CN208949422U - Pickling formula integration hypochlorite generator - Google Patents
Pickling formula integration hypochlorite generator Download PDFInfo
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- CN208949422U CN208949422U CN201821852848.7U CN201821852848U CN208949422U CN 208949422 U CN208949422 U CN 208949422U CN 201821852848 U CN201821852848 U CN 201821852848U CN 208949422 U CN208949422 U CN 208949422U
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- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 title claims abstract description 118
- 238000005554 pickling Methods 0.000 title claims abstract description 26
- 230000010354 integration Effects 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000003860 storage Methods 0.000 claims abstract description 84
- 239000007788 liquid Substances 0.000 claims abstract description 75
- 239000002253 acid Substances 0.000 claims abstract description 57
- 239000005708 Sodium hypochlorite Substances 0.000 claims abstract description 54
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims abstract description 53
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical class [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 43
- 230000006837 decompression Effects 0.000 claims abstract description 14
- 238000013022 venting Methods 0.000 claims abstract description 13
- 229920006395 saturated elastomer Polymers 0.000 claims description 31
- 239000012266 salt solution Substances 0.000 claims description 24
- 239000010865 sewage Substances 0.000 claims description 24
- 238000002156 mixing Methods 0.000 claims description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract description 3
- 239000012895 dilution Substances 0.000 abstract description 2
- 238000010790 dilution Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 150000003839 salts Chemical class 0.000 description 18
- 235000002639 sodium chloride Nutrition 0.000 description 18
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- 239000012267 brine Substances 0.000 description 8
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 8
- 244000248349 Citrus limon Species 0.000 description 7
- 235000005979 Citrus limon Nutrition 0.000 description 7
- 230000009286 beneficial effect Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 5
- 238000005868 electrolysis reaction Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000000284 extract Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 230000003020 moisturizing effect Effects 0.000 description 4
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000012800 visualization Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000003902 lesion Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- PVGBHEUCHKGFQP-UHFFFAOYSA-N sodium;n-[5-amino-2-(4-aminophenyl)sulfonylphenyl]sulfonylacetamide Chemical compound [Na+].CC(=O)NS(=O)(=O)C1=CC(N)=CC=C1S(=O)(=O)C1=CC=C(N)C=C1 PVGBHEUCHKGFQP-UHFFFAOYSA-N 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model relates to pickling formula integration hypochlorite generators, the saturated common salt water pot inlet is connected by the first valve with external water source, the storage acid tank inlet is connected by the second valve with external water source, first inlet of automatic proportioner is connected by decompression venting valve with external water source, the saturated common salt water pot liquid outlet and storage acid tank liquid outlet are connected with the second inlet of automatic proportioner respectively, the automatic proportioner liquid outlet is connected by third valve with hypochlorite generator's ontology inlet, the sodium hypochlorite ontology liquid outlet is connected with sodium hypochlorite storage tank inlet, the fan outlet is connected with sodium hypochlorite storage tank air inlet.Pickling formula integration hypochlorite generator is easy to operate, dilution accuracy is high, and construction maintenance is convenient, and uses pickling mode cleaning electrode, effectively increases the service life of electrolytic cell.
Description
Technical field
The utility model relates to hypochlorite generator field more particularly to pickling formula integration hypochlorite generators.
Background technique
The weak brine proportion inputted in traditional integrated hypochlorite generator is fixed on bucket using liquid-level switch,
Weak brine is matched by control liquid level, and this proportion will lead to that matched proportion density is inaccurate, and the measurement for being not only liquid-level switch misses
Difference causes matched proportion density inaccurate, and the variation of weather can also have an impact the matched proportion density of weak brine, to influence hypochlorous acid
The production of sodium solution；And the cleaning of the integrated hypochlorite generator of tradition is to clean electrolytic cell by way of pole,
The method meeting lesion electrode plate of pole cleaning, influences the service life of electrode.
Utility model content
For this reason, it may be necessary to provide pickling formula integration hypochlorite generator, occur to solve traditional integrated sodium hypochlorite
Device uses difficult problem.
