Prepn process of hollow chitosam fiber film for pervaporation separation
A technology of pervaporation and chitosan, used in semi-permeable membrane separation, chemical instruments and methods, membrane technology, etc. Effect
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Embodiment 1
[0038] Dissolve 6.5 grams of CS in a 4% acetic acid aqueous solution, and pour it into the spinning tank after standing, filtering, and degassing. A filter is attached to the spinneret, and the filter screen is 250 mesh. The inner / outer diameter of the spinneret is 1.0 / 2.0mm, and the core liquid is a 10% NaOH solution at room temperature. Such as figure 1 ( figure 1 The markings in are: 1—core liquid tank; 2—advection pump; 3—regulating valve; 4—pressure gauge; 5—insulation layer; 6—spinning tank; 7—filter; 8—sprinkler; 9—gel Bath; 10-hollow fiber membrane; 11-membrane storage tank). In the process of spinning hollow fiber membrane, high-pressure nitrogen is used as the pressure source to extrude the casting liquid from the spinneret. At the same time, the core liquid enters the hollow fiber cavity from the center hole of the spinneret under the action of the advection pump as a support and an internal coagulation medium. After the casting solution leaves the spinneret, it passe...
Embodiment 2
[0042] according to Figure 5 Perform pervaporation performance test ( Figure 5 The marks in are: 12—membrane separator; 13—constant flow pump; 14—material liquid tank; 15—receiving bottle; 16—vacuum pump; 17—three-way; 18—low pressure vacuum pump), the process is as follows. Turn on the material-liquid circulation pump to circulate the material-liquid between the material-liquid tank and the membrane separator while heating the material-liquid in the material-liquid tank. When the material liquid temperature is constant at the set temperature, turn on the vacuum pump. Make the system under negative pressure. After permeating for 1 to 4 hours to reach a steady state, record the time, and collect the permeate with a cold trap. Accurately weigh the collected permeate. Measure the composition percentage of the permeate by gas chromatograph. With the azeotrope containing 70wt% methanol / 30wt% dimethyl carbonate as the feed liquid, at 50℃, after membrane separation, the methanol content...
Embodiment 3
[0044] according to Figure 5 The pervaporation performance test was performed, and the process was the same as in Example 2, and the concentration of the material liquid was changed to 10 wt% of methanol, and the above experiment was repeated. The result is as Figure 6 As shown, the methanol content in the permeate reaches 78 wt%.
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