Invention content
It is an object of the invention to overcome above-mentioned the shortcomings of the prior art, and provide a kind of secondary chlorine of multi-channel structure
Sour natrium electrolytic cell device, middle pipe dress electrolytic cell are provided with several independent electrolyte chambers, and multichannel buffer tank corresponds to each electrolysis
Chamber is provided with independent exhalant canal, makes electrolytic efficiency higher.
The object of the present invention is achieved like this:
A kind of sodium hypochlorite electrolytic cell assembly of multi-channel structure, the electrolytic cell assembly include multichannel buffer tank, with
The pipe of multichannel buffer tank connection fills electrolytic cell;The pipe fills the electrolyte chamber that electrolytic cell includes several mutually isolated, described mostly logical
Road surge tank corresponds to each electrolyte chamber and is provided with independent exhalant canal;The multichannel buffer tank is provided with electrolyte into medicine
Mouthful, each electrolyte chamber is provided with finished fluid outlet.
Several spacing boards are provided in the pipe dress electrolytic cell, pipe dress electrolytic cell is separated into several mutually independent electrolysis
Chamber.
Several electrode plates are provided in the pipe dress electrolytic cell, pipe dress electrolytic cell both sides are respectively arranged with fixed plate electrode
Cathode terminal, anode terminal.
The electrode plate includes anode plate, cathode plate;The anode plate is arranged on anode terminal, and cathode plate setting exists
On cathode terminal.
The electrolytic cell assembly includes electrolysis power, the electrolysis power anode jointed anode binding post, and electrolysis power is negative
Pole connects cathode terminal.
The cushion block for spaced electrodes plate is provided between two adjacent electrode plates, electrode plate is fixed by screw arbor assembly
Connection.
The pipe dress electrolytic cell further includes electrolytic zinc-coated steel sheet, and the electrolytic zinc-coated steel sheet includes anode electrolysis plate, catholyte plate, the sun
Pole electrolytic zinc-coated steel sheet is arranged on anode plate, and catholyte plate is arranged on cathode plate.
The electrode plate is fabricated by titanium-base, and the anode plate surface is protected coated with nano level ruthenium iridium oxide
Layer.
The pipe dress electrolytic cell and spacing board are fabricated by hard polyvinyl chloride or organic glass.
The electrolytic cell assembly is provided with the metering pump being connected to electrolyte feeding opening.
Beneficial effects of the present invention are as follows:
Pipe dress electrolytic cell is provided with several independent electrolyte chambers, and multichannel buffer tank corresponds to each electrolyte chamber and is provided with independence
Exhalant canal, make electrolyte evenly into each electrolyte chamber, the utilization rate of electric energy is high in electrolytic process, electrolytic process fever
Measure it is low, pipe dress electrolytic cell in hydrogen can be discharged in time, reduce pipe dress electrolytic cell heat, improve electrolytic efficiency.
Specific implementation mode
The invention will be further described with reference to the accompanying drawings and embodiments.
Referring to Fig. 1, the sodium hypochlorite electrolytic cell assembly of this multi-channel structure, the electrolytic cell assembly includes multichannel buffer
Tank 2, the pipe being connected to multichannel buffer tank 2 fill electrolytic cell 3;The pipe dress electrolytic cell 3 includes several mutually isolated electrolyte chamber
31, the multichannel buffer tank 2 corresponds to each electrolyte chamber 31 and is provided with independent exhalant canal 21;The multichannel buffer tank 2
It is provided with electrolyte feeding opening 1, each electrolyte chamber 31 is provided with finished fluid outlet 6, and hydrogen equally exports 6 rows from finished fluid
Go out, multiple finished fluid outlets 6 ensure that the timely discharge of hydrogen, ensure that production safety, and the interpolar that need not be additionally arranged
Hydrogen gas segregator reduces the production cost of electrolytic cell assembly.
