CN107011450A - A kind of production method of high-purity octenylsuccinate potato starch ester - Google Patents
A kind of production method of high-purity octenylsuccinate potato starch ester Download PDFInfo
- Publication number
- CN107011450A CN107011450A CN201710261179.XA CN201710261179A CN107011450A CN 107011450 A CN107011450 A CN 107011450A CN 201710261179 A CN201710261179 A CN 201710261179A CN 107011450 A CN107011450 A CN 107011450A
- Authority
- CN
- China
- Prior art keywords
- starch
- water
- ethanol
- purity
- content
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B31/00—Preparation of derivatives of starch
- C08B31/02—Esters
- C08B31/04—Esters of organic acids, e.g. alkenyl-succinated starch
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Cosmetics (AREA)
- Medicinal Preparation (AREA)
Abstract
A kind of high-purity octenylsuccinate potato starch ester and its production method, are mainly included the following steps that:Starch processing, esterification, isolate and purify and the step such as cold nebulization.The present invention's is particular in that:Esterification is carried out during concentration, the esterifying efficiency of starch is higher;Meanwhile, the ethanol water gradually reduced using ethanol content carries out washing purifying, can lift product purity.
Description
Technical field
The invention belongs to technical field of modified starch, and in particular to octenyl amber is efficiently prepared as raw material using farina
The method of amber acid-starch ester.
Background technology
Starch octenylsuccinate is a major class converted starch, and only one in grocery trade is allowed to use in China
Plant, i.e. starch octenyl succinate anhydride.Starch octenyl succinate anhydride be white powder, nontoxic, free from extraneous odour, can be molten in the hot water
Solution, can dissolve, transparent liquid has good stability in acid-base solution after being handled through pre-gelatinized in cold water.Starch
After being acted on through octenyl succinic acid anhydride, the viscosity of starch is improved, and the anti-aging stability of cooking material is improved.Sometimes, this derivative
Thing can also improve the texture feature of starch.
Starch octenylsuccinate is best suitable for the wall material of microencapsulation, and it can substitute gum arabic, can be to food
Product dispensing such as essence, pigment, vitamin, mineral matter, enzyme preparation and microorganism carry out embedding treatment.
The content of the invention
React gentle it is an object of the invention to provide one kind, separate octenylsuccinate potato efficient, easy to operate
The preparation method of starch ester, the microencapsulation wall available for liposoluble substance.
A kind of high-purity octenylsuccinate potato starch ester and its production method, comprise the following steps:
(1) starch is handled:Take second alcohol and water, in mass ratio 2:1 mixing, is then uniformly sprayed on farina, until
The ethanol content of starch is 10-12%, carries out x-ray irradiation processing, exposure rate is 8-10KGy/h, and irradiation time is 12-14
Minute;
(2) esterification:Using the starch after step (1) processing as raw material, add water until the water content of starch is 70-
72%, using octenyl succinic acid anhydride and alcohol mixeding liquid as esterifying agent, octenyl succinic acid anhydride addition is the 12- of starch quality
14%, when starch water content is reduced to 9-11% during esterification, course of reaction are carried out during temperature is 62-65 DEG C of concentration reactor
Stop concentration reaction, obtain starch octenyl succinate anhydride;
(3) isolate and purify:3 washings are carried out to starch octenyl succinate anhydride and are centrifuged;3 washings:Adopt for 1st time
Washed with ethanol content 16-18% ethanol water, the 2nd time is to be entered using ethanol content 7-8% ethanol water
Row washing, the 3rd time is to drink water washing;
(4) cold nebulization:The starch octenyl succinate anhydride isolated and purified is added water, adjusts pH to 3.9-4.1, is sprayed
It is dried to obtain product;The EAT of spray drying is 168-170 DEG C, and leaving air temp is 73-75 DEG C.
Step (2) described esterifying agent:The mass ratio of octenyl succinic acid anhydride and ethanol is 1:7.0-7.2.
Advantage of the invention is that:
1st, in farina processing procedure, ethanol water is uniformly sprayed on farina, when carrying out X-ray processing
With good collaboration cavitation, while ethanol volatilization can allow farina porous.
2nd, esterification is carried out in concentration reactor, esterification, control concentration speed is carried out during concentration
And reaction speed, the esterifying efficiency of starch greatly improves.
3rd, after starch esterification reaction, the ethanol water gradually reduced using ethanol content carries out washing purifying, can be very
The octenyl succinic acid anhydride of residual is adsorbed well, increases product purity, while not destroying the stability of starch ester product.
Embodiment
Embodiment one
(1) starch is handled:Take second alcohol and water, in mass ratio 2:1 mixing, is then uniformly sprayed on farina, until
The ethanol content of starch is 12%, carries out x-ray irradiation processing, and exposure rate is 10KGy/h, and irradiation time is 12 minutes;
(2) esterification:Using above-mentioned starch as raw material, add water until the water content of starch is 72%, with octenyl succinic
Acid anhydrides and alcohol mixeding liquid are esterifying agent, and the mass ratio of octenyl succinic acid anhydride and ethanol is 1:- 7.2, octenyl succinic acid anhydride
Addition is the 14% of starch quality, and starch contains in esterification, course of reaction is carried out during temperature is 65 DEG C of concentration reactors
Water stops concentration reaction when being reduced to 11%, obtain starch octenyl succinate anhydride;
(3) isolate and purify:3 washings are carried out to starch ester and are centrifuged, the 1st time water-soluble using the ethanol of ethanol content 18%
Liquid is washed, and the 2nd time is the ethanol water for using ethanol content 8%, and the 3rd time is to drink water washing;
(4) cold nebulization:The starch octenyl succinate anhydride isolated and purified is added water into tune pH to 4.0, is spray-dried
Obtain product;The EAT of spray drying is 170 DEG C, and leaving air temp is 75 DEG C.
