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    • 11. 发明专利
    • MEMBRANE SEPARATOR FOR WATER TREATMENT
    • JPH0929070A
    • 1997-02-04
    • JP18706795
    • 1995-07-24
    • TOHOKU ELECTRIC POWER COKURITA WATER IND LTD
    • ISHIYAMA KAZUHIROSASAKI YUTAKADOI TADASHISATO TAKESHIMATSUTANI NAOKI
    • B01D61/14C02F1/44
    • PROBLEM TO BE SOLVED: To accurately detect the clogging degree of a membrane by calculating an amt. of transmitted water in terms of reference differential pressure and reference temp. from the amt. of transmitted water detected by a transmitted water amt. detection means. SOLUTION: At first, an amt. of transmitted water is calculated from the detection value of a flowmeter F-1 and the membrane area of a membrane module 4. Then, the amt. of transmitted water under a reference condition is calculated in terms of reference differential pressure and reference temp. from the respective detection values of pressure gauges P-1, P-2, P-3 and the viscosity calculated from the temp. detected by a thermometer T-1 and the future amt. of transmitted water under the reference condition can be estimated from the transition of this calculated amt. of transmitted water. Therefore, the amt. of transmitted water under the reference condition necessary for chemical washing is preset and, when the amt. of transmitted water under the reference condition lowers to this set value, chemical washing is performed to make it possible to perform chemical washing corresponding to the state of a membrane. Since the lowering of the amt. of transmitted water under the reference condition can be easily estimated, a chemical washing period can be easily estimated and the operation control of the apparatus becomes easy.
    • 12. 发明专利
    • METHOD FOR CLEANING MEMBRANE MODULE WITH CLEANING AGENT
    • JPH11319515A
    • 1999-11-24
    • JP13531498
    • 1998-05-18
    • TOHOKU ELECTRIC POWER COKURITA WATER IND LTD
    • SASAKI YUNIHEI MIKIOFUJITA HIROYUKISATO TAKESHI
    • B01D65/02B01D65/06
    • PROBLEM TO BE SOLVED: To significantly reduce the consumption of a cleaning agent, and dispense with a specical chemical-resistant member as a material for a heating installation, piping or the like by supplying a cleaning agent to and filling an untreated water and concentrated water chamber with the cleaning agent and supplying a heated water to a permeating water chamber, when cleaning a membrane module with a cleaning agent. SOLUTION: When treating an untreated water by membrane separation, the untreated water is guided to the primary side 1A of a membrane module 1 through piping, and the permeating water which permeates to the secondary side 1B is delivered through a water collecting valve V-5. When cleaning the membrane module with a cleaning agent, the water collecting valve V-5, V-3, V-4 are closed and the valves V-1, V-2 are opened. Then a cleaning liquid is supplied to the primary side 1A of the membrane module 1 from a cleaning liquid tank 2 with the help of a cleaning pump 3 to replace the liquid on the primary side 1A with the cleaning liquid. After that, the valves V-1, V-2 are closed and the valves V-3, V-4 are opened. Further, a heated process water in a heated process water circulation tank 5 is circulated to the secondary side 1B of the membrane module 1 using a circulation pump 6 and thereby the cleaning liquid on the primary side 1A is heated to increase the effect to clean the membrane.
    • 17. 发明专利
    • MEMBRANE SEPARATION DEVICE
    • JPH10180047A
    • 1998-07-07
    • JP34517296
    • 1996-12-25
    • KURITA WATER IND LTD
    • MATSUTANI NAOKISATO TAKESHI
    • B01D61/58
    • PROBLEM TO BE SOLVED: To stably and efficiently execute a treatment by providing a constant flow rate valve or a flow control value at the permeated water outlet side of each membrane module. SOLUTION: A flocculation treated liquid is passed through a membrane module 1A by a feed pump 4 and a circulating pump 5 and the concentrated water by the membrane module 1A is passed through a membrane module 1B. The concentrated water by the membrane 1B is circulated to the membrane module 1A by the circulating pump 5. On the other hand, each permeated water from the membrane module 1A and 1B is taken out through each constant flow rate valve 7A and 7B and a back washing pot 8 as a treated water. Each permeated water from the membrane module 1A and 1B is adjusted to a fixed flow rate respectively by the constant flow rate valve 7A and 7B, the permeated quantity from the membrane module 1A and 1B are controlled to be equal to each other to equalize the load and the progress of the membrane soiling is almost equalized and as a result, the membrane surface is effectively used and the performance of the whole membrane separation device is stably maintained over a long period.
    • 18. 发明专利
    • MEMBRANE SEPARATION DEVICE
    • JPH10180008A
    • 1998-07-07
    • JP34753396
    • 1996-12-26
    • KURITA WATER IND LTD
    • TAKADOI TADASHISATO TAKESHICHIKASAWA KIYOHITO
    • C02F1/44B01D21/01C02F1/52
    • PROBLEM TO BE SOLVED: To prevent the decrease in flux in a membrane module by adding an org. polymer flocculant (polymer) to the liquid which is subjected to flocculation treatment with an inorg. flocculant so that fine particles are flocculated into flocs with a larger particle size and to increase the density. SOLUTION: The raw water is introduced into a first reaction tank 1, where an inorg. flocculant such as an aluminum compd. and iron compd., and if necessary a pH controlling agent are added to the water to flocculate under specified pH condition. The treated liquid by flocculation in the first reaction tank 1 is then introduced into a second reaction tank 2, where a polymer is added. As for the polymer, various kinds such as anion, cation and nonion polymers can be used. These polymers may be used as a single state or a mixture of two or more. The treated liquid by flocculation in the second reaction tank 2 is circulated by a circulating pump P through a circulation tank 3 and sent to a membrane module 4. After the water permeated through the membrane of the membrane module 4, the water as a treated water is discharged to the outside, while the concentrated water is returned to the circulation tank 3.
    • 19. 发明专利
    • MEMBRANE MODULE
    • JPH10146519A
    • 1998-06-02
    • JP30908896
    • 1996-11-20
    • KURITA WATER IND LTD
    • TAKADOI TADASHISATO TAKESHIMATSUTANI NAOKICHIKASAWA KIYOHITO
    • B01D63/02
    • PROBLEM TO BE SOLVED: To improve the workability at the time of evaluating the power of a membrane module, which is produced by filling a casing with membrane elements, by forming aperture parts which can be opened and closed to make it possible to touch hollow fiber membranes in the inside in at least two positions. SOLUTION: In the case membrane module evaluation is carried out at the time when the collected amount of permeated water of a membrane separation apparatus can not be recovered even if the membrane module is washed, a vessel 24, which is a pressure container, and covering covers 25, 26 composing a casing 20 of the membrane module are disassembled and the hollow fiber membranes 11 in the pottings 12, 13 of the vessel 24 are observed. Moreover, covers 27' 28' of a pair of aperture parts 27, 28 installed in the vessel 24 are also disassembled to observe the hollow fiber membranes 11 in the vessel 24. Then, any one of hollow fiber membranes 11 in the vessel 24 is cut from one aperture part 27 and at the same time another part of a hollow fiber membrane 11 is cut from the other aperture part 28 and the cut part is taken out through the aperture part 28 and based on the part of the taken out hollow fiber membrane 11, the deterioration of the hollow fiber membranes 11 is evaluated.