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    • 1. 发明专利
    • BIOLOGICAL DENITRIFICATION APPARATUS
    • JPH08155491A
    • 1996-06-18
    • JP30073594
    • 1994-12-05
    • KURITA WATER IND LTD
    • MITA MASAICHIRONISHIKAWA SHOZOKAGIWADA MASAKOFUKASE TETSURO
    • C02F3/34
    • PURPOSE: To prevent sludge in a denitrification tank from floating and to enable stable and efficient denitrification by removing sludge which floated from the denitrification tank in which dirty water is passed through a sludge bed added with elemental sulfur in a upward current, adding a surface active agent to the sludge in a reaction vessel, mixing them, and returning liquid in the reaction vessel to the denitrification tank. CONSTITUTION: In a denitrification apparatus, raw water is introduced from a raw water inflow pipe 2 to the bottom part of a denitrification tank 1 in which a fluidized bed 1A added with elementary sulfur as an electron donor is formed to be denitrified in an upward current. The treated water is removed from the upper part of the tank through a treated water take off pipe 3. In this process, an extraction pipe 4 for floating sludge is placed near the upper part of the fluidized bed 1A, sludge extracted from the pipe 4, after being added with a surfactant in a surfactant storage tank 6 by a pipe 5, is modified in a reaction vessel 7, and the modified sludge is refluxed to the bottom part of the denitrification tank 1 through a pipe 8. In this way, the sludge is prevented from floating and flowing out so that the amount of sludge held in the denitrification tank 1 is kept high.
    • 2. 发明专利
    • ACTIVE OXYGEN DETECTING METHOD
    • JPH07301618A
    • 1995-11-14
    • JP9338894
    • 1994-05-02
    • KURITA WATER IND LTD
    • NISHIKAWA SHOZO
    • G01N27/416
    • PURPOSE:To easily and quickly detect presence of active oxygen generation without using an expensive device or reagent by soaking a copper electrode and reference electrode in water containing oxidation-reduction pigment, and after mixing of a testing object, measuring a potential difference between both the electrodes. CONSTITUTION:A copper electrode 1 and reference electrode 2 are soaked in test water, a potentiometer is connected between both the electrodes, and then a testing object, namely a sample which is tested whether or not it generates active oxygen in the case of being added to the water is added and mixed to measure a potential difference. In this case, a copper plate and copper wire can be used as the copper electrode 1 while an Ag-AgCl electrode or the like can be used as the reference electrode 2. As a quantity of testing object to be added and mixed into the test water, about 0.2-2g for 100ml of the test water is appropriate. In the case of the testing object which generates the active oxygen when being added and mixed into the test water, increase of potential difference is immediately recognized. On the other hand, in the case of the testing object which rarely generates the active oxygen, the increase of potential difference is not recognized.
    • 3. 发明专利
    • ANAEROBIC TREATMENT AND APPARATUS THEREFOR
    • JPH09206786A
    • 1997-08-12
    • JP1912896
    • 1996-02-05
    • KURITA WATER IND LTD
    • YODA MOTOYUKIFUKASE TETSURONISHIKAWA SHOZO
    • C02F3/28C02F11/04
    • PROBLEM TO BE SOLVED: To provide an anaerobic treatment method for an org. waste liquid capable of shortening stagnation time even if an anaerobic treatment is executed with high load with the waste liquid contg. solid org. matter and executing the volumetric reduction of the sludge at a low energy consumption rate and inexpensively by the simple device and operation capable of reducing the volume of the formed sludge and an apparatus therefor. SOLUTION: The in-vessel liquid 11 is withdrawn from an acid forming vessel 1 and is subjected to sepn. of solid from the liquid in a member separator 2. Part 6 of the thickened sludge is returned to the acid forming vessel 1 and other part 18 is introduced to a reforming vessel 3, such as heat treating vessel, ozone treating vessel or high-voltage pulse discharge treating vessel by which the sludge is reformed to easily decomposable sludge. This sludge is returned to the acid forming vessel 1 and is subjected to the anaerobic treatment. The volume of the generated sludge is reduced. The separated liquid of the membrane separator 2 is subjected to high-speed methane fermentation in a high-load methane fermentation vessel 4.
