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A kind of processing method of gluten water

A treatment method and technology for gluten water, applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problem of poor soaking effect product quality, gluten protein powder yield Not high problems, to achieve the effect of easy handling, small size, and improved productivity

Active Publication Date: 2015-08-19
COFCO GROUP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to overcome the low yield of gluten protein powder obtained by the gluten water treatment method of the prior art and directly recycle the process water to the corn soaking process and germ and fiber washing process, the corn The soaking effect and the defects of product quality deterioration provide a process water that can increase the yield of gluten protein powder and meet the reuse requirements at the same time, that is, the high-quality process water can be directly reused to improve the cycle of process water Treatment of Gluten Water Recycled to Corn Steep Effect for Corn Steep Process and Recycled to Germ, Fiber Wash Process for Starch Wash Effect

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] This example is used to illustrate the treatment method of gluten water provided by the present invention.

[0030] (1) According to 350m 3The total flow of / h sends dilute gluten water (concentration of protein-containing solids is 1.7% by weight) on average into two disc separators and concentrates dilute gluten water simultaneously (total of dilute gluten water) Feed amount is 350m 3 / h, the feeding volume of each unit is 175m 3 / h, the rotating speed of centrifugation is 3400 rpm respectively, and the temperature of centrifugation is 45 ℃), the total flow that obtains the first aqueous phase is 200m 3 / h (the content of protein-containing solids in the first aqueous phase is 0.3% by weight) and the total flow of the first dense phase is 150m 3 / h (the dense phase flow rate of each separator is 75m 3 / h) (the solids content containing protein in the first dense phase is 3.8% by weight); 150m 3 / h, the rotating speed of centrifugation is 3500 rev / min, the temper...

Embodiment 2

[0033] This example is used to illustrate the treatment method of gluten water provided by the present invention.

[0034] (1) According to 380m 3 The total flow of / h sends dilute gluten water (concentration of protein-containing solids is 1.5% by weight) on average into two disc separators and concentrates dilute gluten water simultaneously (total volume of dilute gluten water) Feed amount is 380m 3 / h, the feeding volume of each unit is 190m 3 / h, the rotating speed of centrifugation is 3300 rev / min respectively, the temperature of centrifugation is 45 ℃), the total flow that obtains the first aqueous phase is 234m 3 / h (the content of protein-containing solids in the first aqueous phase is 0.28% by weight) and the total flow of the first dense phase is 146m 3 / h (the dense phase flow rate of each separator is 73m 3 / h) (the solid content of protein in the first dense phase is 3.5% by weight); 146m 3 / h, the rotating speed of centrifugation is 3400 rev / min, the temper...

Embodiment 3

[0037] This example is used to illustrate the treatment method of gluten water provided by the present invention.

[0038] (1) According to 360m 3 The total flow of / h sends dilute gluten water (concentration of protein-containing solids is 1.6% by weight) on average into two disc separators and concentrates dilute gluten water simultaneously (total volume of dilute gluten water) Feed amount is 360m 3 / h, the feeding volume of each unit is 180m 3 / h, the rotational speed of centrifugation is 3300 rev / min respectively, the temperature of centrifugation is 45 ℃), the total flow that obtains the first aqueous phase is 231m 3 / h (the content of protein-containing solids in the first aqueous phase is 0.31% by weight) and the total flow of the first dense phase is 129m 3 / h (the dense phase flow rate of each separator is 64.5m 3 / h) (the content of protein-containing solids in the first dense phase is 3.9% by weight); the first dense phase is sent to a disc separator again for s...

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PUM

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Abstract

A treatment method of gluten water. The method comprises condensation of gluten water. A method for condensation of gluten water includes the steps of: (1) carrying out a first condensation on gluten water to obtain a first concentrated phase and a first water phase, wherein conditions of the first condensation enable an obtained first water phase to contain less than 0.3 wt% of solid containing protein; and (2) carrying out a second condensation on the first concentrated phase to obtain a second concentrated phase and a second water phase, wherein conditions of the second condensation enable the second concentrated phase to contain more than 10 wt% of solid containing protein. The product of the second concentrated phase (concentrated gluten) obtained by the method of the invention has similar or higher concentration compared with that of a concentrate obtained by a prior art; water quality of the obtained first water phase is obvious superior to that of the water phase obtained by one-time condensation of the prior art; and volume of the second water phase that requires a second treatment is smaller, and the treatment is easier.

Description

technical field [0001] The invention relates to a treatment method for gluten water. Background technique [0002] The extraction process of starch is the process of separating the main components of corn kernels. There are two types of separation of the components of corn kernels: dry method and wet method, and the main separation operation is grinding. Therefore, there are dry grinding and wet grinding. . [0003] Wet milling is a common process in the current corn starch industry. It is mainly the process of crushing, degerming, fine grinding and sieving of soaked corn to separate the germ and fiber slag to obtain crude starch milk. After the starch is extracted through the grinding and sieving process, the obtained starch milk is still coarse starch milk, which still contains a large amount of protein-containing solids and soluble substances, and the concentration of the powder slurry is relatively thin, which needs to be refined and concentrated to provide for final pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08B30/10C02F9/02A23K1/00
Inventor 岳国君郝小明罗虎艾咏平徐兆勇娄新建郜培鲁艳秋高占争王旭
Owner COFCO GROUP
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