首页> 外国专利> Hydraulic module for the production of a disinfection agent according to electrodiaphragmalysis principle by multistage active material enrichment, disinfection agent cleaning and fully automatic decalcification process

Hydraulic module for the production of a disinfection agent according to electrodiaphragmalysis principle by multistage active material enrichment, disinfection agent cleaning and fully automatic decalcification process

机译:液压模块,用于根据电隔膜原理通过多级活性物质富集,消毒剂清洗和全自动脱钙过程生产消毒剂

摘要

The hydraulic module for the production of a disinfection agent on electrodiaphragmalysis principle by multistage active material enrichment, disinfection agent cleaning and fully automatic decalcification process, is claimed. An effective diaphragmalysis/disinfection agent production is enabled. The hydraulic has fully automatic, water hardness and produced disinfection agent volume-dependent decalcification function. The hydraulic enables high-concentrated and clean disinfection agent production. The quality of the disinfection agent remains water hardness- and pressure dependent constant. The hydraulic module for the production of a disinfection agent on electrodiaphragmalysis principle by multistage active material enrichment, disinfection agent cleaning and fully automatic decalcification process, is claimed. An effective diaphragmalysis/disinfection agent production is enabled. The hydraulic has a fully automatic, water hardness and produced disinfection agent volume-dependent decalcification function. The hydraulic enables a high-concentrated and clean disinfection agent production. The quality of the disinfection agent remains water hardness- and pressure dependent constant. In the decalcification rinsing, the plant carries out the fully automatic and complete decalcification rinsing of the reactors-, valves-, connection tubes and reaction glasses that is dependent upon the raw water hardness as also by the brine quantity flowed by the reactors. The decalcification rinsing is carried out through the rinsing agent moved in the hydraulic in circuit. The pump sucks the rinsing agent in hydraulic and carries out the rinsing that promotes the brine into a mixer or to a second pump used for the acid rinsing. The pre-rinsing and clear rinsing of the hydraulic are realized with direction water and with brine. The gases emerging in the rinsing process escape by the reaction glasses and/or degassing tube. The hydraulic switch is realized by magnet-, compressed air- or motor operating valves. The brine is obtained by a piston, tube or membrane pump in a brine mixing container as also directly in a flow-through mixer. The conveying of weak brine is carried out in the reactors/hydraulics by an extra pump, the piston, circuit or tube pump using brine mixing container. The activation of the pump, which conveys the concentrated brine from the brine tray container into the mixer is controlled by an electronic control. The conveying of weak brine in the reactors/hydraulic is carried out directly by the water pressure by the through-flow mixer. The control, which actuates the pump is controlled by a flow meter in flow dependent manner. The pressure variations and flow speed variations produced by the pump are dismantled by a pneumatic- or mechanical impulse pressure damper. Ceramic, treated or untreated diaphragms are used in special diaphragmalysis reactors for the separation of anode- and cathode areas, where the anode areas are not connected hydraulically in parallel. The reactors have round or angular cross-section and are realized as monoblock. The single electrode receives the cathode- and/or anode functions for several reactors. The anode is constructed as a rod, disk, web or tube. The anode is coated with an individual stainless steel metal or with a mixture of different metals and/or oxides. The tubes are provided for the concentration increase of the disinfection agent. The disinfection causing materials are separated by the undesirable electrolysis column products through the separation. A reaction glass is used for an effective separation. An extra reaction-/disinfection glass is used for the flow volume monitoring of the produced disinfection agent. The flow monitoring glass has a level monitoring. Fluids are used for processing raw water, weak brine and/or disinfection agent and citric acid is used for processing of rinsing means. The materials emerged in the reaction glass are obtained through the electrolysis and/or through the chemical reactions.
机译:本发明要求保护一种液压模块,该液压模块用于通过电隔膜的原理通过多阶段活性物质富集,消毒剂清洁和全自动脱钙过程来生产消毒剂。可以进行有效的隔膜分析/消毒剂生产。液压系统具有全自动,水硬度和产生的消毒剂体积依赖性脱钙功能。液压装置可实现高浓度和清洁消毒剂的生产。消毒剂的质量保持与水硬度和压力有关的常数。本发明要求保护一种液压模块,该液压模块用于通过电隔膜的原理通过多阶段活性物质富集,消毒剂清洁和全自动脱钙过程来生产消毒剂。可以进行有效的隔膜分析/消毒剂生产。液压系统具有全自动,水硬度和根据体积产生消毒剂的脱钙功能。液压装置可实现高浓度和清洁消毒剂的生产。消毒剂的质量保持与水硬度和压力有关的常数。在脱钙漂洗中,工厂对反应器,阀门,连接管和反应玻璃进行全自动和完全脱钙漂洗,这取决于原水的硬度以及反应器中流过的盐水量。脱钙漂洗是通过在液压回路中移动的漂洗剂进行的。泵以液压方式抽吸冲洗剂,然后进行冲洗,从而将盐水提升到混合器或第二台用于酸洗的泵中。液压油的预冲洗和清冲洗可通过定向水和盐水实现。冲洗过程中出现的气体通过反应玻璃和/或脱气管逸出。液压开关通过电磁阀,压缩空气阀或马达操作阀实现。盐水是通过活塞,管式或隔膜泵在盐水混合容器中获得的,也可以直接在流通混合器中获得。弱盐水的输送是通过使用盐水混合容器的额外泵,活塞泵,回路泵或管式泵在反应器/液压油中进行的。泵的启动是通过电子控制器控制的,该泵将浓盐水从盐水托盘容器中输送到混合器中。反应器/液压中弱盐水的输送直接通过通流混合器的水压进行。致动泵的控制装置由流量计以流量相关的方式控制。由泵产生的压力变化和流速变化通过气动或机械脉冲压力阻尼器消除。在特殊的隔膜分析反应器中,使用陶瓷处理过的或未处理过的隔膜来分隔阳极和阴极区域,其中阳极区域不是通过液压方式并联连接的。反应器具有圆形或有角的横截面,并实现为整体式。单个电极接受几个反应器的阴极和/或阳极功能。阳极构造为棒,盘,网或管。阳极涂有单独的不锈钢金属或不同金属和/或氧化物的混合物。提供这些管用于增加消毒剂的浓度。引起消毒的材料通过分离被不希望的电解塔产物分离。反应玻璃用于有效分离。额外的反应/消毒玻璃用于监控生产的消毒剂的流量。流量监控玻璃具有液位监控器。流体用于处理原水,稀盐水和/或消毒剂,柠檬酸用于处理冲洗装置。通过电解和/或通过化学反应获得出现在反应玻璃中的材料。

著录项

  • 公开/公告号DE102009024488A1

    专利类型

  • 公开/公告日2010-12-30

    原文格式PDF

  • 申请/专利权人 PAULY GMBH;

    申请/专利号DE20091024488

  • 发明设计人 PAULY ALEXANDER CHRISTIAN;

    申请日2009-06-10

  • 分类号C25B1/26;

  • 国家 DE

  • 入库时间 2022-08-21 17:47:54

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