Method for producing dephenolized cottonseed protein
A technology for dephenolized gossypol protein and cotton kernel, which is applied in the field of production of dephenolized gossypol protein, can solve the problems of large degree of protein denaturation and high relative energy consumption, and achieves the effects of less destructiveness, good effect, and reduction of thermal denaturation time.
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Embodiment 1
[0037] 1. Put 200g cotton kernels into a cotton kernel sieve and sieve them into large kernels and fine powder;
[0038] 2. Soften and press the big kernels sieved in step 1, put the processed big kernels into a flat dryer to adjust the moisture, and the percentage of the adjusted moisture is 3%;
[0039] 3. The material prepared by the plate dryer in step 2 is transported to the degreasing extractor, the extraction agent is 6# solvent oil with a solid-liquid ratio of 1:0.5, and the countercurrent extraction is 6 times;
[0040] 4. Transport the material treated in step 3 to the dephenol leaching device, and use basic methanol for countercurrent extraction 6 times, wherein the concentration of basic methanol is 88 °, and the amount of alkali added to the basic methanol is 0.2% of the water in the solution ;
[0041] 5. Spray acidic methanol with the material after step 4 is processed by the dephenol leaching device, and the amount of acid added to the acidic methanol is 1% of...
Embodiment 2
[0046] 1. Put 200g cotton kernels into a cotton kernel sieve and sieve them into large kernels and fine powder;
[0047] 2. Soften and press the big kernels sieved in step 1, put the processed big kernels into a flat dryer to adjust the moisture, and the percentage of the adjusted moisture is 3%;
[0048] 3. The material prepared by the plate dryer in step 2 is transported to the degreasing extractor, the extraction agent is 6# solvent oil with a solid-liquid ratio of 1:1, and the countercurrent extraction is 6 times;
[0049] 4. Transport the material treated in step 3 to the dephenol leaching device, and use basic methanol for countercurrent extraction 6 times, wherein the concentration of basic methanol is 88°, and the amount of alkali added to the basic methanol is 2% of the water in the solution ;
[0050] 5. Spray acidic methanol with the material after step 4 is processed by the dephenol leaching device, and the amount of acid added to the acidic methanol is 1% of the ...
Embodiment 3
[0055] 1. Put 200g cotton kernels into a cotton kernel sieve and sieve them into large kernels and fine powder;
[0056] 2. Soften and press the big kernels sieved in step 1, put the processed big kernels into a flat dryer to adjust the moisture, and the percentage of the adjusted moisture is 3%;
[0057] 3. The material prepared by the plate dryer in step 2 is transported to the degreasing extractor, the extraction agent is 6# solvent oil with a solid-liquid ratio of 1:1, and the countercurrent extraction is 6 times;
[0058] 4. Transport the material treated in step 3 to the dephenol leaching device, and use basic methanol for countercurrent extraction 6 times, wherein the concentration of basic methanol is 88 °, and the amount of alkali added to the basic methanol is 1% of the water in the solution ;
[0059]5. Spray acidic methanol with the material after step 4 is processed by the dephenol leaching device, and the amount of acid added to the acidic methanol is 1% of the ...
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