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    • 2. 发明专利
    • Nitrogen/phosphor removal treatment method and nitrogen/phosphor removal treatment apparatus
    • 氮/磷离子去除处理方法和氮/磷除去处理装置
    • JP2013212490A
    • 2013-10-17
    • JP2012240208
    • 2012-10-31
    • Toshiba Corp株式会社東芝
    • YAMANAKA OSAMUMENJU TAKUYOSHIZAWA NAOTOKIUCHI TOMOAKI
    • C02F3/30C02F3/34
    • PROBLEM TO BE SOLVED: To provide a nitrogen/phosphor removal treatment apparatus and a nitrogen/phosphor removal treatment method, capable of efficiently removing nitrogen and phosphor from sewage and industrial waste water at low energy costs.SOLUTION: Nitrogen compounds and phosphor compounds are detected from a gas phase and/or a liquid phase in an aerobic tank, wherein: (i) in a case of NH4-N>Nlim and PO4-P≤Plim, a DTA is subjected to high-speed mode driving so that the anaerobic cum aerobic tank is brought into an aerobic treatment atmosphere; (ii) in a case of NH4-N≤Nlim and PO4-P>Plim, the DTA is subjected to low-speed mode driving so that the anaerobic cum aerobic tank is turned into an anaerobic treatment atmosphere; (iii) in a case of NH4-N>Nlim and PO4-P>Plim, a sewage inflow amount is reduced or the DTA is switched to a low-speed mode or the driving is stopped; and (iv) in a case of NH4-N≤Nlim and PO4-P≤Plim, the DTA is subjected to the high-speed mode driving until the concentration of the nitrogen compounds becomes equal to a threshold or the concentration of the phosphor compounds becomes equal to a threshold.
    • 要解决的问题:提供一种氮/磷除去处理装置和氮/磷去除处理方法,能够以低能量成本有效地从污水和工业废水中除去氮和磷。解决方案:检测氮化合物和磷光体化合物 来自有氧罐中的气相和/或液相,其中:(i)在NH4-N> Nlim和PO4-P≤Plim的情况下,对DTA进行高速模式驱动,使得厌氧 暨好氧池进入有氧处理气氛; (ii)在NH4-N≤Nlim和PO4-P> Plim的情况下,DTA进行低速模式驱动,使厌氧和好氧罐变成厌氧处理气氛; (iii)在NH4-N> Nlim和PO4-P> Plim的情况下,污水流入量减少或DTA切换到低速模式或驾驶停止; 和(iv)在NH4-N≤Nlim和PO4-P≤Plim的情况下,对DTA进行高速模式驱动,直到氮化合物的浓度等于阈值或荧光体化合物的浓度 变得等于阈值。
    • 3. 发明专利
    • Soil purification system
    • 土壤净化系统
    • JP2013088361A
    • 2013-05-13
    • JP2011231078
    • 2011-10-20
    • Toshiba Corp株式会社東芝
    • HAYAMI TOKUSUKEHARAGUCHI SATOSHIMATSUNAGA KENTAROYOSHINO MASATOMENJU TAKUKIKUCHI SHIGETONAGAMORI YASUHIKOTODOROKI TOMOHIRO
    • G21F9/28
    • PROBLEM TO BE SOLVED: To provide a soil purification system capable of purifying soil by collecting radioactive cesium from masses of soil while suppressing increase in sizes of apparatuses, complication and increase of energy consumption.SOLUTION: The soil purification system includes a separator, a desorption apparatus, an adsorption tower, and a circulator. The separator applies separation processing to soil including clay minerals to which radioactive cesium is stuck to separate the soil into first particles containing the clay minerals and second particles other than the first particles. The desorption apparatus extracts the radioactive cesium attached to the first particles by an acid aqueous solution of less than 100°C and outputs a cesium containing solution containing the extracted radioactive cesium. The adsorption tower is filled with an adsorbent for adsorbing the radioactive cesium and adsorbs the radioactive cesium contained in the cesium containing solution being in contact with the adsorbent. The circulator circulates a purified solution obtained after adsorbing the radioactive cesium by the adsorption tower to the desorption apparatus.
    • 要解决的问题:提供一种能够通过从大量土壤中收集放射性铯来净化土壤的土壤净化系统,同时抑制装置尺寸的增加,并发症和能量消耗的增加。 解决方案:土壤净化系统包括分离器,解吸装置,吸附塔和循环器。 分离器对包括粘土矿物在内的土壤进行分离处理,放射性铯被粘附到土壤上以将土壤分离成含有粘土矿物和除第一颗粒之外的第二颗粒的​​第一颗粒。 脱附装置通过小于100℃的酸性水溶液提取与第一颗粒附着的放射性铯,并输出含有提取的放射性铯的含铯溶液。 吸附塔填充有用于吸附放射性铯的吸附剂,并吸附与吸附剂接触的含铯溶液中所含的放射性铯。 循环器将通过吸附塔吸附放射性铯后获得的纯化溶液循环到解吸装置。 版权所有(C)2013,JPO&INPIT
    • 4. 发明专利
    • Membrane filtration system
    • 膜过滤系统
    • JP2011131191A
    • 2011-07-07
    • JP2009295622
    • 2009-12-25
    • Toshiba Corp株式会社東芝
    • MATSUSHIRO TAKESHIYOKOGAWA KATSUYAMENJU TAKUFUKUDA MIISOMA TAKAHIROSEKI HIDEJINODA KAZUHIKOKIMIJIMA KAZUHIKO
    • C02F1/44B01D21/01B01D61/20B01D65/02B01D71/02C02F1/28
    • PROBLEM TO BE SOLVED: To suppress clogging of a membrane by separating or collecting granular activated carbon or the like in the previous stage of a membrane filtration apparatus in the system to remove and adsorb soluble components and a trace amount of deleterious substances.
