Dialysis solution regeneration method
A dialysate and permeate technology, applied in dialysis systems, chemical instruments and methods, semi-permeable membrane separation, etc. The effect of fewer problems and cost reduction
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Embodiment 1
[0139] The reverse osmosis membrane element manufactured using the separation membrane A was fed with the raw water B at a pressure of 2.0 MPa, and operated so that the recovery rate became 60%. The obtained concentrate was passed through a reverse osmosis membrane element produced using the separation membrane A, and operated so that the recovery rate became 50%. The recovery rate as a reverse osmosis membrane system is 80%. The urea removal rate was calculated from the obtained permeate and found to be 82%.
Embodiment 2
[0141] With respect to the reverse osmosis membrane element manufactured using the separation membrane A, the raw water B was passed in at a pressure of 1.5 MPa, and it operated so that the recovery rate might become 60%. The obtained concentrated liquid was passed through the reverse osmosis membrane element produced using the separation membrane A, and it operated so that the recovery rate might become 50%. The recovery rate as a reverse osmosis membrane system is 80%. The urea removal rate was calculated from the obtained permeate and found to be 77%.
Embodiment 3
[0143] In the reverse osmosis membrane element produced using the separation membrane B, the raw water B was passed through at a pressure of 2.0 MPa, and the recovery rate was 60%. The obtained concentrate was passed through a reverse osmosis membrane element produced using the separation membrane B, and operated so that the recovery rate became 50%. The recovery rate as a reverse osmosis membrane system is 80%. When the urea removal rate was calculated from the obtained permeate, it was 69%.
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