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Continuous preparation process of zanthoxylum bungeanum seed protein

A preparation process, technology of Zanthoxylum bungeanum seed, applied in the field of continuous preparation technology of Zanthoxylum bungeanum seed protein, can solve problems such as reaction, long-term precipitation, interference with processing technology, protein denaturation, etc., and achieve the goal of shortening extraction time, increasing reaction rate, and increasing yield Effect

Pending Publication Date: 2020-07-03
上海辰钿实业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The common degreasing process of protein raw materials mostly uses solvents such as ethanol and petroleum ether for degreasing. These solvents are not only costly, but also have solvent residues that interfere with subsequent processing processes and traditional high-temperature processes that cause denaturation of the prepared proteins to varying degrees.
In addition, the protein separation process after degreasing is mostly intermittent processes such as alkali-soluble acid analysis method, enzymatic hydrolysis method, membrane separation method, ion exchange method, ultrafiltration concentration method, etc., which require a long time for reaction and precipitation in the tank

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A continuous preparation process for prickly ash seed protein, comprising the following processing steps:

[0023] (1) After the pretreatment of Zanthoxylum bungeanum seeds, use tetrafluoroethane as the extraction solvent, subcritically extract oil and fat at 2MPa and 40°C for 40min, and collect degreased Zanthoxylum bungeanum seed meal;

[0024] (2) The pepper seed meal is ultrafinely crushed and passed through a 200-mesh sieve, and then enters the ultrasonic continuous countercurrent unit together with dilute sodium hydroxide solution for ultrasonic hedging and countercurrent reaction. The pH of the system in the ultrasonic continuous countercurrent unit is 9 and the temperature is 20 ° C. , after the ultrasonic hedging and countercurrent reaction, the protein slurry with a solid-liquid ratio of 1:30 is obtained, and the ultrasonic frequency of the ultrasonic continuous countercurrent unit is 15Hz;

[0025] (3) Put the protein slurry through an ultrasonic vibrating si...

Embodiment 2

[0029] A continuous preparation process for prickly ash seed protein, comprising the following processing steps:

[0030] (1) After the Zanthoxylum bungeanum seed is pretreated, use a mixed solvent of methyl ether and butane with a volume of 1:1 as the extraction solvent, subcritically extract the oil at 0.8 MPa and 50°C for 45 minutes, and collect the degreased Zanthoxylum bungeanum seed meal;

[0031] (2) The pepper seed meal is ultrafinely crushed and passed through a 100-mesh sieve, and then enters the ultrasonic continuous countercurrent unit together with dilute sodium hydroxide solution for ultrasonic hedging and countercurrent reaction. The pH of the system in the ultrasonic continuous countercurrent unit is 10 and the temperature is 25 ° C. , After ultrasonic hedging and countercurrent reaction, protein slurry with a solid-liquid ratio of 1:10 is obtained, and the ultrasonic frequency of the ultrasonic continuous countercurrent unit is 50Hz;

[0032] (3) Put the prote...

Embodiment 3

[0036] A continuous preparation process for prickly ash seed protein, comprising the following processing steps:

[0037] (1) After the Zanthoxylum bungeanum seed is pretreated, the mixed solvent of tetrafluoroethane and ethanol with a volume ratio of 1:1 is used as the extraction solvent, and the oil is subcritically extracted at 1.6MPa and 30°C for 50min, and the degreased Zanthoxylum bungeanum seed meal is collected;

[0038] (2) The pepper seed meal is ultrafinely crushed and passed through a 120-mesh sieve, and then enters the ultrasonic continuous countercurrent unit together with dilute sodium hydroxide solution for ultrasonic hedging and countercurrent reaction. The pH of the system in the ultrasonic continuous countercurrent unit is 8 and the temperature is 30 ° C. , After ultrasonic hedging and countercurrent reaction, protein slurry with a solid-liquid ratio of 1:15 is obtained, and the ultrasonic frequency of the ultrasonic continuous countercurrent unit is 60Hz;

...

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PUM

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Abstract

The invention provides a continuous preparation process of zanthoxylum bungeanum seed protein, which comprises the following steps: pretreating zanthoxylum bungeanum seeds, extracting grease by adopting a subcritical process, and collecting degreased zanthoxylum bungeanum seed meal; carrying out superfine grinding on zanthoxylum bungeanum seed meal, sieving, carrying out ultrasonic hedging countercurrent reaction together with alkali liquor, wherein when the ultrasonic hedging countercurrent reaction is performed, the system is alkalescent; obtaining protein slurry after the ultrasonic hedgingcountercurrent reaction; enabling the protein slurry to pass through an ultrasonic vibrating screen and then a centrifugal machine to screen out insoluble substances twice, so as to obtain protein clear liquid; and adding an acid solution into the protein clear liquid to regulate the system to be weakly acidic, separating by using a centrifuge, and carrying out freeze drying by using a freeze dryer to obtain the zanthoxylum bungeanum seed protein. The continuous preparation process combining subcritical degreasing, ultrasonic oscillation continuous extraction, weak acid settling separation and high-speed freezing separation is adopted, the finished zanthoxylum bungeanum seed protein product with good quality and high yield is obtained, the reaction time is short, and the production efficiency is high.

Description

technical field [0001] The invention belongs to the field of biotechnology, in particular to a continuous preparation process of prickly ash seed protein. Background technique [0002] Zanthoxylum bungeanum is the main by-product in the production of Zanthoxylum bungeanum peel, which contains 18% protein in addition to rich oil. At present, the research on the extraction process of Zanthoxylum bungeanum protein is based on laboratory data or refers to the separation process of animal protein and soybean protein. The common degreasing process of protein raw materials mostly uses solvents such as ethanol and petroleum ether for degreasing. These solvents are not only costly, but also have solvent residues that interfere with subsequent processing processes and traditional high-temperature processes that denature the prepared proteins to varying degrees. In addition, the protein separation process after degreasing is mostly intermittent processes such as alkali-soluble acid an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07K1/14
CPCC07K1/145
Inventor 陈卓
Owner 上海辰钿实业有限公司
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