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    • 42. 发明专利
    • METHOD FOR DEHYDRATING DIGESTED SLUDGE
    • JPH0924400A
    • 1997-01-28
    • JP17735295
    • 1995-07-13
    • KURITA WATER IND LTD
    • HANAMI YUICHITAKEUCHI TADAOOYAMA AKIO
    • B01D21/01C02F11/14
    • PROBLEM TO BE SOLVED: To greatly improve the filtration rate of a dehydrating machine, such as belt press, at the time of a dehydration treatment of digested sludge, to decrease the amt. of the dehydrated cake obtd. by the treatment and the moisture content thereof and to reduce the number of the required units of the dehydrating machines and the disposition cost of the dehydrated cake. SOLUTION: The digested sludge is subjected to a flocculation treatment by adding a cation polymer thereto. The flocculated sludge is subjected to gravity dehydration. The gravity dehydrated sludge is tempered by adding an inorg. flocculating agent thereto. Amphoteric polymer is added to the tempered sludge and the sludge is dehydrated by the dehydrating machine. The digested sludge is subjected to the flocculation treatment by the cation polymer and, after the sludge is gravity dehydrated, the inorg. flocculating agent is added thereto and, therefore, the required amt. of the inorg. flocculating agent to be added is drastically decreased. The dehydratability of the sludge added with the inorg. flocculating agent is good and the filtration rate is improved. The moisture content of the dehydrated cake obtd. in such a manner is lowered.
    • 43. 发明专利
    • BIODEODORIZING DEVICE
    • JPH02198612A
    • 1990-08-07
    • JP1637989
    • 1989-01-27
    • KURITA WATER IND LTD
    • TAKEUCHI TADAOOYAMA AKIOWATANABE KEISHIN
    • B01D53/38B01D53/34B01D53/81
    • PURPOSE:To increase the amount of microbes supported with a packing layer and to improve the treatment capacity for malodor gas by concentrating and recovering the malodor gas decomposing microbes washed out of the packing layer with sprinkled water. CONSTITUTION:Malodor gas passes through the packing layer 2 formed by packing the carrier supporting the microbes decomposing malodor gas components in a treatment tower 1 to carry out deodorizing. In this case, water is sprinkled on the packing layer 2 by a sprinkling means 4, and the microbes included in the sprinkled water drained from the packing layer 2 where water is sprinkled by the sprinkling means 4 are concentrated by a membrane concentration means 6 using such as precise filter membranes. The microbes concentrated by the membrane concentration means 6 are returned to the packing layer 2 through a storage vessel 8, a pump 9 and a circulating pipe 10, etc. As a result, the amount of microbes supported by the packing layer is increased and the treating capacity for malodor gas is improved thereby.
    • 44. 发明专利
    • Dephosphorization method
    • 去磷化方法
    • JP2005177679A
    • 2005-07-07
    • JP2003425073
    • 2003-12-22
    • Kurita Water Ind Ltd栗田工業株式会社
    • OYAMA AKIOSUMITA ICHIROSUNAHARA TAKASHIGE
    • C02F1/58B01D9/02
    • PROBLEM TO BE SOLVED: To provide a dephosphorization method for removing phosphorus in posphorus-containing wastewater up to a low concentration at a high treatment speed by a fluidized bed type crystallization method. SOLUTION: Raw water containing phosphoric acid is passed through a reaction tank 2 filled with seed crystals, which are formed by precipitating calcium phosphate on the surface of calcium carbonate, as an ascending stream to form a fluidized bed of the seed crystals in the reaction tank 2 and phosphorus in raw water is removed as calcium phosphate crystals in the reaction tank 2 by adding a calcium compound and/or an alkali agent to raw water. A cylinder 9 opened at both ends is provided in the reaction tank 2 so that the axial direction is set to an up and down direction and at least the lower part is positioned in the fluidized bed F and a descending stream forming means 10 for forming a descending stream is provided in the cylinder 9. The particle size of the seed crystals is set to 0.2-0.5 mm, the passage LV of raw water in the reaction tank 2 is set to 20-25 m/h, SV is set to 5-10 h -1 and the T-P of inflow water to the reaction tank 2 is set to 6 mg/L or below to obtain treated water with T-P of 1 mg/L or below. COPYRIGHT: (C)2005,JPO&NCIPI
    • 待解决的问题:提供一种通过流化床型结晶法以高处理速度除去含磷酸盐废水中的磷至高浓度去除的脱磷方法。 解决方案:将含有磷酸的原水通过填充有晶种的反应槽2,该晶种是通过在碳酸钙的表面上沉淀磷酸钙形成的,作为上升流,以形成晶种的流化床 通过向原水中添加钙化合物和/或碱剂,反应槽2和磷在原料水中作为磷酸钙晶体除去。 在反应罐2中设置有在两端开口的缸体9,使得轴向方向设定为上下方向,并且至少下部部件位于流化床F中,并且下降流形成装置10形成 下降流提供在圆筒9中。晶种的粒径设定为0.2-0.5mm,反应槽2中的原水的通道LV设定为20-25m / h,SV设定为5 -10h -1 ,并将反应槽2的入流水的TP设定为6mg / L以下,得到TP为1mg / L以下的处理水。 版权所有(C)2005,JPO&NCIPI
