Process for extracting the soyabean oligosaccharides by air-float purification and film integration

A soybean oligosaccharide, membrane integration technology, applied in application, food preparation, food science and other directions, can solve the problems of membrane pore blockage, membrane flux attenuation, environmental pollution and so on

Inactive Publication Date: 2008-10-15
逄镜萍
View PDF0 Cites 16 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because whey protein has a certain viscosity, it is easy to attach to the membrane and form a gel, which will block the membrane pores, resulting in rapid decay of the membrane flux, so that the ultrafiltration cannot be performed normally.
[0007] 2. Membrane cleaning problem
Because soybean whey contains some small molecular proteins with good thermal stability and electrolyte stability, it is impossible to completely separate the protein by filtration, or if the protein is not properly operated, it will cause serious membrane pollution. The problem is that despite various cleaning methods, it is difficult to restore the original flux, and even make the ultrafiltration membrane unable to operate normally
[0008] 3. Environmental pollution problems
Since the protein in the soybean whey is usually separated by a plate and frame filter, a large amount of diatomite must be added as a filter aid, so a large amount of mixed waste of diatomite and protein will be generated during the operation, and cause environmental pollution

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Process for extracting the soyabean oligosaccharides by air-float purification and film integration

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] Example 1: (1) Coagulation by heating. Firstly, the soybean whey liquid is heated to 95° C. under the condition of pH value=4.5, and kept for 20 minutes to denature the whey protein in the whey liquid and coagulate and precipitate.

[0044] (2) Cooling, sending the heated condensed whey liquid into a cooler, and indirect heat exchange with cooling water, so that its temperature drops to 35°C.

[0045] (3) High-speed centrifugation, the cooled whey liquid is sent to a high-speed centrifuge for solid-liquid separation. The solid phase is discharged, and the liquid phase is sent to the flocculation tank for pH adjustment.

[0046] (4) PH value adjustment flocculation, high-speed centrifuge is separated liquid phase, sends into pH value adjustment flocculation tank, under stirring condition of 30 revs / min, add the sodium hydroxide solution of 10% concentration, adjust PH=7 to make milk Albumin flocculation and precipitation.

[0047] (5) Secondary high-speed centrifugatio...

Embodiment 2

[0059] Example 2: (1) Coagulation by heating. Firstly, when the soybean whey liquid is heated to 100° C. under the condition of pH value=4.7, keep it for 30 minutes to denature the whey protein in the whey liquid and coagulate and precipitate.

[0060] (2) Cooling, sending the heated condensed whey liquid into a cooler, and indirect heat exchange with cooling water, so that its temperature drops to 42°C.

[0061] (3) High-speed centrifugation, the cooled whey liquid is sent to a high-speed centrifuge for solid-liquid separation. The solid phase is discharged, and the liquid phase is sent to the flocculation tank for pH adjustment.

[0062] (4) PH value adjustment flocculation, high-speed centrifuge is separated liquid phase, sends into pH value adjustment flocculation tank, under stirring condition of 30 revs / min, add the sodium hydroxide solution of 30% concentration, adjust PH=9 to make milk Albumin flocculation and precipitation.

[0063] (5) Secondary high-speed centrifu...

Embodiment 3

[0075] Example 3: (1) Coagulation by heating. Firstly, when the soybean whey liquid is heated to 98° C. under the condition of pH value=4.0, keep it for 25 minutes to denature the whey protein in the whey liquid and coagulate and precipitate.

[0076] (2) Cooling, sending the heated condensed whey liquid into a cooler, and indirect heat exchange with cooling water, so that its temperature drops to 40°C.

[0077] (3) High-speed centrifugation, the cooled whey liquid is sent to a high-speed centrifuge for solid-liquid separation. The solid phase is discharged, and the liquid phase is sent to the flocculation tank for pH adjustment.

[0078] (4) PH value adjustment flocculation, high-speed centrifuge is separated liquid phase, sends into pH value adjustment flocculation tank, under 30 rev / min stirring conditions, add the sodium hydroxide solution of 25% concentration, adjust PH=8 to make milk Albumin flocculation and precipitation.

[0079] (5) Secondary high-speed centrifugati...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a method for extracting edible oligosaccharides, specifically a method for extracting soybean oligosaccharides from soybean whey liquid by flotation purification and membrane concentration. The method comprises the following steps: thermal coagulation, cooling, high-speed centrifugal separation, pH adjustment and flocculation, secondary high-speed centrifugal separation, flotation separation, first-stage ultrafiltration, decolorization with ion exchange resin, electrodialysis desalination, further desalination with ion exchange resin, second-stage ultrafiltration, reverse osmosis concentration, activated carbon decolorization, diatomite filtration, terminal ultrafiltration and negative-pressure evaporation concentration. The invention has the advantages that: 1. based on the reasonable combination of proper molecular weight cut-off of ultrafiltration membrane and membrane assembly, operation mode and efficient cleaning, the method works continuously and stably for long time; 2. the method realizes the pretreatment by using multi-stage high-efficiency centrifugal separation technique, without using filter aids and producing pollutants, and the separated protein residue can be recycled; and 3. the method has simple process and low equipment and operation costs.

Description

Technical field: [0001] The invention relates to a method for extracting edible oligosaccharides, in particular to a method for extracting soybean oligosaccharides by air flotation purification and membrane integration, and extracting soybean oligosaccharides from soybean whey liquid. Background technique: [0002] Soybean oligosaccharides undergo biological action in the intestines to produce carbon dioxide and other gases, causing uncomfortable flatulence, which cannot be digested and absorbed by the human body, and are considered not to be nutrients for the human body, thus negating the use value of soybean oligosaccharides. However, as people have found through research in recent years, soybean oligosaccharides are not the substances that cause flatulence, but more importantly, they are the best proliferation substances for bifidobacteria that are closely related to the growth of the human body, the normal metabolism of the body, and the prevention and treatment of diseas...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): A23L1/09A23L1/28A23L1/20A23L29/30A23L31/00
Inventor 逄镜萍张菁
Owner 逄镜萍
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products