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49562-37-0

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49562-37-0 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 49562-37-0 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 4,9,5,6 and 2 respectively; the second part has 2 digits, 3 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 49562-37:
(7*4)+(6*9)+(5*5)+(4*6)+(3*2)+(2*3)+(1*7)=150
150 % 10 = 0
So 49562-37-0 is a valid CAS Registry Number.
InChI:InChI=1/C4H9NO5S/c1-4(2,3(5)6)10-11(7,8)9/h1-2H3,(H2,5,6)(H,7,8,9)

49562-37-0SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 17, 2017

Revision Date: Aug 17, 2017

1.Identification

1.1 GHS Product identifier

Product name (1-amino-2-methyl-1-oxopropan-2-yl) hydrogen sulfate

1.2 Other means of identification

Product number -
Other names 2-methyl-2-sulphatopropionamide

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:49562-37-0 SDS

49562-37-0Relevant articles and documents

Process for chemical reactions involving cyanohydrins

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Page/Page column 5-6; 8, (2008/06/13)

The present invention provides a method for minimizing the decomposition of cyanohydrins in exothermic chemical reactions involving cyanohydrins. The method comprises providing a reaction medium and reactants to a tubular reactor having internal mixing means, mixing the reaction medium and reactants to form a homogenous reaction mixture, removing heat from the reaction process and reacting the reactants to produce a mixed product having a bulk temperature. The method may further comprise cooling the reaction medium to a temperature from 1-10° C. cooler than the bulk temperature of the mixed product prior to providing the reaction medium to the tubular reactor.

Process for methacrylic acid and methacrylic acid ester production

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Page/Page column 3; Sheet 1, (2008/06/13)

Provided herein are improved methods for producing methacrylic acid and methacrylate esters using combined or “integrated” processing steps including integrated hydrolysis, integrated cracking systems, and combinations thereof. In one embodiment, other aspects of an methacrylic acid and methacrylate ester production trains are integrated. Also provided are methods to purify crude methacrylic acid streams to form glacial methacrylic acid that is at least 95% pure.

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