Movatterモバイル変換


[0]ホーム

URL:


CN105461764A - Method for refining alkyl polyglycoside - Google Patents

Method for refining alkyl polyglycoside
Download PDF

Info

Publication number
CN105461764A
CN105461764ACN201510911751.3ACN201510911751ACN105461764ACN 105461764 ACN105461764 ACN 105461764ACN 201510911751 ACN201510911751 ACN 201510911751ACN 105461764 ACN105461764 ACN 105461764A
Authority
CN
China
Prior art keywords
alkyl polyglycoside
fatty alcohol
distillation
purification
polyglycoside
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201510911751.3A
Other languages
Chinese (zh)
Inventor
周志强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SUZHOU HUAZHOU TAPES CO Ltd
Original Assignee
SUZHOU HUAZHOU TAPES CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SUZHOU HUAZHOU TAPES CO LtdfiledCriticalSUZHOU HUAZHOU TAPES CO Ltd
Priority to CN201510911751.3ApriorityCriticalpatent/CN105461764A/en
Publication of CN105461764ApublicationCriticalpatent/CN105461764A/en
Pendinglegal-statusCriticalCurrent

Links

Classifications

Landscapes

Abstract

The invention discloses a method for refining alkyl polyglycoside. The method comprises the following steps: 1) rough processing: taking glucose and fatty alcohol to be processed into crude alkyl polyglycoside under the action of an acid catalyst at the temperature of 90-100 DEG C; 2) degassing: evaporating alkyl polyglycoside obtained through rough processing on a film evaporator, and removing impurities in crude alkyl polyglycoside in a gaseous manner to obtain secondary refined alkyl polyglycoside; 3) degreasing: distilling secondary refined alkyl polyglycoside by using a molecular distillation method, removing fatty alcohol in secondary refined alkyl polyglycoside first, and collecting left finished alkyl polyglycoside, wherein the distilled fatty alcohol can be recycled again through cooling and used for preparing crude alkyl polyglycoside in the step 1; 4) fine processing: conducting second molecular distillation on obtained finished alkyl polyglycoside, rising the distillation temperature, and removing various types of alcohol in finished alkyl polyglycoside so as to obtain refined alkyl polyglycoside. According to the method, the operation is simple, the prepared alkyl polyglycoside is high in purity, good in quality and high in yield, and the production process is environment-friendly and pollution-free.