One multichannel buffer tank 2 is set before pipe fills electrolytic cell 3, and pipe dress electrolytic cell 3 is provided with several independent electricity
Solve chamber 31, multichannel buffer tank 2 corresponds to each electrolyte chamber 31 and is provided with independent exhalant canal 21, make electrolyte evenly into
Each electrolyte chamber 31, keeps the concentration of electrolyte gradient in each electrolyte chamber 31 low, i.e., each position electrolyte is dense in electrolyte chamber 31
Degree is not much different, and the utilization rate of electric energy is high in electrolytic process, and electrolytic process calorific value is low, reduces the heat of pipe dress electrolytic cell 3, carries
High electrolytic efficiency.
Multichannel buffer tank 2 must can guarantee that electrolyte stablizes outflow, and the quantity of exhalant canal 21, and size must be through
Stringent calculating is crossed, electrolyte various concentration is measured and is electrolysed consumed electric energy, the heat of generation obtains water outlet by measuring and calculation
The quantity and size in channel 21, which must assure that, is in that energy consumption is minimum in electrolyte electrolytic process, each under the operating mode of heat minimum
The product of kind specification is required for completing after stringent test.
Recirculated cooling water, the electrolytic cell in the present invention is arranged due to the excessive needs of heat in conventional electrolytic cell in electrolytic cell
Device need not be filled in pipe is arranged cooling device in electrolytic cell 3, simplify the internal structure of pipe dress electrolytic cell 3, reduce electrolytic cell
The production cost of device.
Further, several spacing boards 8 are provided in the pipe dress electrolytic cell 3, pipe dress electrolytic cell 3 is separated into several phases
Mutual independent electrolyte chamber 31.
Further, several electrode plates 4 are provided in the pipe dress electrolytic cell 3,3 both sides of pipe dress electrolytic cell are respectively arranged with
Cathode terminal 7, the anode terminal 5 of fixed plate electrode 4.
Further, the electrode plate 4 includes anode plate, cathode plate;The anode plate is arranged on anode terminal 5,
Cathode plate is arranged on cathode terminal 7.
Further, the electrolytic cell assembly includes electrolysis power, the electrolysis power anode jointed anode binding post 5,
Electrolysis power cathode connects cathode terminal 7.
Further, the cushion block for spaced electrodes plate 4 is provided between two adjacent electrode plates 4, electrode plate 4 passes through
Screw arbor assembly 9 is fixedly connected, and 9 each component of screw arbor assembly is fabricated by Kynoar, the corrosion resistance of Kynoar
By force, oxidation resistance is strong, is suitable for sodium hypochlorite electrolysis production.
Further, the pipe dress electrolytic cell 3 further includes electrolytic zinc-coated steel sheet, and the electrolytic zinc-coated steel sheet includes anode electrolysis plate, cathode electricity
Plate is solved, the anode electrolysis plate is arranged on anode plate, and catholyte plate is arranged on cathode plate.
Further, the electrode plate 4 is fabricated by titanium-base, and the anode plate surface is coated with nano level ruthenium iridium
Protective oxide film.
Further, the pipe dress electrolytic cell 3 and spacing board 8 are fabricated by hard polyvinyl chloride or organic glass, firmly
Polyvinyl chloride, the corrosion resistance of organic glass are strong, and oxidation resistance is strong, and have certain intensity, are suitable for sodium hypochlorite
Electrolysis production.
Further, the electrolytic cell assembly is provided with the metering pump being connected to electrolyte feeding opening 1.
Specific production stage is as follows:
Electrolyte is conveyed by metering pump to be entered through electrolyte feeding opening 1 in multichannel buffer tank 2, multichannel buffer tank 2
Each exhalant canal 21 to 31 conveying electrolyte of corresponding electrolyte chamber, electrolyte is electrolysed in independent electrolyte chamber 31,
Finished fluid and hydrogen are discharged in time by the finished product medicine outlet 6 of respective electrolyte chamber 31.
Above-described embodiment is the preferred embodiment of the present invention, and the present invention can also have other embodiments.The technology of this field
Personnel can also make equivalent variations or replacement under the premise of without prejudice to spirit of that invention, these equivalent modifications or replacement are wrapped
It is contained in the range set by the application claim.