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    • 3. 发明专利
    • MEMBRANE SEPARATOR
    • JPS63278505A
    • 1988-11-16
    • JP11251387
    • 1987-05-11
    • NIPPON STEEL CORP
    • INAMI RYUICHISUEHIRO SHOICHITAIMA HISAO
    • B01D61/02B01D61/08B01D61/10B01D61/14B01D61/18B01D61/20B01D65/02B01D65/04
    • PURPOSE:To make the title membrane separator compact by connecting the liq. concentrate outlet from the membrane separation unit, in which a check valve plug provided with a membrane face cleaner is inserted into each internal pressure type tubular membrane, to the suction port of a reciprocating pump, and providing a check valve seat at the inlet for the raw liq. to be treated. CONSTITUTION:Compressed air from a compressor 45 is supplied alternately into the air chambers 30 on both sides to operate the reciprocating pump 7. In the suction stage of the pump 7, the check value plug 3 provided with a membrane face cleaner 2 is pressed by the flow of the raw liq. 40 sucked into the internal pressure type tubular membrane 1 from the inlet 8 for the liq. to be treated, and lifted up while cleaning the membrane face. The raw liq. is further sucked into a pump chamber 31. In the discharge stage of the pump 7, the inside of the pump chamber 31 is pressurized, and the check valve plug 3 is pressed down while again cleaning the membrane face by the back flow of the raw liq. The check valve 3 then abuts on the check valve seat 9 and stops. Since the inlet 8 is closed and the inside of the membrane 1 is pressurized, the raw liq. permeates through the membrane 1 from the inside to the outside, and the permeated liq. flows out from a discharge pipe 39. The liq. concentrate returns to a raw liq. tank 41 from a discharge port 26.
    • 4. 发明专利
    • METHOD FOR PROCESSING BY REVERSE OSMOSIS MEMBRANE
    • JPH0929252A
    • 1997-02-04
    • JP18687695
    • 1995-07-24
    • NIPPON STEEL CORP
    • SHIBATA TOSHIYUKITAIMA HISAOSUEHIRO SHOICHIFUSHIDA TAKASHIMATSUMOTO HIDEYUKI
    • B01D61/04C02F1/44
    • PROBLEM TO BE SOLVED: To simplify pretreatment and to obtain the same level of the quality of processed water and permeation performance as the conventional one by performing the processing while air is mixed into raw water in a process for treating sand-filtered raw water by passing it through a reverse osmosis membrane for processing waste water and industrial waste water by utilizing the reverse osmosis membrane. SOLUTION: In a method wherein the secondarily processed water of a waste water or an industrial waste water is used as a raw water and it is highly processed by using a reverse osmosis membrane, a processing apparatus 7 constituted by providing a sand filtering device 2 for pretreatment of the raw water 1, an air mixing hole 4a for mixing air 4 into the raw water 3 filtered by means of this sand filtering device 2 and a spirally shaped reverse osmosis membrane 6 in which a spacer for widening a raw water flow path is thickened, is used. In adition, in a process wherein the sand- filtered raw water 3 is processed by passing it through the reverse osmosis membrane 6, the raw water is processed while air 4 is continuously or intermittently mixed into the raw water 3. In this case, mixing of the air 4 is pref. performed intermittently. In addition, the amt. of the air 4 is regulated to about 20% of the amt. of the raw water to be fed.
    • 5. 发明专利
    • SUBMERGED ICE STORING AND THERMAL ACCUMULATING DEVICE WITH ICE PIECES AND WATER MIXING AND TRANSPORTING MEANS
    • JPH03144235A
    • 1991-06-19
    • JP27997489
    • 1989-10-30
    • NIPPON STEEL CORP
    • INAMI RYUICHISUEHIRO SHOICHIIGARASHI MASAYUKI
    • F24F5/00F25C1/00
    • PURPOSE:To provide an effective utilization of latent heat of ice in a cooling load and prevent an ice from being changed into a block by a method wherein ice pieces and cold water are stored in the same thermal accumulating tank and all the ice pieces are mixed with cold water and then both ice pieces and cold water are transported. CONSTITUTION:When ices are made at night, thermal accumulated water 11 in a thermal accumulating tank 1 from a water pipe passage 6 is continuously changed into some ice pieces 13 by an ice making machine 5 and then the ice pieces are discharged from a lower part of the thermal accumulating tank 1 into thermal accumulating water through a water feeding pipe passage 2. The ice pieces 13 are immersed in a part below an ice making plate 4A and then the ices are stored there. When a cooling load is to be required at daytime, an ice feeding machine 3A in an ice discharging pipe passage 3 and a pump 8 are operated. Cold water 12 and ice pieces 13 are formed continuously into mixed cold water and they are fed to a cooling pipe 9. Hot water return water is returned back into the thermal accumulating tank 1 through a return water pipe 10. In addition, the ice pieces are stored while being floated, and then a transporting of the ices may easily be carried out. With such an arrangement, it is possible to provide an effective utilization of latent heat of ice and to prevent some ice pieces from being formed into ice blocks.
