WO2010031227A1 - An apparatus for making high pressure ozonated water - Google Patents

An apparatus for making high pressure ozonated water Download PDF

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Publication number
WO2010031227A1
WO2010031227A1 PCT/CN2008/072968 CN2008072968W WO2010031227A1 WO 2010031227 A1 WO2010031227 A1 WO 2010031227A1 CN 2008072968 W CN2008072968 W CN 2008072968W WO 2010031227 A1 WO2010031227 A1 WO 2010031227A1
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WO
WIPO (PCT)
Prior art keywords
water
pressure mixing
pressure
stage
barrel
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Application number
PCT/CN2008/072968
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French (fr)
Chinese (zh)
Inventor
徐名勇
Original Assignee
Hsu Ming Yung
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Publication of WO2010031227A1 publication Critical patent/WO2010031227A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • B01F23/2341Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
    • B01F23/23413Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using nozzles for projecting the liquid into the gas atmosphere
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23761Aerating, i.e. introducing oxygen containing gas in liquids
    • B01F23/237613Ozone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/70Spray-mixers, e.g. for mixing intersecting sheets of material
    • B01F25/72Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/81Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/81Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
    • B01F33/811Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged

Definitions

  • the present invention relates to a multistage high pressure mixing device for producing high pressure ozone water (pressure: 0.3 to 7.0 kg/cm2), which is a mixing device for ozone gas and water.
  • Ozone water is widely used due to its disinfection and sterilization function.
  • the low pressure ozone water pressure currently manufactured is 0.15 ⁇ 0.
  • the low-pressure ozone water mixing device can not meet the requirements of high-pressure cleaning and scouring and sanitizing treatment, and the low-pressure ozone water mixing device also has the disadvantages of low mixing efficiency and high aeration.
  • the ozone gas reaches a certain concentration in the use space, Inflicts damage on the human body.
  • it is necessary to increase the supercharging device, which has the disadvantages of high cost, high noise and vibration, and often cannot be tolerated by the supercharging device. Oxidation and failure in the short term.
  • this multi-stage high-pressure mixing device capable of producing high-pressure ozone water through many years of efforts and a large number of experiments, by which the mixing efficiency can be effectively improved, and high-pressure ozone water is produced.
  • the applicant has invented this multi-stage high-pressure mixing device capable of producing high-pressure ozone water through many years of efforts and a large number of experiments, by which the mixing efficiency can be effectively improved, and high-pressure ozone water is produced.
  • the object of the present invention is to provide a multi-stage high-pressure mixing device for manufacturing high-pressure ozone water with a simple structure, convenient use, safety, high mixing efficiency, long service life and low cost, in order to overcome the deficiencies of the prior art.
  • a multi-stage high-pressure mixing device for manufacturing high-pressure ozone water which has a water inlet, characterized in that the water inlet is respectively connected to at least two stages of high-pressure mixing barrels, each stage of high pressure
  • the mixing barrel is provided with a water inlet hole, a water outlet hole and an air inlet hole, and a water inlet electromagnetic valve is arranged between the water inlet port and the water inlet hole of the high pressure mixing barrel, and the air inlet port passes through the high pressure tube and the first stage high pressure mixing barrel.
  • the air holes are connected, and the water outlet hole of the high-pressure mixing barrel of the first stage is connected to the air inlet hole of the lower-stage high-pressure mixing barrel through the high-pressure pipe, and the water outlet hole of the first-stage high-pressure mixing barrel is connected to the first-stage gas-water separation device through the high-pressure pipe, and each High pressure mixing
  • the barrels are provided with a spray atomization device connected to the water inlet hole, and the high-pressure mixing barrel net frame is arranged inside the last high-pressure mixing barrel, and the gas-water separation net is arranged on the high-pressure mixing barrel net frame, the first-stage gas water
  • the water outlet of the separation device is connected to the water inlet of the second-stage gas-water separation device, and the water outlet of the second-stage gas-water separation device is connected to the water outlet through the water outlet solenoid valve and the pressure regulating valve, the first-stage gas-water separation device and the second-stage
  • the gas outlet of the gas-water separation device is connected to the reduction device, and the reduction
  • each of the high-pressure mixing barrels has a barrel body, on the barrel body
  • the lower end is respectively connected with the upper cover of the high pressure mixing barrel and the lower cover of the high pressure mixing barrel.
  • the water inlet hole and the air inlet hole of the high pressure mixing barrel are arranged on the upper cover of the high pressure mixing barrel, and the water outlet hole of the high pressure mixing barrel is set on the lower cover of the high pressure mixing barrel. .
  • the spray atomization device is connected below the water inlet hole of the lower end of the high pressure mixing barrel, and the nozzle nut is connected outside the nozzle, and the lower end of the nozzle inside the nozzle nut is provided.
  • the barrel body is sealed with a high pressure mixing barrel upper cover and a high pressure mixing barrel lower cover by a 0-type sealing jaw.
