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    • 1. 发明专利
    • Monitoring method for aeration tank
    • 气罐监测方法
    • JP2009066496A
    • 2009-04-02
    • JP2007236170
    • 2007-09-12
    • Panasonic Corpパナソニック株式会社
    • FUJITA TOSHIHIKO
    • C02F3/12G01N33/18
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To solve the following problem: in a monitoring method for an aeration tank where the oxygen consumption rates of sludge are measured at a plurality of points along the down flow direction of the aeration tank and the time change of the consumption rates are displayed, it is difficult to visually grasp the time change of a processing state of the aeration tank because a plurality of curves coexist on a graph. SOLUTION: A plurality of the oxygen consumption rates are integrated with respect to a volume to a measuring position to plot an oxygen consumption rate in the whole aeration tank in a curve on the graph, thereby enabling a visual grasp of a load state of the aeration tank. COPYRIGHT: (C)2009,JPO&INPIT
    • 解决以下问题:在曝气池的监测方法中,在曝气池的沿下游流动方向的多个点测量污泥的耗氧量,并且, 显示消耗速率,由于多个曲线共存在图上,难以目视地掌握曝气池的处理状态的时间变化。 解决方案:将多个氧消耗率相对于体积积分到测量位置,以绘制图中曲线中的整个曝气池中的氧消耗率,从而使得能够可视地掌握负载状态 的曝气池。 版权所有(C)2009,JPO&INPIT
    • 2. 发明专利
    • Treatment state judging method of aeration tank and wastewater treatment control system using it
    • 处理状态判定方法使用水箱和废水处理控制系统
    • JP2009165958A
    • 2009-07-30
    • JP2008006594
    • 2008-01-16
    • Panasonic Corpパナソニック株式会社
    • FUJITA TOSHIHIKOIWASAKI MASATAKA
    • C02F3/12B01D17/02B01D17/035B01D17/12C02F1/24C02F3/00
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To solve the problem that it is misjudged whether an endogenous breathing transition point is a proper position because the distribution of carbon dioxide producing velocities becoming a standard is changed by a change in the activity or the like of sludge, in a treatment state judging method of an aeration tank for measuring the distribution of the carbon dioxide producing velocities of mixed solutions of sludge and wastewater at a plurality of places along the flow direction in the aeration tank to specify the endogenous breathing transition point and controlling the aeration tank so that the endogenous breathing transition point comes to a proper position and a wastewater treatment control system using it. SOLUTION: Since the carbon dioxide producing velocity of endogenous breathing can be always updated using the mixed solution in the aeration tank by comparing the judgment of whether the endogenous breathing transition point is the proper position with the value of the carbon dioxide producing velocity of the endogenous breathing, it can be properly judged whether the endogenous breathing transition point is the proper position even in the case where the activity of sludge changes. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了解决由于二氧化碳生成速度成为标准的分布因污泥的活性等的变化而改变,内因呼吸过渡点是否适当的位置被误判的问题 在曝气池的处理状态判断方法中,用于测量在曝气池中沿着流动方向的多个位置处的污泥和废水的混合溶液的二氧化碳产生速度的分布,以指定内源性呼吸转变点和控制 曝气池,使得内源性呼吸转变点达到适当的位置,并使用其进行废水处理控制系统。

      解决方案:由于内源性呼吸的二氧化碳产生速度可以总是使用曝气池中的混合溶液进行更新,比较内源性呼吸转变点是否适当位置与二氧化碳产生速度值的判断 的内源性呼吸,即使在污泥活动变化的情况下,也可以适当地判断内源性呼吸转变点是否适当。 版权所有(C)2009,JPO&INPIT

    • 3. 发明专利
    • Water quality measuring device
    • 水质测量装置
    • JP2009080071A
    • 2009-04-16
    • JP2007250910
    • 2007-09-27
    • Panasonic Corpパナソニック株式会社
    • IWASAKI MASATAKAFUJITA TOSHIHIKO
    • G01N33/18C02F3/12