Description

A kind of process for purification of alkyl polyglycoside
Technical field
The present invention relates to energy field, be specifically related to a kind of process for purification of alkyl polyglycoside.
Background technology
Alkyl polyglycoside is also alkyl glycoside, APG for short, synthesized by renewable resources natural fat alcohol and glucose, it is the more comprehensive new non-ionic surfactants of a kind of performance, have the characteristic of conventional nonionic and anion surfactant concurrently, having high surface, good ecological security and intermiscibility, is internationally recognized first-selection " green " functional surfactant.
The alkyl polyglycoside produced in prior art is due to the difference of production technique, and cause the quality of alkyl polyglycoside product also just to differ, Problems existing is also relatively many, as purity is poor, the impurity mixed is more, and processing step is many, troublesome poeration, the synthetic ratio of product is low, causes the wasting of resources larger.
Summary of the invention
The object of the present invention is to provide a kind of simple to operate, process for purification of producing the alkyl polyglycoside that product purity is high, quality good, product yield is large, production technique is environment friendly and pollution-free.
Technical scheme of the present invention is, a kind of process for purification of alkyl polyglycoside, comprises the steps:
1) rough processing: get glucose and fatty alcohol an acidic catalyst act on the temperature of 90-110 DEG C under be processed into alkyl polyglycoside crude product;
2) degassed: the alkyl polyglycoside of roughing to be placed on thin-film evaporator and to evaporate, the impurity in alkyl polyglycoside crude product is removed with gaseous form, obtain time fine work alkyl polyglycoside;
3) degreasing: use the method for molecular distillation to distill to secondary fine work alkyl polyglycoside, fatty alcohol in secondary fine work alkyl polyglycoside is removed in advance, leave finished product alkyl polyglycoside, the fatty alcohol distilled is reclaimed by cooling and is reused for producing of alkyl polyglycoside crude product in step 1;
4) precision work: the alkyl polyglycoside finished product obtained is carried out to second time molecular distillation and raises distillation temperature, makes all kinds of alcohol in alkyl polyglycoside finished product remove, obtains alkyl polyglycoside fine work.
In a preferred embodiment of the present invention, in described step 1, an acidic catalyst is Witco 1298 Soft Acid.
In a preferred embodiment of the present invention, in described step 2, the vaporization temperature of thin-film evaporator is 135-170 DEG C.
In a preferred embodiment of the present invention, the distillation temperature of described step 3 Middle molecule distillation is 155-200 DEG C.
In a preferred embodiment of the present invention, the distillation temperature raised in described step 4 is 30-50 DEG C.
Of the present invention is a kind of process for purification of alkyl polyglycoside, and the present invention is simple to operate, produce that product purity is high, quality good, product yield is large, production technique is environment friendly and pollution-free.
Embodiment
Below preferred embodiment of the present invention is described in detail, can be easier to make advantages and features of the invention be readily appreciated by one skilled in the art, thus more explicit defining is made to protection scope of the present invention.
Of the present invention is a kind of process for purification of alkyl polyglycoside, comprises the steps:
1) rough processing: get glucose and fatty alcohol an acidic catalyst act on the temperature of 90-110 DEG C under be processed into alkyl polyglycoside crude product;
2) degassed: the alkyl polyglycoside of roughing to be placed on thin-film evaporator and to evaporate, the impurity in alkyl polyglycoside crude product is removed with gaseous form, obtain time fine work alkyl polyglycoside;
3) degreasing: use the method for molecular distillation to distill to secondary fine work alkyl polyglycoside, fatty alcohol in secondary fine work alkyl polyglycoside is removed in advance, leave finished product alkyl polyglycoside, the fatty alcohol distilled is reclaimed by cooling and is reused for producing of alkyl polyglycoside crude product in step 1;
4) precision work: the alkyl polyglycoside finished product obtained is carried out to second time molecular distillation and raises distillation temperature, makes all kinds of alcohol in alkyl polyglycoside finished product remove, obtains alkyl polyglycoside fine work.
Further, in described step 1, an acidic catalyst is Witco 1298 Soft Acid.
Further, in described step 2, the vaporization temperature of thin-film evaporator is 135-170 DEG C.
Further, the distillation temperature of described step 3 Middle molecule distillation is 155-200 DEG C.
Further, the distillation temperature raised in described step 4 is 30-50 DEG C.
Of the present invention is a kind of process for purification of alkyl polyglycoside, and by the way, the present invention is simple to operate, produce that product purity is high, quality good, product yield is large, production technique is environment friendly and pollution-free.
The foregoing is only the specific embodiment of the present invention; but protection scope of the present invention is not limited thereto; any those of ordinary skill in the art are in the technical scope disclosed by the present invention; the change can expected without creative work or replacement, all should be encompassed within protection scope of the present invention.Therefore, the protection domain that protection scope of the present invention should limit with claims is as the criterion.