  • the high pressure mixing drum is 2-10, that is, the number of high pressure mixing drums is 2-10.
  • the gas-water separation net is made of an ozone-resistant mesh material.
  • the gas-water separation net is made of a microporous titanium mesh of 100 mesh or more or an ozone-resistant mesh material.
  • the present invention can produce the following positive effects:
  • the present invention performs a first-stage high-pressure mixing of tap water having a pressure of 1.5 to 9.0 kg/cm 2 and a high-pressure ozone gas having a pressure of 0.35 to 9.0 kg/cm 2 , and the pressure in the mixing system is
  • the water jet blades 4-7, 6-7, 8-7 and the pressure regulating valve 11 in each stage of the mixing tank are adjusted to 0.3 to 7.0 kg/cm2, and the tap water is mixed with the mixture of ozone gas and ozone water in multiple stages.
  • the invention adopts multi-stage mixing, and the whole device is uniform High-pressure parts and high-pressure components are connected by high-pressure pipes, which can effectively produce high-pressure ozone water with a pressure of 0.3 ⁇ 7.0kg/cm2, and can improve the mixing efficiency of ozone gas and water to over 80%, and achieve remarkable Reduce the effect of ozone aeration.
  • Figure 1 is a block diagram showing the structure of the present invention
  • FIG. 2 is a schematic structural view of a multi-stage mixing barrel of the present invention
  • FIG. 3 is an enlarged view showing the structure of the spray atomizing device of the mixing tub of FIG. 2;
  • Fig. 4 is a cross-sectional view taken along line A-A of Fig. 2.
  • Embodiment A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water (see FIG. 1 to FIG. 4), which has a water inlet 1, and a water inlet 1 is respectively connected to at least two high-pressure mixing barrels, and the number of high-pressure mixing barrels can be
  • the number of the high-pressure mixing barrels in the embodiment is three, that is, the first-stage high-pressure mixing barrel 4, the second-stage high-pressure mixing barrel 6, and the third-stage high-pressure mixing barrel 8, and the water inlet 1 passes through the first stage.
  • the water solenoid valve 3 is connected to the water inlet hole 4-1 of the first stage high pressure mixing drum 4, and the water inlet port 1 is connected to the water inlet hole 6-1 of the second stage high pressure mixing barrel 6 through the second stage water inlet solenoid valve 5.
  • the water inlet 1 is connected to the water inlet hole 8.1 of the third stage high pressure mixing tank 8 through the third stage water inlet solenoid valve 7, the first stage high pressure mixing barrel 4, the second stage high pressure mixing barrel 6 and the third stage high pressure mixing.
  • the structure of the barrel 8 is basically the same.
  • the structure of the high pressure mixing barrel 8 is exemplified below:
  • the third stage high pressure mixing barrel 8 has a barrel 8-10, and the upper and lower ends of the barrel 8-10 are respectively connected by a bolt 8-12.
  • the water inlet hole 8-1 and the air inlet hole 8-2 are respectively disposed on the end faces of the high pressure mixing barrel upper cover 8-3, and the water outlet holes 8-13 are arranged on the high pressure mixing barrel lower cover 8-11.
  • the high pressure mixing tank 8 is provided with a spray atomizing device (see Fig. 3), which is connected to the nozzle 8-5 below the water inlet hole 8-1 at the lower end of the high pressure mixing barrel upper cover 8-3, and the nozzle 8-5 is connected externally.
  • the nozzle nut 8-6, the lower end of the nozzle 8-5 in the nozzle nut 8-6 is provided with a water jet edge 8-7.
  • the inner stage of the first stage high pressure mixing tank 8 is provided with a high pressure mixing barrel grid 8-9, a gas water separating net 8-8 is installed on the grid, and the gas water separating net 8-8 uses a microporous titanium of 100 mesh or more. Made of mesh or other ozone resistant mesh material. These two parts are not present in the first stage high pressure mixing tank 4 and the second stage high pressure mixing tank 6.
  • the first stage high pressure mixing drum 4 has a barrel body 4-10, and the upper and lower ends of the barrel body 4-10 are respectively connected by a bolt 4-12 to the high pressure mixing barrel upper cover 4-3 and the high pressure mixing barrel lower cover 4-11, and Sealed by type 0 4-4 sealed.
  • the water inlet hole 4-1 and the air inlet hole 4-2 are respectively disposed on the end faces of the upper cover 4-3 of the high pressure mixing barrel, and the water outlet holes 4-13 are provided on the lower cover 4-11 of the high pressure mixing barrel.
  • the high pressure mixing tank 4 is provided with a spray atomizing device which is connected to the nozzle 4-5 below the water inlet hole 4-1 at the lower end of the high pressure mixing barrel upper cover 4-3, and the nozzle nut 4 is connected outside the nozzle 4-5. 6.
  • the lower end of the nozzle 4-5 in the nozzle nut 4-6 is provided with a water jet edge 4-7.
