CN103027073A - Generating device for weak hypochlorous acid disinfectant with no need for power supply - Google Patents
Generating device for weak hypochlorous acid disinfectant with no need for power supply Download PDFInfo
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- CN103027073A CN103027073A CN2013100006361A CN201310000636A CN103027073A CN 103027073 A CN103027073 A CN 103027073A CN 2013100006361 A CN2013100006361 A CN 2013100006361A CN 201310000636 A CN201310000636 A CN 201310000636A CN 103027073 A CN103027073 A CN 103027073A
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- Prior art keywords
- water
- gas
- valve
- control valve
- mixer
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000000645 desinfectant Substances 0.000 title abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 239000007788 liquid Substances 0.000 claims abstract description 26
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims abstract description 12
- RTKIYNMVFMVABJ-UHFFFAOYSA-L thimerosal Chemical compound [Na+].CC[Hg]SC1=CC=CC=C1C([O-])=O RTKIYNMVFMVABJ-UHFFFAOYSA-L 0.000 claims description 32
- 229940033663 thimerosal Drugs 0.000 claims description 32
- 239000002253 acid Substances 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 7
- 230000005611 electricity Effects 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 abstract 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 14
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 239000005708 Sodium hypochlorite Substances 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 229960002668 sodium chloride Drugs 0.000 description 2
- 235000002639 sodium chloride Nutrition 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- UKLNMMHNWFDKNT-UHFFFAOYSA-M sodium chlorite Chemical compound [Na+].[O-]Cl=O UKLNMMHNWFDKNT-UHFFFAOYSA-M 0.000 description 1
- 229960002218 sodium chlorite Drugs 0.000 description 1
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Abstract
The invention relates to a generating device for a weak hypochlorous acid disinfectant with no need for a power supply. The generating device is characterized in that the generating device comprises a CO2 gas supply passage, an NaClO solution supply passage, a water supply passage, a disinfectant passage, gas-water mixers and a gas-water control system, wherein the CO2 gas supply passage is formed by sequentially connecting a gas bottle, a pressure reducing valve, a flow control valve, mechanical valves and a speed-regulating valve; the NaClO solution supply passage is formed by sequentially connecting a solution storage tank, a check valve, a flow control valve and a liquid-liquid mixer; the disinfectant passage is formed by sequentially connecting the liquid-liquid mixer, a pH (Potential of Hydrogen) measurer, a speed-regulating valve and a disinfectant storage tank; the gas-water control system regulates and controls two gas cylinders, mechanical levers and the mechanical valves through water pressure, buoyancy and gas pressure so as to control the opening and closing of the CO2 gas supply passage; CO2 and the water are fully mixed and dissolved in the two gas-water mixers connected in parallel to prepare carbonated water; the carbonated water is mixed with an NaClO solution obtained by a siphon principle in the liquid-liquid mixer to prepare the hypochlorous acid disinfectant; and the hypochlorous acid disinfectant passes through the pH measurer and the speed-regulating valve and enters the disinfectant storage tank.
Description
Technical field
The present invention relates to a kind of generating apparatus that does not need the hypochlorous acid thimerosal that power supply controls.
Background technology
Thimerosal take hypochlorous acid as main component is with aqueous sodium hypochlorite solution and diluted mixed in hydrochloric acid at present, perhaps the hydrochloric acid Direct Electrolysis is obtained the thimerosal take hypochlorous acid as main component, also can carry out electrolysis by in the septate electrolytic cell of tool between positive pole and the negative pole, adding sodium chloride, thereby generate hypochloric acid water solution at side of the positive electrode.
But, in the process with aqueous sodium hypochlorite solution and mixed in hydrochloric acid, be difficult to control the dosage of the hydrochloric acid of interpolation, easily produce chlorine (Cl
2) or chlorine dioxide (ClO
2) gas, generally containing the safety instruction that all can have " forbidding using with acid " on the commercially available disinfectant container of sodium chlorite.In addition, be 5.5~6.5 o'clock owing to containing the thimerosal of clorox at pH, the hypochlorous acid molecule content is the highest, and bactericidal effect is also best.If near hypochlorous acid contains proportional high pH 5 the regulation electrolytic condition, accurate control device then must be arranged, and in reality, electrolytic condition can only be extended near the control device the pH 7.When adding sodium-chloride water solution between positive pole and negative pole, establishing in the septate electrolytic cell, dilute with water after the hypochlorous acid that generates high concentration, when generating by this thimerosal take hypochlorous acid as main component, need in the hypochlorous acid that electrolysis generates, add watery hydrochloric acid and carry out the pH adjustment, but generate the thimerosal of desirable pH, just must strictly control the concentration of watery hydrochloric acid, the thimerosal that generates desired concentration must be adjusted the amount of watery hydrochloric acid, must carry out the control of unreality in order to make concentration and pH reach together desirable value, but actually can only set the scope of pH wider.
