Extraction method of cottonseed protein
A cottonseed protein and extraction method technology, applied in the field of cottonseed processing, can solve the problems of increasing the amount and difficulty of recycling and purifying waste methanol, difficult to control free gossypol and aflatoxin, and the content of mildewed aflatoxin in cottonseed. The effect of reducing the amount of cottonseed protein, reducing methanol solvent consumption, and reducing the amount of steam used
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Embodiment 1
[0062] The cottonseed is pre-treated to obtain cotton kernels, and then the cotton kernels are degreased to obtain degreased cotton meal; the degreased cotton meal is sent from the feeding device 1 to the primary leaching tank 2, and extracted at 30°C for the first stage Leaching and extraction, the material is discharged from the bottom of the tank after continuous stirring in the tank, and is sent to the secondary leaching tank 3 by the first conveyor 9, extracted at 40°C for secondary leaching and extraction, and then discharged by the first conveyor 9 after continuous stirring. into the tertiary leaching tank 4, extracted at 45°C for tertiary leaching and extraction, and then the material discharged from the tertiary leaching tank 4 is sent to the leaching and draining machine 5 to drain by the second conveyor 11, and the material is drained and then transported to Desolvation and drying. The extraction time of the material is 10 minutes under continuous stirring in the le...
Embodiment 2
[0065] The cottonseed is pre-treated to obtain cotton kernels, and then the cotton kernels are degreased to obtain degreased cotton meal; the degreased cotton meal is sent from the feeding device 1 to the primary leaching tank 2, and extracted at 40°C for primary extraction Leaching and extraction, the material is discharged from the bottom of the tank after continuous stirring in the tank, and is sent to the secondary leaching tank 3 by the first conveyor 9, extracted at 35°C for secondary leaching and extraction, and then discharged by the first conveyor 9 after continuous stirring. into the tertiary leaching tank 4, extracted at 50°C for tertiary leaching and extraction, and then the material discharged from the tertiary leaching tank 4 is sent to the leaching and draining machine 5 by the second conveyor 11 to drain, and the material is drained and then transported to Desolvation and drying. The extraction time of the material is 15 minutes under continuous stirring in the...
Embodiment 3
[0069] The cottonseed is pre-treated to obtain cotton kernels, and then the cotton kernels are degreased to obtain degreased cotton meal; the degreased cotton meal is sent from the feeding device 1 to the primary leaching tank 2, and extracted at 40°C for primary extraction Leaching and extraction, the material is discharged from the bottom of the tank after continuous stirring in the tank, and sent to the secondary leaching tank 3 by the first conveyor 9, extracted at 45°C for secondary leaching and extraction, after continuous stirring, it is discharged from the first conveyor 9 into the tertiary leaching tank 4, extracted at 55°C for tertiary leaching and extraction, and then the material discharged from the tertiary leaching tank 4 is sent to the leaching and draining machine 5 to drain by the second conveyor 11, and the material is drained and then transported to Desolvation and drying. The extraction time of the material is 25 minutes under continuous stirring in the lea...
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