  • the second stage high pressure mixing barrel 6 has a barrel body 6-10, and the upper and lower ends of the barrel body 6-10 are respectively connected by a bolt 6-12 to a high pressure mixing barrel upper cover 6-3, a high pressure mixing barrel lower cover 6-11, and Type 0 seal ⁇ 6-4 sealed.
  • the water inlet hole 6-1 and the air inlet hole 6-2 are respectively arranged on the end surface of the upper cover 6-3 of the high pressure mixing barrel, and the water outlet hole 6-13 is arranged on the lower cover 6-11 of the high pressure mixing barrel.
  • the high-pressure mixing tank 6 is provided with a spray atomizing device, which is connected to the nozzle 6-5 below the water inlet hole 6-1 at the lower end of the high-pressure mixing barrel upper cover 6-3, and the nozzle nut 6- is connected outside the nozzle 6-5. 6.
  • the lower end of the nozzle 6-5 in the nozzle nut 6-6 is provided with a water jet edge 6-7.
  • the air inlet 2 is connected to the air inlet hole 4-2 of the first stage high pressure mixing drum 4 through a high pressure pipe, and the water outlet hole 4-13 of the first stage high pressure mixing barrel 4 is connected to the air inlet of the second stage high pressure mixing barrel 6 through a high pressure pipe.
  • the hole 6-2, the water outlet hole 6-13 of the second stage high pressure mixing barrel 6 is connected to the air inlet hole 8-2 of the third stage high pressure mixing barrel 8 through the high pressure pipe, and the water outlet hole 8-13 of the third stage high pressure mixing barrel 8
  • the water inlet of the first-stage gas-water separation device 9 is connected to the water inlet of the first-stage gas-water separation device 9 through a high-pressure pipe
  • the water outlet of the second-stage gas-water separation device 10 is connected to the water inlet of the second-stage gas-water separation device 10
  • the nozzle is connected to the water outlet 13 through the water discharge solenoid valve 11 and the pressure regulating valve 12.
  • the air outlets of the first and second stage gas-water separation devices are connected to the reduction device 14, and the reduction device 14 is connected to the exhaust port 15.
  • the high-pressure ozone gas with a pressure of 0.35 ⁇ 9.0kg/cm2 enters the first-stage mixing tank 4 through the air inlet 2, and the ozone gas enters from the air inlet hole 4-2 on the upper cover 4-3 of the high-pressure mixing barrel, and meets the water mist.
  • the gas and water are dissolved in the ozone water, and the crucible is subjected to the first stage high pressure mixing in the barrel.
  • Ozone water and part of the water-insoluble ozone gas flow together through the water outlet holes 4-13 on the lower lid of the high-pressure mixing tank 4-11, through the high-pressure connecting pipe and the intake air on the upper cover 6-3 of the second high-pressure mixing barrel
  • the hole 6-2 enters the second stage high pressure mixing barrel 6-10, the second stage water inlet solenoid valve 5 is opened, the tap water enters the second stage mixing barrel 6, and the water is pressurized from the second stage high pressure mixing barrel 6-10.
  • the water inlet hole 6-1 on the mixing tank upper cover 6-3 flows in, and the water-insoluble ozone gas carried by the ozone water sprays the atomized water in the second-stage high-pressure mixing barrel 6-10 with the nozzle 6-5.
  • the mist is mixed in the second stage, and the ozone gas which is not dissolved in water is mixed into ozone water, which can be effectively treated by the two-stage high pressure mixing. Improve the mixing efficiency, but there is still a small amount of ozone gas which is not soluble in water.
  • Ozone water carries a small amount of ozone gas together and flows through the water outlet hole 6-13 on the lower cover 6-11 of the high pressure mixing tank, and is covered from the third stage high pressure mixing barrel.
  • the air inlet 8-2 on the 8-3 flows into the third stage high pressure mixing barrel 8-10, and the third stage water inlet solenoid valve 7 is opened, the tap water enters the third stage mixing barrel 8, and the water is discharged from the third stage high pressure.
  • the water inlet hole 8-1 on the upper lid 8-3 of the high pressure mixing tank on the mixing tank 8-10 flows in, and the third stage mixing is performed in the third stage high pressure mixing tank 8-10.
  • the third-stage high-pressure mixing tank 8-10 is equipped with a gas-water separation net 8-8.
  • the gas-water separation net 8-8 (see Fig. 4) is made of a 100-mesh or 100-mesh microporous titanium mesh or other ozone-resistant mesh material.
  • the ozone water When the ozone water carries the ozone bubbles flowing through the gas-water separation net 8-8 in the third-stage mixing tank 8, the ozone bubbles entrained in the ozone water are broken up into a plurality of micro-bubbles, and the micro-bubbles float and are sprayed into the mixing barrel. The water mist is then dissolved into ozone water, which avoids the ozone bubbles being carried away by the ozone water, further improving the mixing efficiency of ozone gas and water.
  • the ozone water carries a small amount of ozone gas together and flows through the high pressure mixing barrel under the cover 8-11.
