CN209507690U - Automate electrolysis unit - Google Patents
Automate electrolysis unit Download PDFInfo
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- CN209507690U CN209507690U CN201920036718.4U CN201920036718U CN209507690U CN 209507690 U CN209507690 U CN 209507690U CN 201920036718 U CN201920036718 U CN 201920036718U CN 209507690 U CN209507690 U CN 209507690U
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Abstract
The utility model relates to a kind of automation electrolysis units, include: organization of supply, rabbling mechanism, it is electrolysed mechanism, mixed organization, sensing mechanism and control mechanism, the organization of supply and rabbling mechanism can provide aqueous solution and hydrochloride aqueous solution respectively, and being electrolysed mechanism and capable of being electrolysed to hydrochloride aqueous solution and form oxidation is compound gas, wherein, it is compound gaseous state aqueous solution that aqueous solution and oxidation are compound gas mixing formation oxidation by mixed organization, and sensing mechanism can sense hydrochloride aqueous solution and oxidation is the water level height of both compound gaseous state aqueous solutions to form level sensing information, then control device can control organization of supply according to level sensing information, rabbling mechanism, electrolysis mechanism is operated with mixed organization, and then automatically generating hydrochloride aqueous solution and oxidation is compound gaseous state aqueous solution, whereby, the utility model can be certainly Dynamic production oxidation is compound gaseous state aqueous solution come to reduce human cost, and then opposite can improve production efficiency.
Description
Technical field
The utility model about it is a kind of can mass production oxidation be compound gaseous state aqueous solution electrolysis unit, especially
It is a kind of to produce the electrolysis unit that oxidation is compound gaseous state aqueous solution automatically, use reduction human cost.
Background technique
Since oxidation is that compound gas itself has not pairs of free active electrons, so that oxidation is compound gas
State aqueous solution has potent oxidability, can be used to protein, the victory peptide, DNA of the pathogen such as oxidizing bacteria, virus, mould
Or RNA, it uses to eliminate the pathogen such as this, and since gaseous oxidation is that compound gas can not provide user conveniently and make
With, therefore the industries such as cultivation and sewage treatment ... are herded in health care, food processing, environmental protection, industrial water, the rising sun at present
In, be mostly the formation soluble in water oxidation of compound gas by oxidation it is compound gaseous state aqueous solution, enables user that can conveniently make
With oxidation be composite water solution carry out disinfection, sterilize, deodorization.
However, being all to form oxidation come electrolytic saltwater using existing electrolysis unit at present to improve aforementioned missing
Compound gas, then by oxidation be compound gas it is soluble in water to form oxidation be compound gaseous state aqueous solution, still, when existing
There is electrolysis unit when being electrolysed, existing electrolysis unit needs to employ the remaining capacity that operator carrys out keyholed back plate saline solution, and
When the remaining capacity of operator's discovery saline solution is very few, operator must just be allowed with the existing electrolysis unit of manual operation
Existing electrolysis unit generates more saline solutions, and whereby, for existing electrolysis unit after operating a period of time, operator is necessary
Taking time, it is depleted to avoid saline solution to confirm that the residual capacity of saline solution comes, and then existing electrolysis unit could continue to produce
Oxidation is compound gaseous state aqueous solution, and leading to existing electrolysis unit can not mass production oxidation be in a short time compound gaseous state
Aqueous solution.
New content
The main purpose of the utility model is that reducing the operator of operation electrolysis unit, and controlled with control mechanism
It is compound gaseous state aqueous solution that electrolysis unit produces oxidation automatically, allow electrolysis unit in a short time can mass production oxidation system it is multiple
Mould assembly gaseous state aqueous solution, so allow user can be easy to use oxidation be compound gaseous state aqueous solution carry out disinfection, sterilize with
And deodorization.
To realize foregoing purpose, the utility model is about a kind of automation electrolysis unit, the automation electrolysis unit
Mainly by an organization of supply, a rabbling mechanism, an electrolysis mechanism, a mixed organization, a sensing mechanism and control mechanism institute
It constitutes, the organization of supply is to provide an aqueous solution, and the rabbling mechanism is to receive the aqueous solution, and by the water
Solution and multiple salt particles stir to form a hydrochloride aqueous solution to contain salt, then the electrolysis mechanism is connected to described with one
The electrolytic cell of rabbling mechanism and one be connected to the electrolytic cell power-supply unit, the electrolytic cell is to contain the salt
Water aqueous solution, and the power-supply unit can provide voltage to the electrolytic cell, make the electrolytic cell water-soluble to the salt water
It is compound gas that liquid, which is electrolysed to form an oxidation,.
In addition, the mixed organization, with a gas-liquid mixed component and one be connected to the gas-liquid mixed component at
Product slot, the gas-liquid mixed component are connected to the organization of supply and electrolytic cell simultaneously, and the aqueous solution and oxidation system is multiple
It is compound gaseous state aqueous solution that mould assembly gas mixing, which forms the oxidation that one is sent to the pan tank, wherein the sensing mechanism
The first liquid level sensor and one for being installed on the rabbling mechanism with one are installed on the second level sensing of the pan tank
Device, first liquid level sensor can sense the water level height positioned at hydrochloride aqueous solution described in the rabbling mechanism inside with shape
At one first level sensing information, and second liquid level sensor can be sensed positioned at oxidation system described in the pan tank inside
The water level height of compound gaseous state aqueous solution is to form one second level sensing information.
In addition, the control mechanism simultaneously be connected to the organization of supply, rabbling mechanism, electrolysis mechanism, mixed organization with
Sensing mechanism, the control mechanism can be controlled according to the first level sensing information the organization of supply and rabbling mechanism into
Row running to generate the hydrochloride aqueous solution, and the control mechanism can be controlled according to the second level sensing information it is described
Organization of supply, electrolysis mechanism and mixed organization are operated, and allowing the pan tank to fill with the oxidation is that compound gaseous state is water-soluble
Liquid.