To achieve the above object, pickling formula integration hypochlorite generator, including saturated salt solution are inventor provided
Tank, storage acid tank, automatic proportioner, hypochlorite generator's ontology, sodium hypochlorite storage tank and blower, the saturated salt solution
Saturated common salt water pot inlet and saturated common salt water pot liquid outlet are offered on tank, offered on the storage acid tank storage acid tank into
Liquid mouth and storage acid tank liquid outlet, offer the first inlet, the second inlet and automatic mixing on the automatic proportioner
Device liquid outlet offers hypochlorite generator's ontology inlet and sodium hypochlorite hair on hypochlorite generator's ontology
Device ontology liquid outlet is given birth to, sodium hypochlorite storage tank inlet and sodium hypochlorite storage are offered on the sodium hypochlorite storage tank
Canister incoming gas mouth；
The saturated common salt water pot inlet is connected by the first valve with external water source, and the storage acid tank inlet is logical
It crosses the second valve to be connected with external water source, first inlet of automatic proportioner passes through decompression venting valve and external water source phase
Connection, the saturated common salt water pot liquid outlet and storage acid tank liquid outlet are connected with the second inlet of automatic proportioner respectively,
The automatic proportioner liquid outlet is connected by third valve with hypochlorite generator's ontology inlet, the sodium hypochlorite
Ontology liquid outlet is connected with sodium hypochlorite storage tank inlet, the fan outlet and sodium hypochlorite storage tank air inlet phase
Connection.
Further, the saturated common salt water pot liquid outlet is opened in above saturated salt solution pot sidewall.
Further, the storage acid tank liquid outlet is opened in below storage acid tank side wall.
Further, first flowmeter, the hypochlorite generator are provided at the saturated common salt water pot inlet
Second flowmeter is provided at ontology inlet.
Further, it is provided with the 4th valve at the saturated common salt water pot liquid outlet, is set at the storage acid tank liquid outlet
It is equipped with the 5th valve.
Further, the 6th valve, are provided at first sewage draining exit, the second sewage draining exit and third sewage draining exit
Seven valves and the 8th valve.
Further, hypochlorite generator's ontology inlet is connected by the 9th valve with blow-off line, institute
It states hypochlorite generator's ontology liquid outlet and is connected by the tenth valve with blow-off line.
Further, first valve, the second valve, the 4th valve, the 5th valve, the 9th valve and the tenth valve
It is solenoid valve.
Further, the third valve is diaphragm valve.
It is different from the prior art, above-mentioned technical proposal has the advantages that pickling formula integration hypochlorite generator
In automatic proportioner using water flow provide power extract saturated salt solution from saturated common salt water pot, to realize weak brine
Automatic mixing, after electrolysis, automatic proportioner using water flow provide power from storage acid tank in extract saturated lemon, electricity
The configuration of solution liquid shares same proportioner with acid solution configuration and completes, and pickling formula integration hypochlorite generator is easy to operate, dilute
Accuracy height is released, construction maintenance is convenient, and uses pickling mode cleaning electrode, effectively increases the service life of electrolytic cell.
Detailed description of the invention
Fig. 1 is the process flow chart of the present embodiment pickling formula integration hypochlorite generator.
Description of symbols:
1, saturated common salt water pot；
2, acid tank is stored up；
3, automatic proportioner；
4, hypochlorite generator's ontology；
5, sodium hypochlorite storage tank；
6, blower；
7, external water source；
71, decompression venting valve；
81, the first valve；
82, the second valve；
83, third valve；
84, the 4th valve；
85, the 5th valve；
86, the 6th valve；
87, the 7th valve；
88, the 8th valve；
89, the 9th valve；
80, the tenth valve；
9, blow-off line；
01, first flowmeter；
02, second flowmeter.
Specific embodiment
Technology contents, construction feature, the objects and the effects for detailed description technical solution, below in conjunction with specific reality
It applies example and attached drawing is cooperated to be explained in detail.
Referring to Fig. 1, the utility model provides a kind of pickling formula integration hypochlorite generator, including saturated salt solution
Tank 1, storage acid tank 2, automatic proportioner 3, hypochlorite generator's ontology 4, sodium hypochlorite storage tank 5 and blower 6, the saturation
Salt water pot is for containing saturated salt solution, and the storage acid tank is for containing saturated lemon, in other examples, storage acid
The saturated acids such as saturation hydrochloric acid solution or saturation sulfuric acid solution can be contained in slot, saturated lemon is safer and environmentally friendly, because
This is preferably saturated lemon.The sodium hypochlorite storage tank is for containing liquor natrii hypochloritis.