  • the water outlet holes 8-13 enter the gas water separation device.
  • the pressure inside the multistage high pressure mixing device is adjusted to 0.3 to 7.0 kg/cm2 by the water jet blades 4-7, 6-7, 8-7 and the pressure regulating valve 11 to meet the demand for efficient mixing. If the mixing efficiency of the three-stage mixing tank does not achieve the desired effect, the number of mixing barrels can be additionally increased to increase the number of mixing, such as the fourth-stage mixing barrel, the fifth-stage mixing barrel, etc., to achieve higher Demand. After multiple stages of mixing, a very small amount of ozone gas is mixed in the ozone water to flow through the first-stage gas-water separation device 9 and the second-stage gas-water separation device 10, and the ozone water and the water-insoluble ozone gas are separated.
  • the high-pressure ozone water having a pressure of 0.3 to 7.0 kg/cm2 flows out of the water outlet 13 through the water discharge solenoid valve 11 and the pressure regulating valve 12.
  • the ozone gas is reduced to oxygen by the reduction device 14 and is discharged from the exhaust port 15.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

An apparatus for making high pressure ozonated water includes several high pressure mixing pot(4,6,8) in series, each of which comprises a spraying and atomizing means(4-5,6-5,8-5), a water feeding hole, a water discharging hole and an air feeding hole. A water inlet(1) of said apparatus is connected to the high pressure mixing pots(4,6,8), and a gas inlet(2) thereof is connected to the first high pressure mixing pot(4). A net rack(8-9) with a gas-water separating net(8-8) is provided inside of the last high pressure mixing pot(8) connecting with a first gas-water separator(9). The first gas-water separator(9) is connected to a second gas-water separator(10) connecting with a water outlet(13), and both separators(9,10) are connected to a gas outlet(15) through a reductor(14).

Description

一种高压臭氧水制造装置  High-pressure ozone water manufacturing device
技术领域 Technical field
[1] 本发明涉及一种制造高压力臭氧水 (压力为 0.3~7.0kg/cm2) 的多级高压混合装 置,属于臭氧气和水的混合装置。  [1] The present invention relates to a multistage high pressure mixing device for producing high pressure ozone water (pressure: 0.3 to 7.0 kg/cm2), which is a mixing device for ozone gas and water.
背景技术  Background technique
[2] 臭氧水因有消毒杀菌功能而被广泛使用, 目前制造的低压臭氧水压力为 0.15~0.  [2] Ozone water is widely used due to its disinfection and sterilization function. The low pressure ozone water pressure currently manufactured is 0.15~0.
25kg/cm2, 无法满足高压清洗和冲刷等消毒卫生处理的要求, 且低压臭氧水的 混合装置还存在混合效率低及曝气量高的缺点, 当臭氧气在使用空间达到一定 的浓度吋, 会对人体造成伤害。 若要得到压力为 0.3~7.0kg/cm2的高压力臭氧水 , 则需要增加增压装置, 增压装置具有高成本、 高噪音及震动的缺点, 而且往 往由于增压装置不能耐受臭氧的强氧化而短期内失效。 为了解决这些不足, 申 请人通过多年的努力和大量的试验发明了这种能够制造高压力臭氧水的多级高 压混合装置, 通过这种装置可以有效的提高混合效率, 制造出高压力的臭氧水 , 使臭氧水的应用更加方便、 安全、 广泛。  25kg/cm2, can not meet the requirements of high-pressure cleaning and scouring and sanitizing treatment, and the low-pressure ozone water mixing device also has the disadvantages of low mixing efficiency and high aeration. When the ozone gas reaches a certain concentration in the use space, Inflicts damage on the human body. In order to obtain high-pressure ozone water with a pressure of 0.3~7.0kg/cm2, it is necessary to increase the supercharging device, which has the disadvantages of high cost, high noise and vibration, and often cannot be tolerated by the supercharging device. Oxidation and failure in the short term. In order to solve these shortcomings, the applicant has invented this multi-stage high-pressure mixing device capable of producing high-pressure ozone water through many years of efforts and a large number of experiments, by which the mixing efficiency can be effectively improved, and high-pressure ozone water is produced. To make the application of ozone water more convenient, safe and extensive.
对发明的公开  Disclosure of invention
技术问题  technical problem
[3] 本发明的目的在于克服上述已有技术的不足而提供一种结构简单, 使用方便、 安全, 混合效率高、 使用寿命长, 成本低的制造高压力臭氧水的多级高压混合 装置。  [3] The object of the present invention is to provide a multi-stage high-pressure mixing device for manufacturing high-pressure ozone water with a simple structure, convenient use, safety, high mixing efficiency, long service life and low cost, in order to overcome the deficiencies of the prior art.
