CN2431291Y - Generator for producing large flow of ozone water - Google Patents
Generator for producing large flow of ozone water Download PDFInfo
- Publication number
- CN2431291Y CN2431291Y CN 00218357 CN00218357U CN2431291Y CN 2431291 Y CN2431291 Y CN 2431291Y CN 00218357 CN00218357 CN 00218357 CN 00218357 U CN00218357 U CN 00218357U CN 2431291 Y CN2431291 Y CN 2431291Y
- Authority
- CN
- China
- Prior art keywords
- water
- ozone
- valve
- links
- ball valve
- Prior art date
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The utility model relates to a producing device for producing ozone water of high flow quantity, which comprises an ozone producer by using an electrolytic method, a flow quantity adjusting valve for inlet water, a mixing tower, an exhaust gas absorber, a DC current stabilizing power supply, pipelines, a raw water storage barrel, a water supplementing pump, a water supplementing switch, and a high-voltage switch. A lower port of the mixing tower is connected with a back flushing water inlet ball valve and a water outlet ball valve, an upper port of the mixing tower is connected with a water inlet ball valve and a back flushing water discharging ball valve, and a venturi pipe is connected with the water inlet valve. An ozone outlet is connected with a gas inlet of the venturi pipe, and an automatic gas returning valve is connected with a gas inlet of the venturi pipe. A cooling water adjusting valve is connected with the ozone producer behind a flow meter and returns back to the mixing tower, and the exhaust gas absorber is connected with an automatic gas discharging valve. Due to the adoption of the measures, the utility model can continuously produce ozone water of high flow quantity.
Description
The utility model relates to a kind of ozone water in large flux generating apparatus, and it belongs to the ozone technology Application Areas.
Utilized the ozone source of physics electric discharge to prepare ozone water before the utility model, concentration is low, and produced simultaneously oxynitride has caused the pollution of water and should not use.The employing electrolysis ozone generator is that the device of the preparation ozone water of ozone source has 97212224.9.
97212224.9 described ozone water preparation facilities comprises solid polymer electrolyte film composite electrode electrolysis ozone generator device, the water outlet watch-dog of limiting the quantity of, gas-water mixer, air water separator, ozone reduction device, entering water electromagnetic valve, throttling valve, casing, connecting tube and dc current stabilized power supply and automatic control circuit; The solid polymer electrolyte film composite electrode electrolysis ozone generator communicates with gas-water mixer, gas-water mixer is communicated with water source from the beginning through throttling valve, magnetic valve, gas-water mixer also communicates with atmosphere behind air water separator, ozone reduction device, and water outlet is arranged on the air water separator.This device ozone water flow is little, electrolysis desired raw material water adds complexity, and the outlet of electrolysis ozone generator ozone gas can not be negative pressure, and the ozone water water outlet can not arbitrarily move, can not prolong.Settling in the gas-water mixer can't clean, and the electrolysis type ozone generator cooling is not enough.
The purpose of this utility model is; Overcome the deficiency of existing ozone water generating device, a kind of ozone water in large flux generating apparatus is provided, further improve ozone utilization rate.
Realize that the technical measures that the purpose of this utility model is taked are: the utility model comprises electrolytic process ozone generating-device, flooding velocity variable valve, mixing column, tail gas absorber, dc current stabilized power supply, pipeline, it is characterized in that: this device also is provided with the raw water water butt, the raw water water butt links to each other with small pump, small pump links to each other with high-voltage switch gear with the moisturizing switch by check valve, the moisturizing switch links to each other with electrolytic process ozone generating-device fluid infusion mouth, and electrolytic process ozone generating-device hydrogen air outlet links to each other with the raw water water butt; Water inlet pipe links to each other with the recoil water intake ball valve with the flooding velocity variable valve, and the mixing column end opening links to each other with recoil water intake ball valve, water outlet ball valve; Mixing column is suitable for reading to link to each other with water intake ball valve, recoil draining ball valve; The Venturi meter water-in links to each other with the flooding velocity variable valve by under meter; The Venturi meter water outlet links to each other with water intake ball valve; Electrolytic process ozone generating-device ozone outlet links to each other with the Venturi meter inlet mouth by check valve, and automatic return-air valve links to each other with the Venturi meter inlet mouth behind the mixing column; Have cooling sea water regulating valve to link to each other with electrolytic process ozone generating-device water coolant clamping plate, cooling water intake behind the under meter, electrolytic process ozone generating-device cooling water outlet links to each other with mixing column, and tail gas absorber links to each other with automatic exhaust steam valve.