In a preferred embodiment, the reactive tank and one that the gas-liquid mixed unit contains the aqueous solution with one are connect
Receive the gas mixer that the oxidation is compound gas, the reactive tank connects one first motor, and the first motor energy
The aqueous solution inside the reactive tank will be located at and first flow through the inside that the gas mixer flows back into the reactive tank again, so that
It is the inside that compound gas flows back into the reactive tank that the aqueous solution, which carries the oxidation secretly, makes way for the water of the reactive tank
It is compound gaseous state aqueous solution that solution, which is changed into the oxidation,.
The sensing mechanism further has a third liquid level sensor for being installed on the reactive tank, the third liquid level
It is the water level height of compound gaseous state aqueous solution to form one that sensor, which can be sensed positioned at oxidation described in the reactive tank inside,
Third level sensing information, and the control mechanism starts the organization of supply, electricity according to the third level sensing information
It is compound gaseous state aqueous solution that solution mechanism and gas mixer, which are operated to generate the oxidation,.
In this embodiment, the sensing mechanism further has a second concentration sensing for being installed on the reactive tank
Device, it is the dense of compound gaseous state aqueous solution that second concentration sensor, which can be sensed positioned at oxidation described in the reactive tank inside,
Degree allows the control mechanism according to second concentration information to form second concentration information for being transferred to the control mechanism
And controlling the oxidation is that compound gaseous state aqueous solution is delivered to the pan tank.
In another preferred embodiment, the mixed organization further has one second motor and a dilution trap, and described
The oxidation can be that compound gaseous state aqueous solution flows into the dilution between the pan tank and dilution trap by two motor
The inside of slot, and the dilution trap is connected to the organization of supply, and receiving the aqueous solution and oxidation is compound vaporous water
Solution makes the aqueous solution and oxidation to be compound gaseous state aqueous solution forms a concentration in the internal mix of the dilution trap to be lower than
The oxidation is that the dilution oxidation of compound gaseous state aqueous solution is compound gaseous state aqueous solution.
Wherein, the sensing mechanism further has the 4th liquid level sensor for being installed on the dilution trap, and described
Four liquid level sensors can sense positioned at dilution oxidation described in the dilution trap inside be compound gaseous state aqueous solution water level it is high
It is low to form one the 4th level sensing information, and the control mechanism starts the confession according to the 4th level sensing information
It answers mechanism to be operated with second motor, allows the aqueous solution and oxidation is that compound gaseous state aqueous solution flows into the dilution
The inside of slot is compound gaseous state aqueous solution to form the dilution oxidation.
In another embodiment, the sensing mechanism further has a temperature sensing for being installed on the electrolytic cell
Device, the temperature sensor can sense the temperature positioned at hydrochloride aqueous solution described in the electrolyte bath and be transferred to forming one
The temperature information of the control mechanism enables the control mechanism to generate an information warning or stopping according to the temperature information
The power-supply unit provides voltage to the electrolytic cell.
In another preferred embodiment, the electrolytic cell of the electrolysis mechanism is connected to the organization of supply, so that the electrolysis
Slot can receive the aqueous solution, and the electrolytic cell is equipped with the discharge electrically-controlled valve of a limitation liquid flowing, wherein the sensing machine
Structure further has the 5th liquid level sensor for being installed on the electrolytic cell, and the 5th liquid level sensor can sense and be located at
Aqueous solution described in the electrolyte bath water level height to form one the 5th level sensing information, then the control mechanism according to
Start the automatically controlled valve function according to the 5th level sensing information, makes way for the aqueous solution energy of the electrolyte bath
It is discharged.
In aforementioned four embodiments, the rabbling mechanism have one be connected to the saline slot of the organization of supply with
And one be connected to the saline slot salt water storage tank, the salt water storage tank to contain the hydrochloride aqueous solution, and
First liquid level sensor of the sensing mechanism is installed, also, the sensing mechanism further has one to be installed on the salt water
First concentration sensor of stirred tank, first concentration sensor can be sensed positioned at salt water water described in the saline slot
The salt concentration of solution allows the control mechanism according to described in form first concentration information for being transferred to the control mechanism
First concentration information and control the hydrochloride aqueous solution and be delivered to the salt water storage tank.
In addition, the flowmeter and one of fluid flow can be calculated and change by being equipped with one between the rabbling mechanism and electrolytic cell
The electrically-controlled valve of liquid flowing is limited, the flowmeter and electrically-controlled valve are electrically connected at the control mechanism, and work as the control machine
When structure receives second concentration information, the electrically-controlled valve can allow the hydrochloride aqueous solution to flow to the flowmeter, make institute
State the flow that flowmeter calculates the hydrochloride aqueous solution, when the flow that the flowmeter calculates the hydrochloride aqueous solution have reached it is silent
Recognize value, the electrically-controlled valve can stop the hydrochloride aqueous solution and flow to the flowmeter.
It is compound gaseous state aqueous solution that the characteristics of the utility model, which is that sensing mechanism can sense hydrochloride aqueous solution and oxidation,
The remaining capacity of the two, and when sensing mechanism sense hydrochloride aqueous solution and oxidation be both compound gaseous state aqueous solutions capacity
When very few, control mechanism can control organization of supply, rabbling mechanism, electrolysis mechanism and mixed organization and be operated to give birth to automatically
It produces hydrochloride aqueous solution and oxidation is compound gaseous state aqueous solution, can be reduced operator whereby, when electrolysis unit is operated
To reduce human cost, so allow electrolysis unit in a short time can mass production oxidation be compound gaseous state aqueous solution.