The concrete model of hypochlorite generator's ontology may is that HD TS-50-NaClO, HDT-100-NaClO,
HDT-200-NaClO, HDT-300-NaClO or HDT-500-NaClO.The concrete model of blower is: CY076.Automatic mixing
2510 type of model of device.
The working principle of the decompression venting valve 71 is using the intracorporal opening and closing element aperture of control valve come regulating water flow, will
The pressure reduction of water flow, while the aperture of the effect adjusting opening and closing element by downstream pressure, make downstream pressure be maintained at certain model
In enclosing, in the continually changing situation of inlet pressure, keep outlet pressure in the range of setting.Decompression venting valve is by outer water receiving
After the water flow decompression processing exported in source 7, further stationary flow pressure, in the present embodiment, decompression venting valve is directly external
Tap water water source.
The principle of automatic proportioner is by the different fluid balance of external water source and saturated salt solution two-way pressure to pressure
Power is identical, then mixes according to a certain percentage, to reach required concentration ratio value.First is offered on the automatic proportioner
Inlet, the second inlet and automatic proportioner liquid outlet, the first inlet, the second inlet on the automatic proportioner
And automatic proportioner liquid outlet is provided with the lower section of automatic proportioner.
Saturated common salt water pot inlet and saturated common salt water pot liquid outlet are offered on the saturated common salt water pot, at this
In embodiment, saturated common salt water pot inlet is opened in above saturated salt solution pot sidewall, and saturated common salt water pot liquid outlet is also opened
Above saturated salt solution pot sidewall, salt deposit is equipped in saturated common salt water pot tank, external water source passes through saturated common salt water pot
Inlet injected clear water into saturated common salt water pot, the salt in tank are dissolved in clear water, since the salt in salt deposit is excessive, energy
Enough guarantee the salt water concentration saturation dissolved in saturated common salt water pot, the saturated salt solution in saturated common salt water pot passes through saturation food
The saturated common salt water pot liquid outlet output saturated salt solution opened up on salt water pot sidewall, avoids being deposited in saturated salt solution pot bottom
Salt deposit in salt flowed in subsequent processing with saturated salt solution.
Storage acid tank inlet is offered on the storage acid tank and storage acid tank liquid outlet, the storage acid tank inlet are opened in
It storing up above acid tank side wall, the storage acid tank liquid outlet is opened in below storage acid tank side wall, the beneficial effect is that, facilitate storage acid tank
In liquid export groove body completely, accelerate output speed furthermore with the liquid pressure that stores in groove body.
The first inlet, the second inlet and automatic proportioner liquid outlet are offered on the automatic proportioner, it is described
Hypochlorite generator's ontology inlet is offered on hypochlorite generator's ontology and hypochlorite generator's ontology goes out liquid
Mouthful, hypochlorite generator's ontology inlet is opened in below sodium chlorate generator ontology, the sodium chlorate generator sheet
Body liquid outlet is opened in above sodium chlorate generator ontology, and the saturated salt solution or acid solution matched from automatic proportioner is all made of
The mode of bottom in and top out passes in and out sodium chlorate generator ontology, the beneficial effect is that, enable to saturated salt solution or acid solution
Full of electrolytic cell, better electrolysis effectiveness is obtained.
Sodium hypochlorite storage tank inlet and sodium hypochlorite storage canister incoming gas are offered on the sodium hypochlorite storage tank
Mouthful, sodium hypochlorite storage tank inlet and sodium hypochlorite storage tank air inlet are opened on sodium hypochlorite storage tank
Side.
The saturated common salt water pot inlet is connected by the first valve 81 with external water source, the storage acid tank inlet
It is connected by the second valve 82 with external water source, first inlet of automatic proportioner passes through decompression venting valve and outer water receiving
Source is connected, and the saturated common salt water pot liquid outlet and storage acid tank liquid outlet are connected with the second inlet of automatic proportioner respectively
It connecing, the automatic proportioner liquid outlet is connected by third valve 83 with hypochlorite generator's ontology inlet, and described time
Sodium chlorate ontology liquid outlet is connected with sodium hypochlorite storage tank inlet, the fan outlet and sodium hypochlorite storage tank into
Port is connected, and above-mentioned all connection relationships are connected by pipeline and realized.
In certain preferred embodiments, the number of first valve is two, is motor-driven valve and diaphragm valve respectively,
The effect of motor-driven valve is to control the water inlet start and stop of external water source, and the effect of diaphragm valve is that the flow of adjusting external water source inflow is big
It is small.
