Method for removal of saccharide from anthocyanin with nanofiltration membrane
An anthocyanin and nanofiltration membrane technology, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of high energy consumption, large solvent recovery, complicated operation, etc. Simple and easy to operate, solve the effect of long process flow
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Embodiment 1
[0013] The membrane area is 130m 2 1. A polyimide membrane with a molecular weight cut-off of 1000 Da was used to treat 350 g of an aqueous solution containing 0.5 wt % anthocyanins, wherein the glucose content was 2.0 wt % and the fructose content was 1.4 wt %. Treat for 1 hour at a temperature of 25°C and an operating pressure of 0.7 MPa to obtain 240 g of anthocyanin solution with an anthocyanin content of 0.721 wt%, wherein the glucose content is 1.81 wt%, and the fructose content is 1.21 wt%.
Embodiment 2
[0015] The membrane area is 130m 2 1. A polysulfone membrane with a molecular weight cut-off of 1000 Da is used to treat 350 g of an aqueous solution containing 0.5 wt % anthocyanins, wherein the glucose content is 2.0 wt % and the fructose content is 1.4 wt %. At a temperature of 25° C. and an operating pressure of 0.7 MPa, the process was performed for 1 hour to obtain 240 g of anthocyanin solution with an anthocyanin content of 0.729 wt%, wherein the glucose content was 1.80 wt%, and the fructose content was 1.22 wt%.
Embodiment 3
[0017] The membrane area is 130m 2 1. A polyethersulfone membrane with a molecular weight cut-off of 1500Da was used to treat 350 g of an aqueous solution containing 0.5 wt% anthocyanins, wherein the glucose content was 2.0 wt%, and the fructose content was 1.4 wt%. At a temperature of 25° C. and an operating pressure of 0.7 MPa, the process was performed for 1 hour to obtain 240 g of anthocyanin solution with an anthocyanin content of 0.726 wt%, wherein the glucose content was 1.84 wt%, and the fructose content was 1.23 wt%.
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