技术解决方案  Technical solution
[4] 本发明的目的可以通过以下措施来实现: 一种制造高压力臭氧水的多级高压混 合装置, 它具有进水口, 其特征在于进水口分别连接至少两级高压混合桶, 每 级高压混合桶均设有进水孔、 出水孔及进气孔, 进水口与高压混合桶的进水孔 之间设有进水电磁阀, 进气口通过高压管与第一级高压混合桶的进气孔相连, 前一级高压混合桶的出水孔通过高压管连接下一级高压混合桶的进气孔, 最后 一级高压混合桶的出水孔通过高压管连接第一级气水分离装置, 每级高压混合 桶均设有与进水孔相连的喷淋雾化装置, 最后一级高压混合桶的内部设有高压 混合桶网架, 高压混合桶网架上设有气水分离网, 第一级气水分离装置的出水 口连接第二级气水分离装置的进水口, 第二级气水分离装置的出水口通过出水 电磁阀、 压力调节阀连接出水口, 第一级气水分离装置和第二级气水分离装置 的出气口连接还原装置, 还原装置连接排气口。 [4] The object of the present invention can be achieved by the following measures: A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water, which has a water inlet, characterized in that the water inlet is respectively connected to at least two stages of high-pressure mixing barrels, each stage of high pressure The mixing barrel is provided with a water inlet hole, a water outlet hole and an air inlet hole, and a water inlet electromagnetic valve is arranged between the water inlet port and the water inlet hole of the high pressure mixing barrel, and the air inlet port passes through the high pressure tube and the first stage high pressure mixing barrel. The air holes are connected, and the water outlet hole of the high-pressure mixing barrel of the first stage is connected to the air inlet hole of the lower-stage high-pressure mixing barrel through the high-pressure pipe, and the water outlet hole of the first-stage high-pressure mixing barrel is connected to the first-stage gas-water separation device through the high-pressure pipe, and each High pressure mixing The barrels are provided with a spray atomization device connected to the water inlet hole, and the high-pressure mixing barrel net frame is arranged inside the last high-pressure mixing barrel, and the gas-water separation net is arranged on the high-pressure mixing barrel net frame, the first-stage gas water The water outlet of the separation device is connected to the water inlet of the second-stage gas-water separation device, and the water outlet of the second-stage gas-water separation device is connected to the water outlet through the water outlet solenoid valve and the pressure regulating valve, the first-stage gas-water separation device and the second-stage The gas outlet of the gas-water separation device is connected to the reduction device, and the reduction device is connected to the exhaust port.
[5] 为了进一步实现本发明的目的, 所述的每级高压混合桶均具有桶体, 桶体的上 [5] In order to further achieve the object of the present invention, each of the high-pressure mixing barrels has a barrel body, on the barrel body
、 下端分别连接高压混合桶上盖、 高压混合桶下盖, 高压混合桶的进水孔、 进 气孔设在高压混合桶上盖上,高压混合桶的出水孔设在高压混合桶下盖上。 The lower end is respectively connected with the upper cover of the high pressure mixing barrel and the lower cover of the high pressure mixing barrel. The water inlet hole and the air inlet hole of the high pressure mixing barrel are arranged on the upper cover of the high pressure mixing barrel, and the water outlet hole of the high pressure mixing barrel is set on the lower cover of the high pressure mixing barrel. .
[6] 为了进一步实现本发明的目的, 所述的喷淋雾化装置是在高压混合桶上盖下端 进水孔的下方连接喷嘴, 喷嘴外连接喷嘴螺帽, 喷嘴螺帽内喷嘴的下端设有喷 水刀口。  [6] In order to further achieve the object of the present invention, the spray atomization device is connected below the water inlet hole of the lower end of the high pressure mixing barrel, and the nozzle nut is connected outside the nozzle, and the lower end of the nozzle inside the nozzle nut is provided. There is a water jet knife.
[7] 为了进一步实现本发明的目的, 所述的桶体与高压混合桶上盖、 高压混合桶下 盖之间由 0型密封圏密封。  [7] In order to further achieve the object of the present invention, the barrel body is sealed with a high pressure mixing barrel upper cover and a high pressure mixing barrel lower cover by a 0-type sealing jaw.
[8] 为了进一步实现本发明的目的, 所述的高压混合桶为 2— 10级, 即高压混合桶 的数量为 2— 10。 [8] In order to further achieve the object of the present invention, the high pressure mixing drum is 2-10, that is, the number of high pressure mixing drums is 2-10.
[9] 为了进一步实现本发明的目的, 所述的气水分离网用耐臭氧的网状材质制成。  [9] In order to further achieve the object of the present invention, the gas-water separation net is made of an ozone-resistant mesh material.
[10] 为了进一步实现本发明的目的, 所述的气水分离网用 100目或 100目以上的微孔 钛板网或耐臭氧的网状材质制成。  [10] In order to further achieve the object of the present invention, the gas-water separation net is made of a microporous titanium mesh of 100 mesh or more or an ozone-resistant mesh material.