In addition, present device all be at electric energy driving, control under finish, and bulky, make, use cost is too high, be difficult to promote the popularization use, this thimerosal generating apparatus not only expends a large amount of electric energy, and the equipment operating place all is in humidity and has in the environment of water simultaneously, very easily leak electricity, the electric shock phenomenon, the life security that threatens the people; Apparatus of the present invention are that prevention, the control of various diseases is provided convenience, and particularly advantage is more obvious when various burst natural calamity.
Summary of the invention
For addressing the above problem, the invention provides a kind of small-sized generating apparatus that does not need the faintly acid hypochlorous acid thimerosal that power supply controls, comprise CO
2Air feed path, confession water passage, clorox feed flow path, thimerosal path, Bas Discharged path, the gentle water control system of gas-water mixer.Wherein, CO
2The air feed path is connected in sequence by gas cylinder, pressure-reducing valve, flow control valve, precision pressure adjuster, mechanical valve, flow speed control valve; Be formed by connecting by water source, flow control valve for water passage; Clorox feed flow path is connected in sequence by clorox fluid reservoir, check valve, flow control valve, liquid liquid mixer; The thimerosal path is connected in sequence by liquid liquid mixer, pH measuring appliance, flow speed control valve, thimerosal storage tank.The air water control system is to be supplied water to gas-water mixer A by the water source, enter gas-water mixer B through gas-water mixer A in parallel and the connecting path of B respectively, pass through simultaneously connecting path, flow speed control valve, two Y-piece joints, at this moment air is discharged through flow control valve, and the pressure-acting of water is in cylinder, after opening machinery valve by mechanical lever, CO
2Gas arrives another machinery valve, and machinery valve is opened CO under buoyancy power transmission shaft and mechanical lever effect simultaneously
2Gas arrives another cylinder through flow speed control valve, keeps opening of machinery valve, meanwhile CO
2Gas is by flow speed control valve, be mixed into gas-water mixer A and B in parallel, CO in gas-water mixer A and B at T-shaped pipe joint and water
2Gas fully mixes and is dissolved in the water with water makes carbonated water, and carbonated water is mixed with the liquor natrii hypochloritis who arrives by the liquid siphon principle in the liquid liquid mixer, enters the thimerosal storage tank through pH measuring appliance, flow speed control valve.Hydraulic pressure descends when closing the water source, and two cylinder pressures reduce, and the buoyancy power transmission shaft descends simultaneously, and at this moment two machinery valve autoshutdowns have cut off CO
2The air feed path, thus do not need electricity consumption to finish Pneumatic-hydraulic interlocked control overall process, made faintly acid hypochlorous acid thimerosal.
By regulation and control source pressure be 0.1~0.2MPa, flow is 8 liter/mins during flowing water; Regulation and control CO
2The gas precision pressure regulator makes CO
2Gas pressure is 0.35MPa, thereby so that thimerosal pH remains on 5.5~6.5, makes thimerosal reach the strongest bactericidal effect.
Description of drawings
Fig. 1 is the overall structure figure that does not need the hypochlorous acid thimerosal generating apparatus of power supply.
Wherein: gas cylinder (1), pressure-reducing valve (2), flow control valve (3), precision pressure adjuster (4), mechanical valve (5), mechanical valve (6), Y-piece joint (7), flow speed control valve (8), T-shaped pipe joint (9), flow speed control valve (10), cylinder (11), water source (12), flow control valve (13), gas-water mixer A (14), gas-water mixer B (15), connecting path (16), connecting path (17), buoyancy power transmission shaft (18), mechanical lever (19), connecting path (20), Y-piece joint (21), Y-piece joint (22), cylinder (23), mechanical lever (24), flow speed control valve (25), T-shaped pipe joint (26), clorox fluid reservoir (27), check valve (28), flow control valve (29), liquid liquid mixer (30), pH measuring appliance (31) flow speed control valve (32), thimerosal storage tank (33), flow control valve (34).