Since adopted above measure, the utility model can prepare big flow (1 ton～10 tons/hour) ozone water continuously, the consistency of ozone water height, and the raw water supply is convenient; Mixing column can clean easily by recoil; Ozone utilization rate improves 10%～20%; The ozone water water outlet can be connected to the use point as required.
Below in conjunction with drawings and Examples the utility model is further described:
Figure one is the utility model structural representation.Among the figure, (1) electrolytic process ozone generating-device, (2) ozone escape pipe, (3) CWR, (4) moisturizing switch, (5) check valve, (6) high-voltage switch gear, (7) cooling water inlet pipe, (8) small pump, (9) water intake ball valve, (10) ozone muffler, (11) tail gas absorber, (12) recoil draining ball valve, (13) water shoot, (14) are return-air valve automatically, (15) automatic exhaust steam valve, (16) rising pipe, (17) water outlet ball valve, (18) mixing column, (19) recoil water intake ball valve, (20) water inlet pipe, (21) flooding velocity variable valve, (22) under meter, (23) cooling sea water regulating valve, (24) Venturi meter, (25) check valve, (26) raw water water butt, (27) fluid infusion water inlet pipe, (28) return water pipe, (29) small pump transformer, (30) stabilized current supply, (31) cooling connecting leg.
The utility model is described in further detail below in conjunction with embodiment:
The utility model structure is referring to figure one, and wherein (number of patent application: 00218261.0) can adopt a plurality ofly, this electrolytic process ozonizer (1) is a power supply with conventional direct supply (30) to electrolytic process ozone generating-device (1), and working current is 13.5 amperes.When the raw water in the electrolytic process ozonizer (1) is less than 1/3, open moisturizing switch (4), produce raw water that ozone need consume from raw water water butt (26) by fluid infusion water inlet pipe (27), suck by small pump (8), and enter the fluid infusion mouth of electrolytic process ozonizer (1) by check valve (5), moisturizing switch (4).The water that negative electrode produces in electrolytic process ozonizer (1) work flows back to raw water water butt (26) by return water pipe (28).Fluid infusion finishes moisturizing switch (4) when closing, and forms high pressure by small pump (8) in pipeline between small pump (8) and moisturizing switch (4), and 24 volts of direct supplys that small pump (8) is provided by transformer (29) are cut off in high-voltage switch gear (6) action.High pressure wherein is by check valve (5), small pump (8), the common maintenance of moisturizing switch (4).The cooling sea water regulating valve (23) of the water coolant of electrolytic process ozone generating-device (1) after by under meter (22) drawn, and electrolytic process ozone generating-device (1) cooled off the back flow into mixing column (18) by CWR (3), and flow is 80 liters/hour.Ozone is entered the inlet mouth of Venturi meter (24) by check valve (25) by ozone escape pipe (2).When making ozone water, recoil water intake ball valve (19), recoil draining ball valve (12) keep closing, and tap water carries out Flow-rate adjustment after under meter (22) enters Venturi meter (24) water-in by water inlet pipe (20) through flooding velocity variable valve (21).Water outlet by Venturi meter (24) carry out the first step turbulent mixing in Venturi meter (24) after flows out, and enter mixing column (18) through water intake ball valve (9) and carry out the mixing of second step, be porous corrosion resistant filler pottery etc. in the mixing column (18).Complete mixed ozone water flows out to use point through automatic return-air valve (14), automatic exhaust steam valve (15), water outlet ball valve (17) by rising pipe (16) by the end opening of mixing column (18).Automatically return-air valve (14) ozone that will fail to utilize fully is delivered to the inlet mouth of Venturi meter (24) through ozone muffler (10), has made full use of ozone.Automatic exhaust steam valve (15) is introduced tail gas absorber (11) with residual ozone and is absorbed, and eliminates environmental pollution.Reach 500 ton hours when handling water yield accumulative total, the reply oxidizing tower carries out bob-weight and cleans, close flooding velocity variable valve (21), water intake ball valve (9), cooling sea water regulating valve (23), water outlet ball valve (17) during recoil, open recoil draining ball valve (12), recoil water intake ball valve (19), tap water is entered by mixing column (18) end opening by water inlet pipe (20), recoil water intake ball valve (19), the interior settling of mixing column (18) is taken out of by recoil draining ball valve (12), water shoot (13) flowed out.