Detailed description of the invention
Fig. 1 is the schematic diagram that the utility model automates electrolysis unit；
Fig. 2 is the schematic diagram of electrolytic cell；
Fig. 3 is the schematic diagram of switch unit；
Fig. 4 is the schematic diagram of gas mixer；
Fig. 5 A is the schematic diagram for being electrolysed mechanism and carrying out electrolysis operation；
Fig. 5 B is the schematic diagram that mixed organization forms that oxidation is compound gaseous state aqueous solution；
Fig. 5 C be the first liquid level sensor cooperate control mechanism carry out using schematic diagram；
Fig. 5 D be the second liquid level sensor and the first concentration sensor cooperation control mechanism carry out using schematic diagram；
Fig. 5 E be third liquid level sensor and the second concentration sensor cooperation control mechanism carry out using schematic diagram；
Fig. 5 F be the 4th liquid level sensor cooperate control mechanism carry out using schematic diagram；
Fig. 5 G is the schematic diagram that the 5th liquid level sensor cooperates control mechanism to clean electrolytic cell；
Fig. 5 H be temperature sensor cooperate control mechanism carry out using schematic diagram.
Description of symbols: 1- automates electrolysis unit；10- organization of supply；11- aqueous solution input pipe；The storage of 12- aqueous solution
Deposit slot；13- the first aqueous solution efferent duct；14- the second aqueous solution efferent duct；15- third aqueous solution efferent duct；16- the 4th is water-soluble
Liquid efferent duct；20- rabbling mechanism；21- saline slot；22- salt water storage tank；23- salt water inlet pipe；24- salt water delivery pipe；
25- flowmeter；26- electrically-controlled valve；30- is electrolysed mechanism；31- electrolytic cell；311- is electrolysed efferent duct；The upper delivery pipe of 312-；Under 313-
Delivery pipe；314- discharges electrically-controlled valve；32- switch unit；321- the first salt water water inlet pipe；321a- first switches electrically-controlled valve；322-
Second salt water water inlet pipe；322a- second switches electrically-controlled valve；323- the first aqueous solution water inlet pipe；323a- third switches electrically-controlled valve；
324- the second aqueous solution water inlet pipe；324a- the 4th switches electrically-controlled valve；The first ingress pipe of 325-；The second ingress pipe of 326-；33- electricity
Source supply unit；40- mixed organization；41- gas-liquid mixed component；411- reactive tank；412- gas mixer；412a- mixing unit；
412b- first connecting portion；412c- second connecting portion；The first mixing tube of 413-；The second mixing tube of 414-；The first motor of 415-；
42- pan tank；421- finished product input pipe；422- finished product efferent duct；The second motor of 423-；43- dilution trap；50- sensing mechanism；
The first liquid level sensor of 51-；The second liquid level sensor of 52-；53- third liquid level sensor；The 4th liquid level sensor of 54-；55-
Five liquid level sensors；56- temperature sensor；The first concentration sensor of 57-；The second concentration sensor of 58-；60- control mechanism.
Specific embodiment
The utility model is further described with attached drawing combined with specific embodiments below, the advantages of the utility model and feature
Will be with description and it is apparent.
Refering to Figure 1, the utility model automates electrolysis unit 1 mainly by an organization of supply 10, a rabbling mechanism
20, an electrolysis mechanism 30, a mixed organization 40, a sensing mechanism 50 and a control mechanism 60 are constituted, and organization of supply 10 is used
To provide an aqueous solution, in this embodiment, organization of supply 10 has an aqueous solution input pipe 11 that can convey the aqueous solution
And one be connected to aqueous solution input pipe 11 aqueous solution reserve tank 12, and aqueous solution reserve tank 12 is described water-soluble to contain
Liquid, and connect one first aqueous solution efferent duct 13, one second aqueous solution efferent duct 14, a third aqueous solution efferent duct 15 and one
4th aqueous solution efferent duct 16, whereby, when the aqueous solution flows into aqueous solution reserve tank 12 via aqueous solution input pipe 11,
The aqueous solution inside aqueous solution reserve tank 12 can separately flow into again the first, second, third and fourth aqueous solution efferent duct 13,14,
15,16 inside.
There is rabbling mechanism 20 a saline slot 21 and a salt water storage tank 22, saline slot 21 to be connected to supply
First aqueous solution efferent duct 13 of mechanism 10, enables the aqueous solution to flow into salt water via the first aqueous solution efferent duct 13 and stir
Saline slot 21 aqueous solution and multiple salt particles can be stirred to form the salt water to contain salt for the inside for mixing slot 21
Aqueous solution, in this embodiment, the multiple salt particle can be the artificial inside for being voluntarily incorporated in saline slot 21, wherein
Salt water storage tank 22 has one can convey the salt water inlet pipe 23 of the hydrochloride aqueous solution and one to convey the salt water water-soluble
The salt water delivery pipe 24 of liquid, and salt water inlet pipe 23 is connected to saline slot 21, so that being located inside saline slot 21
The hydrochloride aqueous solution can flow into the inside of salt water storage tank 22 via salt water inlet pipe 23, and salt water storage tank 22 can be deposited
Put the hydrochloride aqueous solution, wherein the installation of salt water delivery pipe 24 one can calculate and change the flowmeter 25 and one of fluid flow
Limit the electrically-controlled valve 26 of liquid flowing.