Through test and detect, 32% octenylsuccinate potato starch ester embedding 45%DHA, embedding rate reach 95% with
On, stability is good, and shelf life was up to more than 10 months.
Claims (2)
1. a kind of production method of high-purity octenylsuccinate potato starch ester, it is characterised in that comprise the following steps:
(1) starch is handled:Take second alcohol and water, in mass ratio 2:1 mixing, is then uniformly sprayed on farina, until starch
Ethanol content be 10-12%, carry out x-ray irradiation processing, exposure rate is 8-10KGy/h, irradiation time is 12-14 points
Clock;
(2) esterification:Using step (1) processing after starch as raw material, add water until starch water content be 70-72%, with
Octenyl succinic acid anhydride is esterifying agent with alcohol mixeding liquid, and octenyl succinic acid anhydride addition is the 12-14% of starch quality,
Temperature is dense to carry out stopping when starch water content is reduced to 9-11% in esterification, course of reaction in 62-65 DEG C of concentration reactor
Contracting reaction, obtains starch octenyl succinate anhydride;
(3) isolate and purify:3 washings are carried out to starch octenyl succinate anhydride and are centrifuged;3 washings:Use second 1st time
Alcohol content 16-18% ethanol water is washed, and the 2nd time is to be washed using ethanol content 7-8% ethanol water
Wash, the 3rd time is to drink water washing;
(4) cold nebulization:The starch octenyl succinate anhydride isolated and purified is added water, adjusts pH to 3.9-4.1, is spray-dried
Obtain product;The EAT of spray drying is 168-170 DEG C, and leaving air temp is 73-75 DEG C.
2. a kind of production method of high-purity octenylsuccinate potato starch ester according to claim 1, its feature
It is:Step (2) described esterifying agent:The mass ratio of octenyl succinic acid anhydride and ethanol is 1:7.0-7.2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710261179.XA CN107011450A (en) | 2017-04-20 | 2017-04-20 | A kind of production method of high-purity octenylsuccinate potato starch ester |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710261179.XA CN107011450A (en) | 2017-04-20 | 2017-04-20 | A kind of production method of high-purity octenylsuccinate potato starch ester |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107011450A true CN107011450A (en) | 2017-08-04 |
Family
ID=59447554
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710261179.XA Pending CN107011450A (en) | 2017-04-20 | 2017-04-20 | A kind of production method of high-purity octenylsuccinate potato starch ester |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107011450A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106279450A (en) * | 2016-08-30 | 2017-01-04 | 李郑松 | A kind of preparation method of porous starch octenyl succinate anhydride |
-
2017
- 2017-04-20 CN CN201710261179.XA patent/CN107011450A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106279450A (en) * | 2016-08-30 | 2017-01-04 | 李郑松 | A kind of preparation method of porous starch octenyl succinate anhydride |
Non-Patent Citations (3)
Title |
---|
于新等: "《天然食品添加剂》", 31 March 2014, 中国轻工业出版社 * |
扶雄等: "《食用变性淀粉》", 31 March 2016, 中国轻工业出版社 * |
童丹等: "《马铃薯变性淀粉加工技术》", 31 October 2015, 武汉大学出版社 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101336905A (en) | Production method of alpha-linolenic acid microcapsule | |
CN103641837B (en) | A kind of method of chlorophyll copper sodium extracting from silkworm excrement | |
CN108642105A (en) | A kind of method of enzyme process inclusion tributyrin | |
CN103783225A (en) | Black buckwheat tea and preparation method thereof | |
CN101773244A (en) | Method for preparing water-soluble functional red yeast rice and product thereof | |
CN108770948A (en) | It is a kind of using maltodextrin and cyclodextrin as the tributyrin microcapsules of wall material | |
CN105348165A (en) | Method for extracting astaxanthin yeast, yeast extract and glucan from yeast | |
CN107011450A (en) | A kind of production method of high-purity octenylsuccinate potato starch ester | |
CN103059147B (en) | The method of starch stearate prepared by a kind of tapioca (flour) | |
CN105533011A (en) | Ginkgo fruit tea production process | |
CN107141362A (en) | Ocentyl succinic cornstarch ester prepared by a kind of synchronous concentration reaction method | |
CN107098983A (en) | A kind of production method of high added value ocentyl succinic Lotus Root Starch ester | |
CN106967177A (en) | Ocentyl succinic wheaten starch ester prepared by a kind of vacuum infrared collaboration processing | |
CN104341223A (en) | Organic-inorganic compound fertilizer produced from earthworm amino acids through chelating process, and its preparation method | |
CN104905274A (en) | Embedding and diluting method for L-selenium methyl selenocysteine | |
CN107141361A (en) | A kind of production method of high esterification ocentyl succinic water caltrop starch ester | |
CN107141363A (en) | A kind of high efficiency preparation method of ocentyl succinic rice starch ester | |
CN106977612A (en) | A kind of porous tapioca starch sodium octenyl succinate | |
CN113081869B (en) | Haematococcus pluvialis astaxanthin microcapsule and preparation method thereof | |
CN107048290A (en) | A kind of preparation method of nutrient fruit cream | |
CN103385434A (en) | Production method for instant kudzuvine root starch based on structural micro-modification | |
CN105249399A (en) | Preparation method of solid lactic acid | |
CN102140143B (en) | Method for extracting chitin from crab shells | |
CN104193836A (en) | Production process for medicinal hydroxypropyl starch | |
CN104273433A (en) | Method for processing preboiled rice through composite bio-enzyme fermentation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170804 |