Fixed enzyme membrane reactor, preparation thereof and method for producing biological diesel oil by the same
A technology of membrane reactors and immobilized enzymes, applied in the direction of enzyme production/bioreactors, fixed on/in organic carriers, biological raw materials, etc., can solve the problem of reducing catalytic efficiency, easy inactivation of enzymes, and increasing production costs and other problems, to achieve the effect of improving catalytic efficiency, not easy to desorb, and high specific surface area
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[0028] Example 1
[0029] Dissolve acrylonitrile / 2-methacryloyloxy-ethyl-phosphatidylcholine / hydroxyethyl methacrylate terpolymer with a molecular weight of 200,000 in dimethylformamide to prepare a concentration of 4wt.% spinning solution. Under the conditions of a spinning voltage of 7kV, a spinneret solution flow rate of 0.1mL / h, and a receiving distance of 8cm, electrospinning was carried out to prepare an ultrafine fiber composite membrane with a fiber diameter of 1000nm. Polyester non-woven fabric was used as the supporting material. Fill it in the inner and outer double-cylindrical membranes to form a membrane reaction device ③, as shown in the accompanying drawings, the inner cylinder of the membrane device is called the inner side of the membrane device membrane ④, and the cavity between the inner and outer cylinder peripheral surfaces is It is called the outer side of the membrane device membrane ⑤. Three membrane devices were connected in series to form one-, two-...
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[0030] Example 2
[0031] Dissolve acrylonitrile / 2-methacryloyloxy-ethyl-phosphatidylcholine / hydroxyethyl methacrylate terpolymer with a molecular weight of 150,000 in dimethylformamide to prepare a concentration of 5wt.% spinning solution. Under the conditions of a spinning voltage of 8kV, a spinneret solution flow rate of 1mL / h, and a receiving distance of 10cm, electrospinning was performed to prepare an ultrafine fiber composite membrane with a fiber diameter of 500nm. Polyester non-woven fabric was used as the supporting material. It is filled in a roll-type membrane tool, and a plurality of membrane tools are connected in series to form one, two, and three-stage membrane reactors. By means of cross-flow filtration, the epichlorohydrin was first circulated in the membrane reactor device at 27 °C for 1.5 hours, and then the lipase solution with a concentration of 8 g / L was circulated in the membrane reactor device at 27 °C. 1.5 hours; during the cycle, both epichlorohydr...
Example Embodiment
[0032] Example 3
[0033] Dissolve acrylonitrile / 2-methacryloyloxy-ethyl-phosphatidylcholine / hydroxyethyl methacrylate terpolymer with a molecular weight of 100,000 in dimethylformamide to prepare a concentration of 4wt.% spinning solution. Under the conditions of spinning voltage of 10 kV, flow rate of spinneret solution of 2 mL / h, and receiving distance of 25 cm, electrospinning was carried out to prepare ultra-fine fiber composite membrane with fiber diameter of 200 nm. Polyester non-woven fabric was used as supporting material. It is filled in a roll-type membrane tool, and a plurality of membrane tools are connected in series to form one-, two-, and three-stage enzyme membrane reactors. By means of cross-flow filtration, the epichlorohydrin was first circulated in the membrane reactor device at 25 °C for 2 hours, and then the lipase solution with a concentration of 10 g / L was circulated in the membrane reactor device at 25 °C. 2 hours; during the cycle, both epichlorohy...
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