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a water quality measuring device capable of accurately calculating an oxygen utilization speed coefficient by preventing erroneous measurement caused by leeches attached on an MLSS meter as a measuring instrument of a sludge density which is necessary to calculate the oxygen utilization speed coefficient of mixed water of discharged water and sludge that is water to be treated in a biotreatment tank. SOLUTION: When the water to be treated is supplied to a measuring tank 117, a water flow is generated in a periphery of a detection part of the MLSS meter 125. At that time, the leeches are not attached (or the attached leeches are separated), and thus, the sludge density of the water to be treated (MLSS) is measured. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种水质测量装置,其能够通过防止由附着在MLSS仪表上的水蛭所引起的错误测量来准确计算氧气利用速度系数,作为计算污泥密度所需的污泥密度的测量仪器 排放水混合水的氧气利用速度系数和生物处理槽中被处理水的污泥。

      解决方案:当待处理的水被供应到测量罐117时,在MLSS仪表125的检测部分的周围产生水流。此时,未附接水蛭(或附着 水蛭分离),因此测量待处理水(MLSS)的污泥密度。 版权所有(C)2009,JPO&INPIT

    • 4. 发明专利
    • Method of measuring treatment condition of sludge and sludge reduction system using it
    • 使用其测量污泥和减少污泥的处理条件的方法
    • JP2008302295A
    • 2008-12-18
    • JP2007151416
    • 2007-06-07
    • Panasonic Corpパナソニック株式会社
    • FUJITA TOSHIHIKO
    • C02F11/00C02F3/12C02F11/12G01N15/06
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a method of measuring treatment conditions of sludge which is arranged in a sewage treatment plant, business establishment, etc., to be used in a sludge reduction system for reducing sludge by converting sludge again into a substrate and solves the problem that there is yet no measuring method which enables the high-precision measurement of the rate of conversion into a substrate and combines durability, low costs and saving of maintenance sufficient for outdoor applications. SOLUTION: The method comprises the step of taking the ratio of sludge to the total volume of the mixed liquid as the volume ratio, calculating the coefficient of the volume concentration from the ratio of the concentration of the sludge to the volume ratio, and calculating the ratio of conversion into a substrate from the coefficient of the volume concentration. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种测量污水处理条件的方法,该污泥布置在污水处理厂,企业等中,用于通过将污泥再次转化为污泥减少系统来减少污泥 基板,并且解决了没有能够高精度地测量转换成基板的速率的测量方法的问题,并且结合了耐用性,低成本和节省足够用于户外应用的维护。 解决方案:该方法包括以污泥与混合液的总体积比为体积比的步骤,根据污泥浓度与体积比计算体积浓度系数, 以及根据体积浓度的系数计算转化成底物的比例。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Particle pulverizing method and device
    • 颗粒粉化方法和装置
    • JP2009112939A
    • 2009-05-28
    • JP2007288363
    • 2007-11-06
    • Panasonic Corpパナソニック株式会社
    • KUSAKABE MASAKAZUFUJITA TOSHIHIKO
    • C02F11/00
    • PROBLEM TO BE SOLVED: To increase an impact force applied to particles and improve pulverization efficiency in a particle pulverizing method and device where an impact part is arranged on the bottom of a cylindrical particle pulverization tank composed of a side face and a bottom face and rotates in a liquid object to be treated containing particles to pulverize the particles by an impact force between the collision surface of the impact part and the particles.
      SOLUTION: In the particle pulverizing method and device, an area through which a rotary blade 11, which is the impact part, passes includes a flow changing rib 12, which is a direction changing means for changing the flow direction of the object to be treated, thereby enabling increasing the impact force to the particles contained in the object to be treated and improving the pulverization efficiency.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了增加施加到颗粒上的冲击力并提高颗粒粉碎方法中的粉碎效率,并且其中冲击部分布置在由侧面和底部构成的圆柱形颗粒粉碎罐的底部上的装置 面对并在包含颗粒的待处理的液体物体中旋转,以通过冲击部分的碰撞表面和颗粒之间的冲击力来粉碎颗粒。 解决方案:在颗粒粉碎方法和装置中,作为冲击部分的旋转叶片11经过的区域包括换流肋12,其是用于改变物体的流动方向的方向改变装置 从而能够增加对包含在被处理物中的粒子的冲击力,提高粉碎效率。 版权所有(C)2009,JPO&INPIT
    • 7. 发明专利
    • Method of controlling concentration of etchant constituent
    • 控制腐殖质浓度的方法
    • JP2010267872A
    • 2010-11-25
    • JP2009118911
    • 2009-05-15
    • Panasonic Corpパナソニック株式会社
    • FUJITA TOSHIHIKOYAMAGUCHI NORIOTAKEYAMA TAKAO
    • H01L21/306
    • PROBLEM TO BE SOLVED: To provide a novel technique for a method of controlling concentration of an etchant constituent.