It please refers to shown in Fig. 1 and Fig. 2, there is an electrolytic cell 31, a switch unit 32 and a power supply to supply for electrolysis mechanism 30
Unit 33 is answered, electrolytic cell 31 is connected to switch unit 32, and is equipped with an electrolysis efferent duct 311, two for being connected to mixed organization 40
Upper delivery pipe 312 and two lower delivery pipes 313, and delivery pipe 312 and one of them time delivery pipe 313 be both one of them on
It is connected to a cathode (not shown) of electrolytic cell 31, then on another both delivery pipe 312 and another lower delivery pipe 313 connect
An anode (not shown) of electrolytic cell 31 is passed through, in addition, respectively installation one can limit the row of liquid flowing to each lower delivery pipe 313
Electrically-controlled valve 314 is put, and switch unit 32 is connected to the second aqueous solution efferent duct 14 and rabbling mechanism of organization of supply 10 simultaneously
20 salt water delivery pipe 24, and can selectively control and the aqueous solution or the hydrochloride aqueous solution is allowed to flow into the interior of electrolytic cell 31
Portion, as shown in Fig. 2, switch unit 32 has one first salt water water inlet pipe 321, one second salt water water inlet pipe in this embodiment
322, one first aqueous solution water inlet pipe 323 and one second aqueous solution water inlet pipe 324, the first and second salt water water inlet pipe 321,322 is all
It is connected to salt water delivery pipe 24, and first that the first salt water water inlet pipe 321 installation one can limit the hydrochloride aqueous solution flowing cuts
Electrically-controlled valve 321a is changed, then it is automatically controlled to limit the second switching that the hydrochloride aqueous solution flows for the second salt water water inlet pipe 322 installation one
Valve 322a, wherein both the first and second aqueous solution water inlet pipe 323,324 is connected to the second aqueous solution efferent duct 14, and the first water
Solution enters the third switching electrically-controlled valve 323a of one limitation of the installation of the water 323 energy aqueous solution flowing, then the second aqueous solution enters water 324
Installation can limitation aqueous solution flowing the 4th switching electrically-controlled valve 324a, as shown in figure 3, the first salt water water inlet pipe 321 with
Both first aqueous solution water inlet pipe 323 is connected to first ingress pipe 325 for being connected to 31 anode of electrolytic cell, and the second salt water
Both water inlet pipe 322 and the second aqueous solution 343 are connected to second ingress pipe 326 for being connected to 31 cathode of electrolytic cell.
Again refering to Figure 1, power-supply unit 33 is electrically connected at electrolytic cell 31, as shown, flowmeter 25 with
Both electrically-controlled valves 26 are between rabbling mechanism 20 and electrolytic cell 31, and electrically-controlled valve 26 can selectively allow salt water delivery pipe 24 to present
Connected state or closed state, wherein when connected state is presented in the existing electrically-controlled valve 26 of salt water delivery pipe 24, the salt water water
Solution can flow to switch unit 32 from salt water storage tank 22, conversely, presenting when the existing electrically-controlled valve 26 of salt water delivery pipe 24
When closed state, the hydrochloride aqueous solution can not flow to switch unit 32 from salt water storage tank 22.
Again refering to Figure 1, mixed organization 40 has a gas-liquid mixed component 41, a pan tank 42 and a dilution trap
43, the reactive tank 411 and one that gas-liquid mixed component 41 is connected to pan tank 42 with one are connected to the gas of electrolysis efferent duct 311
Body mixer 412 enables gas-liquid mixed component 41 to be connected to organization of supply 10 and electrolytic cell 31 simultaneously, wherein reactive tank 411
One first mixing tube 413 and one second mixing tube 414 are equipped between gas mixer 412, so that reactive tank 411 is via the
One, two mixing tubes 413,414 and be connected to gas mixer 412, and second that reactive tank 411 is connected to organization of supply 10 is water-soluble
Liquid efferent duct 14 enables reactive tank 411 to receive the aqueous solution.
It please refers to shown in Fig. 3, gas mixer 412 is equipped with a mixing unit 412a for being connected to electrolysis efferent duct 311, mixing
Portion 412a is presented hollow pattern, and is smaller than the first and second mixing tube 413,414 in internal aperture, and the one end mixing unit 412a
A first connecting portion 412b for being connected to the first mixing tube 413 is extended to form, and is prolonged in one end far from first connecting portion 412b
Stretch the second connecting portion 412c to be formed and be connected to the second mixing tube 414, wherein the internal holes of first and second interconnecting piece 412b, 412c
Taper pattern is presented in diameter, in addition, there is pan tank 42 a finished product input pipe 421 and one for being connected to reactive tank 411 to be connected to
The finished product efferent duct 422 of dilution trap 43, and dilution trap 43 is connected to the 4th aqueous solution efferent duct 16 of organization of supply 10, to connect
Receive the aqueous solution.
Again refering to Figure 1, sensing mechanism 50 have one first liquid level sensor 51, one second liquid level sensor 52,
The 5th liquid level sensor 55 of the 4th liquid level sensor 54,1 of one third liquid level sensor 53,1, a temperature sensor 56,1
One concentration sensor 57 and one second concentration sensor 58, as shown, the first liquid level sensor 51 is installed on rabbling mechanism
20 salt water storage tank 22, and the water level height for being located at hydrochloride aqueous solution described in 22 inside of salt water storage tank can be sensed, and the
Two liquid level sensors 52 are installed on pan tank 42, and can sense the water level height for being located at liquid in 42 inside of pan tank, wherein the
Three liquid level sensors 53 are installed on reactive tank 411, and can sense the water level height for being located at liquid described in 411 inside of reactive tank
It is low, and the 4th liquid level sensor 54 is installed on dilution trap 43, and can sense and be located at liquid described in 43 inside of dilution trap
Water level height, in addition, both the 5th liquid level sensor 55 and temperature sensor 56 are installed on electrolytic cell 31, wherein the 5th liquid
Level sensor 55 can sense the water level height for being located at liquid in 31 inside of electrolytic cell, and temperature sensor 56 can sense and be located at electrolysis
The temperature height of liquid in 31 inside of slot, as shown, the first concentration sensor 57 is installed on saline slot 21, and can salt water
The concentration of liquid in 21 inside of stirred tank, then the second concentration sensor 58 is installed on reactive tank 411, and can sense and be located at reactive tank
The concentration of liquid in 411 inside, in addition, control mechanism 60 is connected to organization of supply 10, rabbling mechanism 20, electrolysis mechanism simultaneously
30, mixed organization 40 and sensing mechanism 50, and can control organization of supply 10, rabbling mechanism 20, electrolysis mechanism 30, mixed organization 40
It is operated with sensing mechanism 50.