    • 6. 发明专利
    • MEMBRANE SEPARATION TREATING DEVICE
    • JPS63256101A
    • 1988-10-24
    • JP8890887
    • 1987-04-13
    • NIPPON STEEL CORP
    • INAMI RYUICHISUEHIRO SHOICHITAIMA HISAO
    • B01D61/08B01D61/10B01D61/18B01D61/20B01D63/06B01D65/04B01D65/06
    • PURPOSE:To prevent the deposition of a gel layer on the surface of a membrane, to miniaturize the title device, and to reduce the cost of the device by connecting the liq. concentrate outlet of the membrane separation unit wherein a membrane surface cleaning body is inserted in an internal pressure-type tubular membrane to the suction port of a reciprocating pump, and connecting a check valve to the inlet for a raw liq. to be treated. CONSTITUTION:The compressed air from a compressor 40 is alternately supplied to air chambers 26 on both sides through an air supply pipe 41 and a supply and discharge unit 31 to operate the reciprocating pump 6, and the raw liq. 36 to be treated in a raw liq. tank 37 is sucked into the internal pressure-type tubular membrane 1 and a pump room 27 from a check valve 8. The inside of the membrane 1 and pump room 27 are depressurized, and the membrane surface cleaning body 2 is pressed by the flow of the raw liq. 36, goes up while cleaning the membrane surface, collides against an upper partition plate 11, and stops. When the pump 6 begins to discharge, the check valve 8 is closed, the insides of the pump room 27 and membrane 1 are pressurized, the raw liq. permeates the membrane 1 from the inside to the outside, the membrane surface cleaning body 2 is pressed down by the back flow of the raw liq., and the membrane surface is again cleaned. The liq. concentrate not permeating the membrane is returned to the raw liq. tank 37 from a discharge port 22.
    • 7. 发明专利
    • RECOVERING AND FIXING METHOD OF CARBON DIOXIDE
    • JPH1057745A
    • 1998-03-03
    • JP21632796
    • 1996-08-16
    • NIPPON STEEL CORP
    • FUKUNAGA KAZUHISAMIKI OSAMUKIMURA TETSUOTADA KATSUMISUEHIRO SHOICHIMOTOUCHI TOSHITAKE
    • B01D53/62B01D53/14
    • PROBLEM TO BE SOLVED: To recover and fix carbon dioxide at a high recovery ratio by absorbing carbon dioxide in an alkali solution, introducing the alkali solution into an algae culture pond and, after fixing carbon dioxide to the algae, separating into the algae and a liquid and circulating and reusing the liquid. SOLUTION: A combustion waste gas from a thermal power plant 5 or the like is desulfurized, denitrificated and after that, introduced to an absorbing tower 4 to absorb carbon dioxide in the combustion waste gas in the alkali solution such as a sodium hydroxide aq. solution. Next, the alkali solution in which carbon dioxide is absorbed is introduced into a fixing reactor 8 as the algae culture pond. Then, carbon dioxide in the solution is incorporated and fixed by the algae such as spirulina in the fixing reactor 8. After that, the liquid discharged from the fixing reactor 8 is transiently stored in a treated water tank 9, the algae portion is separated and removed in a concentration equipment 10 and, after being transiently stored in a separated liquid receiving tank 11, the liquid portion is returned to a supply pipe 31 by a circulating pipe line 12 and supplied to the carbon dioxide absorbing tower 4 to be reused.