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    • 62. 发明专利
    • METHOD AND APPARATUS FOR REGENERATING MEMBRANE EVAPORATIVE CONCENTRATOR OF WASTE FLUID
    • JPH05192543A
    • 1993-08-03
    • JP818292
    • 1992-01-21
    • HITACHI LTD
    • FUNABASHI KIYOMIYAMAGUCHI TETSUOMIURA HIDEKAZUSAWA TOSHIO
    • B01D61/36B01D65/06C02F1/04C02F1/44
    • PURPOSE:To obtain treated water of high purity by a method wherein the water pressure on the condensed water side of a membrane evaporative concentrator is kept higher than that on the waste fluid side thereof and the lowering of the formation amount of condensed water is detected to wash a hydrophobic porous membrane with chemicals and the washed membrane is dried to be regenerated. CONSTITUTION:A waste fluid is introduced into a tank 7 and cooling water is supplied to the cooling chamber 13 of a membrane evaporative concentrator 1 through a circulating system 3. The waste fluid in an evaporation chamber 12 has high temp. to generate evaporation and the generated steam is diffused through a hydrophobic porous membrane to be condensed in the cooling chamber 12. Therefore, the surfactant in the waste fluid is conc. on the surface of the membrane and the particles of the surfactant are settled into the membrane to make the membrane hydrophilic and the waste fluid penetrates in the membrane to become liquid flow. Since the pressure of the cooling chamber 13 is higher than that of the evaporation chamber 12 at this time, cooling water flows in the waste fluid. This inflow amount is increased by making the membrane hydrophilic and an evaporation speed decreases. A chemical agent such as hydrogen peroxide is sent to the cooling chamber 13 from a tank 9 to wash org. matter. Thereafter, a blower 10 is operated to dry the chemical solution remaining in the pores of the membrane 11 to remove the same.
    • 63. 发明专利
    • MEMBRANE METHOD AND DEVICE FOR EVAPORATING AND CONCENTRATING WASTE LIQUID
    • JPH04346823A
    • 1992-12-02
    • JP12086291
    • 1991-05-27
    • HITACHI LTD
    • FUNABASHI KIYOMIYAMAGUCHI TETSUOKUROKAWA HIDEAKISAWA TOSHIO
    • B01D61/36C02F1/04G21F9/08
    • PURPOSE:To prevent leak by simple operation and to obtain high purity treated water for a long time by keeping water pressure on the condensed water side of waste liquid treating device within a specific range and keeping the water pressure on the condensed water side higher than that on the waste liquid side. CONSTITUTION:When treating waste liquid by a membrane evaporating concentrator 1 equipped with an evaporating chamber 12 and a cooling chamber 13 separated by a hydrophobic porous membrane 11, water pressure in the cooling chamber 13 is kept in the range of 10 to 500KPa and water pressure in the cooling chamber 13 is kept higher than that in the evaporating chamber 12. When the waste liquid is evaporated, the vapor is diffused in a hydrophobic porous membrane 11 and condensed in the cooling chamber 13. And after sodium sulfate in the waste liquid is concentrated on the surface of the membrane 11 to deposit it in the membrane and the waste liquid enters the membrane 11, the waste liquid reaches the cooling chamber 13 to produce liquid flow. At that time, as water pressure in the evaporating chamber 12 is higher than that in the cooling chamber 13, sodium sulfate deposited in the membrane 11 is washed by cooling water flow to restore hydrophobic property of the membrane.
    • 66. 发明专利
    • METHOD AND APPARATUS FOR TREATING WASTE LIQUID
    • JPH03106488A
    • 1991-05-07
    • JP24219289
    • 1989-09-20
    • HITACHI LTD
    • YAMAGUCHI TETSUOSAWA TOSHIOKIKUCHI JUN
    • B01D53/22B01D5/00B01D53/26C02F1/04
    • PURPOSE:To obtain a highly pure condensed water, reduce the corrosion of material and prevent the contamination of a membrane by a method wherein a waste liq. is evaporated under normal pressure and at a medium and low temp. without boiling, and the resulting vapor is passed through a hydrophobic porous membrane for recovery. CONSTITUTION:A noncondensable gas is brought into contact with a high temp. waste liq. in order to evaporate the waste liq., accompanied by vapor. In this manner the waste liq. can be evaporated under normal pressure and at a low and medium temp. Since a hydrophobic porous membrane is not used on the evaporating surface, there is also no problem of contaminating the membrane. The noncondensable gas accompanied by the aforesaid vapor is caused to contact with the hydrophobic porous membrane 20 provided parallel to the passage 18 of said gas so as to recover the vapor. Since the vapor alone is thus passed through the membrane to be condensed, while the droplets of the waste liq. accompanied by the noncondensable gas are not allowed to pass therethrough, a highly pure condensed water can be obtained. Furthermore, by producing a circulation of the noncondensable gas between the high temp. waste liq. and the hydrophobic porous membrane, the movement and diffusion of the vapor given off by the waste liq. can be accelerated without using decompression device.