| 摘要 |
<p>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.</p> |