      SOLUTION: A membrane filtration system includes: a raw water receiving well 2 in which a raw water taken from the water source is stored; an activated carbon addition unit 8 for supplying an activated carbon to the raw water receiving well; a solid-liquid separation apparatus 3 for separating the activated carbon to be processed in the raw water from the water; a flocculating agent addition unit 9 for supplying a flocculating agent; a floc forming pond 5 for forming a floc; and a membrane filtration apparatus 6 for separating undissolved components to the water. The system is characterized by installing the solid-liquid separation apparatus in the latter stage of the raw water receiving well in the system.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:通过在系统中的膜过滤装置的前一阶段中分离或收集颗粒活性炭等来抑制膜的堵塞,以除去和吸附可溶性组分和微量的有害物质。 解决方案:膜过滤系统包括:原水接收井2,其中存储从水源获取的原水; 用于向原水接收井供应活性炭的活性炭添加单元8; 用于从原水中分离待处理活性炭的固液分离装置3; 用于供给絮凝剂的絮凝剂添加单元9; 用于形成絮凝物的絮状物形成池5; 以及用于将未溶解的组分分离成水的膜过滤装置6。 该系统的特征在于在系统中的原水接收井的后段安装固液分离装置。 版权所有(C)2011,JPO&INPIT
    • 5. 发明专利
    • Solid-liquid separation system
    • 固液分离系统
    • JP2010214248A
    • 2010-09-30
    • JP2009061420
    • 2009-03-13
    • Toshiba Corp株式会社東芝
    • FUKUDA MIIMENJU TAKUYAMAMOTO YASUSHIAOKI KAZUYOSHIYAMANASHI ICHIROHAYAMI TOKUSUKENODA KAZUHIKO
    • B01D21/26B01D21/01B01D21/24B01D21/30C02F1/52
    • C02F1/38C02F1/56C02F2209/06
    • PROBLEM TO BE SOLVED: To reduce a treatment time and an installation space by improving the separation efficiency in a solid-liquid separation system.
      SOLUTION: The solid-liquid separation system includes a flocculant injector 13 for injecting a flocculant, flocculating solids in raw water, into the raw water, a first flocculant aid injector 16 for injecting a flocculant aid for hardening or strengthening flocs generated in the flocculant injected raw water by the flocculant, and a centrifugal separator 18 having a floc forming portion for rotating the flocculant injected raw water in it to aggregate the solids in the raw water into flocs and a solid recovering portion for rotating the raw water at a higher speed than the floc forming portion to separate the flocs from the raw water.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:通过提高固液分离系统的分离效率来减少处理时间和安装空间。 解决方案:固液分离系统包括用于将絮凝剂絮凝剂絮凝在原水中的絮凝剂注入器13,第一絮凝剂助剂注射器16,用于注入絮凝剂以硬化或加强絮凝剂 絮凝剂通过絮凝剂注入原水;以及离心分离器18,其具有絮凝形成部,用于使絮凝剂注入原水中,将原水中的固体聚集成絮状物,固体回收部分将原水在 比絮状物形成部分高的速度,以将絮凝物与原水分离。 版权所有(C)2010,JPO&INPIT
    • 6. 发明专利
    • Method for treating organic solid-containing waste water, and treatment method therefor
    • 有机固体废水处理方法及其处理方法
    • JP2009022955A
    • 2009-02-05
    • JP2008283437
    • 2008-11-04
    • Toshiba Corp株式会社東芝
    • MATSUSHIRO TAKESHISHIBAZAKI KAZUOASHIKAGA NOBUYUKIMENJU TAKUSHIGENIWA SHINOBU
    • C02F3/28C02F1/78C02F11/06
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To provide a method for treating organic solid-containing waste water where organic solid-containing waste water can be treated at high precision with a small additional amount of ozone, and to provide a treatment device therefor. SOLUTION: The treatment device for organic solid-containing waste water is provided with: an acid generation tank 12 which introduces organic solid-containing waste water thereinto and performs acid generation; and an ozone reaction tank 15 arranged at the downstream side of the acid generation tank 12. The downstream side of the ozone reaction tank 15 is provided with a pH control tank 16 and a biological treatment tank 17. The space between the ozone reaction tank 15 and the acid generation tank 12 is provided with a return tube 31 having a return pump 19a. By circulating waste water between the acid generation tank 12 and the ozone reaction tank 15, acid generation and solubilization in the waste water are simultaneously performed, and the waste water can be surely treated. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种处理含有机固体废水的方法,其中可以用少量附加量的臭氧以高精度处理有机固体废水,并提供其处理装置。 解决方案:含有机固体废水的处理装置设有:将有机固体废水引入其中并进行酸生成的酸生成槽12; 臭氧反应槽15配置在酸生成槽12的下游侧。臭氧反应槽15的下游侧设置有pH控制箱16​​和生物处理槽17.臭氧反应槽15 并且酸生成槽12设置有具有返回泵19a的返回管31。 通过在酸生成槽12和臭氧反应槽15之间循环废水,同时进行废水中的酸生成和溶解,并且可以可靠地处理废水。 版权所有(C)2009,JPO&INPIT
    • 8. 发明专利
    • Flocculating sedimentation treating equipment
    • 絮凝处理设备
    • JP2008055299A
    • 2008-03-13
    • JP2006234229
    • 2006-08-30
    • Toshiba Corp株式会社東芝
    • YOKOGAWA KATSUYAMENJU TAKUMATSUSHIRO TAKESHIMURAYAMA SEIICHI
    • B01D21/01B01D21/30C02F1/52
    • PROBLEM TO BE SOLVED: To provide a flocculating sedimentation treating equipment which is made possible to perform more efficient flocculating sedimentation treatment, by paying attention to the number of revolutions of a stirrer in a floc forming pond and controlling the number of revolutions of the stirrer corresponding to raw water conditions and flocculation state.