      SOLUTION: This method of controlling concentration of an etchant constituent includes: collecting an etchant sample from an etchant tank of a wet etching device; measuring the concentration of an etchant constituent of the etchant sample by ion exchange chromatography; and adding an etchant constituent in the etchant tank to set the concentration of the etchant in the etchant tank in a set range based on information of the measurement; wherein the etchant contains phosphoric acid as an etchant constituent. The method of controlling concentration of an etchant constituent further includes moving a holding time of a peak of the phosphoric acid by changing pH of an eluent when a detected peak waveform of the phosphoric acid overlaps a peak waveform of another etchant constituent after an ion exchange column is used a plurality of times in the concentration measurement of the etchant constituent.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种用于控制蚀刻剂成分浓度的方法的新技术。 控制腐蚀剂成分浓度的方法包括:从湿蚀刻装置的蚀刻槽收集蚀刻剂样品; 通过离子交换色谱法测量蚀刻剂样品的蚀刻剂成分的浓度; 并且在蚀刻槽中添加蚀刻剂成分,基于测量的信息将蚀刻剂槽中的蚀刻剂的浓度设定在设定范围内; 其中蚀刻剂含有作为蚀刻剂成分的磷酸。 控制蚀刻剂成分浓度的方法还包括当检测到的磷酸的峰值波形与离子交换柱之后的另一蚀刻剂成分的峰值波形重叠时,通过改变洗脱液的pH来移动磷酸的保留时间 在蚀刻剂成分的浓度测定中多次使用。 版权所有(C)2011,JPO&INPIT
    • 8. 发明专利
    • Treatment state judging method of aeration tank and wastewater treatment control system using it
    • 处理状态判定方法使用水箱和废水处理控制系统
    • JP2009165959A
    • 2009-07-30
    • JP2008006595
    • 2008-01-16
    • Panasonic Corpパナソニック株式会社
    • KUSAKABE MASAKAZUFUJITA TOSHIHIKOIWASAKI MASATAKA
    • C02F3/12B01D17/035C02F1/24C02F3/00
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To solve the problem that the frequent renewal of the standard distribution of oxygen consumption velocities is impossible because wastewater treatment must be temporarily interrupted at each time when the standard distribution is updated and the treatment state of the aeration tank can not be properly judged, in a control method of the aeration tank for measuring the oxygen consumption velocities of mixed solution of activated sludge and wastewater at a plurality of places with respect to the flow direction in a pressing-out flow type aeration tank to form the distribution of oxygen consumption velocities and comparing this distribution with the standard distribution to control the pressing-out flow type aeration tank. SOLUTION: The relation between an oxygen consumption velocity under a load condition becoming a standard and time is measured using a batchwise aeration tank and the relation between the oxygen consumption velocity and the time of the batchwise aeration tank is replaced with the relation of the oxygen consumption velocity and the time of the pressing-out flow type aeration tank to form the standard distribution. By this method, the treatment state of the aeration tank can be properly judged at a low cost. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了解决因为废水处理必须在更新标准分布时每次暂时中断和曝气池的处理状态时,不可能频繁更新耗氧速度标准分布的问题 在用于测量多个位置上的活性污泥和废水的混合溶液相对于压出式曝气池中的流动方向的氧气消耗速度的曝气池的控制方法中,不能正确地判断,以形成 氧气消耗速度的分布,并将该分布与标准分布进行比较,以控制压出式曝气池。 解决方案:使用间歇式曝气池测量负荷条件下的氧气消耗速度与时间之间的关系,并将间歇式曝气池的耗氧速度与时间之间的关系替换为 氧气消耗速度和压出式曝气池的时间形成标准分布。 通过这种方法,可以以低成本适当地判断曝气池的处理状态。 版权所有(C)2009,JPO&INPIT
    • 9. 发明专利
    • Sludge treatment apparatus
    • 泥浆处理设备
    • JP2009119331A
    • 2009-06-04
    • JP2007293938