In certain preferred embodiments, the number of second valve is two, is motor-driven valve respectively and unpowered
Valve, in use, motor-driven valve are in normally open, normal open state are in for controlling external water source inlet pipeline, without dynamic
Power valve is functionally similar to liquid-level switch, and working mechanism is when the acid solution in storage acid tank overflows to pipeline from storage acid tank inlet
When interior, unpowered valve closing is cut off the water supply.
In certain preferred embodiments, the 4th valve 84, the storage are provided at the saturated common salt water pot liquid outlet
The 5th valve 85 is provided at acid tank liquid outlet.After inputting automatic proportioner in saturated salt solution self-saturation salt water pot, such as
Fruit does not close decompression venting valve in time, and automatic proportioner will continue to extract saturated salt solution out of saturated common salt water pot, make
It is configured at weak brine excessive.Similarly, after the completion of the work of sodium hypochlorite electrolytic cell Inner electrolysis, decompression venting valve and the are opened
Five valves configure dilute citric acid by automatic proportioner, after the completion of configuration, close the 5th valve and decompression venting valve, avoid making
At the excessive problem of dilute citric acid configuration.
Pickling formula integration hypochlorite generator when in use, open the first valve, the water in external water source is logical
Supersaturated salt water pot inlet flows into saturated common salt water pot, and the salt dissolved in saturated common salt water pot forms saturated salt solution,
After precipitating after a period of time, the 4th valve and decompression venting valve are opened, external water source is subtracted by decompression venting valve
It is inputted in automatic proportioner after pressing pressure stabilization function, the power that automatic proportioner is provided using the water flow of external water source input will be saturated
Saline solution extracts from saturated common salt water pot and carries out quantitative proportioning into automatic proportioner, forms the weak brine of predetermined concentration, from
Proportioned a certain concentration weak brine inputs sodium hypochlorite by the third valve at automatic proportioner liquid outlet in dynamic proportioner
In generator ontology, weak brine is dilute from hypochlorite generator's ontology inlet input below hypochlorite generator's ontology
The liquor natrii hypochloritis that salt water generates after electrolytic tank electrolysis occurs by the sodium hypochlorite above hypochlorite generator's ontology
The output of device ontology liquid outlet, is finally injected into sodium hypochlorite storage tank by sodium hypochlorite storage tank inlet, starts blower, wind
Machine is by being blown into air in hypochlorite generator in sodium hypochlorite storage tank air inlet, to dilute from hypochlorite generator
The high concentration hydrogen that the liquor natrii hypochloritis of output carries, after the Dilution air that blower is blown into, in sodium hypochlorite storage tank
Gas is emitted into air above sodium hypochlorite storage tank.
Etching procedures after accumulative electrolysis 60 as a child starts when pickling, close the first valve and the 4th valve, open the
Five valves store up the saturated lemon in acid tank by storage acid tank liquid outlet output, and automatic proportioner utilizes external water source input
The power that water flow provides extracts saturated lemon from crude acid slot carries out quantitative proportioning into automatic proportioner, configured dilute
Citric acid is delivered to electrolytic cell from automatic proportioner liquid outlet and is impregnated.Into after the completion of acid, dilute lemon acid soak electrolytic cell 15
Minute.
In the present embodiment, the pipeline connected between hypochlorite generator's liquid outlet and sodium hypochlorite storage tank inlet
Be that gap is connect at sodium hypochlorite storage tank inlet, i.e., there are gap between pipeline and sodium hypochlorite storage tank inlet,
Gas in sodium hypochlorite storage tank drains into atmosphere from above-mentioned gap.
In certain preferred embodiments, first flowmeter 01 is provided at the saturated common salt water pot inlet, it is described
Second flowmeter 02, the concrete model of first flowmeter are provided at hypochlorite generator's ontology inlet are as follows: DN15160L,
The concrete model of second flowmeter are as follows: DN1540L, DN15100L or DN15160L, it can be according to hypochlorite generator's sheet
The concrete model of body selects different size of flowmeter.The beneficial effect that first flowmeter is arranged is: visualization is controlled into full
With the inflow of salt water pot, it is ensured that saturation effect, too small then shadow is not achieved in the saturation degree of salt water when dissolved salt, the excessive dissolved salt of flow
Ring equipment moisturizing efficiency.The beneficial effect that second flowmeter is arranged is: hypochlorite generator's liquid feeding end flowmeter: visualization
Into electrolytic cell flow, facilitate debugging and to maintain equipment.
