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    • 8. 发明专利
    • Apparatus for treating organic waste water
    • 用于处理有机废水的设备
    • JP2006068632A
    • 2006-03-16
    • JP2004254679
    • 2004-09-01
    • Asahi Beer Eng:KkAsahi Breweries LtdSumitomo Heavy Ind Ltdアサヒビール株式会社住友重機械工業株式会社株式会社アサヒビールエンジニアリング
    • SUZUKI TETSUSHINORITAKE SHIGERUIMABAYASHI SEIJIUECHI KAZUO
    • C02F3/28C02F3/12C02F11/00
    • Y02E50/343Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a treatment apparatus capable of highly treating even if waste water contains a large number of organic solid matters. SOLUTION: This apparatus for treating organic waste water 100 is connected with an acid formation tank 14, an anaerobic treatment tank 16, an acid formation tank 18, an anaerobic treatment tank 20 and a solubilization treatment tank 22 in series. The anaerobic treatment tank 20 includes a waste water introduction part 42, an upward flow part 44 which has a side wall partitioning a space containing anaerobic sludge, makes an upward flow of introduced organic waste water through the anaerobic sludge and carries out anaerobic treatment, a solid-liquid separation part 48 which separates the solid matter from treated water treated in the upward flow part 44 and overflowing the upper end of the upward flow part 44, and a fluid circulation path 50 which connects the solid-liquid separation part 48 with a more upward portion than a portion introduced with the organic waste water in the upward flow part 44, and guides the solid matter separated by the solid-liquid separation part 48 to the upward flow part 44. An SS (suspended solid) is effectively separated from the treated water by the solid-liquid separation part 48. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供即使废水含有大量有机固体物质也能够高度处理的处理装置。 解决方案:这种处理有机废水100的装置与一个酸化槽14,一个厌氧处理槽16,一个酸化槽18,一个厌氧处理槽20和一个增溶处理槽22串联连接。 厌氧处理槽20包括废水引入部42,具有分隔有含有厌氧污泥的空间的侧壁的向上流动部44,通过厌氧污泥向上方引入有机废水,进行厌氧处理, 固体分离部分48将固体物质与向上流动部分44中处理的处理水分离并溢出向上流动部分44的上端;以及流体循环路径50,其将固液分离部分48与 比在向上流动部分44中引入有机废水的部分更向上部分,并且将由固液分离部分48分离的固体物质引导到向上流动部分44. SS(悬浮固体)被有效地从 通过固液分离部分48处理的水。版权所有(C)2006,JPO&NCIPI
    • 10. 发明专利
    • Anaerobic treatment apparatus and anaerobic treatment method
    • 厌氧处理装置和厌氧处理方法
    • JP2007090168A
    • 2007-04-12
    • JP2005280471
    • 2005-09-27
    • Asahi Beer Eng:KkAsahi Breweries LtdSumitomo Heavy Ind Ltdアサヒビール株式会社住友重機械工業株式会社株式会社アサヒビールエンジニアリング
    • SUZUKI TETSUSHINORITAKE SHIGERUIMABAYASHI SEIJIUECHI KAZUO
    • C02F3/28
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To provide an anaerobic treatment apparatus and an anaerobic treatment method, in each of which organic waste water can be subjected to stable anaerobic treatment while dispensing with such a pretreatment that a solid is separated/solubilized beforehand and while reducing the amount of sludge to be generated. SOLUTION: Solid-containing organic waste water is decomposed into an organic acid in a first acid generation tank 11. The organic waste water treated in the first acid generation tank 11 is introduced into a first reaction tank 12 and treated anaerobically in a granular sludge bed 13 in the first reaction tank while measuring a gasification rate of dissolved COD, namely, a generation rate of methane to be generated in the first reaction tank and supplying a part of the gas to be generated in at least one of the first acid generation tank and the first reaction tank to the lower part of the first reaction tank according to the measured gasification rate. Since the gasification rate is used as an index when judged whether the solid is biodegradable or non-biodegradable and the gas to be generated in at least one of the first acid generation tank and the first reaction tank is supplied to the first reaction tank according to the measured gasification rate, the biodegradable solid can be retained and decomposed in the first reaction tank and the non-biodegradable solid can be discharged from the first reaction tank. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了提供厌氧处理装置和厌氧处理方法,在每种有机废水可以进行稳定的厌氧处理的同时分配预先分解/溶解固体的预处理,同时 减少产生的污泥量。 解决方案:固体含有机废水在第一酸产生罐11中分解成有机酸。将在第一酸生成槽11中处理的有机废水引入第一反应槽12中,并在 在测量溶解COD的气化速率的同时测量第一反应槽中的颗粒污泥床13,即在第一反应罐中产生的甲烷的产生速率,并在第一反应槽中的至少一个中提供待产生的气体的一部分 根据测定的气化率,将酸反应槽和第一反应槽分配到第一反应槽的下部。 由于在判断固体是生物降解性还是不可生物降解性的情况下使用气化率作为指标,并且将根据第一反应槽中的至少一个产生的第一酸生成槽和第一反应槽中产生的气体供给至第一反应槽 可测量的气化速率,可生物降解的固体可以在第一反应槽中保留和分解,并且不可生物降解的固体可以从第一反应槽排出。 版权所有(C)2007,JPO&INPIT