    • 2007-11-13
    • Panasonic Corpパナソニック株式会社
    • OTANAGI TAKUYAFUCHIGAMI SHINICHIROSAKAKIBARA TAKASHIFUJITA TOSHIHIKO
    • C02F11/02B01D65/02
    • Y02W10/27
    • PROBLEM TO BE SOLVED: To provide a sludge treatment apparatus capable of proceeding a well-balanced self oxidation-oxidation-nitrification-denitrification reaction of sludge in a balanced manner in parallel by supplying chemicals to a biological treatment tank, and obtaining a stable sludge reduction ratio by accelerating the whole decomposition speed of sludge. SOLUTION: The sludge treatment apparatus 20 performs biological treatment by crushing excess sludge by a reconverting-to-substrate means, having nitrogen content less than a given value, generated from an active sludge treatment apparatus 10 for purifying waste water. The sludge treatment apparatus 20 comprises a sludge treatment part 30 and a chemical charge part 50, the sludge treatment part 30 is composed of a biological treatment tank 43 and the reconverting-to-substrate means 33, and the biological treatment tank 43 is provided with an agitation means 32 uniformly agitating sludge, a membrane separation means 36 condensing sludge, and an aeration means 37 under the membrane separation means 36. The chemical charge part 50 has a chemical tank 51 and a chemical transfer pipe 53 transferring the chemical, and the chemical transfer pipe 53 transfers the chemical to the sludge treatment part 30. COPYRIGHT: (C)2009,JPO&INPIT
    • 待解决的问题:提供一种污泥处理装置,其能够通过向生物处理槽供给化学物质平衡地进行平衡的污泥的良好平衡的自氧化 - 氧化 - 硝化 - 脱氮反应,并获得 通过加快污泥的全部分解速度,稳定的污泥减量比。 解决方案:污泥处理装置20通过从用于净化废水的活性污泥处理装置10产生的具有小于给定值的氮含量的再转化 - 底物装置破碎多余的污泥进行生物处理。 污泥处理装置20包括污泥处理部30和化学物质填充部50,污泥处理部30由生物处理槽43和再转移到基板构件33构成,生物处理槽43设置有 均匀搅拌污泥的搅拌装置32,浓缩污泥的膜分离装置36和膜分离装置36下方的曝气装置37.化学物料部分50具有化学品罐51和化学品转移管53, 化学输送管53将化学品转移到污泥处理部分30。版权所有(C)2009,JPO&INPIT
    • 10. 发明专利
    • Sludge volume calculation method, and monitoring method and control method for aeration tank using the same
    • 泥浆体积计算方法,以及使用其的气罐的监测方法和控制方法
    • JP2009226234A
    • 2009-10-08
    • JP2008071018
    • 2008-03-19
    • Panasonic Corpパナソニック株式会社
    • FUJITA TOSHIHIKO
    • C02F3/12
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a method which enables the calculation of a sludge volume, which is an important control item for determining whether the condition of an aeration tank is good or not, at a low cost with no maintenance. SOLUTION: The oxygen utilization rate of a mixed liquid is measured at a plurality of points along the flow-down direction of the aeration tank 4. When a plurality of the measured oxygen utilization rates coincide with each other, it is determined that the aeration tank 4 is under no load condition. The value of the oxygen utilization rate determined as no load condition is stored as a value of the oxygen utilization rate of basal activity. The sludge volume is calculated from the stored value of the oxygen utilization rate of basal activity and/or one of the values of the oxygen utilization rates measured at a plurality of the points. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种能够计算污泥体积的方法,该污泥体积是用于确定曝气池的状况是否良好的重要控制项目,其成本低,无需维护。 解决方案:在曝气池4的下游方向的多个点处测量混合液体的氧气利用率。当多个测量的氧气利用率彼此一致时,确定 曝气池4处于无负载状态。 将作为空载条件确定的氧气利用率的值作为基础活性的氧气利用率的值存储。 从基础活性的氧利用率的存储值和/或在多个点测定的氧气利用率的值之一计算污泥体积。 版权所有(C)2010,JPO&INPIT