Method for preparing food-grade xylo-oligosaccharide from viscose fiber squeezed alkali solution
A technology for squeezing lye and viscose fiber, which is applied in chemical instruments and methods, semi-permeable membrane separation, membrane technology, etc. It can solve the problem of low concentration temperature of nanofiltration membrane, unsuitability for large-scale industrial production, low membrane filtration efficiency, etc. problems, to achieve the effect of low cost, high semi-fiber, and guaranteed filtration efficiency
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Embodiment 1
[0049] A method for preparing food-grade xylo-oligosaccharides by pressing lye from viscose fiber, the specific process steps are as follows:
[0050] A. Membrane concentration
[0051] The pressed lye produced by viscose fiber is pre-filtered to remove large particles of impurities, the permeate is diluted with water, and then enters the first-level nanofiltration membrane for treatment, and the obtained first-level concentrated solution is diluted with water and then enters the second-level nanofiltration membrane for treatment. The secondary concentrated solution is diluted with water and then enters the ceramic membrane for treatment, and the obtained concentrated solution is the concentrated solution of squeezed lye;
[0052] B. Extract semi-fiber
[0053] Add acid to neutralize the concentrated solution of the squeezed lye to obtain a semi-fiber liquid.
[0054] C. Enzymolysis
[0055] Add complex enzymes to the semi-fiber liquid, enzymatic hydrolysis reaction occurs ...
Embodiment 2
[0059] This embodiment is basically the same as Embodiment 1, on this basis:
[0060] In the step A, the molecular weight cut-off of the primary nanofiltration membrane is 200, the molecular weight cut-off of the secondary nanofiltration membrane is 300, and the molecular weight cut-off of the ceramic membrane is 800.
Embodiment 3
[0062] This embodiment is basically the same as Embodiment 1, on this basis:
[0063] In the step A, the molecular weight cut-off of the primary nanofiltration membrane is 300, the molecular weight cut-off of the secondary nanofiltration membrane is 400, and the molecular weight cut-off of the ceramic membrane is 1500.
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