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Heterogeneous hydrocyanation

一种氰化氢、氧化铝的技术,应用在氰化氢加成制备、有机化学、有机化合物/氢化物/配位配合物催化剂等方向

Active Publication Date: 2016-11-30
INVISTA TEXTILES (U K) LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the highly basic nature of supported alkali metal and alkaline earth metal catalysts makes their use necessary in vapor phase processes to avoid problems with the polymerization of both HCN and activated olefins

Method used

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  • Heterogeneous hydrocyanation

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0033] A 50 mL jacketed glass laboratory extractor (reactor) equipped with a magnetic stir bar, digital stir plate and maintained at 100 °C and 760 mmHg was charged with 5.5 ppm Na 2 O content of 3 g of alumina catalyst (Catalox SCFa-140, product of Sasol). The reactor was purged with flowing nitrogen for 30 minutes. Then 8 mL of refined c2PN was added to the reactor. 0.3 mL of adiponitrile (ADN) was added to the reactor for use as an internal standard. The reactor was then agitated at 700 rpm and a flow of HCN (10% in valeronitrile) to the reactor was initiated at 0.5 mL / hour. After 4 hours, the reactor was allowed to cool to room temperature, and any residual HCN was removed from the reactor with flowing nitrogen. Samples were obtained from the reactor and product analysis was performed by gas chromatography.

example 2

[0035] Example 1 was repeated except that 3PN was the olefin evaluated.

example 3

[0037] Example 1 was repeated except that magnesium oxide was used as the catalyst.

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PUM

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Abstract

The present invention relates to an improved process for addition of hydrogen cyanide across olefins and, in particular, to the use of a specific aluminum oxide to catalyze the reaction. The aluminum oxide catalyst must have total alkali metal and / or alkaline earth metal content, measured in the form of alkali metal oxide and / or alkaline earth metal oxide, of less than 3,000 ppm by weight.

Description

technical field [0001] The present invention relates to an improved process for the addition of hydrogen cyanide (HCN) to alkenes, and in particular to the use of specific alumina catalyzed reactions. Background technique [0002] Commercial processes for the production of adiponitrile (an important intermediate in the manufacture of nylon-6,6 and related products) typically involve 3-pentenenitrile (3PN) or 4-pentenenitrile (4PN) in nickel ( 0) Stage of hydrocyanation in the presence of a catalyst to form adiponitrile. It is known that cis-2-pentenenitrile (c2PN) is formed as a by-product during such hydrocyanation. The formation of c2PN represents a loss of adiponitrile yield in the process. Furthermore, c2PN accumulation during hydrocyanation reactions is undesirable since it behaves as a catalyst poison. However, the removal of c2PN is not straightforward. It can be separated from unreacted 3PN by distillation. Alternatively, it can be removed by reaction with alkal...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C253/10C07C255/09
CPCC07C253/10C07C255/09B01J21/066B01J23/02B01J23/04B01J23/06B01J23/10B01J27/236B01J27/26B01J31/06C07C255/22
Inventor 威廉·J·坦三世苏德希尔·N·V·K·阿基
Owner INVISTA TEXTILES (U K) LTD