But the preparation ozone water in large flux of the utility model continous-stable, it is widely used in food-processing, public health, disinfecting field.
Claims (3)
1. ozone water in large flux generating apparatus, comprise electrolytic process ozone generating-device (1), flooding velocity variable valve (21), mixing column (18), tail gas absorber (11), dc current stabilized power supply (30), pipeline, it is characterized in that: this device also is provided with raw water water butt (26), raw water water butt (26) links to each other with small pump (8), small pump (8) links to each other with high-voltage switch gear (6) with moisturizing switch (4) by check valve (5), moisturizing switch (4) links to each other with electrolytic process ozone generating-device (1) fluid infusion mouth, and electrolytic process ozone generating-device (1) hydrogen air outlet links to each other with raw water water butt (26); Water inlet pipe (20) links to each other with recoil water intake ball valve (19) with flooding velocity variable valve (21), and mixing column (18) end opening links to each other with recoil water intake ball valve (19), water outlet ball valve (17); Mixing column (18) is suitable for reading to link to each other with water intake ball valve (9), recoil draining ball valve (12); Venturi meter (24) water-in links to each other with flooding velocity variable valve (21) by under meter (22); Venturi meter (24) water outlet links to each other with water intake ball valve (9); Electrolytic process ozone generating-device (1) ozone outlet links to each other with Venturi meter (24) inlet mouth by check valve (25), and mixing column (18) back return-air valve (14) automatically links to each other with Venturi meter (24) inlet mouth; There is cooling sea water regulating valve (23) to link to each other behind the under meter (22) with electrolytic process ozone generating-device (1) water coolant clamping plate, cooling water intake, electrolytic process ozone generating-device (1) cooling water outlet links to each other with mixing column (18), and tail gas absorber (11) links to each other with automatic exhaust steam valve (15).
2. it is characterized in that by claim 1 described a kind of ozone water in large flux generating apparatus electrolytic process ozonizer (1) adopts single water tank.
3. it is characterized in that by claim 1 described a kind of ozone water in large flux generating apparatus ozone escape pipe (2), ozone muffler (10) all link to each other with Venturi meter (24) inlet mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00218357 CN2431291Y (en) | 2000-07-11 | 2000-07-11 | Generator for producing large flow of ozone water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00218357 CN2431291Y (en) | 2000-07-11 | 2000-07-11 | Generator for producing large flow of ozone water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2431291Y true CN2431291Y (en) | 2001-05-23 |
Family
ID=33583749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00218357 Expired - Fee Related CN2431291Y (en) | 2000-07-11 | 2000-07-11 | Generator for producing large flow of ozone water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2431291Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295326A (en) * | 2010-06-22 | 2011-12-28 | 刘迅 | Water electrolysis device |
| WO2011160446A1 (en) * | 2010-06-22 | 2011-12-29 | Liu Xun | Water electrolytic device |
| CN103657459A (en) * | 2013-08-26 | 2014-03-26 | 上海维埃姆环保科技有限公司 | Ozone water production equipment |
| CN107115798A (en) * | 2017-04-24 | 2017-09-01 | 杭州天霁环境科技有限公司 | High-oxygen water preparation system |
| CN108328578A (en) * | 2018-01-29 | 2018-07-27 | 荣成海奥斯生物科技有限公司 | The filling apparatus of gaseous state effective chlorine aqueous solution |
| CN110180418A (en) * | 2019-07-11 | 2019-08-30 | 广州市德百顺电气科技有限公司 | A kind of ozone water solution mixing arrangement |
-
2000
