Method for preparing protein nitrogen source applicable to fermentation and food by rice

A protein nitrogen, rice technology, applied in food preparation, application, food science and other directions, can solve the problems of limited use, high storage requirements, dark appearance and color of syrup

Inactive Publication Date: 2009-09-23
GUANGZHOU SHUANGQIAO +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of the above-mentioned patents is that the protein in the rice that can be used as an organic nitrogen source and a complete amino acid composition of 8% to 11% is removed. The amount of source is obviously insufficient. Therefore, the inventor of the present application proposed an improved syrup for fermentation in the patent No. ZL200610033796.6 titled "Method for preparing N-containing syrup for fermentation by multi-enzyme method from rice and rice flour". method, also using the protein in rice and rice flour as the nitrogen source for fermentation by means of enzymatic hydrolysis of pro

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] (1) Mix 100 parts by weight of rice flour with water, stir for 0.5 hour, control the slurry concentration to be 30%, adjust the pH value of the slurry to 6.1~6.4, add calcium chloride, Ca 2+ Termamyl 120L high-temperature α-amylase was added in an amount of 0.02 parts by weight, liquefied by continuous spraying at 110°C and heat preservation treatment at 98-100°C for 140min.

[0032] (2) Saccharification: Cool the liquefied liquid to 61°C-63°C, pH value is 4.1-4.5, add 0.02 parts by weight of Dextrozyme DX 1.5X glucoamylase (containing glucoamylase and pullulanase) or 0.04 parts by weight of Dextrozyme GA glucose For amylase, after 10 hours of hydrolysis time, 0.001 parts by weight of NovoCorADL acid lipase was added to carry out synergistic hydrolysis, and the hydrolysis was continued for 60 hours.

[0033] (3) Heating: adjust the pH value of the saccharification solution obtained in step (2) to 5.1-5.4 to the isoelectric point of the protein, heat to 90°C-95°C, keep i...

Embodiment 2

[0040] (1) Mix 100 parts by weight of rice flour with water, stir for 0.5 hour, control the slurry concentration to be 35%, adjust the pH value of the slurry to 6.3~6.4, add calcium chloride, Ca 2+ Termamyl 120L high-temperature α-amylase was added in an amount of 0.1 parts by weight, continuously sprayed at 112°C for liquefaction and kept at 98-100°C for 100 minutes.

[0041] (2) Saccharification: Cool the liquefied liquid to 63°C-65°C, pH value is 4.1-4.5, add 0.002 parts by weight of Dextrozyme DX 1.5X glucoamylase (containing glucoamylase and pullulanase) and 0.1 parts by weight of DextrozymeGA glucose starch Enzyme, after 10 hours of hydrolysis time, add 0.001 weight part of Lipex lipase to carry out synergistic hydrolysis, and continue hydrolysis for 60 hours.

[0042] (3) Heating: adjust the pH value of the saccharification solution obtained in step (2) to 5.1-5.4 to the isoelectric point of the protein, heat to 90°C-95°C, keep it for 20-25 minutes, and let stand to pre...

Embodiment 3

[0049] (1) Mix the rice flour of 100 parts by weight with water, stir for 0.5 hour, control the slurry concentration to be 42%, adjust the pH value of the slurry to 6.1~6.3, add calcium chloride, Ca 2+ The content of Termamyl 2Xα-amylase is about 45mg / kg, adding Termamyl 2Xα-amylase in an amount of 0.8 parts by weight, continuous jet liquefaction at 110°C-112°C and heat preservation treatment at 98°C-100°C for 40min.

[0050] (2) Saccharification: Cool the liquefied liquid to 58°C-62°C, pH value is 5.2-5.4, add 1 weight part of malt, 0.08 weight part of Promozyme D2 debranching enzyme, and 0.09 weight part of Palatase 20000L lipase for synergistic hydrolysis , hydrolyzed for 25 hours.

[0051] (3) Heating: heat the saccharification solution to 90°C-95°C, keep it for 20-25 minutes, and let it stand for filtration;

[0052] (4) Filtering and washing with hot water using a filter machine to reclaim residual sugar to obtain sugar grains;

[0053] (5) Further hydrolysis and separ...

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PUM

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Abstract

The invention discloses a method for preparing organic nitrogen source applicable to fermentation and food by taking rice or rice flour as raw material and carrying out acid process or enzymatic hydrolysis for scum left through pressing and filtering in the process of filtering starch syrup produced in an enzymatic method. The method comprises the following steps: the rice or the rice flour is washed and ground to be milk, calcium chloride and liquefying amylase are added to the milk for consecutive spraying liquefaction to obtain liquefied liquid, various saccharifying enzymes and/or germinating malts and lipase are added to the liquefied liquid for synergistic saccharification, the starch syrup is obtained by filtering saccharified product and refining and concentrating filtrate; the scum obtained by filtering and pressing is washed by water, the residual sugar in the scum is obtained by filtering and pressing, and the washing liquor is used for size mixing; alkaline lipase is added to the left washed sugar-free grains to further hydrolyze the fat in material, rice sugar-free grains protein with higher protein content is obtained by filtering and washing, and rice sugar-free grains protein is hydrolyzed by edible hydrochloric acid or protease to prepare the organic nitrogen source which can be used as the fermentation raw material of a biopharmaceutical process.

Description

technical field [0001] The invention relates to the reuse of sugar grains left after starch syrup is produced by using rice or rice flour as raw materials, in particular to a method for preparing protein nitrogen sources for fermentation and food from rice sugar grains. Background technique [0002] With the development of modern enzyme preparation industry, people can use various amylases to liquefy, saccharify and hydrolyze starch or starchy raw materials, including rice, to produce starch sugar products such as glucose (syrup), malt syrup, beer fermentation sugar, etc., for food and fermentation industry. The enzymatic process uses the specificity of enzymes to hydrolyze starch from rice, flour and other grain food materials, separate and remove non-sugar substances such as protein and fat, and produce the required starch sugar. [0003] The general technological process of producing starch syrup from rice at present includes the steps of impurity removal, rice washing, ...

Claims

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Application Information

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IPC IPC(8): A23L1/03A23L1/28A23L29/00
Inventor 黄立新徐正康赵谋明周彦斌罗建勇罗思
Owner GUANGZHOU SHUANGQIAO
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