      SOLUTION: In the flocculating sedimentation treating equipment which makes a raw water flow into a mixing pond 13, a flocculant is injected and the raw water is rapidly stirred, then floc is formed in the floc forming pond 16 while being stirred, and the floc is sedimented to be treated in a sedimentation pond 18; the stirring strength in the floc forming pond 16 is found by finding a speed gradient G to achieve a target floc forming speed N from the floc grain sizes and the number of floc grains in a water to be treated found from the measuring result by a floc state measuring means 25, by using a relation formula for finding the floc forming speed N based on the speed gradient G to be found from the stirring strength and coefficient of viscosity of the water to be treated in the floc forming pond 16, the floc grain sizes and the number of floc grains, while taking the floc forming speed N as a target value.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种可以进行更有效的絮凝沉降处理的絮凝沉降处理设备,通过注意絮凝池中的搅拌器的转数和控制转速 搅拌器对应于原水条件和絮凝状态。 解决方案:在使原水流入混合池13的絮凝沉降处理设备中,注入絮凝剂,并迅速搅拌原水,然后在絮状物形成池16中搅拌时形成絮凝物, 絮凝沉淀沉淀池18处理; 通过找到速度梯度G,通过从絮凝物颗粒尺寸和待处理水中的絮凝物颗粒数由絮凝物的测量结果发现的速度梯度G来发现絮状物形成池16中的搅拌强度 状态测量装置25,通过使用基于从絮状物形成池16中的待处理水的搅拌强度和粘度系数求出的速度梯度G来求出絮状物形成速度N的关系式, 尺寸和絮体颗粒数,同时以絮凝物形成速度N为目标值。 版权所有(C)2008,JPO&INPIT
    • 9. 发明专利
    • Membrane filtration system
    • 膜过滤系统
    • JP2007021443A
    • 2007-02-01
    • JP2005210529
    • 2005-07-20
    • Toshiba Corp株式会社東芝
    • MENJU TAKUTSUTSUMI MASAHIKOMATSUSHIRO TAKESHIGOTO HISAAKI
    • C02F1/44B01D65/02G01N30/88
    • PROBLEM TO BE SOLVED: To enhance the rate of operation of a membrane filtration system by accurately judging a chemical washing period, a filter membrane replacing period, etc. even when a sludge bottom material is mixed with raw water at the time of a period of water shortage in summer not only to suppress the operation cost of the system low but also to increase the amount of membrane treatment water.
      SOLUTION: The target value "Q" of the amount of membrane treatment water corresponding to the concentration of manganese derived by a manganese densitometer 6 is operated by a membrane treatment water amount target value operator 7 and the flow rate of the membrane treatment water measured by a membrane treatment flowmeter 3 is compared with the target value "Q" output from the membrane treatment water amount target value operator 7 by a membrane treatment water amount constant control device 4. The comparison result is judged to control the water sending amount of a membrane supply pump 1 so as to set it to the target value "Q" of the amount of membrane treatment water.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了通过精确地判断化学洗涤时间,过滤膜更换时间等来提高膜过滤系统的操作速度,即使当污泥底材料与原水混合时, 夏季缺水时期不仅要抑制系统的运行成本低,而且还要增加膜处理用水量。 解决方案:由锰密度计6衍生的锰浓度对应的膜处理水的目标值“Q”由膜处理用水量目标值算子7进行操作,膜处理的流量 将通过膜处理流量计3测量的水与膜处理用水量常数控制装置4的膜处理用水量目标值算出器7输出的目标值“Q”进行比较。判断比较结果,控制送水量 的膜供给泵1,以将其设定为膜处理水的量的目标值“Q”。 版权所有(C)2007,JPO&INPIT