有益效果  Beneficial effect
[11] 本发明可产生如下积极效果: 本发明将压力为 1.5~9.0kg/cm2的自来水和压力为 0.35~9.0kg/cm2的高压臭氧气进行第一级高压混合, 混合系统内的压力由每级混 合桶内的喷水刀口 4-7、 6-7、 8-7和压力调节阀 11调整到 0.3~7.0kg/cm2, 后将自 来水与臭氧气和臭氧水的混合物进行多级混合。 当臭氧水携带臭氧气泡流经最 后一级混合桶内的气水分离网吋, 臭氧水中夹带的臭氧气泡被打散成许多微气 泡, 微气泡浮起, 与喷入混合桶内的水雾再溶合为臭氧水, 此气水分离网避免 了臭氧气泡被臭氧水带走, 更进一步提高了臭氧气与水的混合效率。 依次经过 多级混合后, 还有极少量的臭氧气混在臭氧水中流经第一级和第二级气水分离 装置将臭氧水和未溶于水的臭氧气分离。 本发明釆用多级混合, 整个装置均釆 用高压零件、 高压组件通过高压管连接而成, 能够有效的制造出压力为 0.3~7.0k g/cm2的高压臭氧水, 并且能够使臭氧气与水的混合效率提高到 80%以上, 并且 达到显著降低臭氧曝气量的效果。 [11] The present invention can produce the following positive effects: The present invention performs a first-stage high-pressure mixing of tap water having a pressure of 1.5 to 9.0 kg/cm 2 and a high-pressure ozone gas having a pressure of 0.35 to 9.0 kg/cm 2 , and the pressure in the mixing system is The water jet blades 4-7, 6-7, 8-7 and the pressure regulating valve 11 in each stage of the mixing tank are adjusted to 0.3 to 7.0 kg/cm2, and the tap water is mixed with the mixture of ozone gas and ozone water in multiple stages. When ozone water carries ozone bubbles through the gas-water separation network in the last-stage mixing tank, the ozone bubbles entrained in the ozone water are broken up into many micro-bubbles, and the micro-bubbles float up, and the water mist sprayed into the mixing tank Dissolved into ozone water, this gas-water separation net avoids ozone bubbles being carried away by ozone water, further improving the mixing efficiency of ozone gas and water. After multiple stages of mixing, a very small amount of ozone gas is mixed in the ozone water and passed through the first-stage and second-stage gas-water separation devices to separate the ozone water from the water-insoluble ozone gas. The invention adopts multi-stage mixing, and the whole device is uniform High-pressure parts and high-pressure components are connected by high-pressure pipes, which can effectively produce high-pressure ozone water with a pressure of 0.3~7.0kg/cm2, and can improve the mixing efficiency of ozone gas and water to over 80%, and achieve remarkable Reduce the effect of ozone aeration.
附图说明  DRAWINGS
[12] 图 1是本发明的的结构框图; Figure 1 is a block diagram showing the structure of the present invention;
[13] 图 2是本发明的多级混合桶的结构示意图; [13] FIG. 2 is a schematic structural view of a multi-stage mixing barrel of the present invention;
[14] 图 3是图 2的混合桶的喷淋雾化装置的结构放大图; [13] FIG. 3 is an enlarged view showing the structure of the spray atomizing device of the mixing tub of FIG. 2;
[15] 图 4是图 2的 A-A剖面图。 [15] Fig. 4 is a cross-sectional view taken along line A-A of Fig. 2.
本发明的最佳实施方式  BEST MODE FOR CARRYING OUT THE INVENTION
[16] 下面结合说明书附图对本发明的具体实施方式作详细说明: [16] The specific embodiments of the present invention are described in detail below with reference to the accompanying drawings:
实施例: 一种制造高压力臭氧水的多级高压混合装置 (参见图 1一图 4) , 它具 有进水口 1, 进水口 1分别连接至少两个高压混合桶, 高压混合桶的数量可根据 需要而定, 本实施例中高压混合桶的数量为 3个, 即第一级高压混合桶 4、 第二 级高压混合桶 6及第三级高压混合桶 8, 进水口 1通过第一级进水电磁阀 3与第一 级高压混合桶 4的进水孔 4 - 1连接, 进水口 1通过第二级进水电磁阀 5与第二级高 压混合桶 6的进水孔 6 - 1连接, 进水口 1通过第三级进水电磁阀 7与第三级高压混 合桶 8的进水孔 8 - 1连接, 第一级高压混合桶 4、 第二级高压混合桶 6及第三级高 压混合桶 8的结构基本相同, 下面以高压混合桶 8为例说明其结构: 第三级高压 混合桶 8具有桶体 8-10, 桶体 8-10的上、 下端分别由螺栓 8-12连接高压混合桶上 盖 8-3、 高压混合桶下盖 8-11, 并由 0型密封圏 8-4密封。 高压混合桶上盖 8-3的端 面上分别设有进水孔 8-1、 进气孔 8-2,高压混合桶下盖 8-11上设有出水孔 8-13。 高 压混合桶 8设有喷淋雾化装置 (参见图 3) , 该装置是在高压混合桶上盖 8-3下端 进水孔 8-1的下方连接喷嘴 8-5, 喷嘴 8-5外连接喷嘴螺帽 8-6, 喷嘴螺帽 8-6内喷嘴 8-5的下端设有喷水刀口 8-7。 最后一级高压混合桶 8的内部设有高压混合桶网架 8 -9 , 网架上安装气水分离网 8-8, 气水分离网 8-8用 100目或 100目以上的微孔钛板 网或其他耐臭氧的网状材质制成。 第一级高压混合桶 4和第二级高压混合桶 6内 没有这两个零件。 