In certain preferred embodiments, on the saturated common salt water pot, storage acid tank and sodium hypochlorite storage tank respectively
Offer the first sewage draining exit, the second sewage draining exit and third sewage draining exit, first sewage draining exit, the second sewage draining exit and third row
Dirty mouth is connected to blow-off line 9.First sewage draining exit, the second sewage draining exit and third sewage draining exit are respectively used to saturated salt solution
Waste liquid discharge in tank, storage acid tank and sodium hypochlorite storage tank, due to the pickling, formula integration hypochlorite generator is direct
Using tap water as external water source, the sundries such as silt are carried in tap water, the use of through a long time, saturated common salt water pot,
Sundries precipitating can be generated in storage acid tank and sodium hypochlorite storage tank, pass through the first sewage draining exit, the second sewage draining exit and third
Sewage draining exit discharges the sundries in saturated common salt water pot, storage acid tank and sodium hypochlorite storage tank respectively, to safeguard the pickling formula
The normal operation of integrated hypochlorite generator；
It is highly preferred that be provided at first sewage draining exit, the second sewage draining exit and third sewage draining exit the 6th valve 86,
7th valve 87 and the 8th valve 88, user can be controlled by the 6th valve of opening and closing, the 7th valve and the 8th valve
Saturated common salt water pot, storage acid tank and sodium hypochlorite storage tank processed discharge sundries into blow-off line.
In certain preferred embodiments, hypochlorite generator's ontology inlet passes through the 9th valve 89 and blowdown
Pipeline is connected, and hypochlorite generator's ontology liquid outlet is connected by the tenth valve 80 with blow-off line.Its is beneficial
Effect is, during into acid, the air in electrolytic cell and dilute citric acid beyond cell capacity redundance pass through electricity
Tenth valve in solution slot exit drains into blow-off line.After acid cleaning process, user will by opening the 9th valve
Acid solution in electrolytic cell drains into blow-off line.
In certain preferred embodiments, first valve, the second valve, the 4th valve, the 5th valve, the 9th valve
And the tenth valve be solenoid valve.First valve, the second valve, the 4th valve, the 5th valve, the 9th valve and the tenth valve
Door can control the first valve, the second valve, the 4th valve, the 5th valve, the 9th valve and the tenth by control circuit
The opening and closing of valve, reaches Electronic control.
In certain preferred embodiments, the third valve is diaphragm valve, the beneficial effect is that: diaphragm valve is than common
Ball valve precision is higher, can fine adjustments uninterrupted, feed liquor flow precisely makes equipment yield more accurate.
In certain preferred embodiments, there are two liquid-level switches, two liquid levels to open for setting on saturated salt solution top tank structure
Close setting up and down, two liquid-level switch effects are as follows: when water level is lower than the liquid-level switch of lower section in tank, open saturated common salt water pot
Moisturizing, during moisturizing, when water level is more than the liquid-level switch of top in tank, moisturizing stops, and the first valve is closed, and stops to saturation
Continue to fill the water in salt water pot.Sodium hypochlorite stores setting on top tank structure, and there are three liquid-level switches, three liquid-level switch settings to exist
On same vertical line, liquid-level switch is fixed on sodium hypochlorite storage top tank structure, and adjacent liquid-level switch is placed equidistant with, three liquid levels
On-off action are as follows: when water level is located at the liquid-level switch of bottom in tank, sodium hypochlorite production work starts the starting that feeds intake, and works as tank
When interior water level is located at intermediate liquid-level switch position, sodium hypochlorite production work automatic running, when water level is more than the top in tank
When liquid-level switch, sodium hypochlorite production work is automatically stopped.It should be noted that although herein to above-mentioned each implementation
Example is described, but is not intended to limit the scope of patent protection of the utility model.Therefore, based on the innovation of the utility model
Theory, the change and modification carried out to embodiment described herein or made based on the specification and figures of the utility model
Above technical scheme is directly or indirectly used in other related technical areas, by equivalent structure or equivalent flow shift
Including within the protection scope of the utility model patent.
