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Method for integrated utilization for sunflower seeds

A technology for sunflower seeds and sunflower seed kernels is applied in the field of chlorogenic acid and sunflower seed protein peptides, which can solve the problems of short shelf life, perishability, waste of resin resources, etc.

Inactive Publication Date: 2013-03-20
武汉普赛特膜技术循环利用有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The defects of this process and the problems of the product are: high-temperature pressing causes a chemical reaction in the material system to generate free fatty acids, which are easily corrupted, resulting in a short shelf life of edible oil; the oil yield of the pressing process is only 50%, and the remaining fatty substances need to use organic solvent n-hexane Extraction, there should be residues of organic solvents in the finished oil, which will seriously affect human health; due to high temperature, the protein in the cake will be denatured and the chlorogenic acid will be volatilized, so the cake can only be used as feed, wasting excellent protein and chlorogenic acid resources; meanwhile, sunflower seed hulls are not utilized, wasting natural resin resources

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] 50kg of sunflower seeds were mechanically dehulled to obtain 12.5kg of sunflower shells and 37.5kg of sunflower kernels; crush the sunflower kernels with a colloid mill, add 187.5kg of water, raise the temperature to 50°C, adjust the pH to 5, and add cellulose Enzyme 187.5g, enzymatic hydrolysis for 2h; after the enzymolysis is completed, separate the three-phase separator to obtain the oil phase, water phase and solid phase; carry out alkali refining deacidification and deodorization of the oil phase to obtain 14.5kg of sunflower oil; separate the water phase and the solid phase with acid protease to obtain two enzymolysis solutions A and B, and combine the two enzymolysis solutions (that is, add 75g of acid protease to the water phase, raise the temperature to 50°C, adjust the pH to 3.5, enzymolysis for 2 hours, and the enzymolysis is complete Obtain enzymatic solution A; add 100kg of water to the solid phase, raise the temperature to 50°C, adjust the pH to 3.5, add 11...

Embodiment 2

[0040]50kg of sunflower seeds were mechanically dehulled to obtain 12.5kg of sunflower shells and 37.5kg of sunflower kernels; crush the sunflower kernels with a colloid mill, add 187.5kg of water, raise the temperature to 60°C, adjust the pH to 5.5, and add cellulose Enzyme 375g, enzymolysis 3h; Carry out three-phase separator separation after enzymolysis is completed, obtain oil phase, water phase and solid phase; Oil phase is subjected to alkali refining deacidification and deodorization to obtain sunflower oil 15.7kg; Water phase and Enzymolyze the solid phase with acid protease to obtain two enzymolysis solutions A and B, combine the two enzymolysis solutions (add 112.5g acid protease to the water phase, raise the temperature to 60°C, adjust the pH to 4.5, enzymolysis for 3 hours, and the enzymolysis is complete Obtain enzymolysis solution A; add 100kg of water to the solid phase, raise the temperature to 60°C, adjust the pH to 4.5, add acid protease 150, enzymolysis for 3...

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PUM

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Abstract

The invention relates to a method for integrated utilizing sunflower seeds. Addition amount of each substance adopted by the method is on the basis of weight of sunflower kernels. The method comprises that: shells of the sunflower seeds are removed, and furfural resin are prepared from the shells of the sunflower seeds; the sunflower kernels are sequentially carrying out a wet crushing, a extracting through cellulase at a moderate temperature, a three-phase separating and a refining process for oil phase to obtain a pure natural sunflower oil; the seperated water phase and the seperated solid phase are sequentially carrying out a extracting through acid protease at a moderate temperature, a routine centrifuging, removing impurities through a ultrafiltration membrane, a decolouring through active carbon, a adsorbing and a desorbing through a macroporous adsorptive resin, then the collected liquid from the macroporous adsorptive resin is concentrated through a nanofiltration membrane and carries out a powder-drying to obtain a sunflower seed protein peptides, and eluent is concentrated through a nanofiltration membrane and carries out a refining to obtain chlorogenic acid. According to the present invention, resource of the sunflower seed is utilized reasonably; technology for integrated utilizing the sunflower seeds has advantages of simplicity, availability and safe operation; yield of the sunflower oil, the sunflower seed protein peptides, the chlorogenic acid and the furfural resin are respectively 90%, 80%, 55% and 90%; secondary pollution and a plurality of waste water are not generated.

Description

technical field [0001] The invention relates to a production method for intensively processing sunflower seeds using biotechnology, and mainly relates to a method for extracting furfural resin, sunflower oil, chlorogenic acid and sunflower protein peptide from sunflower seeds. Background technique [0002] Sunflower seeds are the fruit of sunflower, which belongs to the genus Helianthus of the family Asteraceae. It is an annual herb, also known as sunflower. In the past two decades, the production of sunflower seeds has developed rapidly, and the output of sunflower seeds in the world has become an important oil crop second only to soybeans. At present, my country has a relatively wide cultivation area. In recent years, the annual output of sunflower seeds in the country is about 1.3 million tons, and the annual output of sunflower seeds in Northwest China is about 850,000 tons. [0003] The sunflower seed shell accounts for about 25% by weight, and the sunflower seed shell...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C11B1/04C11B1/00C11B3/00C11B3/06C12P21/06C07C69/73C07C67/52C07D307/50A23K1/14A23K10/14A23K10/30
CPCY02P60/87
Inventor 万端极徐国念吴正奇李猷毛波刘锐
Owner 武汉普赛特膜技术循环利用有限公司
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