同样第一级高压混合桶 4具有桶体 4- 10, 桶体 4-10的上、 下端 分别由螺栓 4-12连接高压混合桶上盖 4-3、 高压混合桶下盖 4-11, 并由 0型密封圏 4-4密封。 高压混合桶上盖 4-3的端面上分别设有进水孔 4-1、 进气孔 4-2,高压混合 桶下盖 4-11上设有出水孔 4-13。 高压混合桶 4设有喷淋雾化装置, 该装置是在高 压混合桶上盖 4-3下端进水孔 4-1的下方连接喷嘴 4-5, 喷嘴 4-5外连接喷嘴螺帽 4-6 , 喷嘴螺帽 4-6内喷嘴 4-5的下端设有喷水刀口 4-7。 第二级高压混合桶 6具有桶体 6-10, 桶体 6-10的上、 下端分别由螺栓 6-12连接高压混合桶上盖 6-3、 高压混合桶 下盖 6-11, 并由 0型密封圏 6-4密封。 高压混合桶上盖 6-3的端面上分别设有进水 孔 6-1、 进气孔 6-2,高压混合桶下盖 6-11上设有出水孔 6-13。 高压混合桶 6设有喷 淋雾化装置, 该装置是在高压混合桶上盖 6-3下端进水孔 6-1的下方连接喷嘴 6-5 , 喷嘴 6-5外连接喷嘴螺帽 6-6, 喷嘴螺帽 6-6内喷嘴 6-5的下端设有喷水刀口 6-7。 进气口 2通过高压管连接第一级高压混合桶 4的进气孔 4-2,第一级高压混合桶 4的 出水孔 4-13通过高压管连接第二级高压混合桶 6的进气孔 6-2, 第二级高压混合桶 6的出水孔 6-13通过高压管连接第三级高压混合桶 8的进气孔 8-2, 第三级高压混 合桶 8的出水孔 8-13通过高压管连接第一级气水分离装置 9的进水口, 第一级气水 分离装置 9的出水口连接第二级气水分离装置 10的进水口, 第二级气水分离装置 10的出水口通过出水电磁阀 11、 压力调节阀 12连接出水口 13。 第一级和第二级 气水分离装置的出气口连接还原装置 14, 还原装置 14连接排气口 15。 Embodiment: A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water (see FIG. 1 to FIG. 4), which has a water inlet 1, and a water inlet 1 is respectively connected to at least two high-pressure mixing barrels, and the number of high-pressure mixing barrels can be The number of the high-pressure mixing barrels in the embodiment is three, that is, the first-stage high-pressure mixing barrel 4, the second-stage high-pressure mixing barrel 6, and the third-stage high-pressure mixing barrel 8, and the water inlet 1 passes through the first stage. The water solenoid valve 3 is connected to the water inlet hole 4-1 of the first stage high pressure mixing drum 4, and the water inlet port 1 is connected to the water inlet hole 6-1 of the second stage high pressure mixing barrel 6 through the second stage water inlet solenoid valve 5. The water inlet 1 is connected to the water inlet hole 8.1 of the third stage high pressure mixing tank 8 through the third stage water inlet solenoid valve 7, the first stage high pressure mixing barrel 4, the second stage high pressure mixing barrel 6 and the third stage high pressure mixing. The structure of the barrel 8 is basically the same. The structure of the high pressure mixing barrel 8 is exemplified below: The third stage high pressure mixing barrel 8 has a barrel 8-10, and the upper and lower ends of the barrel 8-10 are respectively connected by a bolt 8-12. The mixing tank upper cover 8-3, the high pressure mixing barrel lower cover 8-11, and sealed by the 0 type sealing jaw 8-4. The water inlet hole 8-1 and the air inlet hole 8-2 are respectively disposed on the end faces of the high pressure mixing barrel upper cover 8-3, and the water outlet holes 8-13 are arranged on the high pressure mixing barrel lower cover 8-11. The high pressure mixing tank 8 is provided with a spray atomizing device (see Fig. 3), which is connected to the nozzle 8-5 below the water inlet hole 8-1 at the lower end of the high pressure mixing barrel upper cover 8-3, and the nozzle 8-5 is connected externally. The nozzle nut 8-6, the lower end of the nozzle 8-5 in the nozzle nut 8-6 is provided with a water jet edge 8-7. The inner stage of the first stage high pressure mixing tank 8 is provided with a high pressure mixing barrel grid 8-9, a gas water separating net 8-8 is installed on the grid, and the gas water separating net 8-8 uses a microporous titanium of 100 mesh or more. Made of mesh or other ozone resistant mesh material. These two parts are not present in the first stage high pressure mixing tank 4 and the second stage high pressure mixing tank 6. Similarly, the first stage high pressure mixing drum 4 has a barrel body 4-10, and the upper and lower ends of the barrel