CN101234953A - Method for synthesizing hexade/octode mixing alcohol polyoxyethylene - Google Patents

Method for synthesizing hexade/octode mixing alcohol polyoxyethylene Download PDF

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Publication number
CN101234953A
CN101234953A CNA2007101648011A CN200710164801A CN101234953A CN 101234953 A CN101234953 A CN 101234953A CN A2007101648011 A CNA2007101648011 A CN A2007101648011A CN 200710164801 A CN200710164801 A CN 200710164801A CN 101234953 A CN101234953 A CN 101234953A
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CN
China
Prior art keywords
octode
hexade
octodecanol
hexadecanol
mixed
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Pending
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CNA2007101648011A
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Chinese (zh)
Inventor
王伟松
王新荣
孟照平
马定连
罗青
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Individual
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Individual
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Priority to CNA2007101648011A priority Critical patent/CN101234953A/en
Publication of CN101234953A publication Critical patent/CN101234953A/en
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Abstract

A synthesizing method of hexadecanol/octodecanol-mixed polyoxyethylene ether belongs to the filed of synthesizing technology of organic compounds. Hexadecanol/octodecanol-mixed polyoxyethylene ether is produced through polymerization of raw materials including mixed hexadecanol/octodecanol and ethylene oxide under the existence of a catalyst. The weight proportion of the mixed hexadecanol/octodecanol and ethylene oxide is 1:0.145-18.6; the catalyst is one of or a mixture containing more than one of solid sodium methylate, methanol solution of sodium methylate, KOH, NaOH, etc, and the addition thereof is 0.05-0.2 weight percent of prepared hexadecanol/octodecanol-mixed polyoxyethylene ether. Through rational determination of technological parameters and conditions such as raw material proportion, catalyst amount, polymerization temperature and time, etc., the method of the invention can have the advantages of mild reaction condition, low equipment requirement and high product yield and, in addition, has no impurity or pollutant production. The product has light color, good appearance, wide adjustable molecular weight range and high mutual modulation effect when in mixed application with products having other properties.

Description

The synthetic method of hexade/octode mixing alcohol polyoxyethylene
Technical field
The present invention relates to a kind of synthetic method of hexade/octode mixing alcohol polyoxyethylene, belong to technical field of organic compound synthesis.
Background technology
Existing 16 or polyoxyethylene octadecanol uses all is single alcohol, the alcohol mixture product is seldom arranged, its single use properties has limited use range.
Summary of the invention
It is reasonable to the purpose of this invention is to provide a kind of technology, have better use properties the synthetic method of hexade/octode mixing alcohol polyoxyethylene.
The present invention is the synthetic method of hexade/octode mixing alcohol polyoxyethylene, is raw material with 16/18 alcohol mixtures and oxyethane, it is characterized in that carrying out polyreaction and make in the presence of catalyzer; The weight ratio of described 16/18 alcohol mixtures and oxyethane is 1: 0.145~18.6; Described catalyzer is a solid sodium methylate, methanol solution of sodium methylate, and KOH, the mixture of any one or more of NaOH etc., its add-on is 0.05~0.2% of the hexade/octode mixing alcohol polyoxyethylene weight percent that makes.
Described polymeric reaction temperature can be 120~180 ℃.
Described polymerization reaction time can be 5~20 hours.
The molecular weight of described hexade/octode mixing alcohol polyoxyethylene can be 353~3500g/mol.
The present invention compares by the analysis to existing polyether product synthetic method, through optimization design and repetition test research, rationally determined processing parameter and conditions such as proportioning raw materials, catalyst levels, polymeric reaction temperature, time, the reaction conditions gentleness, low for equipment requirements.And the yield height does not have impurity to generate environmental friendliness.The hexade/octode mixing alcohol polyoxyethylene lighter color that makes by the present invention, appearance property is good, the scope of adjustable csa molecule amount is big: hydroxyl value 159.0~27.7mgKOH/g, molecular weight 353~3500g/mol (molecular weight=56110/ hydroxyl value) mixes the intermodulation height that uses with other performance products.Have good emulsification, level dyeing performance, warm viscosity, biological degradability.Product is non-ionic type in alkalescence and neutral medium, be cationic in acidic medium; The levelling agent that is used for acidic complex dye can reduce dye bath sulfuric acid consumption, reduces the fabric strength damage; Also can make neutral dye, the levelling agent of vat dyes, the stripping agent of wool, polyamide fabric etc.
Embodiment
The preparation of reactor before implementing: with distilled water the 2.5L autoclave is washed several times earlier, till clean, dried reactor, standby after being cooled to 50~80 ℃.
Embodiment 1:
Add 600g 16 alcohol mixtures and 1.1g powdery sodium methylate in reactor, be warmed up to 130 ℃, vacuum hydro-extraction added oxyethane 346g after 1 hour, 150 ℃ react completely after, cool to 80 ℃ of dischargings.
Embodiment 2:
Add 400g 16 alcohol mixtures and 1.1g solid KOH in reactor, be warmed up to 130 ℃, vacuum hydro-extraction added oxyethane 1046g after 1 hour, 150 ℃ react completely after, cool to 80 ℃ of dischargings.
Embodiment 3:
Add the mixture (preparing burden by 1: 1 ratio) of 200g 16 alcohol mixtures and 1.1g powdery sodium methylate and NaOH in reactor, be warmed up to 130 ℃, vacuum hydro-extraction is after 1 hour, adding oxyethane 875g, 150 ℃ react completely after, cool to 80 ℃ of dischargings.
Embodiment 4:
Add the mixture (preparing burden by 1: 1 ratio) of 60g sorbyl alcohol and 1.0g solid KOH and NaOH in reactor, be warmed up to 130 ℃, vacuum hydro-extraction is after 1 hour, adding oxyethane 759g, 150 ℃ react completely after, cool to 80 ℃ of dischargings.
The prepared hexade/octode mixing alcohol polyoxyethylene of the various embodiments described above after tested, index is as follows:
Embodiment Hydroxyl value (mgKOH/g) Molecular weight (g/mol)
1 136.8 410
2 59.6 940
3 40.4 1390
4 16.0 3500
The present invention is not limited to the foregoing description, when practical application, can require and use occasion according to the different performance of hexade/octode mixing alcohol polyoxyethylene, select the different proportionings in the foregoing description, or the different proportionings except that the various embodiments described above, but all do not limit the scope of the invention in any form.

