CN106044982A - Novel ozone water hybrid system - Google Patents
Novel ozone water hybrid system Download PDFInfo
- Publication number
- CN106044982A CN106044982A CN201610547570.1A CN201610547570A CN106044982A CN 106044982 A CN106044982 A CN 106044982A CN 201610547570 A CN201610547570 A CN 201610547570A CN 106044982 A CN106044982 A CN 106044982A
- Authority
- CN
- China
- Prior art keywords
- liquid
- valve
- ozone
- liquid mixer
- hybrid system
- 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.)
- Pending
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/23—O3
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a novel ozone water hybrid system used for sterilization in the purified water production packaging process. The novel ozone water hybrid system is characterized in that the system comprises a gas-liquid mixer and a liquid-liquid mixer which is connected with an outlet of the gas-liquid mixer, an ozone generator and a raw water pipe are connected to an inlet of the gas-liquid mixer, the raw water pipe is connected with an inlet of the liquid-liquid mixer, a buffer tank is connected to an outlet of the liquid-liquid mixer, and a delivery pump is connected to an outlet of the buffer tank. According to the novel ozone water hybrid system, raw water and ozone are mixed through the gas-liquid mixer, the raw water and the ozone are further mixed through the liquid-liquid mixer, the product water concentration is stale and uniform, and the sterilizing effect is improved.
Description
Technical field
The invention belongs to pure water production technical field, relate generally to a kind of novel produce packaging process for pure water
The Ozone Water hybrid system of middle sterilization.
Background technology
It is a critically important problem that pure water produces sterilization in packaging process, is mostly to sterilize by Ozone Water.Mesh
Front ozone and the mixing apparatus of water, main hybrid mode is Bubbling method, i.e. ozone enters bottom mixing column by pipeline, through micro-
Hole bubbler distributes micro-bubble, and bubble is dissolved in, ozone, the water that mixing column top enters in uphill process in mixing column
In.Along with the pressure at the bottom of tower is the biggest, aeration air pressure at the bottom of the admission pressure driving tower of ozone will be the strongest, and energy consumption increases.It addition, it is defeated
Sending pump bottom mixing column, the unstable easily by-pass flow of gas-to-liquid contact, ozone concentration is unstable uniformly.How to prepare the smelly of even concentration
Oxygen water, is that pure water produces the key issue of sterilization in packaging process.
Summary of the invention
It is an object of the invention to provide a kind of novel Ozone Water hybrid system, the ozone of even concentration can be prepared
Water.
In order to solve above-mentioned technical problem, the present invention is addressed by following technical proposals:
A kind of novel Ozone Water hybrid system, it is characterised in that: include air and liquid mixer and export the liquid being connected with it
Liquid mixer, the import of described air and liquid mixer connects ozonator and raw water tubes, and described raw water tubes also mixes with liquid liquid
The import of device connects, and the outlet of described liquid liquid mixer connects buffer tank, and the outlet of described buffer tank connects delivery pump.
Further, the described delivery pump other end connect have ozone concentration detector, described ozone concentration detector another
End connection has outlet tube and return duct, described return duct to be connected with the import of air and liquid mixer, described return duct and gas-liquid mixed
Pipeline between the import of device is provided with reflux inlet.
Further, the described ozone concentration detector other end is also associated with circulation pipe, described circulation pipe and buffer tank
Connecting, described circulation pipe is provided with circulating valve.
Further, described raw water tubes water inlet end is provided with water intaking valve, and described water intaking valve mixes with air and liquid mixer and liquid liquid
The first regulation valve and the second regulation valve it is respectively equipped with on pipeline between device.
Further, the outlet of described liquid liquid mixer and buffer tank side and top be respectively equipped with the first liquid feed valve and
Second liquid feed valve, the outlet at bottom of described buffer tank is additionally provided with tapping valve.
Further, it is provided with liquid level sensor inside buffer tank.
