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2-(2-hydroxyethoxy)ethyl acrylate is a chemical compound that is commonly used in the production of various commercial products such as adhesives, coatings, and paints. It is a clear, colorless liquid with a slight odor, and is soluble in water. 2-(2-hydroxyethoxy)ethyl acrylate is known for its ability to enhance the flexibility, adhesion, and durability of coatings and adhesives. It is also used as a raw material in the synthesis of polymers and resins.
Used in Adhesive Industry:
2-(2-hydroxyethoxy)ethyl acrylate is used as a component in adhesive formulations for its ability to improve the flexibility and adhesion properties of the final product.
Used in Coating Industry:
2-(2-hydroxyethoxy)ethyl acrylate is used as a raw material in the production of coatings to enhance their durability and flexibility.
Used in Paint Industry:
2-(2-hydroxyethoxy)ethyl acrylate is used in paint formulations to improve the adhesion and durability of the paint on various surfaces.
Used in Polymer and Resin Synthesis:
2-(2-hydroxyethoxy)ethyl acrylate is used as a monomer in the synthesis of polymers and resins, contributing to the development of materials with specific properties for various applications.
It is important to handle and use 2-(2-hydroxyethoxy)ethyl acrylate with caution as it can cause skin and eye irritation, and may be harmful if ingested or inhaled in large quantities. Appropriate safety measures and protective equipment should be used when working with this chemical compound.

13533-05-6

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13533-05-6 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 13533-05-6 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 1,3,5,3 and 3 respectively; the second part has 2 digits, 0 and 5 respectively.
Calculate Digit Verification of CAS Registry Number 13533-05:
(7*1)+(6*3)+(5*5)+(4*3)+(3*3)+(2*0)+(1*5)=76
76 % 10 = 6
So 13533-05-6 is a valid CAS Registry Number.
InChI:InChI=1/C7H12O4/c1-6(7(9)10)2-4-11-5-3-8/h8H,1-5H2,(H,9,10)/p-1

13533-05-6SDS

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-hydroxyethoxy)ethyl prop-2-enoate

1.2 Other means of identification

Product number -
Other names 2-Propenoic acid,2-(2-hydroxyethoxy)ethyl ester

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:13533-05-6 SDS

13533-05-6Downstream Products

13533-05-6Relevant academic research and scientific papers

Phosphate cross-linking agent and preparation method thereof, phosphate-based cross-linked gel polymer electrolyte and preparation method and application thereof

-

Paragraph 0047-0048; 0052, (2020/08/17)

According to the invention, the safety of the battery can be improved based on introduction of phosphate into the gel polymer electrolyte, , the adjustable flexibility is improved by introduction of aPEO chain segment, and the stability and the polymerization capability are improved by introduction of acrylate; thus, further research is carried out on the basis of the prior art, the polyfunctional phosphate cross-linking agent is obtained and is applied to the preparation of the phosphate-based cross-linked gel polymer electrolyte, so the cross linking agent can be copolymerized with other functional monomers to synthesize gel polymer electrolyte; the gel polymer electrolyte has the advantages of simple and convenient preparation method, high ionic conductivity, high thermal stability andgood electrochemical stability, the assembled sodium ion battery has good cycling stability and high-temperature performance, and the phosphate-based gel polymer electrolyte with high safety is provided for quasi-solid sodium/lithium ion batteries.

Process for the production of hydroxyalkyl (meth)acrylates

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Page/Page column 2-3, (2009/09/05)

The present invention relates to a process for producing high purity hydroxyalkyl (meth)acrylates. Specifically, the present invention relates to an improved process which can commercially and advantageously yield high purity hydroxyalkyl (meth)acrylates from (meth)acrylic acid and alkylene oxides.

A process for the production of hydroxyalkyl (meth)acrylates

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Page/Page column 3-4, (2008/12/07)

The present invention relates to a process for producing high purity hydroxyalkyl (meth)acrylates. Specifically, the present invention relates to an improved process which can commercially and advantageously yield high purity hydroxyalkyl (meth)acrylates from (meth)acrylic acid and alkylene oxides.

