CN206940428U - Hypochlorous acid thimerosal process units with spraying mechanism - Google Patents
Hypochlorous acid thimerosal process units with spraying mechanism Download PDFInfo
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- CN206940428U CN206940428U CN201720733719.5U CN201720733719U CN206940428U CN 206940428 U CN206940428 U CN 206940428U CN 201720733719 U CN201720733719 U CN 201720733719U CN 206940428 U CN206940428 U CN 206940428U
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- liquid
- carbon dioxide
- cushion chamber
- spraying mechanism
- hypochlorous acid
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Abstract
It the utility model is related to hypochlorous acid thimerosal production equipment,Specifically one kind can make full use of raw material,Improve the hypochlorous acid thimerosal process units with spraying mechanism of production efficiency,Provided with running water delivery pipe,Carbon dioxide canister,Air and liquid mixer,Triple valve,Static mixer,Cushion chamber,Drain pipe,Injection device,Liquor natrii hypochloritis's tank,Wherein water and carbon dioxide are sent into air and liquid mixer by running water delivery pipe and carbon dioxide canister respectively,The output end of air and liquid mixer is connected with triple valve first port,The second port of triple valve is connected through stoste pipeline with liquor natrii hypochloritis's tank,Stoste pipeline is provided with injection device,3rd port of triple valve is connected with the input of static mixer,With rational in infrastructure,Reaction is abundant,Reaction efficiency is high,Automaticity is high,The advantages of small volume etc. is notable.
Description
Technical field：
Hypochlorous acid thimerosal production equipment is the utility model is related to, specifically one kind can make full use of raw material, carry
The hypochlorous acid thimerosal process units with spraying mechanism of high efficiency.
Background technology：
It is well known that hypochlorite solutions especially liquor natrii hypochloritis belongs to efficient chlorine-containing disinfectant, it is existing most of public
Many places are carried out disinfection using liquor natrii hypochloritis, and its disinfection principle is to make the hypochlorite and air in liquor natrii hypochloritis
In carbon dioxide reaction produce hypochlorous acid, hypochlorous acid is effective disinfection composition.Hypochlorous acid is existed only in solution, high
Strength solution is in yellow, and low concentration solution is colourless, often there is sharp aroma, and it is a kind of extremely unstable weak acid, is had very strong
Oxidisability and blanching effect, because it is not easy to maintain, traditional thimerosal is more by preparing hypochlorite solutions and adding stabilization
Sold after agent, in order to improve Disinfection Effect, hypochlorite concentration is higher, directly and skin contact, and cannot make during use
With having residual after disinfectant, environment is polluted, in order to reduce corrosion of the thimerosal to skin and article, existing thimerosal makes
Used time is also required to dilute, but this dilution is only realized by manually adding clear water, is reduced the concentration of hypochlorite, is caused to sterilize
Effect also reduces.
The production of hypochlorous acid thimerosal at this stage is realized based on following principle：By sodium hypochlorite stoste and water and carbon dioxide
Fully reaction, makes the hypochlorite in solution be combined with hydrogen ion, forms hypochlorous acid.In order to improve the effective of hypochlorous acid thimerosal
Property, it is fed into excessive carbon dioxide, unnecessary titanium dioxide into reaction vessel by snorkel during production
Carbon is drained as waste gas, causes the waste of raw material, environment is had undesirable effect.
The content of the invention：
The utility model is for shortcoming and defect present in prior art, it is proposed that one kind can make full use of raw material,
Improve production efficiency, automaticity height, reaction efficiency height, small volume, in light weight, equipment price is cheap, can also reduce life
Produce the hypochlorous acid thimerosal process units with spraying mechanism of cost.
The utility model can be reached by following measures：
A kind of hypochlorous acid thimerosal process units with spraying mechanism, provided with running water delivery pipe, carbon dioxide canister,
Air and liquid mixer, triple valve, static mixer, cushion chamber, drain pipe, injection device, wherein liquor natrii hypochloritis's tank, running water
Water and carbon dioxide are sent into air and liquid mixer, the output end of air and liquid mixer and threeway by delivery pipe and carbon dioxide canister respectively
Valve first port is connected, and the second port of triple valve is connected through stoste pipeline with liquor natrii hypochloritis's tank, on stoste pipeline
Provided with injection device, the 3rd port of triple valve is connected with the input of static mixer, the output end of static mixer with
Cushion chamber is connected, and cushion chamber is provided with the liquid outlet being connected with drain pipe, it is characterised in that spraying mechanism is additionally provided with, it is described
Spraying mechanism is located at cushion chamber top, and spraying mechanism is provided with liquid atomiser, the inlet and static mixer of liquid atomiser
Drain pipe road be connected；The cushion chamber is sealing and the cavity of lucifuge, and cushion chamber is provided with inlet, liquid outlet, exhaust
Mouthful, and liquid feed valve, liquid valve and pressure-releasing electromagnetic valve are respectively equipped with inlet, liquid outlet, exhaust outlet.