Claims (4)

1, a kind of synthetic method of hexade/octode mixing alcohol polyoxyethylene is a raw material with 16/18 alcohol mixtures and oxyethane, it is characterized in that carrying out polyreaction and make in the presence of catalyzer; The weight ratio of described 16/18 alcohol mixtures and oxyethane is 1: 0.145~18.6; Described catalyzer is a solid sodium methylate, methanol solution of sodium methylate, and KOH, the mixture of any one or more of NaOH, its add-on is 0.05~0.2% of the hexade/octode mixing alcohol polyoxyethylene weight percent that makes.
2, by the synthetic method of the described hexade/octode mixing alcohol polyoxyethylene of claim 1, it is characterized in that described polymeric reaction temperature is 120~180 ℃.
3, by the synthetic method of the described hexade/octode mixing alcohol polyoxyethylene of claim 1, it is characterized in that described polymerization reaction time is 5~20 hours.
4, by the synthetic method of the described hexade/octode mixing alcohol polyoxyethylene of claim 1, the molecular weight that it is characterized in that described hexade/octode mixing alcohol polyoxyethylene is 353~3500g/mol.
CNA2007101648011A 2007-12-21 2007-12-21 Method for synthesizing hexade/octode mixing alcohol polyoxyethylene Pending CN101234953A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2007101648011A CN101234953A (en) 2007-12-21 2007-12-21 Method for synthesizing hexade/octode mixing alcohol polyoxyethylene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2007101648011A CN101234953A (en) 2007-12-21 2007-12-21 Method for synthesizing hexade/octode mixing alcohol polyoxyethylene

Publications (1)

Publication Number Publication Date
CN101234953A true CN101234953A (en) 2008-08-06

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2007101648011A Pending CN101234953A (en) 2007-12-21 2007-12-21 Method for synthesizing hexade/octode mixing alcohol polyoxyethylene

Country Status (1)

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CN (1) CN101234953A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103044674A (en) * 2012-12-14 2013-04-17 江苏省海安石油化工厂 Preparation method of leveling agent
CN107151317A (en) * 2017-04-24 2017-09-12 东莞市隆海新材料科技有限公司 A kind of alkyd paint adds water auxiliary agent and preparation method thereof
CN109400449A (en) * 2018-09-29 2019-03-01 中国日用化学研究院有限公司 A method of preparing alkyl phenyl alcohol polyoxyethylene ether

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103044674A (en) * 2012-12-14 2013-04-17 江苏省海安石油化工厂 Preparation method of leveling agent
CN107151317A (en) * 2017-04-24 2017-09-12 东莞市隆海新材料科技有限公司 A kind of alkyd paint adds water auxiliary agent and preparation method thereof
CN109400449A (en) * 2018-09-29 2019-03-01 中国日用化学研究院有限公司 A method of preparing alkyl phenyl alcohol polyoxyethylene ether
CN109400449B (en) * 2018-09-29 2022-06-10 中国日用化学研究院有限公司 Method for preparing alkyl phenyl alcohol polyoxyethylene ether

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Open date: 20080806