CN104711124A - Soybean lecithin processing technology - Google Patents
Soybean lecithin processing technology Download PDFInfo
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- 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
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- phosphatide
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- oil
- lecithin
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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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
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.
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CN201310672926.0A CN104711124A (en) | 2013-12-12 | 2013-12-12 | Soybean lecithin processing technology |
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CN201310672926.0A CN104711124A (en) | 2013-12-12 | 2013-12-12 | Soybean lecithin processing technology |
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Cited By (8)
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 |
-
2013
- 2013-12-12 CN CN201310672926.0A patent/CN104711124A/en active Pending
Cited By (13)
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 |
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