Liquid atomiser described in the utility model uses centrifugal type atomizer, and mist droplet particle size scope is：2-1200 μm, spray
Mist amount：0.1-100L/H.
Buffering cavity wall described in the utility model is sequentially provided with the first liquid level sensor, the second level sensing from top to bottom
Device, the 3rd liquid level sensor, the 4th liquid level sensor.
The utility model is additionally provided with the controlling organization for control device working condition, and controlling organization includes controller, step
Stepper motor controller, liquid level detection circuit, pressure-releasing electromagnetic valve, carbon dioxide solenoid valve, CO2 flow controller；Wherein control
The control signal all the way of device processed is connected with controllor for step-by-step motor, and controllor for step-by-step motor is connected with injection device stepper motor
Connect, complete injection device control；Four liquid level sensors are provided with liquid level detection circuit, respectively with the signal acquisition terminal of controller
It is connected；Pressure-releasing electromagnetic valve, carbon dioxide solenoid valve, CO2 flow controller export with the control signal of controller respectively
End is connected；Pressure-releasing electromagnetic valve is arranged on cushion chamber exhaust outlet, and CO2 flow controller is arranged on gas transmission pipeline
On, carbon dioxide solenoid valve is arranged in carbon dioxide canister.
The capacity of cushion chamber described in the utility model is more than 1L.
Mixing arrangement described in the utility model uses static mixer.
The utility model distinguishes running water delivery pipe, carbon dioxide snorkel and stoste pipeline during use
It is connected with running water, dioxide bottle, sodium hypochlorite stoste, carbon dioxide and running water are mixed by air and liquid mixer,
And static mixer is admitted to through triple valve, injection device drives stoste to be pumped into triple valve, static subsequently into static mixer
Mixed liquor in blender is admitted to cushion chamber, carries out further buffered, is then exported through drain pipe；Wherein in cushion chamber
Provided with spraying mechanism, cushion chamber stores the excess carbon dioxide gas overflowed in upper level process for preparation during use,
And by the atomizer in spraying mechanism to intracavitary feeding mixed solution, carbon dioxide in the mixed solution and cushion chamber after atomization
Gas further fully contacts, to improve the reaction level of sodium hypochlorite and carbon dioxide.
The utility model compared with prior art, have rational in infrastructure, reaction fully, reaction efficiency is high, automaticity
The advantages of height, small volume etc. are notable.
Brief description of the drawings：
Accompanying drawing 1 is structural representation of the present utility model.
Accompanying drawing 2 is the structural representation of cushion chamber in the utility model.
Accompanying drawing 3 is electrical block diagram of the present utility model.
Reference：.
Embodiment：
The utility model is further described below in conjunction with the accompanying drawings.
As shown in drawings, the utility model proposes a kind of hypochlorous acid thimerosal process units with spraying mechanism, if
There are running water delivery pipe, carbon dioxide canister, air and liquid mixer, triple valve, static mixer, cushion chamber, drain pipe, injection dress
Put, liquor natrii hypochloritis's tank, wherein water and carbon dioxide are sent into gas-liquid respectively and mixed by running water delivery pipe and carbon dioxide canister
Clutch, the output end of air and liquid mixer are connected with triple valve first port, the second port of triple valve through stoste pipeline with time
Sodium chlorate solution's tank is connected, and stoste pipeline is provided with injection device, the 3rd port of triple valve and the input of static mixer
End is connected, and the output end of static mixer is connected with cushion chamber, and cushion chamber is provided with the liquid outlet being connected with drain pipe,
It is characterized in that being additionally provided with spraying mechanism, the spraying mechanism is located at the top of cushion chamber 6, and spraying mechanism is provided with liquid atomiser
10, the inlet 11 of liquid atomiser 10 is connected with the drain pipe road of static mixer；The cushion chamber 6 is sealing and lucifuge
Cavity, cushion chamber 6 is provided with inlet 11, liquid outlet 12, exhaust outlet 13, and on inlet 11, liquid outlet 12, exhaust outlet 13
It is respectively equipped with liquid feed valve, liquid valve and pressure-releasing electromagnetic valve.
Liquid atomiser described in the utility model uses centrifugal type atomizer, and mist droplet particle size scope is：2-1200 μm, spray
Mist amount：0.1-100L/H.
Buffering cavity wall described in the utility model is sequentially provided with the first liquid level sensor, the second level sensing from top to bottom
Device, the 3rd liquid level sensor, the 4th liquid level sensor.