Embodiment
As shown in Figure 1, a kind of generating apparatus that does not need the faintly acid hypochlorous acid thimerosal of power supply is characterized in that, comprises CO
2Air feed path, confession water passage, liquor natrii hypochloritis's feed flow path, thimerosal path, Bas Discharged path, the gentle water control system of gas-water mixer.Wherein, CO
2The air feed path is connected in sequence by gas cylinder (1), pressure-reducing valve (2), flow control valve (3), precision pressure adjuster (4), mechanical valve (5), mechanical valve (6), Y-piece joint (7), flow speed control valve (8), T-shaped pipe joint (9); Be connected in sequence by water source (12), flow control valve (13), T-shaped pipe joint (9) for water passage; Liquor natrii hypochloritis's feed flow path is connected in sequence by clorox fluid reservoir (27), check valve (28), flow control valve (29), liquid liquid mixer (30); The thimerosal path is connected in sequence by T-shaped pipe joint (26), liquid liquid mixer (30), pH measuring appliance (31) flow speed control valve (32), thimerosal storage tank (33).The air water control system is that (hydraulic pressure is 0.1~0.2MPa by water source (12) water supply, flowing water is that flow is 8 liter/mins) enter gas-water mixer A (14) after, pass through respectively gas-water mixer A in parallel and the connecting path (16) of B, (17) enter gas-water mixer B (15), pass through simultaneously connecting path (20), T-shaped pipe joint (26), flow speed control valve (25), Y-piece joint (21) and (22), at this moment air is discharged through flow control valve (34), and the pressure-acting of water is in cylinder (23), after opening machinery valve (5) by mechanical lever (24), CO
2Gas arrives machinery valve (6), and machinery valve (6) is opened CO under buoyancy power transmission shaft (18) and mechanical lever (19) act on simultaneously
2Gas arrives cylinder (11) by Y-piece joint (7) through flow speed control valve (10), keeps opening of machinery valve (6), meanwhile CO
2Gas passes through flow speed control valve (8), is mixed into gas-water mixer A (14) in parallel and gas-water mixer B (15), CO in gas-water mixer A and B at T-shaped pipe joint (9) and water by Y-piece joint (7)
2Gas fully mixes and is dissolved in the water with water makes carbonated water, carbonated water is through T-shaped pipe joint (26), in liquid liquid mixer (30), mix with the liquor natrii hypochloritis who arrives by the liquid siphon principle, enter thimerosal storage tank (33) through pH measuring appliance (31) (pH remains on 5.5~6.5), flow speed control valve (32).Hydraulic pressure descends when closing the water source, and cylinder (11) reduces with cylinder (23) pressure, and buoyancy power transmission shaft (18) descends simultaneously, and at this moment machinery valve (5) and machinery valve (6) autoshutdown have cut off CO
2The air feed path, thus do not need electricity consumption to finish Pneumatic-hydraulic interlocked control overall process, made faintly acid hypochlorous acid thimerosal.
It is emphasized that; embodiment of the present invention is illustrative; rather than determinate; therefore the present invention is not limited to the embodiment described in the embodiment; every other embodiment that is drawn by those skilled in the art's technical scheme according to the present invention belongs to the scope of protection of the invention equally.
Claims (2)
1. a generating apparatus that does not need the faintly acid hypochlorous acid thimerosal of power supply is characterized in that, comprises CO
2Air feed path, confession water passage, liquor natrii hypochloritis's feed flow path, thimerosal path, Bas Discharged path, the gentle water control system of gas-water mixer.Wherein, CO
2The air feed path is connected in sequence by gas cylinder (1), pressure-reducing valve (2), flow control valve (3), precision pressure adjuster (4), mechanical valve (5), mechanical valve (6), Y-piece joint (7), flow speed control valve (8), T-shaped pipe joint (9); Be connected in sequence by water source (12), flow control valve (13), T-shaped pipe joint (9) for water passage; Liquor natrii hypochloritis's feed flow path is connected in sequence by clorox fluid reservoir (27), check valve (28), flow control valve (29), liquid liquid mixer (30); The thimerosal path is connected in sequence by T-shaped pipe joint (26), liquid liquid mixer (30), pH measuring appliance (31) flow speed control valve (32), thimerosal storage tank (33); The air water control system is that (hydraulic pressure is 0.1~0.2MPa by water source (12) water supply, flowing water is that flow is 8 liter/mins) enter gas-water mixer A (14) after, pass through respectively gas-water mixer A in parallel and the connecting path (16) of B, (17) enter gas-water mixer B (15), pass through simultaneously connecting path (20), T-shaped pipe joint (26), flow speed control valve (25), Y-piece joint (21) and (22), at this moment air is discharged through flow control valve (34), and the pressure-acting of water is in cylinder (23), after opening machinery valve (5) by mechanical lever (24), CO
2Gas arrives machinery valve (6), and machinery valve (6) is opened CO under buoyancy power transmission shaft (18) and mechanical lever (19) act on simultaneously
2Gas arrives cylinder (11) by Y-piece joint (7) through flow speed control valve (10), keeps opening of machinery valve (6), meanwhile CO
2Gas passes through flow speed control valve (8), is mixed into gas-water mixer A (14) in parallel and gas-water mixer B (15), CO in gas-water mixer A and B at T-shaped pipe joint (9) and water by Y-piece joint (7)
2Gas fully mixes and is dissolved in the water with water makes carbonated water, carbonated water is through T-shaped pipe joint (26), in liquid liquid mixer (30), mix with the liquor natrii hypochloritis who arrives by the liquid siphon principle, enter thimerosal storage tank (33) through pH measuring appliance (31) (pH remains on 5.5~6.5), flow speed control valve (32); Hydraulic pressure descends when closing the water source, and cylinder (11) reduces with cylinder (23) pressure, and buoyancy power transmission shaft (18) descends simultaneously, and at this moment machinery valve (5) and machinery valve (6) autoshutdown have cut off CO
2The air feed path, thus do not need electricity consumption to finish Pneumatic-hydraulic interlocked control overall process, made faintly acid hypochlorous acid thimerosal.
