Lactose-free milk preparation method based on separation membrane technologies
A lactose-free and membrane-separating technology, applied in dairy products, milk preparations, applications, etc., can solve the problems of easy inactivation of enzymes, difficult recovery of lactase, and high cost of enzymes
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Embodiment 1
[0022] Step 1: 968g of milk after pasteurization is carried out 5 times of dialysis to remove fat components through the PVC hollow fiber membrane with molecular weight cut-off of 100KDa. The obtained retentate was diluted with 738g of deionized water, and then passed through the PVC hollow fiber membrane for the next dialysis, wherein the milk was not diluted during the first dialysis (during the first 4 times of dialysis, each dialysis obtained about 200g of retentate ); combine the permeate obtained from 1~5 times of dialysis (the total amount of the combined permeate is 3256.8g), and obtain relatively small substances containing whey protein, lactose, inorganic salts, small molecule cellulose, dietary fiber, etc. The first permeate; collect the retentate 662g obtained after the 5th dialysis, which is the first retentate containing fat and casein micelles;
[0023] Step 2: the 3256.8g first permeated liquid obtained in step 1 is used to carry out 4 times of dialysis interce...
Embodiment 2
[0029] Step 1: 1936g of milk after pasteurization is carried out 5 times of dialysis to remove fat components through the PVC hollow fiber membrane with molecular weight cut-off of 100KDa. The obtained retentate was diluted with 1438g of deionized water, and then passed through the PVC hollow fiber membrane for the next dialysis, wherein the milk was not diluted during the first dialysis (during the first 4 times of dialysis, each dialysis obtained about 400g of retentate ); combine the permeate obtained from 1~5 times of dialysis (the total amount of permeate combined is 7018.6g), and obtain relatively small substances containing whey protein, lactose, inorganic salts, small molecular cellulose, dietary fiber, etc. The first permeate; collect 663.4g of the retentate obtained after the 5th dialysis, which is the first retentate containing fat and casein micelles;
[0030] Step 2: the 7018.6g first permeated liquid obtained in step 1 is used to carry out 4 times of dialysis to ...
Embodiment 3
[0036] Step 1: 4840g of milk after pasteurization is carried out 5 times of dialysis to remove fat component through the PVC hollow fiber membrane of 100KDa molecular weight cut-off, when described milk is carried out first 4 times of dialysis by PVC hollow fiber membrane, each dialysis The obtained retentate was diluted with 3878g deionized water, and then passed through the PVC hollow fiber membrane for the next dialysis, wherein the milk was not diluted during the first dialysis (during the first 4 times of dialysis, each dialysis obtained about 1000g of retentate ); combine the permeate obtained from 1~5 times of dialysis (the combined total amount of permeate is 18684.5g), and obtain relatively small substances containing whey protein, lactose, inorganic salts, small molecule cellulose, dietary fiber, etc. The first permeate; collect the retentate 1662g obtained after the 5th dialysis, which is the first retentate containing fat and casein micelles;
[0037] Step 2: the 1...
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