The utility model is additionally provided with the controlling organization for control device working condition, and controlling organization includes controller, step
Stepper motor controller, liquid level detection circuit, pressure-releasing electromagnetic valve, carbon dioxide solenoid valve, CO2 flow controller；Wherein control
The control signal all the way of device processed is connected with controllor for step-by-step motor, and controllor for step-by-step motor is connected with injection device stepper motor
Connect, complete injection device control；Four liquid level sensors are provided with liquid level detection circuit, respectively with the signal acquisition terminal of controller
It is connected；Pressure-releasing electromagnetic valve, carbon dioxide solenoid valve, CO2 flow controller export with the control signal of controller respectively
End is connected；Pressure-releasing electromagnetic valve is arranged on cushion chamber exhaust outlet, and CO2 flow controller is arranged on gas transmission pipeline
On, carbon dioxide solenoid valve is arranged in carbon dioxide canister.
The capacity of cushion chamber described in the utility model is more than 1L.
Mixing arrangement described in the utility model uses static mixer.
The utility model distinguishes running water delivery pipe, carbon dioxide snorkel and stoste pipeline during use
It is connected with running water, dioxide bottle, sodium hypochlorite stoste, carbon dioxide and running water are mixed by air and liquid mixer,
And static mixer is admitted to through triple valve, injection device drives stoste to be pumped into triple valve, static subsequently into static mixer
Mixed liquor in blender is admitted to cushion chamber, carries out further buffered, is then exported through drain pipe；Wherein in cushion chamber
Provided with spraying mechanism, cushion chamber stores the excess carbon dioxide gas overflowed in upper level process for preparation during use,
And by the atomizer in spraying mechanism to intracavitary feeding mixed solution, carbon dioxide in the mixed solution and cushion chamber after atomization
Gas further fully contacts, to improve the effect of thimerosal；When starting production, liquid outlet is closed, and liquid is entered by inlet
Enter cushion chamber, Exhaust Open, discharge the air in cushion chamber；When liquid level reaches the first liquid level sensor, exhaust close, go out
Liquid mouth is opened；Carbon dioxide purity can not reach 100%, during production, and waste gas gradually accumulates, liquid level in cushion chamber
It is gradually reduced, when liquid level reaches four liquid level sensors, liquid outlet is closed, Exhaust Open, discharges waste gas, and liquid level reaches first
During liquid level sensor, exhaust close, liquid outlet is opened；During normal production, when liquid level reaches the second liquid level sensor,
Illustrate CO in cushion chamber2Gas deficiency, increases CO2Air inflow, when liquid level reaches three liquid level sensors, illustrate in cushion chamber
CO2Gas is excessive, reduces CO2Air inflow, under normal production scenarios, liquid level is between liquid level sensor 2 and liquid level sensor 3；It is raw
During production, in water outlet, the pH value of test solution, when pH value is more than 6.5, drain tap is opened, discharges waste gas.
The utility model compared with prior art, has the advantages of rational in infrastructure, small volume etc. is notable.
Claims (5)
- A kind of 1. hypochlorous acid thimerosal process units with spraying mechanism, provided with running water delivery pipe, carbon dioxide canister, gas Liquid mixer, triple valve, static mixer, cushion chamber, drain pipe, injection device, liquor natrii hypochloritis's tank, wherein running water are defeated Send pipe and carbon dioxide canister that water and carbon dioxide are sent into air and liquid mixer, the output end and triple valve of air and liquid mixer respectively First port is connected, and the second port of triple valve is connected through stoste pipeline with liquor natrii hypochloritis's tank, is set on stoste pipeline There is injection device, the 3rd port of triple valve is connected with the input of static mixer, and the output end of static mixer is with delaying Rush chamber to be connected, cushion chamber is provided with the liquid outlet being connected with drain pipe, it is characterised in that is additionally provided with spraying mechanism, the spray Leaching mechanism is located at cushion chamber top, and spraying mechanism is provided with liquid atomiser, the inlet of liquid atomiser and static mixer Drain pipe road is connected；The cushion chamber is sealing and the cavity of lucifuge, and cushion chamber is provided with inlet, liquid outlet, exhaust outlet, And liquid feed valve, liquid valve and pressure-releasing electromagnetic valve are respectively equipped with inlet, liquid outlet, exhaust outlet.
- A kind of 2. hypochlorous acid thimerosal process units with spraying mechanism according to claim 1, it is characterised in that institute State liquid atomiser and use centrifugal type atomizer, mist droplet particle size scope is：2-1200 μm, spray amount：0.1-100L/H.