It please refers to shown in Fig. 3 and Fig. 5 A, when automation electrolysis unit 1 carries out electrolysis operation, the unlatching of control mechanism 60 is stirred
Mix the electrically-controlled valve 26 of mechanism 20, the first and second switching electrically-controlled valve 321a, 322a of switch unit 32 and the discharge electricity of electrolytic cell 31
Valve 314 is controlled, so that electrically-controlled valve 26 can continue the hydrochloride aqueous solution being located inside salt water storage tank 22 being provided to switching list
Member 32, and the hydrochloride aqueous solution can be imported the inside for flowing to electrolytic cell 31 by switch unit 32, and the inside of electrolytic cell 31 is allowed to fill
The full hydrochloride aqueous solution can continue to flow into electricity due to being located at the hydrochloride aqueous solution electrically-controlled valve 26 inside salt water storage tank 22
The inside of slot 31 is solved, and when the liquid level for the hydrochloride aqueous solution being located inside electrolytic cell 31 is greater than upper delivery pipe 312
When height and position, the hydrochloride aqueous solution of part can be ejected via upper delivery pipe 312 to overflow to avoid the hydrochloride aqueous solution
Make electrolytic cell 31 water-soluble to the salt water next, power-supply unit 33 provides voltage to electrolytic cell 31 for electrolytic cell 31
Liquid is electrolysed to generate redox reaction, and then the electrolysed hydrochloride aqueous solution will form one to flow into electrolysis defeated
The oxidation of outlet pipe 311 is compound gas, and in this embodiment, the oxidation is that compound gas is set as chlorine dioxide, secondary chlorine
Acid or ozone.
Wherein, the hydrochloride aqueous solution is after electrolysis, positioned at the salt of hydrochloride aqueous solution described in 31 inside of electrolytic cell
Point concentration can be reduced, and still, can be continued due to being located at the existing electrically-controlled valve 26 of the hydrochloride aqueous solution inside salt water storage tank 22
Flow into electrolytic cell 31 inside, and then electrolytic cell 31 can be carried out electrolysis operation when persistently supplement high salt concentration the salt water it is water-soluble
Liquid to reduce to avoid the salt concentration for being located at hydrochloride aqueous solution described in 31 inside of electrolytic cell.
Please refer to shown in Fig. 5 B, formed after the oxidation is compound gas, the oxidation be compound gas via
Electrolysis efferent duct 311 and flow to the gas mixer 412 of gas-liquid mixed component 41, and control mechanism 60 controls organization of supply 10 and mentions
For the aqueous solution, the aqueous solution is made to flow to the reaction of gas-liquid mixed component 41 via third aqueous solution efferent duct 15
Inside slot 411, then, the first motor 415 that the starting of control mechanism 60 one is assembled in the first mixing tube 413, and the first motor 415
It can will be located at the aqueous solution inside reactive tank 411 constantly by the first mixing tube 413 inflow body mixer 412, then by the
Two mixing tubes 414 flow back into the inside of reactive tank 411, wherein when the mixing unit of the aqueous solution inflow gas mixer 412
When 412a, because the inside aperture of mixing unit 412a is less than the first and second mixing tube 413,414, so that the flow velocity of the aqueous solution
It can speed, and then the oxidation of inflow gas mixer 412 is allowed to be that compound gas can rapidly be brought by the aqueous solution
To reactive tank 411, when the oxidation is the inside that compound gas flows into reactive tank 411, the oxidation is compound
A part of gas can carry out being mixed to form an oxidation being that compound gaseous state is water-soluble with the aqueous solution being located inside reactive tank 411
Liquid, and the remaining oxidation is that compound gas can flow into reactive tank 411, and with the water that is located inside reactive tank 411
Solution carries out being mixed to form the oxidation being compound gaseous state aqueous solution, wherein since the inside aperture of mixing unit 412a is small
In the first and second mixing tube 413,414, and then when in order to avoid the aqueous solution inflow gas mixer 412, the aqueous solution meeting
Reactive tank 411 is back to by the first mixing tube 413, multiple gases can be equipped between the first mixing tube 413 and the second mixing tube 414
Mixer 412 allows the reverse osmosis water aqueous solution that can branch to multiple gas mixers 412, in this embodiment, the oxygen
Change is that compound gaseous state aqueous solution is set as aqueous solution of chlorine dioxide, hypochloric acid water solution or ozone water solution.
When 411 inside of reactive tank, the newly formed oxidation is compound gaseous state aqueous solution, the oxidation is compound gas
The oxidation of state aqueous solution is that compound gas concentration amount is lower, but because the oxidation can be again compound by the first motor 415
Gaseous state aqueous solution inflow gas mixer 412, then the oxidation is allowed to be that compound gaseous state aqueous solution flows back into reactive tank 411, make
Obtaining the more oxidation is the inside that compound gas can flow to reactive tank 411, and then the oxidation is compound vaporous water
The oxidation of solution is that compound gas concentration can gradually rise, wherein when the oxidation is the oxidation of compound gaseous state aqueous solution
When being that compound gas concentration reaches default value, Kong Ji mechanism 60 can close the first motor 415, so that the oxidation is compound
Gaseous state aqueous solution can not be again via 413 inflow gas mixer 412 of the first mixing tube.
