CN104711124A - Soybean lecithin processing technology - Google Patents

Soybean lecithin processing technology Download PDF

Info

Publication number
CN104711124A
CN104711124A CN201310672926.0A CN201310672926A CN104711124A CN 104711124 A CN104711124 A CN 104711124A CN 201310672926 A CN201310672926 A CN 201310672926A CN 104711124 A CN104711124 A CN 104711124A
Authority
CN
China
Prior art keywords
phosphatide
water
concentrated
oil
lecithin
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
CN201310672926.0A
Other languages
Chinese (zh)
Inventor
尚庆光
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201310672926.0A priority Critical patent/CN104711124A/en
Publication of CN104711124A publication Critical patent/CN104711124A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/74Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

Landscapes

  • Fats And Perfumes (AREA)

Abstract

The invention relates to a soybean lecithin processing technology. The technology comprises the following steps: (1) pre-heating: removing impurities from machine-squeezed crude oil and then pre-heating to a temperature of 80 DEG C; (2) adding water to carry out hydration, wherein the water addition amount is determined according to the content of lecithin in oil and the change situation of lecithin particles formed during the heating process; (3) concentrating: sucking hydrated lecithin oil residue into a vacuum concentrating cylinder, and heating under stirring; (4) discoloring the lecithin: discoloring the concentrated lecithin so as to produce high-quality lecithin. The provided technology can produce high quality soybean lecithin to fulfill the requirements and needs of people in daily life, and moreover, the technology is simple and convenient and is worthy to promote and use.

Description

A kind of soybean phospholipid processing technology
Technical field
The present invention relates to a kind of soybean phospholipid processing technology, belong to health food processing technique field.
Background technology
Phosphatide is the polar material that a class has particular physiological function, is a kind of tensio-active agent, is the main moiety of people, animal and plant cell membranes in tissue; Natural phosphatide has very high nutritive value and good processing characteristics, phosphatide is not only the important composition composition of people, animal and plant cell membranes in tissue, to absorption, the transhipment of fat, to lipid acid, particularly unsaturated fatty acids plays an important role, soybean phospholipid is the product extracted from the oil foot of production soybean oil, and the content in soybean is 1.2% to 3.2%; The ester that it is made up of glycerine, lipid acid, choline or cholamine, can be dissolved in grease and non-polar solvent; Soybean phospholipid outward appearance is light yellow to light brown powder or translucent viscous liquid material, is slightly with beany, is partially soluble in water, be dissolved in benzene, chloroform, ether, sherwood oil, be insoluble in acetone and acetic ester.
Summary of the invention
The object of the present invention is to provide a kind of soybean phospholipid processing technology, to prepare soybean phospholipid better, supply people edible health.
To achieve these goals, technical scheme of the present invention is as follows:
A kind of soybean phospholipid processing technology, comprises following process:
(1) preheating: after machine squeezing crude oil removes impurity after filtration, pre-heating temperature elevation to 80 degree Celsius;
(2) water hydratable is added: according to the content of phosphatide in oil, and the changing conditions determination amount of water of the phosphatide micelle formed in heat-processed, general amount of water is about 3.5 times of phospholipids content; The water level boiling water added, also have working concentration about about 0.7% hot common salt aqueous solution; Add water speed phosphatide absorption speed and determining, phosphatide water suction then adds water soon and wants fast; Phosphatide water suction is slow, then add water and also want slow; When just having started to add water, stirring velocity wants fast, generally rests between 80 to 100 rpms, and after 20 to 30 minutes, phosphatide has large stretch of cotton-shaped particles generation, slows down by stirring velocity, continuation stirring 20 to 30 minutes, can staticly settle; Upper strata edible vegetable oil after precipitation, after dehydration, is refining oil, and lower floor's oil foot then needs could obtain finished product phosphatide after concentrated;
(3) concentrated: by the phosphatide oil foot after aquation, suck in concentrated cylinder through vacuum, heat up simultaneously and stir; When insulation 80 degrees centigrade, the moisture in vacuum removal phosphatide; In time stirring fluid phosphatide slightly mercerising produces, namely show that moisture meets the requirements, now moisture content is greatly about about 5%, and the phosphatide after concentrated is brown semi solid, namely can be used for food, medicine and industrial;
(4) decolouring of phosphatide: when high-quality phosphatide produced by needs, through concentrated phosphatide, also needs to carry out desolventing technology; The method of desolventing technology: in concentrated cylinder, adds concentrated phosphatide amount 2% to 2.5%, and concentration is the hydrogen peroxide of about 30%, under the condition of 50 degrees Celsius, stops vacuum-sealing decolouring 1 hour; Then start vacuum pump, be warmed up to 70 degrees centigrade, dewater, until the phosphatide color after not having water droplet to decolour in point water vat is light brown.
This beneficial effect of the invention is: the technology of the present invention can the good soybean phospholipid of manufacture mass, meets life requirement and the needs of people, be conducive to the life requirement of people and edible needs, and method is simple and convenient, is applicable to promoting the use of.
Embodiment
Below in conjunction with embodiment, the specific embodiment of the present invention is described, better to understand the present invention.
Embodiment
A kind of soybean phospholipid processing technology, comprises following process:
(1) preheating: after machine squeezing crude oil removes impurity after filtration, pre-heating temperature elevation to 80 degree Celsius;
(2) water hydratable is added: according to the content of phosphatide in oil, and the changing conditions determination amount of water of the phosphatide micelle formed in heat-processed, general amount of water is about 3.5 times of phospholipids content; The water level boiling water added, also have working concentration about about 0.7% hot common salt aqueous solution; Add water speed phosphatide absorption speed and determining, phosphatide water suction then adds water soon and wants fast; Phosphatide water suction is slow, then add water and also want slow; When just having started to add water, stirring velocity wants fast, generally rests between 80 to 100 rpms, and after 20 to 30 minutes, phosphatide has large stretch of cotton-shaped particles generation, slows down by stirring velocity, continuation stirring 20 to 30 minutes, can staticly settle; Upper strata edible vegetable oil after precipitation, after dehydration, is refining oil, and lower floor's oil foot then needs could obtain finished product phosphatide after concentrated;
(3) concentrated: by the phosphatide oil foot after aquation, suck in concentrated cylinder through vacuum, heat up simultaneously and stir; When insulation 80 degrees centigrade, the moisture in vacuum removal phosphatide; When slightly mercerising produces stirring fluid phosphatide, namely show that moisture meets the requirements; Now moisture content is greatly about about 5%, and the phosphatide after concentrated is brown semi solid, namely can be used for food, medicine and industrial;
(4) decolouring of phosphatide: when high-quality phosphatide produced by needs, through concentrated phosphatide, also needs to carry out desolventing technology; The method of desolventing technology: in concentrated cylinder, adds concentrated phosphatide amount 2% to 2.5%, and concentration is the hydrogen peroxide of about 30%, under the condition of 50 degrees Celsius, stops vacuum-sealing decolouring 1 hour; Then start vacuum pump, be warmed up to 70 degrees centigrade, dewater, until the phosphatide color after not having water droplet to decolour in point water vat is light brown.
The above is the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications are also considered as protection scope of the present invention.