Beneficial effects of the present invention have following some:
1, first make former water and ozone be mixed by air and liquid mixer, then make former water and Ozone Water through liquid liquid mixer
Mixing further so that product water concentration is relatively stable uniformly, improves bactericidal effect；
2, ozone concentration is detected by ozone concentration detector, if concentration is improper, with smelly after being refluxed by return duct
Oxygen mixes further, avoids polluting while energy efficient；
3, circulation pipe is connected with buffer tank, and the product water that wouldn't use returns in buffer tank in time, it is to avoid product water is wasted,
It also avoid causes ozone concentration to change when using next time；
4, according to the ozone concentration of detection, in time by regulation valve regulation inflow and water inlet speed, adjust ozone and occur
The power of device, it is achieved energy-saving and cost-reducing purpose；
5, by the second liquid feed valve and the tapping valve of buffer tank, it is achieved the CIP cleaning and sterilizing to buffer tank；
6, the capacity of Ozone Water in buffer tank can be monitored in time by the liquid level sensor within buffer tank, adjust system
Running status.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention；
Wherein 1 be buffer tank, 2 for ozonator, 3 for liquid liquid mixer, 4 for air and liquid mixer, 5 for ozone concentration inspection
Survey instrument, 6 be liquid level sensor, 7 be delivery pump, 8 be water intaking valve, 9 be the first regulation valve, 10 be the second regulation valve, 11 be second
Liquid feed valve, 12 be the first liquid feed valve, 13 for tapping valve, 14 for delivery valve, 15 for circulating valve, 16 for reflux inlet, 17 for canned valve,
18 is drain valve.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is described in further detail:
Ozone Water hybrid system as shown in Figure 1, ozonator 2 and raw water tubes respectively with the import of air and liquid mixer 4
Connecting, the outlet of air and liquid mixer 4 is connected with the import of liquid liquid mixer 3, raw water tubes also with the import of liquid liquid mixer 3 company
Connecing, the outlet Connection Cache tank 1 of liquid liquid mixer 3, the outlet of buffer tank 1 connects delivery valve 14, the other end of delivery valve 14
Connecting and have delivery pump 7, delivery pump 7 other end connects has ozone concentration detector 5, ozone concentration detector 5 other end to set respectively
Having conveying pipe, return duct, circulation pipe, conveying pipe to be provided with filling valve 17 and drain valve 18, return duct is provided with reflux inlet 16, separately
One end is connected with the import of air and liquid mixer 4, and circulation pipe is provided with circulating valve 15, and the other end is connected with buffer tank 1.Raw water tubes enters
Water end (W.E.) is provided with water intaking valve 8, and the pipeline between water intaking valve 8 and air and liquid mixer 4 and liquid liquid mixer 3 is respectively equipped with the first regulation
Valve 9, second regulates valve 10.The outlet of liquid liquid mixer and buffer tank side and top are respectively equipped with the first liquid feed valve 12 and
Two liquid feed valves 11, the bottom of buffer tank is additionally provided with tapping valve 13.Buffer tank 1 is internal is additionally provided with liquid level sensor 6.
Former water is mixed with the dissolving of ozone and is completed by air and liquid mixer 4, more uniform and stable through liquid liquid mixer 5
Ozone concentration, enters buffer tank 1 by the first liquid feed valve 12, after provide product water through delivery pump 7 to filling machine.Work as buffer tank
During 1 preparation water inlet, water intaking valve the 8, first liquid feed valve 12 automatically opens up, and ozonator 2 automatically turns on, by the first regulation valve 9
With the second regulation valve 10 regulating water flow, make former water enter buffer tank 1 through air and liquid mixer 4 and liquid liquid mixer 5, treat buffer tank
When 1 liquid level reaches setting value, i.e. it is ready for providing product water to filling machine.Ozone concentration detector 5 is used to detect in product water
Whether ozone concentration reaches the running status of setting value and filling machine, switching circulating valve 15, drain valve 18, reflux inlet 16 and fill
Valve 17 realizes the circulation of product water, discharges, refluxes and fill.The CIP cleaning and sterilizing of buffer tank 1 is by the second liquid feed valve 11 and row
Liquid valve 13 completes.
In a word, the foregoing is only presently preferred embodiments of the present invention, all equalizations made according to scope of the present invention patent
Change and modification, all should belong to the covering scope of patent of the present invention.
