Semipermeable composite membrane and process for producing the same
A composite semipermeable membrane and manufacturing method technology, applied in semipermeable membrane separation, chemical instruments and methods, membrane technology, etc., can solve the problems of reduced membrane performance, inability to obtain permeate, and inability to fully remove unreacted components , to achieve the effect of no reduction in membrane performance, excellent water permeability and salt rejection
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[0106] Examples are given below to describe the present invention, but these examples do not limit the present invention in any way.
[0107] [Evaluation and measurement method]
[0108] (Determination of permeation flux and salt rejection)
[0109] The prepared flat-membrane composite semipermeable membrane was cut into a predetermined shape and size, and placed in a cell for flat-membrane evaluation. For an aqueous solution containing about 1500 mg / L of NaCl and adjusted to pH 6.5 to 7.5 with NaOH, a differential pressure of 1.5 MPa is applied to the supply side and the permeation side of the membrane at 25°C to bring it into contact with the membrane. Measure the permeation velocity and conductivity of the permeated water obtained by this operation, and calculate the permeation flux (m 3 / m 2 • d) and salt rejection (%). For the salt rejection rate, the correlation (calibration curve) between the NaCl concentration and the conductivity of the aqueous solution was create...
manufacture example 1
[0120] (production of porous support)
[0121] A film-forming coating obtained by dissolving 18% by weight of polysulfone (manufactured by Solvay, P-3500) in N,N-dimethylformamide (DMF) was uniformly coated on a non-woven fabric base material, and the wet thickness is 200 μm. Immediately thereafter, it was immersed in water at 40 to 50° C. to solidify it, and DMF as a solvent was completely extracted and washed to prepare a porous support having a polysulfone microporous layer on a nonwoven fabric substrate.
Embodiment 1
[0123] The produced porous support was heated and dried at 40°C. The water content in the porous support after heating and drying is 1g / m 2 .
[0124] An amine aqueous solution containing 1% by weight of m-phenylenediamine, 3% by weight of triethylamine, and 6% by weight of camphorsulfonic acid (the moving speed of the amine component: 0.02 mg / m) was coated on the above-mentioned porous support. 2 sec), and then remove excess amine aqueous solution by wiping, thereby forming an aqueous solution covering layer. Next, an isooctane solution containing 0.2% by weight of trimesic acid chloride was applied to the surface of the aqueous solution coating layer. Then, excess solution was removed, and then kept in a hot air dryer at 120° C. for 3 minutes to form a surface layer containing polyamide resin on the porous support to obtain an unwashed composite semipermeable membrane. The permeation test was carried out using the fabricated composite semi-permeable membrane without clean...
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