Claims (1)

1. a soybean phospholipid processing technology, is characterized in that: comprise following process:
(1) preheating: after machine squeezing crude oil removes impurity after filtration, pre-heating temperature elevation to 80 degree Celsius;
(2) water hydratable is added: according to the content of phosphatide in oil, and the changing conditions determination amount of water of the phosphatide micelle formed in heat-processed; General amount of water is 3.5 times of phospholipids content; The water level boiling water added, or working concentration is about the hot common salt aqueous solution of about 0.7%; When just having started to add water, stirring velocity wants fast, generally rests between 80 to 100 rpms, and after 20 to 30 minutes, phosphatide has large stretch of cotton-shaped particles generation, slows down by stirring velocity, continuation stirring 20 to 30 minutes, can staticly settle; Upper strata edible vegetable oil after precipitation, after dehydration, is refining oil; Lower floor's oil foot then needs could obtain finished product phosphatide after concentrated;
(3) concentrated: by the phosphatide oil foot after aquation, suck in concentrated cylinder through vacuum, heat up simultaneously and stir; When insulation 80 degrees centigrade, the moisture in vacuum removal phosphatide; When slightly mercerising produces stirring fluid phosphatide, namely show that moisture meets the requirements; Now moisture content is greatly about about 5%;
(4) decolouring of phosphatide: when high-quality phosphatide produced by needs, through concentrated phosphatide, also needs to carry out desolventing technology; The method of desolventing technology: in concentrated cylinder, adds concentrated phosphatide amount 2% to 2.5%, and concentration is the hydrogen peroxide of about 30%, under the condition of 50 degrees Celsius, stops vacuum-sealing decolouring 1 hour; Then start vacuum pump, be warmed up to 70 degrees centigrade, dewater, until the phosphatide color after not having water droplet to decolour in point water vat is light brown.
CN201310672926.0A 2013-12-12 2013-12-12 Soybean lecithin processing technology Pending CN104711124A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310672926.0A CN104711124A (en) 2013-12-12 2013-12-12 Soybean lecithin processing technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310672926.0A CN104711124A (en) 2013-12-12 2013-12-12 Soybean lecithin processing technology

Publications (1)

Publication Number Publication Date
CN104711124A true CN104711124A (en) 2015-06-17

Family

ID=53410844

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310672926.0A Pending CN104711124A (en) 2013-12-12 2013-12-12 Soybean lecithin processing technology

Country Status (1)