Claims (5)

CN201510911751.3A2015-12-112015-12-11Method for refining alkyl polyglycosidePendingCN105461764A (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CN201510911751.3ACN105461764A (en)2015-12-112015-12-11Method for refining alkyl polyglycoside

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CN201510911751.3ACN105461764A (en)2015-12-112015-12-11Method for refining alkyl polyglycoside

Publications (1)

Publication NumberPublication Date
CN105461764Atrue CN105461764A (en)2016-04-06

Family

ID=55599972

Family Applications (1)

Application NumberTitlePriority DateFiling Date
CN201510911751.3APendingCN105461764A (en)2015-12-112015-12-11Method for refining alkyl polyglycoside

Country Status (1)

CountryLink
CN (1)CN105461764A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN1041599A (en)*1988-10-051990-04-25亨克尔西合股份公司The method that directly prepares alkylglycoside
CN1315327A (en)*2000-03-302001-10-03中国石油天然气股份有限公司吉林石化分公司研究院Dealcoholizing process for preparing alkylglucoside
CN102786559A (en)*2011-05-192012-11-21扬州晨化科技集团有限公司Preparation method of octyl glucopyranoside
CN103319549A (en)*2013-07-182013-09-25扬州大学Synthetic method of alkyl glycoside

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN1041599A (en)*1988-10-051990-04-25亨克尔西合股份公司The method that directly prepares alkylglycoside
CN1315327A (en)*2000-03-302001-10-03中国石油天然气股份有限公司吉林石化分公司研究院Dealcoholizing process for preparing alkylglucoside
CN102786559A (en)*2011-05-192012-11-21扬州晨化科技集团有限公司Preparation method of octyl glucopyranoside
CN103319549A (en)*2013-07-182013-09-25扬州大学Synthetic method of alkyl glycoside

Similar Documents

PublicationPublication DateTitle
RU2594159C2 (en)Method of separating ethylene glycol and 1,2-butanediol
CN103772148A (en)Novel method for separating mixture of ethylene glycol and 1, 2-butanediol by adopting azeotropic distillation and extraction coupling technologies
CN101792216A (en)Resource recycling method of glyphosate mother liquor
CN109851586A (en)The purification process of propylene oxide
CN104768908A (en) Method for preparing high-purity anhydrous sugar alcohol by sequentially combining thin-film distillation and short-path distillation
CN114181044A (en)Preparation method of high-purity ditrimethylolpropane
CN103467513A (en)Preparation method of triallyl phosphate
CN105218305A (en)A kind of byproduct recovery process of synthetic gas preparing ethylene glycol
CN105754704A (en)Method for increasing yield of base oil by adopting extracted solution for secondary extraction
CN108587764A (en)Base oil after being recycled to waste lubricating oil carries out refined method
CN103664516A (en)Ethanediol separation process for preparing ethanediol from synthetic gas
CN105461764A (en)Method for refining alkyl polyglycoside
CN108517237B (en)Method for producing environment-friendly cutting fluid by using illegal cooking oil
CN107915837B (en)A kind of production technology of fatty alcohol polyoxyethylene ether sulfate
CN101544537A (en)Method for producing low carbon chemical ethanol from C6 sugar alcohol
CN103214436A (en)Long carbon chain glycol diglycidyl ether and preparation method thereof
CN106986751B (en)Method for extracting crude phenol from phenol oil
CN104592167A (en)Method for preparing phenyl glycidyl ether
CN104086412A (en)Process method for producing butyl oleate by using rape oil fatty acid
CN111559950A (en)Method for separating cyclopentane and 2, 2-dimethylbutane
CN103288584B (en)Reformed arene C 10the processing method of middle extraction high-purity beta-methylnaphthalene
CN205893167U (en)Waste oil NMP solvent refining integrated system
CN105218307A (en)Octyl alconyl produce in light constituent residual night aldehydes add hydrogen retrieval separation method
CN104230658A (en)New method for separating ethanediol and 1, 2-pentanediol from corn fermentation liquid
CN115141236A (en) A kind of separation method of sophorolipid

Legal Events

DateCodeTitleDescription
C06Publication
PB01Publication
C10Entry into substantive examination
SE01Entry into force of request for substantive examination
RJ01Rejection of invention patent application after publication
RJ01Rejection of invention patent application after publication

Application publication date:20160406


[8]ページ先頭

©2009-2025 Movatter.jp