Claims (6)
1. a novel Ozone Water hybrid system, it is characterised in that: include air and liquid mixer and export the liquid liquid being connected with it
Blender, the import of described air and liquid mixer connects ozonator and raw water tubes, described raw water tubes also with liquid liquid mixer
Import connect, the outlet of described liquid liquid mixer connects buffer tank, and the outlet of described buffer tank connects delivery pump.
Ozone Water hybrid system the most according to claim 1, it is characterised in that: the described delivery pump other end connects ozone
Concentration detector, the described ozone concentration detector other end connects outlet tube and return duct, described return duct and gas-liquid mixed
The import of device connects, and the pipeline between described return duct and the import of air and liquid mixer is provided with reflux inlet.
Ozone Water hybrid system the most according to claim 2, it is characterised in that: the described ozone concentration detector other end is also
Connecting has circulation pipe, described circulation pipe to be connected with buffer tank, and described circulation pipe is provided with circulating valve.
Ozone Water hybrid system the most according to claim 1 and 2, it is characterised in that: described raw water tubes water inlet end be provided with into
Water valve, the pipeline between described water intaking valve and air and liquid mixer and liquid liquid mixer is respectively equipped with the first regulation valve and second and adjusts
Joint valve.
Ozone Water hybrid system the most according to claim 1, it is characterised in that: the outlet of described liquid liquid mixer and caching
Tank side and top are respectively equipped with the first liquid feed valve and the second liquid feed valve, and the outlet at bottom of described buffer tank is additionally provided with discharge opeing
Valve.
Ozone Water hybrid system the most according to claim 1, it is characterised in that: it is provided with level sensing inside described buffer tank
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610547570.1A CN106044982A (en) | 2016-07-11 | 2016-07-11 | Novel ozone water hybrid system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610547570.1A CN106044982A (en) | 2016-07-11 | 2016-07-11 | Novel ozone water hybrid system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106044982A true CN106044982A (en) | 2016-10-26 |
Family
ID=57186070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610547570.1A Pending CN106044982A (en) | 2016-07-11 | 2016-07-11 | Novel ozone water hybrid system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106044982A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106892498A (en) * | 2017-03-07 | 2017-06-27 | 广州达意隆包装机械股份有限公司 | A kind of ozone adding set |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5578205A (en) * | 1992-11-24 | 1996-11-26 | Trailigaz | Plant for removing micropollutants from untreated water by the combined action of ozone and hydrogen peroxide |
| CN2564556Y (en) * | 2002-08-16 | 2003-08-06 | 西安三氧环保科技有限公司 | Device for producing large flow ozone water |
| CN101327994A (en) * | 2008-07-17 | 2008-12-24 | 大连海事大学 | A method for ozone treatment of ship's ballast water during discharge |
| CN202829694U (en) * | 2012-08-28 | 2013-03-27 | 四川标源环保科技有限公司 | All-in-one machine used for generation of household ozone water and direct drinking water |
| CN104084067A (en) * | 2014-07-31 | 2014-10-08 | 中法合营王朝葡萄酿酒有限公司 | Fully-automatic ozone water mixing device |
-
2016
- 2016-07-11 CN CN201610547570.1A patent/CN106044982A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5578205A (en) * | 1992-11-24 | 1996-11-26 | Trailigaz | Plant for removing micropollutants from untreated water by the combined action of ozone and hydrogen peroxide |
| CN2564556Y (en) * | 2002-08-16 | 2003-08-06 | 西安三氧环保科技有限公司 | Device for producing large flow ozone water |
| CN101327994A (en) * | 2008-07-17 | 2008-12-24 | 大连海事大学 | A method for ozone treatment of ship's ballast water during discharge |
| CN202829694U (en) * | 2012-08-28 | 2013-03-27 | 四川标源环保科技有限公司 | All-in-one machine used for generation of household ozone water and direct drinking water |
| CN104084067A (en) * | 2014-07-31 | 2014-10-08 | 中法合营王朝葡萄酿酒有限公司 | Fully-automatic ozone water mixing device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106892498A (en) * | 2017-03-07 | 2017-06-27 | 广州达意隆包装机械股份有限公司 | A kind of ozone adding set |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
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| RJ01 | Rejection of invention patent application after publication | ||
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Application publication date: 20161026 |