbei derart bemessen, daß lediglich die für die mechanische Pressung erforderliche Gleitfähigkeit der Masse erzielt wird. Man verwendet in der Hauptsache Wasser oder z. B. Benzin. Der Flüssigkeitszusatz ist nur dann angebracht, wenn die gemahlene Masse keine genügende Menge der zuerst zugegebenen Flüssigkeit mehr enthält oder wenn es erwünscht ist, eine andere Flüssigkeit zu verwenden, oder wenn außer der noch zuzusetzenden festen Substanz noch solche in gelösterAny metal compounds, ζ. B. the oxides, sulfides, carbonates, phosphates of metals, in particular of molybdenum, tungsten, chromium, titanium, vanadium, manganese, iron, cobalt, nickel and the like., Can be used. These are comminuted, expediently up to a particle size of V 3 to Vio ram .> Un ( i then stirred or kneaded with a liquid, e.g. water, for some time. An amount of liquid of at least 20% is advantageously chosen 3 ο 0/0, based on the metal compound; in general, one does not go beyond 100 0/0 In addition to water, aqueous metal salt solutions, dilute acids or organic liquids such as gasoline, benzene and the like can be used as liquids. The pulpy or moist mass produced in this way is then exposed to an elevated temperature, depending on the boiling point of the liquid present, until it has been completely or partially removed, for example up to an amount of 2 to 10% is then ground, for example up to a grain size of 3 mm, and advantageously a further liquid is added to the corn. The amount of liquid is measured in such a way that only that required for mechanical pressing che sliding ability of the mass is achieved. One uses mainly water or z. B. Gasoline. The addition of liquid is only appropriate if the ground mass no longer contains a sufficient amount of the liquid added first or if it is desired to use a different liquid, or if, in addition to the solid substance to be added, there is also a dissolved substance
*) Von dem Patentsucher sind als die Erfinder angegeben worden:*) The patent seeker indicated the following as the inventors:
Dr. Mathias Pier in Heidelberg und Dr. Eugen Anthes in Ludwigshafen, Rhein.Dr. Mathias Pier in Heidelberg and Dr. Eugen Anthes in Ludwigshafen, Rhine.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEI48851D DE706826C (en) | 1934-01-24 | 1934-01-24 | Process for making shaped catalysts |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEI48851D DE706826C (en) | 1934-01-24 | 1934-01-24 | Process for making shaped catalysts |
Publications (1)
Publication Number | Publication Date |
---|---|
DE706826C true DE706826C (en) | 1941-06-06 |
Family
ID=7192402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEI48851D Expired DE706826C (en) | 1934-01-24 | 1934-01-24 | Process for making shaped catalysts |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE706826C (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE952625C (en) * | 1944-08-26 | 1956-11-22 | Bataafsche Petroleum | Process for the production of a highly porous dehydrogenation catalyst |
DE1013630B (en) * | 1955-03-08 | 1957-08-14 | Eugene Jules Houdry | Process for the manufacture of catalysts |
DE1023015B (en) * | 1955-01-28 | 1958-01-23 | Oxy Catalyst Inc | Process for the manufacture of catalysts |
DE1074014B (en) * | 1955-12-10 | 1960-01-28 | Badische Anilin & Soda Fabrik Aktiengesellschaft Ludw igshaf en/Rhem | Process for the production of an active, dimensionally stable alumina support catalyst |
DE1119831B (en) * | 1955-06-10 | 1961-12-21 | Sinclair Refining Co | Process for the production of alumina catalysts |
-
1934
- 1934-01-24 DE DEI48851D patent/DE706826C/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE952625C (en) * | 1944-08-26 | 1956-11-22 | Bataafsche Petroleum | Process for the production of a highly porous dehydrogenation catalyst |
DE1023015B (en) * | 1955-01-28 | 1958-01-23 | Oxy Catalyst Inc | Process for the manufacture of catalysts |
DE1013630B (en) * | 1955-03-08 | 1957-08-14 | Eugene Jules Houdry | Process for the manufacture of catalysts |
DE1119831B (en) * | 1955-06-10 | 1961-12-21 | Sinclair Refining Co | Process for the production of alumina catalysts |
DE1074014B (en) * | 1955-12-10 | 1960-01-28 | Badische Anilin & Soda Fabrik Aktiengesellschaft Ludw igshaf en/Rhem | Process for the production of an active, dimensionally stable alumina support catalyst |
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