Next, control mechanism 60 control it is described oxidation be compound gaseous state aqueous solution can via finished product input pipe 421 and
Flow into pan tank 42 inside, to directly using it is described oxidation be compound gaseous state aqueous solution, then pan tank 42 can be arranged directly
Out it is described oxidation be compound gaseous state aqueous solution, wherein if to directly using it is described oxidation be compound gaseous state aqueous solution
Oxidation is that compound gas is dense excessively high, opens second motor 423 for being installed on finished product efferent duct 422, makes the oxidation system multiple
The inside of mould assembly gaseous state aqueous solution dilution trap 43, then, organization of supply 10 is by the aqueous solution via the 4th aqueous solution efferent duct
16 and flow into the inside of dilution trap 43, making the aqueous solution and oxidation is compound gaseous state aqueous solution in the dilution trap 43
It is compound gaseous state aqueous solution that portion, which is mixed to form a concentration lower than the dilution oxidation that the oxidation is compound gaseous state aqueous solution,.
As shown in Figure 5 C, when electrolytic cell 31 is electrolysed, it is located at hydrochloride aqueous solution described in 22 inside of salt water storage tank
Existing electrically-controlled valve 26 and the inside for continuing to flow into electrolytic cell 31, so that being located at hydrochloride aqueous solution described in 22 inside of salt water storage tank
It is lasting to reduce, and when the first liquid level sensor 51 senses the water level positioned at hydrochloride aqueous solution described in 22 inside of salt water storage tank
When highly too low, the first liquid level sensor 51 will form the first level sensing information for being transferred to control mechanism 60, make to control
Mechanism 60 can control organization of supply 10 and be operated with rabbling mechanism 20 according to the first level sensing information, so that supply
Mechanism 10 provides the saline slot 21 of the aqueous solution to rabbling mechanism 20, and then stirring is formed by institute by rabbling mechanism 20
Hydrochloride aqueous solution is stated, and the first concentration sensor 57 can sense the hydrochloride aqueous solution being located in 21 inside of saline slot
Concentration, when the concentration for being located at hydrochloride aqueous solution described in 21 inside of saline slot reaches default value, the first concentration sensor
57 form first concentration information for being transferred to control mechanism 60, and control mechanism 60 is allowed to control according to first concentration information
The hydrochloride aqueous solution is transmitted to the inside of salt water storage tank 22, when salt water storage tank 22 fills the hydrochloride aqueous solution, the
When one liquid level sensor 51 senses excessively high positioned at the height of water level of hydrochloride aqueous solution described in 22 inside of salt water storage tank, first
Liquid level sensor 51 will form first Stop message for being transferred to control mechanism 60, stop control mechanism 60 according to described first
Stop signal and control organization of supply 10 and rabbling mechanism 20 stops operating to stop producing the hydrochloride aqueous solution.
As shown in Figure 5 D, the oxidation inside pan tank 42 is that compound gaseous state aqueous solution can be by after using
Fade consumption, and is compound gaseous state aqueous solution when the second liquid level sensor 52 is sensed positioned at oxidation described in 42 inside of pan tank
Height of water level it is too low when, the second liquid level sensor 52 will form the second level sensing information for being transferred to control mechanism 60,
Control mechanism 60 is set to control organization of supply 10, electrolysis mechanism 30 and mixed organization 40 according to the second level sensing information
It is operated, wherein when control mechanism 60 receives the second level sensing information, control mechanism 60 first controls supply machine
Structure 10 is operated, and organization of supply 10 is allowed to provide the inside that the hydrochloride aqueous solution flows into electrolytic cell 31, then, control mechanism 60
It controls power-supply unit 33 and provides voltage to electrolytic cell 31, electrolytic cell 31 is allowed to be electrolysed to generate the hydrochloride aqueous solution
The oxidation is compound gas, and then the oxidation caused by mixed organization 40 is allowed to be that compound gaseous state aqueous solution can fill with
Pan tank 42, in addition, when pan tank 42 fills the oxidation and is compound gaseous state aqueous solution, the second liquid level sensor 52 sensing
To be located at 42 inside of pan tank described in oxidation be compound gaseous state aqueous solution height of water level it is excessively high when, the second liquid level sensor
52 will form second Stop message for being transferred to control mechanism 60, control control mechanism 60 according to second Stop message
It is that compound gaseous state is water-soluble that organization of supply 10 processed, electrolysis mechanism 30 and mixed organization 40, which stop operating to stop described the aoxidizing of production,
Liquid.
It please refers to shown in Fig. 5 E, when third liquid level sensor 53 is sensed positioned at oxidation system described in 411 inside of reactive tank
When the height of water level of compound gaseous state aqueous solution is too low, third liquid level sensor 53 will form one be transferred to control mechanism 60
Three level sensing information make control mechanism 60 start organization of supply 10, electrolysis mechanism according to the third level sensing information
30 to be operated with gas mixer 412 to generate the oxidation be compound gaseous state aqueous solution, also, the second concentration sensor
58, which can generate sensing when the oxidation is compound gaseous state aqueous solution in reactive tank 411, is located at oxygen described in 411 inside of reactive tank
Change is the concentration of compound gaseous state aqueous solution, is compound gaseous state aqueous solution when being located at oxidation described in 411 inside of reactive tank
When concentration reaches default value, the second concentration sensor 58 will form second concentration information for being transferred to control mechanism 60, so that
It is that compound gaseous state aqueous solution is delivered to pan tank 42 that control mechanism 60, which controls the oxidation according to second concentration information,
And controlling organization of supply 10, electrolysis mechanism 30 and mixed organization 40 again and stopping operating to stop the production oxidation is compound gas
State aqueous solution.
