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Preparation of zerovalent nickel complexes

Assignee: EIDP Inc
•
Filing: 1981-09-24
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Granted: 1983-05-24
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Expires: 2001-09-24
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Abstract

Abstract Improved reaction rate for nickel powder in the preparation of zero-valent nickel organophosphite ligand complex catalysts using recycle catalyst and ligand.

Inventors

  • 👤 Howard E. Shook, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 23:51
CPC Classifications
C; C07; C07F; C07F15/00; C07F15/04; C07C; C07C253/00; C07C253/08; C07C253/10; C07C253/32; C07C253/34; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 152 words
In a process for the production of dinitriles by the addition of hydrogen cyanide to pentenenitriles in the presence of a zero-valent nickel-organophosphorus ligand containing catalyst promoted with an arylborane wherein the product fluid from said addition is contacted with a paraffin or cycloparaffin at a temperature of at least about 60° C. to form a primary light hydrocarbon extract phase containing catalyst values and a heavy dinitrile phase which phases are separated and wherein said catalyst is initially prepared by reacting elemental nickel with an organophosphorus compound, the improvement which comprises cooling said primary light extract phase sufficiently to form a secondary light phase and a secondary heavy phase, separating the secondary phases, removing substantially all of said hydrocarbon from the secondary light phase, and returning at least a portion of the residue thus obtained from the secondary light phase to the initial catalyst preparation to react with said elemental nickel.
Claim 2
Dependent Claim 152 words
In a process for the production of dinitriles by the addition of hydrogen cyanide to pentenenitriles in the presence of a zero-valent nickel-organophosphorus ligand containing catalyst promoted with an arylborane wherein the product fluid from said addition is contacted with a paraffin or cycloparaffin at a temperature of at least about 60° C. to form a primary light hydrocarbon extract phase containing catalyst values and a heavy dinitrile phase which phases are separated and wherein said catalyst is initially prepared by reacting elemental nickel with an organophosphorus compound, the improvement which comprises cooling said primary light extract phase sufficiently to form a secondary light phase and a secondary heavy phase, separating the secondary phases, removing substantially all of said hydrocarbon from the secondary light phase, and returning at least a portion of the residue thus obtained from the secondary light phase to the initial catalyst preparation to react with said elemental nickel.
Claim 3
Dependent Claim 18 words
The process of claim 1 wherein said light phase extract is cooled to less than about 45° C.
Claim 4
Dependent Claim 20 words
The process of claim 1 wherein said light phase extract is cooled to a temperature in the range 20°-30° C.

References Cited (Backward Citations)

US3496218A Cited
US3766237A Cited
US3773809A Cited
US3903120A Cited
US4082811A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-05-23 1986-11-22 1987-05-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-05-23 1990-11-22 1991-05-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-05-23 1994-11-22 1995-05-24 $7700.00 Window Closed / Lapsed

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