Country Link
CN (1) CN104711124A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104987945A (en) * 2015-06-23 2015-10-21 广西科技大学 Technical method for lowering viscosity of rapeseed oil residues by means of ultrasonic assistance
CN111533765A (en) * 2020-05-26 2020-08-14 内蒙古铂贝曼科技有限公司 Low-iron powder phospholipid
CN111548862A (en) * 2020-05-26 2020-08-18 内蒙古铂贝曼科技有限公司 Self-aggregating aqueous phospholipid
CN111574556A (en) * 2020-05-26 2020-08-25 内蒙古铂贝曼科技有限公司 Normal pressure continuous drying method for preparing solid phospholipid from water-containing phospholipid
CN111574557A (en) * 2020-05-26 2020-08-25 内蒙古铂贝曼科技有限公司 Vacuum continuous drying method for preparing solid phospholipid from water-containing phospholipid
CN111595112A (en) * 2020-05-26 2020-08-28 内蒙古铂贝曼科技有限公司 Preparation method of powdered phospholipid
CN111592938A (en) * 2020-05-26 2020-08-28 内蒙古铂贝曼科技有限公司 Low-iron water-containing phospholipid
CN111970932A (en) * 2018-03-06 2020-11-20 邦吉全球创新有限责任公司 Process for decolorizing phospholipid compositions

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104987945A (en) * 2015-06-23 2015-10-21 广西科技大学 Technical method for lowering viscosity of rapeseed oil residues by means of ultrasonic assistance
CN104987945B (en) * 2015-06-23 2018-04-03 广西科技大学 A kind of technical method that rapeseed oil residue viscosity is reduced using ultrasonic assistant
CN111970932A (en) * 2018-03-06 2020-11-20 邦吉全球创新有限责任公司 Process for decolorizing phospholipid compositions
CN111595112A (en) * 2020-05-26 2020-08-28 内蒙古铂贝曼科技有限公司 Preparation method of powdered phospholipid
CN111574556A (en) * 2020-05-26 2020-08-25 内蒙古铂贝曼科技有限公司 Normal pressure continuous drying method for preparing solid phospholipid from water-containing phospholipid
CN111574557A (en) * 2020-05-26 2020-08-25 内蒙古铂贝曼科技有限公司 Vacuum continuous drying method for preparing solid phospholipid from water-containing phospholipid
CN111548862A (en) * 2020-05-26 2020-08-18 内蒙古铂贝曼科技有限公司 Self-aggregating aqueous phospholipid
CN111592938A (en) * 2020-05-26 2020-08-28 内蒙古铂贝曼科技有限公司 Low-iron water-containing phospholipid
CN111533765A (en) * 2020-05-26 2020-08-14 内蒙古铂贝曼科技有限公司 Low-iron powder phospholipid
CN111533765B (en) * 2020-05-26 2021-11-23 内蒙古铂贝曼科技有限公司 Low-iron powder phospholipid
CN111574556B (en) * 2020-05-26 2022-02-08 内蒙古铂贝曼科技有限公司 Normal pressure continuous drying method for preparing solid phospholipid from water-containing phospholipid
CN111592938B (en) * 2020-05-26 2022-11-22 内蒙古铂贝曼科技有限公司 Low-iron water-containing phospholipid
CN111574557B (en) * 2020-05-26 2023-05-12 内蒙古铂贝曼科技有限公司 Vacuum continuous drying method for preparing solid phospholipid from aqueous phospholipid

Similar Documents

Publication Publication Date Title
CN104711124A (en) Soybean lecithin processing technology
CN102191128B (en) Method for preparing edible idesia oil
CN103859067B (en) A kind of nutrition Rice oil and production method thereof
CN102524429B (en) Method for refining nutritional millet bran oil
CN103834472A (en) Refining process for cosmetic camellia oil
CN102766524B (en) Method for squeezing edible tea seed oil at normal temperature
CN102676291A (en) Method for extracting antarctic krill grease and separating biological active substance
CN103881807A (en) Soybean unsaturated fatty acid extraction method
CN103981021A (en) Method for refining krill oil from Antarctic krill powder
CN105331439A (en) Method for extracting soybean blend oil and compound protein by using aqueous enzymatic method
CN103382413B (en) Refining process for reducing content of MCPD in tea seed oil
CN107586591A (en) A kind of preparation method of fish oil
CN102839049A (en) Technical method of deacidifying vegetable fat
CN101185466B (en) Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining
CN104232300A (en) Method for refining mixed oil of microalgae DHA oil
CN104889141A (en) Comprehensive utilization method for soybean dregs
CN110862862A (en) Method for simultaneously preparing xanthoceras sorbifolia Bunge oil and xanthoceras sorbifolia Bunge protein by aqueous enzymatic method
CN104311595A (en) Method for recovering soybean phosphatide from soybean oil
CN102669661A (en) Shark liver oil soft capsule and production method thereof
CN101787328A (en) Extraction method of Salicorne seed oil
CN101617720A (en) Preparation method of plant oil from blackberry seeds
CN102766525B (en) Method for squeezing tea seed oil at normal temperature
CN103351946B (en) Preparation method of moderately processed ARA (Arachidonic acid) microalgae grease
CN105695079A (en) Method for preparing high-quality rapeseed blend oil
CN105154223A (en) Rice bran oil

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20150617

WD01 Invention patent application deemed withdrawn after publication