PROCESSES FOR PRODUCING HYDROXYALKYL (METH)ACRYLATE

-

, (2008/06/13)

Processes for producing a hydroxyalkyl(meth)acrylate which comprise reacting (meth)acrylic acid with an alkylene oxide in the presence of a catalyst. A first process is characterized in that the amount of the acid ingredient is kept, on calculation, at 0.010 or more in terms of molar ratio to the catalyst present in the liquid reaction mixture and that the liquid reaction mixture from which the hydroxyalkyl (meth) acrylate has been distilled off is used in the subsequent reaction. A second process is characterized in that a dialkylene glycol mono(meth)acylate is supplied to the reaction system to cause the dialkyleneglycol mono(meth)acylate to coexist in the liquid reaction mixture.

PROCESSES FOR PRODUCING HYDROXYALKYL (METH)ACRYLATE

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Page/Page column 24--27; 34-37, (2008/06/13)

Processes for producing a hydroxyalkyl (meth)acrylate which comprise reacting (meth)acrylic acid with an alkylene oxide in the presence of a catalyst. A first process is characterized in that the amount of the acid ingredient is kept, on calculation, at 0.010 or more in terms of molar ratio to the catalyst present in the liquid reaction mixture and that the liquid reaction mixture from which the hydroxyalkyl (meth)acrylate has been distilled off is used in the subsequent reaction. A second process is characterized in that a dialkylene glycol mono(meth)acrylate is supplied to the reaction system to cause the dialkylene glycol mono(meth)acrylate to coexist in the liquid reaction mixture.

Production process for hydroxyalkyl (meth) acrylate

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Page 11-13, (2008/06/13)

There is disclosed a novel production process for a hydroxyalkyl (meth)acrylate in which: the diffusion of harmful substances due to disposal of catalysts can be reduced; and also the amount of the catalyst as used can be greatly saved in the entire production process. This production process comprises the step of carrying out a reaction between (meth)acrylic acid and an alkylene oxide in the presence of a catalyst in order to produce the hydroxyalkyl (meth)acrylate; with the production process being characterized by further comprising the step of recovering the catalyst as has been used for the reaction.

Process for the preparation of hydroxyalkyl(meth)acrylate

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Page 9, (2008/06/13)

The present invention provides: a high-quality hydroxyalkyl (meth)acrylate of which the alkylene glycol di(meth)acrylate content and the acid component content are both low; and its novel production process. The hydroxyalkyl (meth)acrylate, which has a content, in terms of an alkylene glycol di(meth)acrylate as an impurity, of not more than 0.1 weight % and an acid component content of not more than 0.1 weight %, is obtained by a process comprising the step of carrying out a batch reaction between (meth)acrylic acid and an alkylene oxide in the presence of a catalyst in order to produce the hydroxyalkyl (meth)acrylate; with the process making an adjustment as to charging of both raw materials in such a manner that, for, of a time as needed for supplying both raw materials, a supplying time of not less than 40 % of a total supplying time when the raw materials as supplied have a temperature of not lower than 40 °C, the molar ratio of the integrated amount of the alkylene oxide to the integrated amount of the (meth)acrylic acid that have been added to a reactor by then can be more than 1.0.

Formation of macrocyclic ethers by free radical cyclization: Effects of chain length, substituents, and solvents

Philippen, Annie,Degueil-Castaing, Marie,Beckwith, Athelstan L. J.,Maillard, Bernard

, p. 6814 - 6819 (2007/10/03)

Free radical reduction by tributylstannane of w-iodopolyoxaalkyl acrylates derived from tri-, tetra-, penta-, hexa-, and heptaethylene glycols gives mixtures of uncyclized reduction products and macrocyclic ethers formed by endo cyclization. The rate constants for cyclization of the intermediate radicals at 80 °C in benzene were determined under carefully defined conditions to be 15 × 104,13 ×104,5.1 × 104,10 × 104 and 3.6 × 104 s-1, for formation of the 12-, 15-, 18-, 21- and 24-membered rings, respectively. These values indicate that the presence of oxygen atoms in the chains increases the rate by a factor of 10-30 by comparison with the previously reported cyclization of alkenyl species. The rate constants at 80 °C in benzene and the endo/exo ratio for reductive cyclizations of the methacrylate, crotonate, cinnamate, maleate, and fumarate esters of 8-iodo-3,6-dioxaoctanol have been determined. The reduction of the 8-iodo-3,6-dioxaoctyl acrylate in solvents of varying polarity indicated that the cyclization rate has a relatively low solvent dependence.

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