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    • 4. 发明专利
    • DEIONIZED WATER MAKING APPARATUS
    • JP2001259376A
    • 2001-09-25
    • JP2000074227
    • 2000-03-16
    • ORGANO KK
    • TAMURA MAKIO
    • B01D61/48B01D61/58B01D71/56C02F1/32C02F1/44C02F1/469
    • PROBLEM TO BE SOLVED: To provide a deionized water making apparatus achieving the suppression of a rise in the difference pressure due to the passing of water through a reverse osmosis membrane apparatus (RO) or an electric deionized water making apparatus (EDI) during long-term operation by the drastic improvement of the EDI from a structural aspect without using a chemical agent. SOLUTION: The RO and the EDI are connected in series in this order and a desalting chamber is constituted by respectively filling two small desalting chambers, each of which is demarcated by a cation exchange membrane on one side, an anion exchange membrane on the other side and a central intermediate ion exchange membrane, with an anion exchanger and a mixed ion exchanger and concentration chambers are provided on both sides of the desalting chamber through the cation exchange membrane and the anion exchange membrane and the desalting chamber and the concentration chambers are arranged between an anode and a cathode to form the EDI and water to be (treated is allowed to flow in one small desalting chamber filled with the anion exchanger while voltage is applied and, subsequently, the outflow water of the small desalting chamber is allowed to flow in the other small desalting chamber and concentrated water is allowed to flow in the concentration chambers. By this constitution, deionized water containing no microorganisms is obtained from the desalting chamber and the membrane surfaces of the RO and the concentration chambers of the EDI can be suppressed from the generation of slime to the utmost.
    • 6. 发明专利
    • WATER RECOVERING DEVICE FOR FUEL CELL
    • JP2000331703A
    • 2000-11-30
    • JP14350199
    • 1999-05-24
    • ORGANO KK
    • TAMURA MAKIO
    • H01M8/06
    • PROBLEM TO BE SOLVED: To attain preventing enlargement of a system, the smooth and effective recycle of water, and more efficient purification of air by constituting the water recovering lone from a condensing means for partially or entirely liquefying steam generated by oxidation reaction as a line for at least partially desalting the condensed water and supplying it to a fuel supplying system and/or a solid polymer electrolyte. SOLUTION: A gas, generated from methanol and air and containing CO2, H2O and N2, turns into water in a condenser 38 as condensing means of heat exchanger structure, passed via a water recovering line 39, and desalted in a reverse penetration membrane device 41 so as to be reusable. It is partially supplied to a solid polymer electrolyte and fuel feed line 36, so that adverse effects, such as catalytic poison or corrosion of electrode can be minimized. An air-liquid contact means such as a condensed water tank 71 is preferably provided in the water recovering line 39 to purify the supplied air by contacting with the condensed water. According to this, the generation efficiency can be improved, and the large-scaled system equipment concerning a fuel cell 31 can be omitted to provide a system suitable as on-vehicle type or portable type.
    • 8. 发明专利
    • FRESH WATER PRODUCTION DEVICE AND METHOD THEREOF
    • JPH09206749A
    • 1997-08-12
    • JP1781696
    • 1996-02-02
    • ORGANO KK
    • TAMURA MAKIOKUWATA MASAHIROSATO YASUKIYO
    • B01D61/02B01D61/04B01D61/58C02F1/44C02F1/66C02F5/08
    • PROBLEM TO BE SOLVED: To surely prevent a decrease of flux by providing a scale retarder supplying device supplying a scale retarder to a water to be treated and an acid supplying device supplying acid to the concentrated water in the preceding stage in a device in which a concentrated water obtained by subjecting the water to be treated to a reverse osmotic membrane treatment is further subjected to the reverse osmotic membrane treatment. SOLUTION: The water to be treated is separated into the preceding stage concentrated water and a preceding stage permeated water by a preceding stage reverse osmotic membrane device 4. At that time, the scale retarder is supplied to the water to be treated in a feed pipe 2 of the water to be treated with the scale retarder feed unit 6 so that a specified concn. is obtained. Then the preceding stage permeated water is taken outside through a preceding stage permeated water taking out pipe 10 and served as fresh water for various application, but the preceding stage concentrated water is supplied to a post stage reverse osmotic membrane device 14 through a preceding stage concentrated water taking out pipe 12 and separated there into a post stage concentrated water and a post stage permeated water. At that time, the acid is supplied to the preceding stage concentrated water flowing in the preceding stage concentrated water taking out pipe 12 from the acid feed device 16, in this way, the preceding stage concentrated water is controlled in a specified pH value.
    • 9. 发明专利
    • METHOD FOR DETECTING BREAKAGE OF MEMBRANE AND DEVICE THEREFOR
    • JPH08252440A
    • 1996-10-01
    • JP8464295
    • 1995-03-16
    • ORGANO KK
    • OE TAROTAMURA MAKIO
    • G01N15/08B01D65/10G01M3/00
    • PURPOSE: To provide a device for detecting breakage of a membrane in which breakage of the membrane of a membrane type filter is detected surely without delay and reliability is increased. CONSTITUTION: This detecting device 10 for breakage of a membrane is equipped with a membrane module 12 and a fine particle gauge 14 and detects breakage of the membrane of a membrane type filter 16. In the membrane type filter, raw water supplied from a raw water tank 18 through a conveying pump 20 is filtrated by the membrane and separated into permeated water and concentrated water. A first return line 22 and a second return line 24 are connected to the suction side of the conveying pump 20 from the outlet of concentrated water of the membrane type filter and the outlet of concentrated water of the membrane module 12. The fine particle gauge is connected to the second return line and measures the number of fine particles in concentrated water. Pore diameter of the membrane of the membrane module is same as that of the membrane of the membrane type filter or is slightly larger than that. When the membrane of the membrane type filter is broken, the measured value of fine particles measured by the fine particle gauge is immediately increased. Therefore, breakage of the membrane of the membrane type filter is detected without delay.