    • 6. 发明专利
    • WASTEWATER TREATMENT DEVICE
    • JPH1110194A
    • 1999-01-19
    • JP16588897
    • 1997-06-23
    • KURITA WATER IND LTD
    • MATSUI KENSUKENISHIKAWA SHOZOSHIBATA TAKESHI
    • C02F3/30C02F3/34
    • PROBLEM TO BE SOLVED: To recover a part of wastewater as magnesium ammonium phosphate by providing an anaerobic treatment tank, a reaction tank into which treated liquid of the anaerobic treatment tank is introduced, and a denitrification tank into which treated liquid of the reaction tank is introduced or an aerobic treatment tank. SOLUTION: Wastewater is introduced into an anaerobic tank 1 together with a return sludge from a settling tank 3 of a succeeding stage, where phosphorus in the return sludge is discharged on the side of liquid under anaerobic conditions. The treated anaerobic liquid is then introduced into a magnesium ammonium phosphate(MAP) reaction tank 6, where the phosphorus is caused to react with ammonia and Mg compounds to produce MAP. The MAP reaction liquid, from which phosphorus and ammonia have been removed by the production of the MAP, is then fed into an aerobic tank 2, where BOD is removed under conditions of aeration. And the aerobic treated liquid is introduced into the settling tank 3 so as to be separated to solids and liquid and the separated liquid is discharged to the outside as treated water. On the other hand, separated sludge which takes in phosphorus in the form of orthophosphoric acid by a biological treatment is returned to the tank 1 as return sludge.
    • 8. 发明专利
    • Method and apparatus for anaerobic treatment
    • 用于厌氧处理的方法和装置
    • JP2004209479A
    • 2004-07-29
    • JP2004114629
    • 2004-04-08
    • Kurita Water Ind Ltd栗田工業株式会社
    • YODA MOTOYUKIFUKASE TETSURONISHIKAWA SHOZO
    • C02F3/28C02F11/00C02F11/04C02F11/06
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To provide a method and an apparatus for anaerobic treatment of an organic waste liquid which can reduce the volume of sludge generated in the anaerobic treatment, prevent a deterioration in treated water quality, such as increases in chromaticity and COD, and obtain a high treated water quality at a low cost. SOLUTION: Liquid 11 in an anaerobic treatment tank 1 is drawn from the tank, and then subjected to solid-liquid separation in a membrane separator 2 to obtain a treated liquid. A part 5 of concentrated sludge is returned to the anaerobic treatment tank 1, and another part 17 of the sludge is introduced into a modifying tank 3, such as an ozone treatment tank or a high-pressure pulse discharge treatment tank, to modify the sludge to easily biodegradable one, and then returned to the anaerobic treatment tank 1, thereby reducing the volume of generated sludge. COPYRIGHT: (C)2004,JPO&NCIPI
    • 待解决的问题:提供一种有机废液的厌氧处理方法和装置,其可以减少厌氧处理中产生的污泥的体积,防止处理水质的劣化,例如色度的增加和 COD,并以低成本获得高处理水质。 解决方案:将厌氧处理槽1中的液体11从罐中抽出,然后在膜分离器2中进行固液分离,得到处理液。 将浓缩污泥的第5部分返回到厌氧处理槽1,将污泥的另一部分17引入诸如臭氧处理槽或高压脉冲放电处理槽的改性槽3中,以将污泥 易于生物降解,然后返回厌氧处理槽1,从而减少产生污泥的体积。 版权所有(C)2004,JPO&NCIPI
    • 9. 发明专利
    • TREATMENT OF NIGHT SOIL OR THE LIKE
    • JPH1128496A
    • 1999-02-02
    • JP18502797
    • 1997-07-10
    • KURITA WATER IND LTD
    • MATSUI KENSUKESHIBATA TAKESHINISHIKAWA SHOZO
    • C02F3/08C02F1/52C02F1/56C02F3/28C02F11/04C02F11/14
    • PROBLEM TO BE SOLVED: To increase the thermal efficiency and decomposition efficiency of an anaerobic digestion and to improve the quality of concentration separated water and digestion elimination water by adding an inorganic fluocculant into night soil and/or organic sludge, then adding an amphoteric high molecular fluocculant, stirring them to granulate and concentrate and anaerobically digesting the concentrated material. SOLUTION: Night soil, septic tank sludge and surplus sludge are introduced into a fluocculation reaction tank, flocculated by at first adding an inorganic flocculant, stirring and then, adding an amophoteric polymer and, stirring and further, granulated by slowly stirring. The granulated sludge easily separates the water with a simply structured screen to concentrate the water and to digest anaerobically the water in an anaerabic digestion process 2. A digestion supernatant is introduced into an activated sludge process 3 together with the concentration separated water from the screen 5 to be treated with the activated sludge. Since the concentration separated water and the digestion supernatant have an excellent water quality and are particularly low in a COD, chromaticity and the concentration of phosphorus or the like, which are difficult to remove by an activated sludge process, the excellent treated water is obtained by the activated sludge treatment.