US2018297932A1PendingUtilityA1

Nickel diatomaceous earth catalyst and method for producing the same

Assignee: MITSUBISHI GAS CHEMICAL COPriority: Nov 2, 2015Filed: Oct 31, 2016Published: Oct 18, 2018
Est. expiryNov 2, 2035(~9.2 yrs left)· nominal 20-yr term from priority
B01J 37/03C07C 209/48B01J 21/08B01J 37/031B01J 37/16B01J 23/755B01J 37/038B01J 37/08B01J 37/18B01J 37/0236C07C 211/27C07B 61/00B01J 37/0221B01J 35/1019B01J 35/1014B01J 35/002B01J 21/16B01J 35/40B01J 2235/00B01J 35/77B01J 35/45B01J 35/70B01J 35/30B01J 35/391B01J 35/392B01J 35/60B01J 35/613B01J 35/615
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Claims

Abstract

A nickel diatomaceous earth catalyst having a weight loss rate measured by hydrogen-TG at 400 to 600° C. of 0.05 to 2.0%.

Claims

exact text as granted — not AI-modified
1 . A nickel diatomaceous earth catalyst having a weight loss rate measured by hydrogen-TG at 400 to 600° C. of 0.05 to 2.0%. 
     
     
         2 . The nickel diatomaceous earth catalyst according to  claim 1 , wherein a nickel crystallite diameter is 30 to 100 Å. 
     
     
         3 . The nickel diatomaceous earth catalyst according to  claim 1 , wherein a change A in the nickel crystallite diameter between before and after a heat resistance test is 210 Å or less. 
     
     
         4 . The nickel diatomaceous earth catalyst according to  claim 1 , wherein the nickel diatomaceous earth catalyst has a specific surface area of 60 to 180 m 2 /g. 
     
     
         5 . A method for producing a nickel diatomaceous earth catalyst by a precipitation method, comprising:
 adding an alkaline solution as a precipitant to a dispersion liquid in which diatomaceous earth and a salt of a nickel catalyst are mixed; and   performing a drying treatment, a calcination treatment, and a reduction treatment, in this order, to obtain the nickel diatomaceous earth catalyst,   wherein the reduction treatment is performed at a peak temperature +40° C. or more of a hydrogen-TPR measurement on a calcined powder produced by the calcination treatment.   
     
     
         6 . The method for producing a nickel diatomaceous earth catalyst according to  claim 5 , wherein the reduction treatment is performed at the peak temperature +200° C. or less of the hydrogen-TPR measurement on the calcined powder produced by the calcination treatment. 
     
     
         7 . A nickel diatomaceous earth catalyst produced by the method according to  claim 5 . 
     
     
         8 . A method for producing xylylenediamine, the method comprising hydrogenating phthalonitrile in an ammonia solvent in the presence of the nickel diatomaceous earth catalyst according to  claim 1 .

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