GB255884A - Manufacture of nickel catalyst - Google Patents

Manufacture of nickel catalyst

Info

Publication number
GB255884A
GB255884A GB18327/26A GB1832726A GB255884A GB 255884 A GB255884 A GB 255884A GB 18327/26 A GB18327/26 A GB 18327/26A GB 1832726 A GB1832726 A GB 1832726A GB 255884 A GB255884 A GB 255884A
Authority
GB
United Kingdom
Prior art keywords
nickel
treated
hydrogen
hours
mixture
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
GB18327/26A
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
Publication of GB255884A publication Critical patent/GB255884A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B31/00Reduction in general
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/14Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on a carbon-to-carbon unsaturated bond in organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation

Abstract

255,884. I. G. Farbenindustrie Akt.- Ges.,. (Assignees of Farbwerke vorm. Meister, Lucius, & Br³ning). July 22, 1925, [Convention date]. Catalytic agents, preparation and treatment of; hydrogenated organic compounds, catalytic production of.-Catalysts comprising nickel admixed or not with a metal of the iron or silver group are prepared by precipitating the nickel &c. as a crystalline hydroxide or carbonate in presence of a carrier, and then reducing the product with hydrogen at a temperature of 400‹ C. or above. To precipitate the hydroxide or carbonate in crystalline form, precipitation is effected slowly and at raised temperatures, suitable precipitants being alkali carbonates or, when ammonia compounds of nickel &c. are used, air containing carbon dioxide. The catalysts are suitable for use in hydrogenating processes, and in this connection reference is made to the production of isopropyl alcohol, ethylamine, and piperidine from acetone, acetonitrile, and pyridine respectively. According to one example, mixture of ammoniacal nickel nitrate solution and silicic acid gel is heated to 70‹ C. and treated with a strong current of air. The precipitate obtained after about 4 hours is filtered, washed, and dried, and is then treated with hydrogen at a temperature of 100- 130‹ C. which is gradually raised during 5 or 6 hours to 415-420‹ C. When reduction is complete the product is quickly cooled in presence of hydrogen and is poured into a suitable suspending agent such as water or pyridine. According to another example, a mixture of nickel nitrate solution and silicic acid gel is heated to 70‹ C. and treated with sodium carbonate solution added drop by drop over a period of 8 hours, and accord. ing to a further example a mixture of a solution of nickel, cobalt, and copper nitrates and silicic acid gel is similarly treated. In each case the product is further treated as described above.
GB18327/26A 1925-07-22 1926-07-22 Manufacture of nickel catalyst Expired GB255884A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE255884X 1925-07-22

Publications (1)

Publication Number Publication Date
GB255884A true GB255884A (en) 1927-04-28

Family

ID=5965737

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18327/26A Expired GB255884A (en) 1925-07-22 1926-07-22 Manufacture of nickel catalyst

Country Status (1)

Country Link
GB (1) GB255884A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011075494A1 (en) * 2009-12-18 2011-06-23 Invista Technologies S.A.R.L. Nickel metal compositions and nickel complexes derived from basic nickel carbonates
WO2012170297A2 (en) 2011-06-10 2012-12-13 Invista Technologies S.A R.L. Nickel form for preparation of catalytic nickel-ligand complexes
US8450450B2 (en) 2009-08-24 2013-05-28 Invista North America S.A R.L. Polyether glycol manufacturing process
TWI468413B (en) * 2010-09-07 2015-01-11 Invista Tech Sarl Preparing a nickel phosphorus ligand complex
US8969606B2 (en) 2011-06-10 2015-03-03 Invista North America S.A R.L. Calcination and reduction process including a fluidizing bed reactor

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8450450B2 (en) 2009-08-24 2013-05-28 Invista North America S.A R.L. Polyether glycol manufacturing process
WO2011075496A1 (en) * 2009-12-18 2011-06-23 Invista Technologies S.A.R.L. Nickel compositions for preparing nickel metal and nickel complexes
CN102655936A (en) * 2009-12-18 2012-09-05 因温斯特技术公司 Nickel metal compositions and nickel complexes derived from basic nickel carbonates
WO2011075494A1 (en) * 2009-12-18 2011-06-23 Invista Technologies S.A.R.L. Nickel metal compositions and nickel complexes derived from basic nickel carbonates
US8815186B2 (en) 2009-12-18 2014-08-26 Invista North America S.A.R.L. Nickel compositions for preparing nickel metal and nickel complexes
CN102655936B (en) * 2009-12-18 2014-11-05 因温斯特技术公司 Nickel metal compositions and nickel complexes derived from basic nickel carbonates
US9371343B2 (en) 2009-12-18 2016-06-21 Invista North America S.A. R.L. Nickel metal compositions and nickel complexes derived from basic nickel carbonates
US9024049B2 (en) 2010-09-07 2015-05-05 Invista North America S.A.R.L. Nickel compositions for preparing nickel metal and nickel complexes
US9371346B2 (en) 2010-09-07 2016-06-21 Invista North America S.A.R.L. Preparing a nickel phosphorus ligand complex
TWI468413B (en) * 2010-09-07 2015-01-11 Invista Tech Sarl Preparing a nickel phosphorus ligand complex
WO2012170297A2 (en) 2011-06-10 2012-12-13 Invista Technologies S.A R.L. Nickel form for preparation of catalytic nickel-ligand complexes
US9050591B2 (en) 2011-06-10 2015-06-09 Invista North America S.A.R.L. Nickel form for preparation of catalytic nickel-ligand complexes
US8969606B2 (en) 2011-06-10 2015-03-03 Invista North America S.A R.L. Calcination and reduction process including a fluidizing bed reactor
WO2012170300A2 (en) 2011-06-10 2012-12-13 Invista Technologies S.A R.L. Improvement in metal-ligand catalyst formation
US9981257B2 (en) 2011-06-10 2018-05-29 Invista North America S.A.R.L. Metal-ligand catalyst formation

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