2. the regulation and control source pressure is 0.1~0.2MPa, and flow is 8 liter/mins during flowing water; Regulation and control CO
2The gas precision pressure regulator makes CO
2Gas pressure is 0.35MPa, thus make thimerosal pH remain on 5.5~6.5 and concentration controlled.
Priority Applications (1)
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CN201310000636.1A CN103027073B (en) | 2013-01-05 | 2013-01-05 | Generating device for weak hypochlorous acid disinfectant with no need for power supply |
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CN201310000636.1A CN103027073B (en) | 2013-01-05 | 2013-01-05 | Generating device for weak hypochlorous acid disinfectant with no need for power supply |
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CN103027073B CN103027073B (en) | 2014-09-03 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105621360A (en) * | 2014-10-29 | 2016-06-01 | 广东先导稀材股份有限公司 | Preparation method of hypochlorite |
CN108849971A (en) * | 2018-07-15 | 2018-11-23 | 西安青叶生物科技有限公司 | A kind of preparation and its application method using acidulous hypochlorous acid's type thimerosal |
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 |
JP2021053546A (en) * | 2019-09-27 | 2021-04-08 | 合同会社Fmc | Manufacturing equipment and manufacturing method for carbonic acid-containing hypochlorous acid water |
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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JP2004181445A (en) * | 2002-10-11 | 2004-07-02 | Viita Kk | Sterilized water production apparatus |
CN1774290A (en) * | 2003-04-14 | 2006-05-17 | 冈崎龙夫 | Method and device for generating carbonated water |
WO2006090869A1 (en) * | 2005-02-23 | 2006-08-31 | Veeta Inc. | Process for producing sterile water containing hypochlorous acid or chlorous acid as its main component and apparatus therefor |
CN101124169A (en) * | 2005-02-23 | 2008-02-13 | 威踏株式会社 | Process for producing sterile water containing hypochlorous acid or chlorous acid as its main component and apparatus therefor |
JP4828012B2 (en) * | 2000-05-12 | 2011-11-30 | 東亜ディーケーケー株式会社 | Disinfection water generation method and apparatus |
CN203233951U (en) * | 2013-01-05 | 2013-10-16 | 马惠祥 | Generating device of weak acidic hypochlorous disinfectant without power supply |
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2013
- 2013-01-05 CN CN201310000636.1A patent/CN103027073B/en not_active Expired - Fee Related
Patent Citations (6)
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JP4828012B2 (en) * | 2000-05-12 | 2011-11-30 | 東亜ディーケーケー株式会社 | Disinfection water generation method and apparatus |
JP2004181445A (en) * | 2002-10-11 | 2004-07-02 | Viita Kk | Sterilized water production apparatus |
CN1774290A (en) * | 2003-04-14 | 2006-05-17 | 冈崎龙夫 | Method and device for generating carbonated water |
WO2006090869A1 (en) * | 2005-02-23 | 2006-08-31 | Veeta Inc. | Process for producing sterile water containing hypochlorous acid or chlorous acid as its main component and apparatus therefor |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105621360A (en) * | 2014-10-29 | 2016-06-01 | 广东先导稀材股份有限公司 | Preparation method of hypochlorite |
CN105621360B (en) * | 2014-10-29 | 2018-06-26 | 广东先导稀材股份有限公司 | Preparation method of hypochlorite |
CN108849971A (en) * | 2018-07-15 | 2018-11-23 | 西安青叶生物科技有限公司 | A kind of preparation and its application method using acidulous hypochlorous acid's type thimerosal |
JP2021053546A (en) * | 2019-09-27 | 2021-04-08 | 合同会社Fmc | Manufacturing equipment and manufacturing method for carbonic acid-containing hypochlorous acid water |
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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