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57843-53-5

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  • N,n,n',n'-tetrakis(2-hydroxypropyl)hexanediamide

    Cas No: 57843-53-5

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57843-53-5 Usage

Flammability and Explosibility

Nonflammable

Check Digit Verification of cas no

The CAS Registry Mumber 57843-53-5 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 5,7,8,4 and 3 respectively; the second part has 2 digits, 5 and 3 respectively.
Calculate Digit Verification of CAS Registry Number 57843-53:
(7*5)+(6*7)+(5*8)+(4*4)+(3*3)+(2*5)+(1*3)=155
155 % 10 = 5
So 57843-53-5 is a valid CAS Registry Number.

57843-53-5SDS

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 N,N,N',N'-tetrakis(2-hydroxypropyl)hexanediamide

1.2 Other means of identification

Product number -
Other names EINECS 260-982-3

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:57843-53-5 SDS

57843-53-5Synthetic route

hexanedioic acid dimethyl ester
627-93-0

hexanedioic acid dimethyl ester

diisopropanolamine
110-97-4

diisopropanolamine

N,N,N',N'-tetrakis(β-hydroxypropyl)adipamide
57843-53-5

N,N,N',N'-tetrakis(β-hydroxypropyl)adipamide

Conditions
ConditionsYield
Stage #1: diisopropanolamine With potassium methanolate at 100℃; for 1h; Green chemistry;
Stage #2: hexanedioic acid dimethyl ester for 2h; Reagent/catalyst; Green chemistry;
89.8%
With potassium methanolate at 100℃; for 4h; Reagent/catalyst;157.3 g

57843-53-5Downstream Products

57843-53-5Relevant articles and documents

Method for preparing N, N, N

-

Paragraph 0018-0041, (2021/11/27)

The method comprises the following steps: (N) adding an excess of diisopropanolamine and an alkaline catalyst into a reaction kettle, then dropwise adding dimethyl adipate N, and preparing N, 1, N N (2): The temperature in the reaction kettle was decreased to the set temperature, and the neutralized acid was added dropwise or batchwise to the reaction kettle under a vacuum condition to neutralize excess diisopropanolamine, and dehydration was performed simultaneously. (3): After completion of the neutralization, a solvent was added to the reaction kettle, and the crystals were stirred and then filtered to separate the diisopropanolamine sulfate. The filtrate was separated off by distillation to give a high purity N, N, NTo the method, unreacted diisopropanolamine raw materials are separated through the high-amine ester, the preparation process is simple, the energy consumption is low, and the separated diisopropanolamine salt can be recycled as an industrial raw material.

Preparation method of N,N,N,N'-tetra(beta-hydroxypropyl)adipamide

-

Paragraph 0014-0029, (2019/04/26)

The invention discloses a preparation method of N,N,N,N'-tetra(beta-hydroxypropyl)adipamide, which includes steps of: 1) adding diisopropanol amine, in excessive amount, and an alkaline catalyst to areaction kettle, heating the reaction kettle to 100 +/- 5 DEG C, adding dimethyl adipate, and preparing a N,N,N,N'-tetra(beta-hydroxypropyl)adipamide crude product under vacuum; 2) cooling the N,N,N,N'-tetra(beta-hydroxypropyl)adipamide crude product to preset temperature and adding the dimethyl adipate, and stirring and crystallizing the product; 3) after the crystallization, adding a co-dispersant and fully stirring the product, and at crystalline temperature, performing positive pressure filtration on the crystal slurry to separate a filter cake and a filtrate, and drying the filter cake toobtain a high-purity product. The method can be used for preparing the high-purity N,N,N,N'-tetra(beta-hydroxypropyl)adipamide product at high yield. The solvent is high in boiling point and flash point; so that the crystalline process, compared with a conventional solvent system, is safe and environment-friendly.

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