It please refers to shown in Fig. 5 F, the dilution oxidation inside dilution trap 43 is compound gaseous state aqueous solution by making
It can be gradually used up after, be compound when the 4th liquid level sensor 54 is sensed positioned at dilution oxidation described in 43 inside of dilution trap
When the height of water level of gaseous state aqueous solution is too low, the 4th liquid level sensor 54 will form the 4th liquid level for being transferred to control mechanism 60
Heat transfer agent, make control mechanism 60 start according to the 4th level sensing information organization of supply 10 and the second motor 423 into
Row running, allows the aqueous solution and oxidation is that compound gaseous state aqueous solution flows into the inside of dilution trap 43 to form the dilution oxygen
Change is compound gaseous state aqueous solution, also, when dilution trap 43 fills the dilution oxidation and is compound gaseous state aqueous solution, the 4th
Liquid level sensor 54 sense positioned at described in 43 inside of dilution trap dilution oxidation be compound gaseous state aqueous solution height of water level
When excessively high, the 4th liquid level sensor 54 will form the 4th Stop message for being transferred to control mechanism 60, make control mechanism 60 according to
Organization of supply 10 is controlled according to the 4th stop signal and the second motor 423 stops operating to stop producing the oxidation system again
Mould assembly gaseous state aqueous solution.
It please refers to shown in Fig. 5 G, when automation electrolysis unit 1 wants to carry out washing and cleaning operation, the control supply of control mechanism 60
Mechanism 10 provides the aqueous solution to switch unit 32, and control mechanism 60 further opens third and fourth switching of switch unit
Electrically-controlled valve 323a, 324a, allow the aqueous solution flow into inside the anode and cathode of electrolytic cell 31 cleaned it is water-soluble to form a waste water
Liquid, when the 5th liquid level sensor 55 is sensed it is excessively high positioned at the height of water level of waste water aqueous solution described in 31 inside of electrolytic cell when,
5th liquid level sensor 55 will form the 5th level sensing information for being transferred to control mechanism 60, and control mechanism 60 is according to institute
State the 5th level sensing information and open discharge electrically-controlled valve 314, make way for the waste water aqueous solution inside electrolytic cell 31 via
Lower delivery pipe 313 and be expelled to a Sewage treatment slot (not shown).
It please refers to shown in Fig. 5 H, when electrolytic cell 31 is electrolysed the hydrochloride aqueous solution, the temperature of the hydrochloride aqueous solution
Degree can be promoted, and worked as temperature sensor 56 and sensed positioned at hydrochloride aqueous solution described in 31 inside of electrolytic cell when the temperature is excessively high,
Temperature sensor 56 will form a temperature information, and the temperature information is transferred to control mechanism 60, wherein control mechanism 60
The excessively high information warning of 31 temperature of an expression electrolytic cell can be generated according to the temperature information or stops power-supply unit
33 provide voltage to electrolytic cell 31, allow electrolytic cell 31 that can not carry out redox reaction to the hydrochloride aqueous solution.
Above explanation and examples are merely exemplary, does not constitute any restrictions to the scope of the utility model.This
Field technical staff should be understood that can be to the utility model technology under the spirit and scope without departing from the utility model
The details and form of scheme are modified or are replaced, but these modifications and replacement are each fallen in the claim of the utility model.
Claims (9)
1. a kind of automation electrolysis unit, characterized by comprising:
One organization of supply, to provide an aqueous solution；
One rabbling mechanism to receive the aqueous solution, and the aqueous solution and multiple salt particles is stirred to form one and contain salt
The hydrochloride aqueous solution divided；
One electrolysis mechanism, the power supply that the electrolytic cell and one for being connected to the rabbling mechanism with one are connected to the electrolytic cell supply
Unit is answered, the electrolytic cell is to contain the hydrochloride aqueous solution, and the power-supply unit can provide voltage to the electricity
Slot is solved, allowing the electrolytic cell be electrolysed to the hydrochloride aqueous solution to form an oxidation is compound gas；
One mixed organization is connected to the pan tank of the gas-liquid mixed component, the gas with a gas-liquid mixed component and one
Liquid electric hybrid module is connected to the organization of supply and electrolytic cell simultaneously, and is compound gas mixing by the aqueous solution and oxidation
Forming the oxidation that one is sent to the pan tank is compound gaseous state aqueous solution；
One sensing mechanism has one to be installed on the first liquid level sensor of the rabbling mechanism and one be installed on the pan tank
The second liquid level sensor, first liquid level sensor can sense positioned at hydrochloride aqueous solution described in the rabbling mechanism inside
Water level height to form one first level sensing information, and second liquid level sensor can sense in the pan tank
Oxidation described in portion is the water level height of compound gaseous state aqueous solution to form one second level sensing information；And
One control mechanism, while being connected to the organization of supply, rabbling mechanism, electrolysis mechanism, mixed organization and sensing mechanism, institute
State that control mechanism can control the organization of supply according to the first level sensing information and rabbling mechanism is operated to produce
The raw hydrochloride aqueous solution, and the control mechanism can be controlled according to the second level sensing information the organization of supply,
Electrolysis mechanism is operated with mixed organization, and allowing the pan tank to fill with the oxidation is compound gaseous state aqueous solution.
2. automation electrolysis unit according to claim 1, it is characterised in that: the rabbling mechanism has one to be connected to institute
State the saline slot of organization of supply and salt water storage tank that one is connected to the saline slot, the salt water storage tank is used
To contain the hydrochloride aqueous solution, and the first liquid level sensor of the sensing mechanism is installed.
