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Separation method and equipment of protein from starch sugar liquefied solution

A technology for protein separation and separation equipment, which is applied in the field of separation and removal of proteins in starch sugar liquefaction liquid, can solve problems such as no disclosure, and achieve the effects of reducing damage, improving equipment life, and saving the consumption of decolorization and filtering auxiliary materials.

Active Publication Date: 2014-03-05
玉锋实业集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since this patent only generally provides a kind of gravity sieve equipment, as for the specific technical information of this gravity sieve, as well as the supporting equipment and its pretreatment process required for the separation of proteins by gravity sieve, they are not disclosed.
However, if there is no proper pretreatment process, so that the starch sugar liquid has a suitable concentration, viscosity, ph value, and suitable stratification, etc., it is impossible to truly realize protein separation by gravity sieve in the industry.

Method used

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  • Separation method and equipment of protein from starch sugar liquefied solution
  • Separation method and equipment of protein from starch sugar liquefied solution
  • Separation method and equipment of protein from starch sugar liquefied solution

Examples

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Effect test

Embodiment 1

[0051] Referring to the accompanying drawings, the protein separation equipment in the starch sugar liquefaction liquid of the present invention comprises successively connected laminar flow tank systems, protein separation storage tanks 2 and protein separation screens 3 in its structure; the laminar flow tank system includes 4 sequentially connected According to the flow of the feed liquid, the top of the front laminar flow tank 1 is connected with the bottom end of the rear laminar flow tank 1 through a pipeline; The feed port 21 is connected, the top of the protein separation storage tank 2 is provided with an overflow port 22, the overflow port 22 is set opposite to the feed port 21, and the protein separation screen 3 is arranged below the overflow port 22 to accept the Feed liquid; the volume of the protein separation storage tank 2 is not less than the 10-minute flow rate of the feed liquid, and the protein separation storage tank 2 is equal to the protein separation sc...

Embodiment 2

[0057] Referring to accompanying drawing, utilize above-mentioned equipment to carry out the method for protein separation in starch sugar liquefaction liquid, its step comprises:

[0058] A, the preparation of starch gelatinization liquid: starch slurry is adjusted to 19.5 Baume degree, regulate pH value 5.5-5.8 with edible sodium carbonate simultaneously, then add the BiotherMosizeFC α-amylase that Biother Green Company produces, the addition amount is every Add 425 ml of α-amylase to 1 ton of starch dry matter, and then liquefy the starch milk at 105-110°C through a high-temperature jet liquefier to obtain starch gelatinization liquid;

[0059] B. The starch gelatinization liquid is processed by the laminar flow tank system to obtain a primary liquefaction liquid: the starch gelatinization liquid flows through four serially connected laminar flow tanks 1 in sequence, and the starch gelatinization liquid flows from the bottom end of each laminar flow tank 1 to the top Outflo...

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Abstract

The invention discloses separation equipment of protein from a starch sugar liquefied solution, which structurally comprises a laminar flow tank system, a protein separation storage tank, and a protein separation sieve which are sequentially connected, wherein the laminar flow tank system comprises 2-6 laminar flow tanks connected in series, and the laminar flow tank at the end is connected with a feed port at the bottom end of the protein separation storage tank through a pipeline; and an overflow port is arranged at the top of the protein separation storage tank, and the protein separation sieve is arranged below the overflow port. The method for separating the protein from the starch sugar liquefied solution by utilizing the equipment comprises the following steps of: preparing a starch pasting liquid; B, treating the starch pasting liquid by the laminar flow tank system to obtain a primary liquefied solution; C, the primary liquefied solution being overflowed from the laminar flow tanks into the protein separation storage tank for layering; and D, the primary liquefied solution being overflowed from the protein separation storage tank to the surface of the protein separation sieve for protein separation. According to the method, a series of targeted treatment of the starch sugar liquefied solution is conducted, and the efficient separation of the protein from the starch sugar liquefied solution is realized by reasonably setting the sieve mesh size and the sieve mesh density of the protein separation sieve.

Description

technical field [0001] The invention relates to the separation and removal technology of protein in starch sugar liquefaction liquid. Background technique [0002] Under the action of α-amylase, the starch is hydrolyzed from a large molecule to a relatively small molecule (dextrin), and the protein in the starch will be freed, because the protein in the liquefaction liquid is basically soluble, and the formed protein is flocculated. shape and high viscosity. At present, most starch sugar manufacturers adopt the method of not treating the liquefied liquid, and then pass through pre-coating vacuum filter or plate and frame filtering equipment to remove it after saccharification. This not only often blocks the liquefied liquid cooling equipment (plate heat exchanger, etc.), shortens the life of the cooling equipment, but also consumes more glucoamylase and filter aids (diatomaceous earth, perlite, activated carbon), etc. There are also manufacturers who use a plate and frame ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07K1/34C07K14/415C13K1/08C12P19/14
Inventor 耿风玲戎永新赵建强
Owner 玉锋实业集团有限公司
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