- A kind of 3. hypochlorous acid thimerosal process units with spraying mechanism according to claim 1, it is characterised in that institute State buffering cavity wall and be sequentially provided with the first liquid level sensor, the second liquid level sensor, the 3rd liquid level sensor, the 4th from top to bottom Liquid level sensor.
- 4. a kind of hypochlorous acid thimerosal process units with spraying mechanism according to claim 1, it is characterised in that also Provided with the controlling organization for control device working condition, controlling organization includes controller, controllor for step-by-step motor, level sensing Circuit, pressure-releasing electromagnetic valve, carbon dioxide solenoid valve, CO2 flow controller；Wherein the control signal all the way of controller with Controllor for step-by-step motor is connected, and controllor for step-by-step motor is connected with injection device stepper motor, completes injection device control； Four liquid level sensors are provided with liquid level detection circuit, are connected respectively with the signal acquisition terminal of controller；Pressure-releasing electromagnetic valve, two Carbonoxide magnetic valve, CO2 flow controller are connected with the control signal output of controller respectively；Pressure-releasing electromagnetic valve It is arranged on cushion chamber exhaust outlet, CO2 flow controller is arranged on gas transmission pipeline, and carbon dioxide solenoid valve is set Put in carbon dioxide canister.
- A kind of 5. hypochlorous acid thimerosal process units with spraying mechanism according to claim 1, it is characterised in that institute The capacity for stating cushion chamber is more than 1L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720733719.5U CN206940428U (en) | 2017-06-22 | 2017-06-22 | Hypochlorous acid thimerosal process units with spraying mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720733719.5U CN206940428U (en) | 2017-06-22 | 2017-06-22 | Hypochlorous acid thimerosal process units with spraying mechanism |
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| Publication Number | Publication Date |
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| CN206940428U true CN206940428U (en) | 2018-01-30 |
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| CN201720733719.5U Active CN206940428U (en) | 2017-06-22 | 2017-06-22 | Hypochlorous acid thimerosal process units with spraying mechanism |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111109288A (en) * | 2020-03-04 | 2020-05-08 | 盛毅 | Preparation method and device of efficient environment-friendly disinfectant |
| CN111346532A (en) * | 2020-03-13 | 2020-06-30 | 唐山市新概念科技有限公司 | Preparation method of carbonic acid-hypochlorous acid water |
| CN112499799A (en) * | 2020-08-10 | 2021-03-16 | 中山市原域企业投资有限公司 | Method and equipment for preparing hypochlorous acid by combining gas-liquid synthesis with ion exchange method |
| CN112593253A (en) * | 2020-11-24 | 2021-04-02 | 山东消博士消毒科技股份有限公司 | Hypochlorous acid hand-washing-free disinfectant manufacturing device |
| CN114617133A (en) * | 2021-09-10 | 2022-06-14 | 深圳日赛医疗科技有限公司 | Disinfectant and preparation method thereof |
-
2017
- 2017-06-22 CN CN201720733719.5U patent/CN206940428U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111109288A (en) * | 2020-03-04 | 2020-05-08 | 盛毅 | Preparation method and device of efficient environment-friendly disinfectant |
| CN111346532A (en) * | 2020-03-13 | 2020-06-30 | 唐山市新概念科技有限公司 | Preparation method of carbonic acid-hypochlorous acid water |
| CN112499799A (en) * | 2020-08-10 | 2021-03-16 | 中山市原域企业投资有限公司 | Method and equipment for preparing hypochlorous acid by combining gas-liquid synthesis with ion exchange method |
| CN112593253A (en) * | 2020-11-24 | 2021-04-02 | 山东消博士消毒科技股份有限公司 | Hypochlorous acid hand-washing-free disinfectant manufacturing device |
| CN114617133A (en) * | 2021-09-10 | 2022-06-14 | 深圳日赛医疗科技有限公司 | Disinfectant and preparation method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190521 Address after: 266000 Building 27, Tian'an Digital City, 88 Chunyang Road, Chengyang District, Qingdao City, Shandong Province Patentee after: Qingdao webac Disinfection Technology Co. Ltd. Address before: 264200 -9, -2, Shengshi garden, torch high tech Industrial Development Zone, Weihai, Shandong Patentee before: Shandong webac Disinfection Technology Co. Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210819 Address after: 266000 r101-3, baidu (Qingdao) Zhichuang base, building 15, No. 8, Tongshun Road, high tech Zone, Qingdao, Shandong Patentee after: Qingdao weibak Biotechnology Co.,Ltd. Address before: 266000 Building 27, Tian'an Digital City, 88 Chunyang Road, Chengyang District, Qingdao City, Shandong Province Patentee before: QINGDAO WEIBAKE DISINFECTION TECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right |