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    • 91. 发明专利
    • SLUDGE DEHYDRATING DEVICE
    • JPS5680398A
    • 1981-07-01
    • JP15634379
    • 1979-12-04
    • KURITA INDUSTRIAL CO LTD
    • TAKEUCHI TADAOISHII YASUHIKO
    • B01D33/04B30B9/20B30B9/24
    • PURPOSE:To facilitate an easy dehydration of the sludge, by holding the sludge in a polymerization dehydrating section of a pair of travelling filter cloth belts having an endless circulating movement each and at the same time providing a high-pressure dehydrating part at the terminal of the dehydrating section. CONSTITUTION:A pair of filter cloth belts 1a and 1b having an endless circulating movement are made to travel in the polymerized state and from the front point A to the point B of the sludge supply position 2. The tension is controlled for the belts 1a and 1b each by means of the tension control roller T and the zigzag movement control roller T', and the dehydrating/driving roller D performs the driving of these belts. Thus the sludge is supplied by the sludge supply device 2, and the water receriver 2' is provided for an automatic dehydration up to the point A. The belts 1a and 1b holding the sludge between advance in a zigzag line and around the roller group 3 to perform the dehydration with the surface pressure. The high-pressure generating means consisting of the return roller 4 and the high-pressure roller 5 is installed at the termianl of the polymerization dehydrating section. Thus the high pressure is applied to the sludge at the 1st and 2nd bands I and II to improve the dehydration performance.
    • 92. 发明专利
    • DEHYDRATOR OF ORGANIC SLUDGE
    • JPS5667519A
    • 1981-06-06
    • JP14276279
    • 1979-11-06
    • KURITA INDUSTRIAL CO LTD
    • HIROTA MORIYUKISAWADA SHIGEKI
    • B01D35/06
    • PURPOSE:To obtain dehydrated sludge of low moisture contents at high capacity by providing pressure electroosmotic dehydrating parts in multiple steps to an apparatus which continuously dehydrates org. sludge through electroosmosis action. CONSTITUTION:A conductive material is provided to the outside circumferential part of at least one pressure roll 3' of the pressure dehydrating part and is also used as one electrode of either anode or cathode. Sludge is held between the main driven belts 1a, 1b in direct contact with this pressure roll 3' serving also as an electrode so that the belts advance around the roll 3' while dehydrating the sludge. Namely, electroosmosis action is effected between the roll 3' and electrode belt 6, whereby pressure dehydration and electroosmotic dehydration are accomplished simultaneously in this section. The electrode belt 6 is put on the roll 3' and the front and rear rolls 3a, 3b disposed in the upper right and left parts thereof in the form of OMEGA, and forms a long pressure and electroosmotic dehydration section 7 covering nearly the entire circumference of the roll 3', and this provides dehydrated sludge at high capacity.
    • 96. 发明专利
    • TREATMENT OF WASTE WATER FROM REFUSE COMBUSTION FACILITY
    • JPS55157389A
    • 1980-12-08
    • JP6493779
    • 1979-05-28
    • KURITA INDUSTRIAL CO LTD
    • SHIRASAWA HIROSHI
    • C02F1/44B01D1/04C02F1/04C02F1/28C02F1/42C02F9/00
    • PURPOSE:To efficiently and nearly completely remove heavy metals and salts using a small-scale equipment and a simple operation by a method wherein waste water from a refuse combustion facility is treated with evaporation and separation, the obtained vapor is treated with reverse osmosis membrane to provide concentrated mercury water, which is treated with a chelate-type ion-exchange resin. CONSTITUTION:Waste water from trash combustion facilities is stored in a tank 3 and then is supplied to an evaporator unit 5. The evaporator 5 is used for evaporating separation process where the waste water is separated into vapor and concentrated liquid. In this process, a considerable amount of mercury in the waste water is transferred to vapor phase. The vapor is guided from vapor tube 9 into a condenser 10 and condensed by cooling in a cooling tower 11, whereby mercury is transferred to the condensed water phase. The condensed water passes through a filter 13 and is guided to a reverse osmosis membrane separator 15, where only solvent water is passed through, and mercury and other solute remain and become concentrated water, which is introduced into an ion-exchange tank 18. There, mercury is adsorbed and removed from concentrated water by chelate-type ion-exchange resin. In this manner, concentrated water from which mercury is removed exits the chelate resin bed and is circulated via connecting pipe 20 into the raw water tank 3.