3. automation electrolysis unit according to claim 2, it is characterised in that: the sensing mechanism further has a peace
The first concentration sensor loaded on the saline slot, first concentration sensor can be sensed positioned at the saline slot
Described in hydrochloride aqueous solution salt concentration to form first concentration information for being transferred to the control mechanism, allow the control
Mechanism controls the hydrochloride aqueous solution and is delivered to the salt water storage tank according to first concentration information.
4. automation electrolysis unit according to claim 1, it is characterised in that: set between the rabbling mechanism and electrolytic cell
There are the electrically-controlled valve of a flowmeter that can calculate and change fluid flow and a limitation liquid flowing, the flowmeter and electrically-controlled valve
It is electrically connected at the control mechanism, and when the control mechanism receives second concentration information, the electrically-controlled valve meeting
It allows the hydrochloride aqueous solution to flow to the flowmeter, so that the flowmeter is calculated the flow of the hydrochloride aqueous solution, when described
When the flow that flowmeter calculates the hydrochloride aqueous solution has reached default value, the electrically-controlled valve can stop the hydrochloride aqueous solution stream
It moves to the flowmeter.
5. automation electrolysis unit according to claim 1, it is characterised in that: the gas-liquid mixed unit has one to contain
The reactive tank of the aqueous solution and the reception oxidation are the gas mixer of compound gas, the reactive tank connection one
First motor, and the aqueous solution inside the reactive tank can first be flowed through the gas mixer and flowed again by first motor
It is back to the inside of the reactive tank, so that it is that compound gas flows back into the reactive tank that the aqueous solution, which carries the oxidation secretly,
Inside, it is compound gaseous state aqueous solution that the aqueous solution for making way for the reactive tank, which is changed into the oxidation,；
The sensing mechanism further has a third liquid level sensor for being installed on the reactive tank, the third level sensing
It is the water level height of compound gaseous state aqueous solution to form a third that device, which can be sensed positioned at oxidation described in the reactive tank inside,
Level sensing information；
The control mechanism starts the organization of supply, electrolysis mechanism and gas mixing according to the third level sensing information
It is compound gaseous state aqueous solution that device, which is operated to generate the oxidation,.
6. automation electrolysis unit according to claim 5, it is characterised in that: the sensing mechanism further has a peace
The second concentration sensor loaded on the reactive tank, second concentration sensor can sense the institute in the reactive tank inside
Concentration that oxidation is compound gaseous state aqueous solution is stated to form second concentration information for being transferred to the control mechanism, is allowed described
It is that compound gaseous state aqueous solution is delivered to the pan tank that control mechanism, which controls the oxidation according to second concentration information,.
7. automation electrolysis unit according to claim 1, it is characterised in that: the mixed organization further has one
The oxidation can be multiple between the pan tank and dilution trap by two motor and a dilution trap, second motor
Mould assembly gaseous state aqueous solution flows into the inside of the dilution trap, and the dilution trap is connected to the organization of supply, and described in receiving
Aqueous solution and oxidation are compound gaseous state aqueous solution, and making the aqueous solution and oxidation is compound gaseous state aqueous solution in the dilution
It is compound vaporous water that the internal mix of slot, which forms a concentration lower than the dilution oxidation that the oxidation is compound gaseous state aqueous solution,
Solution；
The sensing mechanism further has the 4th liquid level sensor for being installed on the dilution trap, the 4th level sensing
It is the water level height of compound gaseous state aqueous solution to form one that device, which can be sensed positioned at dilution oxidation described in the dilution trap inside,
4th level sensing information；
The control mechanism starts the organization of supply according to the 4th level sensing information and second motor carries out
Running, allow the aqueous solution and oxidation be that compound gaseous state aqueous solution flows into the inside of the dilution trap to form the dilution oxygen
Change is compound gaseous state aqueous solution.
8. automation electrolysis unit according to claim 1, it is characterised in that: the sensing mechanism further has a peace
Temperature sensor loaded on the electrolytic cell, the temperature sensor can be sensed positioned at salt water water described in the electrolyte bath
The temperature of solution makes the control mechanism according to the temperature information to form a temperature information for being transferred to the control mechanism
It generates an information warning or stops the power-supply unit and provide voltage to the electrolytic cell.
9. automation electrolysis unit according to claim 1, it is characterised in that: the electrolytic cell of the electrolysis mechanism is connected to
The organization of supply enables the electrolytic cell to receive the aqueous solution, and the electrolytic cell is equipped with a limitation liquid flowing
Discharge electrically-controlled valve；
The sensing mechanism further has the 5th liquid level sensor for being installed on the electrolytic cell, and the 5th liquid level passes
Sensor can sense the water level height positioned at aqueous solution described in the electrolyte bath to form one the 5th level sensing information；With
And
The control mechanism starts the automatically controlled valve function according to the 5th level sensing information, makes way for the electrolytic cell
The internal aqueous solution can be carried out discharge.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920036718.4U CN209507690U (en) | 2019-01-09 | 2019-01-09 | Automate electrolysis unit |
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| CN201920036718.4U CN209507690U (en) | 2019-01-09 | 2019-01-09 | Automate electrolysis unit |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111422952A (en) * | 2019-01-09 | 2020-07-17 | 台湾可林生化科技有限公司 | Automatic change electrolytic device |
| CN113430544A (en) * | 2021-06-22 | 2021-09-24 | 珠海格力电器股份有限公司 | Disinfectant liquid manufacturing machine and control method thereof |
-
2019
- 2019-01-09 CN CN201920036718.4U patent/CN209507690U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111422952A (en) * | 2019-01-09 | 2020-07-17 | 台湾可林生化科技有限公司 | Automatic change electrolytic device |
| CN113430544A (en) * | 2021-06-22 | 2021-09-24 | 珠海格力电器股份有限公司 | Disinfectant liquid manufacturing machine and control method thereof |
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