- 2000-07-11 CN CN 00218357 patent/CN2431291Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295326A (en) * | 2010-06-22 | 2011-12-28 | 刘迅 | Water electrolysis device |
| WO2011160446A1 (en) * | 2010-06-22 | 2011-12-29 | Liu Xun | Water electrolytic device |
| CN103657459A (en) * | 2013-08-26 | 2014-03-26 | 上海维埃姆环保科技有限公司 | Ozone water production equipment |
| CN103657459B (en) * | 2013-08-26 | 2016-02-03 | 上海维埃姆环保科技有限公司 | A kind of ozone water production equipment |
| CN107115798A (en) * | 2017-04-24 | 2017-09-01 | 杭州天霁环境科技有限公司 | High-oxygen water preparation system |
| CN108328578A (en) * | 2018-01-29 | 2018-07-27 | 荣成海奥斯生物科技有限公司 | The filling apparatus of gaseous state effective chlorine aqueous solution |
| CN108328578B (en) * | 2018-01-29 | 2020-03-10 | 荣成海奥斯生物科技有限公司 | Filling device for gaseous available chlorine aqueous solution |
| CN110180418A (en) * | 2019-07-11 | 2019-08-30 | 广州市德百顺电气科技有限公司 | A kind of ozone water solution mixing arrangement |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN2431291Y (en) | Generator for producing large flow of ozone water | |
| CN108178346A (en) | A kind of river depth oxygenate apparatus | |
| CN2504267Y (en) | Ozonized water appts. | |
| CN213895275U (en) | Self-gas circulation air-flotation solid-liquid separation device for oil field produced water treatment | |
| CN212954648U (en) | Supersaturated oxygen-dissolved water preparation device | |
| CN208933196U (en) | A kind of device of the integrated rural sewage treatment using green energy resource | |
| CN205953680U (en) | Super supersaturated with dissolved oxygen aeration equipment | |
| CN212655595U (en) | Automatic control system for water quality of high-level water collecting cooling tower of thermal power plant | |
| CN213803116U (en) | Water inflow dissolved oxygen full-flow control system of denitrification filter | |
| CN207957857U (en) | A kind of anoxic water body in-situ electricity oxygenate apparatus | |
| CN106430587B (en) | Two stages automatic stirring sewage clean water tank with denitrification functions | |
| CN221117117U (en) | Wall-hanging hydrogen water machine | |
| CN101638906A (en) | Energy-saving water supply equipment | |
| CN112058057A (en) | Low-pressure electrolyzed water type mixed ozone water supply deodorization device | |
| CN109111053A (en) | A kind of technique and its device of the integrated rural sewage treatment using green energy resource | |
| CN2359269Y (en) | Portable chlorine dioxide generator | |
| CN205892791U (en) | High -efficiency air flotation dissolves gas device | |
| CN213995473U (en) | A high-efficient ozone dissolves gas device for sewage treatment | |
| CN106050522A (en) | Aeration power generation device in sea water desalination | |
| CN205710942U (en) | A kind of solution for hydro-electrolytic hydroxide mixed gas equipment adds tank automatically | |
| CN2934220Y (en) | Well pump pneumatic direct-supplying deironing demanganizing equipment | |
| CN220827308U (en) | Ultra-micron gas dissolving device | |
| CN2564556Y (en) | Device for producing large flow ozone water | |
| CN219031917U (en) | Water supply oxygenation conversion device | |
| CN221544376U (en) | Water production optimizing device of EDI device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHANGHAI SHIJING PURIFYING SCI-TECH CO., LTD. Free format text: FORMER NAME OR ADDRESS: SHANGHAI HOUSSAY TECHNOLOGY CO., LTD. Free format text: NO CO-PATENTEE; FORMER NAME OR ADDRESS: HU BO |
|
| CP03 | Change of name, title or address |
Address after: 200050 Shanghai, Wuyi Road, Changning District 238 Patentee after: Shanghai Shijing Purifying Sci-Tech Co., Ltd. Address before: 201101 No. 1911, Lane 41, Shanghai, Caobao Road Co-patentee before: Hu Bai Patentee before: Shanghai Orsay Technology Co., Ltd. |
|
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Hu Bai Document name: Notification of Termination of Patent Right |
|
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |