GB825414A - Preparation of an alumina hydrate composition - Google Patents

Preparation of an alumina hydrate composition

Info

Publication number
GB825414A
GB825414A GB28355/57A GB2835557A GB825414A GB 825414 A GB825414 A GB 825414A GB 28355/57 A GB28355/57 A GB 28355/57A GB 2835557 A GB2835557 A GB 2835557A GB 825414 A GB825414 A GB 825414A
Authority
GB
United Kingdom
Prior art keywords
acid
trihydrate
alumina
solution
monohydrate
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
GB28355/57A
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.)
Sinclair Refining Co
Original Assignee
Sinclair Refining Co
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 Sinclair Refining Co filed Critical Sinclair Refining Co
Publication of GB825414A publication Critical patent/GB825414A/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
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04Alumina

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)

Abstract

Alumina hydrate containing trihydrate and amorphous or monohydrate forms, particularly useful as a catalyst base, is prepared by treating sodium aluminate solution with a water-soluble compound acid reacting therewith to reduce the pH to a value not below 10.5 thereby precipitating 10 to 90% of the alumina as trihydrate and thereafter mixing the slurry with a water-soluble acid reacting compound to reduce the pH to below 10, thereby precipitating monohydrate or amorphous hydrous alumina. The trihydrate precipitation is preferably effected at a pH of 11.5 and after the addition of the acid acting compound the pH is preferably allowed to rise to at least 11.6 as the trihydrate precipitates. Gibbsite or bayerite may be formed. The pH of the monohydrate precipitation is preferably less than 7. The trihydrate and the monohydrate precipitations are preferably effected at 20-50 DEG C. Suitable acid acting compounds for addition to the aluminate are the mineral acids such as sulphuric, hydrochloric and nitric acids, carbon dioxide, sulphur trioxide and hydrogen chloride. When gaseous these may be mixed with inert gases such as air or nitrogen. Aluminium salts such as the sulphate, chloride and nitrate may also be used and so may ammonium bicarbonate and bisulphate and sodium bisulphate. Salts of amines and ammonia such as ammonium acetate carbonate and sulphate and carboxylic acids such as formic, acetic and mono- and dichloro acetic acids may be similarly employed. When using carbon dioxide to produce the trihydrate and another acid-reacting material to provide the monohydrate, the final pH should be carried low enough to release the carbon dioxide from the aqueous solution, e.g. a pH of 5.5. The precipitated hydrate may be washed with or without previous drying and the washed hydrates may be dried at a 110-250 DEG C. to remove free water and calcined or activated at 400-700 DEG C., thereby removing the water of crystallization. When employed as a catalyst the alumina may be used in finely-divided form or in tablets up to one inch long. Chemically reactive components from Groups V-VIII of the Periodic Table, particularly vanadium, molybdenum, tungsten, chromium, cobalt, nickel and platinum or mixtures thereof may be deposited on or mixed with the catalyst base; in particular, from 0.1 to 1.5% by weight of platinum or 1% each of cobalt and molybdenum may be used. According to examples: (1) an aqueous sodium aluminate solution having a Na2O to Al2O3 ratio of 1.41 to 1 was reacted with sulphuric acid at 40 DEG C. to decrease the pH to 11.4. While continuing stirring, the temperature fell to 36 DEG C. and the pH rose to 12.1 at which point further sulphuric acid was added to bring the pH down to 5.3 after which the hydrate was filtered dried at 120 DEG C., washed with ammonium hydroxide solution at a pH of about 9 and finally dried at 120 DEG C.; (2) a similar sodium aluminate solution was treated with aluminium sulphate solution at 40 DEG C. with carbon dioxide to reduce the pH to 11.4. The pH then rose to 11.9 and aluminium sulphate was added to reduce the pH to 5.1. The filter cake contained 66% trihydrate and the remainder was boehmite and amorphous hydrate. Further examples relate to the use in the first addition period of the acid-reacting material of carbon dioxide, aluminium sulphate, ammonium acetate and sulphuric acid and, for the second addition of acid-acting material, of aluminium sulphate. (X) A desulphurization catalyst containing cobalt and molybdenum was prepared by treating the final alumina hydrate of Example I above with cobalt carbonate and molybdenum trioxide as an aqueous slurry which was heated to 71 DEG C. The filter cake after removal of mother liquor was dried at 111 DEG C., mixed with a die lubricant and tableted and then calcined in air at 482 DEG C. (XI) A platinum-alumina catalyst is prepared by slurrying the alumina hydrate prepared by Example II above, and adding chloroplatinic acid solution and thereafter adding a solution of hydrogen sulphide in water. The resulting slurry was dried at 110 DEG C. ground and pressed into tablets. The tablets were burned at 482 DEG C. in an atmosphere containing initially 5 parts of air to 300 parts of nitrogen and finally in pure air.
GB28355/57A 1956-09-10 1957-09-09 Preparation of an alumina hydrate composition Expired GB825414A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US825414XA 1956-09-10 1956-09-10

Publications (1)

Publication Number Publication Date
GB825414A true GB825414A (en) 1959-12-16

Family

ID=22171845

Family Applications (1)

Application Number Title Priority Date Filing Date
GB28355/57A Expired GB825414A (en) 1956-09-10 1957-09-09 Preparation of an alumina hydrate composition

Country Status (1)

Country Link
GB (1) GB825414A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800797A (en) * 1993-12-09 1998-09-01 Catalysts & Chemicals Industries Co., Ltd. Process for producing alumina and apparatus therefor
CN112694110A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for continuously preparing pseudoboehmite
CN112694111A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for preparing pseudoboehmite
CN114426297A (en) * 2020-10-29 2022-05-03 中国石油化工股份有限公司 Method for continuously preparing pseudoboehmite
CN114506869A (en) * 2020-10-29 2022-05-17 中国石油化工股份有限公司 Pseudo-boehmite, preparation method and application thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800797A (en) * 1993-12-09 1998-09-01 Catalysts & Chemicals Industries Co., Ltd. Process for producing alumina and apparatus therefor
CN112694110A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for continuously preparing pseudoboehmite
CN112694111A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for preparing pseudoboehmite
CN112694111B (en) * 2019-10-23 2023-05-30 中国石油化工股份有限公司 Method for preparing pseudo-boehmite
CN114426297A (en) * 2020-10-29 2022-05-03 中国石油化工股份有限公司 Method for continuously preparing pseudoboehmite
CN114506869A (en) * 2020-10-29 2022-05-17 中国石油化工股份有限公司 Pseudo-boehmite, preparation method and application thereof
CN114506869B (en) * 2020-10-29 2023-09-01 中国石油化工股份有限公司 Pseudo-boehmite and preparation method and application thereof

Similar Documents

Publication Publication Date Title
US4485189A (en) Catalyst for the desulfurization of industrial waste gases and process for its preparation
US3557025A (en) Method of producing alkalized alumina and products produced thereby
WO2015101275A1 (en) High-concentration carbonyl sulfide conversion-absorption type desulfurizer and carbon disulfide conversion-absorption type desulfurizer and preparation method thereof
US4477367A (en) Crystalline 2-layer lithium-hydroxy aluminates
JPH0324411B2 (en)
GB675349A (en) Catalysts and catalyst carriers containing aluminium oxide and applications thereof
CN111943242A (en) Mesoporous gamma-Al2O3Preparation method of carrier and mesoporous gamma-Al2O3Carrier
US2390272A (en) Purification of gelatinous hydroxides
US3848056A (en) Molten alkaline alkanoic mixtures for absorption of sulfur oxides
US3027234A (en) Manufacture of spheroidal alumina particles from aluminum sulfate
Huang et al. Control of porosity and surface area in alumina: I. Effect of preparation conditions
GB825414A (en) Preparation of an alumina hydrate composition
US3105053A (en) Process for preparing alumina hydrosol and gel
GB1081110A (en) Production of alumina particles
US2956861A (en) Process for the preparation of highly dispersed metallic oxides, particularly zinc oxide
JP3531299B2 (en) Method for producing heat-resistant transition alumina
US3948809A (en) Absorbent and the process for producing it
US3105739A (en) Method for producing alumina free from alkaline earth metal impurities
US2973245A (en) Method of preparing alumina hydrate compositions containing trihydrate
US3104944A (en) Method for producing alumina free from alkaline earth metal impurities
US3027233A (en) Process for the production of alumina from aluminum sulfate
US2910506A (en) Process of preparing low molecular weight alkyl monosulfides
JPS585174B2 (en) Method for producing basic aluminum lactate
SE7511066L (en) PROCEDURE AND FACILITY FOR CLEANING PHOSPHORIC ACID ON THE VATA ROAD
JPS5926330B2 (en) Improved Claus catalyst and its manufacturing method