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1190-22-3

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1190-22-3 Usage

Chemical Properties

Clear colourless liquid

Check Digit Verification of cas no

The CAS Registry Mumber 1190-22-3 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 1,1,9 and 0 respectively; the second part has 2 digits, 2 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 1190-22:
(6*1)+(5*1)+(4*9)+(3*0)+(2*2)+(1*2)=53
53 % 10 = 3
So 1190-22-3 is a valid CAS Registry Number.
InChI:InChI=1/C4H8Cl2/c1-4(6)2-3-5/h4H,2-3H2,1H3/t4-/m1/s1

1190-22-3 Well-known Company Product Price

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  • Aldrich

  • (D59003)  1,3-Dichlorobutane  99%

  • 1190-22-3

  • D59003-25G

  • 1,310.40CNY

  • Detail

1190-22-3SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 10, 2017

Revision Date: Aug 10, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,3-Dichlorobutane

1.2 Other means of identification

Product number -
Other names 1,3-DICHLOROBUTANE

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:1190-22-3 SDS

1190-22-3Relevant articles and documents

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Nuretdinova,O.N. et al.

, (1972)

-

1,4-dichlorobutane production technology

-

Paragraph 0026-0036, (2019/10/23)

The invention provides a 1,4-dichlorobutane production technology. The technology comprises the following steps: 1, preparing 1,4-butanediol, triphosgene, a catalyst and a reaction kettle with an elevated tank, wherein a molar ratio of the 1,4-butanediol to triphosgene is 1:(0.66-0.70); 2, pumping 60-90% of the 1,4-butanediol weighed in step 1 into the reaction kettle, heating the 1,4-butanediol to 40-70 DEG C, adding the triphosgene, and performing stirring until complete dissolving is achieved; 3, pumping the 1,4-butanediol remained the after step 1 and the catalyst into the elevated tank ofthe reaction kettle, performing dissolving until clarity in the reaction kettle, slowly dropwise adding a solution obtained in the elevated tank into the reaction kettle, and collecting a gas generated by a reaction; and 4, lowering the temperature to 0-30 DEG C after the reaction is finished, standing for layering, and collecting the obtained lower yellowish oily liquid to complete the preparation of 1,4-dichlorobutane. The 1,4-dichlorobutane production technology has the advantages of simplicity in operation, mild reaction conditions, greenness, no pollution, low carbon, environmental protection, and realization of large-scale production.

Absolute rate constants for abstraction of chlorine from three chlorinating agents by alkyl radicals

Tanko, James M.,Blackert, Joseph F.

, p. 1775 - 1780 (2007/10/03)

Using the cyclopropylcarbinyl -> homoallyl free radical clock, absolute rate constants for the abstraction of chlorine from molecular chlorine (Cl2), tert-butyl hypochlorite (ButOCl) and N-chloro-3,3-dimethylglutarimide (NCG) have been determined (kCl2=3.0*1010, kButOCl=2.6*109 and kNCG=3.6*107, all in 1 mol-1s-1).

Versatility of Zeolites as Catalysts for Ring or Side-Chain Aromatic Chlorinations by Sulfuryl Chloride

Delaude, Lionel,Laszlo, Pierre

, p. 5260 - 5269 (2007/10/02)

Zeolites catalyze chlorination of aromatics by sulfuryl chloride SO2Cl2.It is possible by an appropriate choice of the catalyst to effect at will, with very high selectivity, either the ring or the side-chain chlorination.Zeolite ZF520 is the choice catalyst for the former, because of its high Broensted acidity.Zeolite NaX (13X) is a fine catalyst for the latter, free-radical chlorination; the reaction is best effected in the presence of a light source; the catalyst can be reused many times with no loss in activity.Both reaction modes, the ionic (ring chlorination)and the radical (side-chain substitution), are likely to occur outside of the channel network in the microporous solid.The effects of various experimental factors - such as the nature of the solvent, the reaction time and temperature, the Broensted acidity of the solid support, the presence of radical inhibitors, and the quantity of catalysts - were investigated.The procedures resulting from this study are very easy to implement in practice and are quite effective.

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