GB833577A - Process for the manufacture of catalysts - Google Patents
Process for the manufacture of catalystsInfo
- Publication number
- GB833577A GB833577A GB1184757A GB1184757A GB833577A GB 833577 A GB833577 A GB 833577A GB 1184757 A GB1184757 A GB 1184757A GB 1184757 A GB1184757 A GB 1184757A GB 833577 A GB833577 A GB 833577A
- Authority
- GB
- United Kingdom
- Prior art keywords
- product
- compound
- stage
- aqueous solution
- impregnating
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/86—Chromium
- B01J23/862—Iron and chromium
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/26—Chromium
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
Abstract
A promoted chromia-alumina catalyst is prepared by (1) reacting aluminium sulphate or aluminium ammonium sulphate with an alkaline precipitant (preferably an aqueous solution of (a) ammonia or (b) sodium aluminate) under conditions effective to form a substantially granular hydrogel precipitate; (2) optionally washing the precipitate; (3) transforming it into a gel, preferably by passing through a colloid mill, particularly wherein the apertures are between 0.001 and 0.005 inch; (4) spray drying the gel under conditions effective to produce microspheroids of relatively uniform size distribution (preferably a chamber spray drier of the rotating disc type is used); (5) washing the product if stage (2) was omitted, preferably with dilute aqueous ammonia and particularly subsequently with water; (6) roasting the dried product at 500-700 DEG C., preferably 600 DEG C.; (7) impregnating with an aqueous solution comprising a compound of chromium and either a compound each of cerium (the technical material containing other lanthanons may be used) and potassium or a compound of iron, nickel or cobalt; (8) separating the impregnated product from any superfluous impregnating solution; and (9) calcinating the impregnated product to decompose the compounds of the active elements into their oxides, preferably at approximately 550 DEG C. For stage (7), one of the following alternatives is preferred:-either the impregnating solution comprises chromic acid and copperas, or the product of the roasting stage is introduced into an aqueous solution containing chromic acid, cerous nitrate and potassium nitrate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1184757A GB833577A (en) | 1957-04-11 | 1957-04-11 | Process for the manufacture of catalysts |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1184757A GB833577A (en) | 1957-04-11 | 1957-04-11 | Process for the manufacture of catalysts |
Publications (1)
Publication Number | Publication Date |
---|---|
GB833577A true GB833577A (en) | 1960-04-27 |
Family
ID=9993777
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1184757A Expired GB833577A (en) | 1957-04-11 | 1957-04-11 | Process for the manufacture of catalysts |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB833577A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112547061A (en) * | 2019-09-25 | 2021-03-26 | 中国石油化工股份有限公司 | Catalyst for preparing propylene by propane dehydrogenation and preparation method thereof |
-
1957
- 1957-04-11 GB GB1184757A patent/GB833577A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112547061A (en) * | 2019-09-25 | 2021-03-26 | 中国石油化工股份有限公司 | Catalyst for preparing propylene by propane dehydrogenation and preparation method thereof |
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