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34235-31-9

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34235-31-9 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 34235-31-9 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 3,4,2,3 and 5 respectively; the second part has 2 digits, 3 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 34235-31:
(7*3)+(6*4)+(5*2)+(4*3)+(3*5)+(2*3)+(1*1)=89
89 % 10 = 9
So 34235-31-9 is a valid CAS Registry Number.

34235-31-9SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 16, 2017

Revision Date: Aug 16, 2017

1.Identification

1.1 GHS Product identifier

Product name [3-[[[3-(aminomethyl)phenyl]methylamino]methyl]phenyl]methanamine

1.2 Other means of identification

Product number -
Other names -

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:34235-31-9 SDS

34235-31-9Upstream product

34235-31-9Downstream Products

34235-31-9Relevant articles and documents

Isophthalonitrile (IPN) hydrogenation over K modified Ni-Co supported catalysts: Catalyst characterization and performance evaluation

Liu, Chang,Wang, Tiefeng

, p. 63725 - 63733 (2015/02/19)

The hydrogenation of isophthalonitrile (IPN) to meta-xylylenediamine (m-XDA) is usually catalyzed by the Raney or supported Ni based catalysts in the presence of basic additive. Although the supported catalysts are safer than the Raney Ni catalysts, they have lower selectivity to m-XDA. This work revealed that the acid sites of NiCo/Al2O3 were responsible for the condensation reactions between amines and imines, which were the dominant side reactions. Besides the original acid sites on γ-Al2O3, the loading of Ni-Co introduced new acid sites, which had a greater contribution to the condensation reactions. The K modification significantly enhanced the selectivity to m-XDA by reducing the two kinds of acid sites. Due to the formation mechanism of new acid sites and the K modification mechanism on these sites, both the K loading and K impregnation sequence affected the catalytic performance. When 3.0 wt% K was introduced to NiCo/Al2O3 by co-impregnation (3KNiCo/Al2O3), the catalyst acidity decreased by 82%, and the selectivity to m-XDA increased from 45.5% to 99.9%. The superiority of the optimized catalyst 3KNiCo/Al2O3 was also confirmed when no basic additive was used.

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