    • 48. 发明专利
    • SLUDGE TREATING DEVICE
    • JPH1128500A
    • 1999-02-02
    • JP18237697
    • 1997-07-08
    • KURITA WATER IND LTD
    • OYAMA AKIO
    • C02F11/14
    • PROBLEM TO BE SOLVED: To effectively dehydrate anaerobic sludge and also to effectively remove and recover phosphorus. SOLUTION: Sludge, to which a cation polymer is added, is flocculated by a first flocculating means 1, and the flocculated sludge is concentrated by a gravity concentrating means 2. The concentrated sludge, to which an inorganic flocculant is added, is flocculated by a second flocculating means 3, and the flocculated sludge, to which an ampholytic polymer flocculant is added, is flocculated by a third flocculating means 4. The flocculated sludge is dehydrated by a dehydrating means 5. The separated water of the gravity concentrating means 2 is treated by a MPA (magnesium ammonium hydrogenphosphate) forming means 6. In this way, when after sludge is flocculated by the cation polymer and is concentrated by gravity, the inorganic flocculant is added, charge neutralization is completely performed, and by adding the ampholytic polymer after that, firm flocs can be formed, allowing the recovery efficiency and the dehydration efficiency of sludge to be markedly improved. By treating the separated water from the gravity concentrating means by the MAP forming means, phosphorus discharged from sludge can be effectively removed and recovered.
    • 49. 发明专利
    • DEPHOSPHORIZATION APPARATUS
    • JPH09262599A
    • 1997-10-07
    • JP7667196
    • 1996-03-29
    • KURITA WATER IND LTD
    • FUKASE TETSUROOTA HIROZOHINA SEIYAOYAMA AKIO
    • C02F3/30
    • PROBLEM TO BE SOLVED: To efficiently recover phosphorus from org. waste water without performing anaerobic digestion by providing a biological phosphorization tank and concentrating the excessive sludge from this treatment tank and discharging phosphorus from conc. sludge and precipitating magnesium ammonium phosphate from a phosphorus-containing soln. SOLUTION: Phosphorus-containing water is subjected to solid-liquid separation in a first sedimentation basin 1 and separated sludge is conc. in a gravity concn. tank 4 while separated water is returned to the first sedimentation basin 1. The separated water after solid-liquid separation is subjected to biological dephosphorization treatment in a biological dephosphorization treatment tank 2 to be supplied to a solid-liquid separation means 3 to separate phosphrus-containing sludge and a part of separated sludge is returned to the biological dephosphrization tank 2 as return sludge and excessive sludge is conc. by a concn. means 5. This conc. sludge is sent to an anaerobic tank 6 and the treated liquid of the anaerobic tank 6 is sent to a solid-liquid separation means 7 to be subjected to solid-liquid separation and separated water is supplied to a dephosphorization tank 8. A magnesium salt is added to the dephosphorization tank 8 to precipitate phosphorus as magnesium ammonium phosphate useful as fertilizer.
    • 50. 发明专利
    • DEHYDRATING METHOD FOR ANAEROBIC DIGESTION SLUDGE
    • JPH08206699A
    • 1996-08-13
    • JP1792595
    • 1995-02-06
    • KURITA WATER IND LTD
    • OYAMA AKIOTAKEUCHI TADAOOI YASUHIROTAKII KAZUO
    • C02F11/00C02F11/04C02F11/14
    • PURPOSE: To efficiently perform dehydration by improving dehydrating property of anaerobic digestion sludge of sewage. CONSTITUTION: After aeration is performed for anaerobic digestion sludge, excess sludge is mixed therewith. Metallic salt is added to the obtained mixed sludge and then an amphoteric organic polymer flocculant is added and aggregation treatment is performed and aggregated sludge is dehydrated by a dehydrator. Anaerobic digestion sludge is aerated to degass carbonic acid gas dissolved in sludge. Thereby, when metallic salt is added in the post-process, aggregation is prevented from being hindered by generation of carbon dioxide gas from sludge. Since alkalinity of anaerobic digestion sludge is high and aggregation properties are bad, excess sludge having low alkalinity is mixed and alkalinity is lowered and aggregation properties are raised. After aggregation properties are improved by aeration and mixing of excess sludge, metallic salt is added and the neutralization of charge is performed. Then, effective aggregation and condensation are performed by adding the amphoteric organic polymer flocculant. Dehydrating properties of the obtained condensed sludge are extremely good and dehydration is performed at high filtration velocity and dehydrated cake having low water content is obtained.