Claims (9)
1. pickling formula integration hypochlorite generator, it is characterised in that: including saturated common salt water pot, storage acid tank, automatic mixing
Device, hypochlorite generator's ontology, sodium hypochlorite storage tank and blower offer saturated common salt on the saturated common salt water pot
Water pot inlet and saturated common salt water pot liquid outlet, storage acid tank inlet is offered on the storage acid tank and storage acid tank goes out liquid
Mouthful, the first inlet, the second inlet and automatic proportioner liquid outlet, the hypochlorous acid are offered on the automatic proportioner
Hypochlorite generator's ontology inlet and hypochlorite generator's ontology liquid outlet are offered on sodium generator ontology, it is described
Sodium hypochlorite storage tank inlet and sodium hypochlorite storage tank air inlet are offered on sodium hypochlorite storage tank；
The saturated common salt water pot inlet is connected by the first valve with external water source, and the storage acid tank inlet passes through the
Two valves are connected with external water source, and first inlet of automatic proportioner is connected by decompression venting valve with external water source
It connects, the saturated common salt water pot liquid outlet and storage acid tank liquid outlet are connected with the second inlet of automatic proportioner respectively, institute
It states automatic proportioner liquid outlet and is connected by third valve with hypochlorite generator's ontology inlet, the sodium hypochlorite sheet
Body liquid outlet is connected with sodium hypochlorite storage tank inlet, and the fan outlet is connected with sodium hypochlorite storage tank air inlet
It connects；
The first sewage draining exit, the second blowdown are offered respectively on the saturated common salt water pot, storage acid tank and sodium hypochlorite storage tank
Mouth and third sewage draining exit, first sewage draining exit, the second sewage draining exit and third sewage draining exit are connected to blow-off line.
2. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the saturated salt solution
Tank liquid outlet is opened in above saturated salt solution pot sidewall.
3. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the storage acid tank goes out liquid
Mouth is opened in below storage acid tank side wall.
4. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the saturated salt solution
It is provided with first flowmeter at tank inlet, is provided with second flowmeter at hypochlorite generator's ontology inlet.
5. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the saturated salt solution
It is provided with the 4th valve at tank liquid outlet, is provided with the 5th valve at the storage acid tank liquid outlet.
6. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: first blowdown
The 6th valve, the 7th valve and the 8th valve are provided at mouth, the second sewage draining exit and third sewage draining exit.
7. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the sodium hypochlorite hair
Raw device ontology inlet is connected by the 9th valve with blow-off line, and hypochlorite generator's ontology liquid outlet passes through the
Ten valves are connected with blow-off line.
8. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: first valve,
Second valve, the 4th valve, the 5th valve, the 9th valve and the tenth valve are solenoid valve.
9. pickling formula integration hypochlorite generator according to claim 1, it is characterised in that: the third valve is
Diaphragm valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821852848.7U CN208949422U (en) | 2018-11-12 | 2018-11-12 | Pickling formula integration hypochlorite generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821852848.7U CN208949422U (en) | 2018-11-12 | 2018-11-12 | Pickling formula integration hypochlorite generator |
Publications (1)
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109055967A (en) * | 2018-11-12 | 2018-12-21 | 福建浩达智能科技股份有限公司 | Pickling formula integration hypochlorite generator |
| CN111676486A (en) * | 2020-06-04 | 2020-09-18 | 山东山大华特科技股份有限公司 | Sodium hypochlorite production process and device for electrolyzing low-concentration brine by using membrane-free method |
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2018
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109055967A (en) * | 2018-11-12 | 2018-12-21 | 福建浩达智能科技股份有限公司 | Pickling formula integration hypochlorite generator |
| CN111676486A (en) * | 2020-06-04 | 2020-09-18 | 山东山大华特科技股份有限公司 | Sodium hypochlorite production process and device for electrolyzing low-concentration brine by using membrane-free method |
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Address after: Floor 20, Building 20, Phase II, Innovation Park, No.7 Wulongjiang Middle Avenue, High tech Zone, Fuzhou City, 350000, Fujian Province Patentee after: FUJIAN HADA INTELLIGENCE TECHNOLOGY CO.,LTD. Address before: Building 62, Juyuanzhou Garden, Jinshan Industrial Zone, No. 618, Jinshan Avenue, Jianxin Town, Cangshan District, Fuzhou City, 350000, Fujian Province Patentee before: FUJIAN HADA INTELLIGENCE TECHNOLOGY CO.,LTD. |