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2-[2-[2-(dimethylamino) ethoxy]ethoxy]-ethanol is a chemical with a specific purpose. Lookchem provides you with multiple data and supplier information of this chemical.

2741-30-2

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2741-30-2 Usage

+ State

Liquid

+ Color

Colorless

+ Odor

Faint, sweet

Chemical Class

Glycol ethers

Usage

Solvent in various applications (e.g. paints, coatings, cleaning products)

Synthesis

+ Reaction of dimethylamine with ethylene oxide
+ Reaction of resulting dimethylaminoethanol with ethylene oxide

Toxicity

Low acute toxicity
+ Prolonged exposure to high levels may cause irritation to eyes, skin, and respiratory system

Handling and Safety

Handle with appropriate precautions and follow safety guidelines.

Check Digit Verification of cas no

The CAS Registry Mumber 2741-30-2 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 2,7,4 and 1 respectively; the second part has 2 digits, 3 and 0 respectively.
Calculate Digit Verification of CAS Registry Number 2741-30:
(6*2)+(5*7)+(4*4)+(3*1)+(2*3)+(1*0)=72
72 % 10 = 2
So 2741-30-2 is a valid CAS Registry Number.

2741-30-2SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 19, 2017

Revision Date: Aug 19, 2017

1.Identification

1.1 GHS Product identifier

Product name 2-[2-[2-(dimethylamino)ethoxy]ethoxy]ethanol

1.2 Other means of identification

Product number -
Other names Kaolizer 23NP

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:2741-30-2 SDS

2741-30-2Relevant academic research and scientific papers

Coupling of Bioreaction and Separation via Novel Thermosensitive Ionic Liquids Applied in the Baker’s Yeast-Catalyzed Reduction of Ethyl 2-oxo-4-phenylbutyrate

Feng, Lifang,Shi, Yugang,Tian, Shiyi,Yang, Yuexi

, (2020/05/16)

The use of baker’s yeast to reduce ethyl 2-oxo-4-phenylbutyrate (EOPB) in conventional biphasic systems is hindered by low productivities due to mass transfer resistance between the biocatalyst and the substrate partitioned into two different phases. To overcome the limitation, a new reaction-separation coupling process (RSCP) was configured in this study, based on the novel thermosensitive ionic liquids (ILs) with polyoxyethylene-tail. The solubility of ILs in common solvents was investigated to configure the unique thermosensitive ionic liquids–solvent biphasic system (TIBS) in which the reduction was performed. [(CH3)2N(C2H5)(CH2CH2O)2H][PF6] (c2) in 1,2-dimethoxyethane possesses the thermosensitive function of homogeneous at lower temperatures and phase separating at higher temperatures. The phase transformation temperature (PTT) of the mixed system of c2/1,2-dimethoxyethane (v/v, 5:18) was about 33 ?C. The bioreaction takes place in a “homogeneous” liquid phase at 30 ?C. At the end of each reduction run, the system temperature is increased upon to the PTT, while c2 is separated from 1,2-dimethoxyethane with turning the system into two phases. The enantiomeric excesses (e.e.) of ethyl (R)-2-hydroxy-4-phenylbutyrate ((R)-EHPB) increased about 25~30% and the yield of ethyl-2-hydroxy-4-phenylbutyrate (EHPB) increased 35% in TIBS, compared with the reduction in 1,2-dimethoxyethane. It is expected that the TIBS established in this study could provide many future opportunities in the biocatalysis.

Integrated preparation method of DMAE and DMAEE in microtubule reactor

-

Paragraph 0035-0036; 0042, (2018/03/23)

The invention discloses an integrated preparation method of DMAE and DMAEE in a microtubule reactor. The method comprises respectively feeding ethylene oxide and an aqueous solution of dimethylamine and water as a catalyst into a micro-tube reactor through a pump according to a mole ratio of ethylene oxide to dimethylamine oo 1-2: 1, setting a reaction temperature in the micro-tube reactor to 60-90 DEG C and pressure to 1.3+/-0.2 Pa and controlling standing time of the materials in the micro-tube reactor in 15-90s, wherein the efflux from the micro-tube reactor is an aqueous solution of DMAE and DMAEE. The method has the advantages of high atomic economy, good reaction selectivity, mild reaction conditions, short reaction time, simple catalyst and simple product separation.

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