Treatment method of gluten water
A treatment method and technology for gluten water, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, centrifugal separation water/sewage treatment, etc. The problem of low yield, etc., to achieve the effect of easy handling, small volume, and improved yield
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Embodiment 1
[0043] This example is used to illustrate the treatment method of gluten water provided by the present invention.
[0044] (1) According to 350m 3 The 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 tempe...
Embodiment 2
[0049] This example is used to illustrate the treatment method of gluten water provided by the present invention.
[0050] Gluten water is processed according to the method of Example 1, the difference is:
[0051] (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...
Embodiment 3
[0055] This example is used to illustrate the treatment method of gluten water provided by the present invention.
[0056] Gluten water is processed according to the method of Example 1, the difference is:
[0057] (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 d...
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Abstract
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