body 4-10 are respectively connected by a bolt 4-12 to the high pressure mixing barrel upper cover 4-3 and the high pressure mixing barrel lower cover 4-11, and Sealed by type 0 4-4 sealed. The water inlet hole 4-1 and the air inlet hole 4-2 are respectively disposed on the end faces of the upper cover 4-3 of the high pressure mixing barrel, and the water outlet holes 4-13 are provided on the lower cover 4-11 of the high pressure mixing barrel. The high pressure mixing tank 4 is provided with a spray atomizing device which is connected to the nozzle 4-5 below the water inlet hole 4-1 at the lower end of the high pressure mixing barrel upper cover 4-3, and the nozzle nut 4 is connected outside the nozzle 4-5. 6. The lower end of the nozzle 4-5 in the nozzle nut 4-6 is provided with a water jet edge 4-7. The second stage high pressure mixing barrel 6 has a barrel body 6-10, and the upper and lower ends of the barrel body 6-10 are respectively connected by a bolt 6-12 to a high pressure mixing barrel upper cover 6-3, a high pressure mixing barrel lower cover 6-11, and Type 0 seal 圏 6-4 sealed. The water inlet hole 6-1 and the air inlet hole 6-2 are respectively arranged on the end surface of the upper cover 6-3 of the high pressure mixing barrel, and the water outlet hole 6-13 is arranged on the lower cover 6-11 of the high pressure mixing barrel. The high-pressure mixing tank 6 is provided with a spray atomizing device, which is connected to the nozzle 6-5 below the water inlet hole 6-1 at the lower end of the high-pressure mixing barrel upper cover 6-3, and the nozzle nut 6- is connected outside the nozzle 6-5. 6. The lower end of the nozzle 6-5 in the nozzle nut 6-6 is provided with a water jet edge 6-7. The air inlet 2 is connected to the air inlet hole 4-2 of the first stage high pressure mixing drum 4 through a high pressure pipe, and the water outlet hole 4-13 of the first stage high pressure mixing barrel 4 is connected to the air inlet of the second stage high pressure mixing barrel 6 through a high pressure pipe. The hole 6-2, the water outlet hole 6-13 of the second stage high pressure mixing barrel 6 is connected to the air inlet hole 8-2 of the third stage high pressure mixing barrel 8 through the high pressure pipe, and the water outlet hole 8-13 of the third stage high pressure mixing barrel 8 The water inlet of the first-stage gas-water separation device 9 is connected to the water inlet of the first-stage gas-water separation device 9 through a high-pressure pipe, and the water outlet of the second-stage gas-water separation device 10 is connected to the water inlet of the second-stage gas-water separation device 10 The nozzle is connected to the water outlet 13 through the water discharge solenoid valve 11 and the pressure regulating valve 12. The air outlets of the first and second stage gas-water separation devices are connected to the reduction device 14, and the reduction device 14 is connected to the exhaust port 15.
[18] 使用吋, 当第一级进水电磁阀 3开启, 压力为 1.5~9.0kg/cm2的自来水从进水口 1 经过第一级进水电磁阀 3进入第一级混合桶 4, 水从高压混合桶上盖 4-3上的进水 孔 4-1流入, 经过喷嘴螺帽 4-6内的喷嘴 4-5能使水流喷淋并有效雾化, 形成极易 与臭氧气溶合的水雾, 流量由喷水刀口 4-7上的小孔调整。 压力为 0.35~9.0kg/cm2 的高压臭氧气经过进气口 2进入第一级混合桶 4, 臭氧气从高压混合桶上盖 4-3上 的进气孔 4-2进入, 与水雾相遇, 气水溶合成臭氧水, 此吋在桶内进行第一级高 压混合。 臭氧水和部分未溶于水的臭氧气一起流过高压混合桶下盖 4-11上的出水 孔 4-13, 通过高压连接管和第二个高压混合桶上盖 6-3上的进气孔 6-2进入第二级 高压混合桶 6-10, 同吋第二级进水电磁阀 5开启, 自来水进入第二级混合桶 6, 水 从第二级高压混合桶 6-10上的高压混合桶上盖 6-3上的进水孔 6-1流入, 臭氧水携 带的未溶于水的臭氧气在第二级高压混合桶 6-10内与喷嘴 6-5喷淋雾化的水雾进 行第二级混合, 将未溶于水的臭氧气混合成臭氧水, 经过二级高压混合能有效 的提高混合效率, 但还有少量臭氧气未溶于水, 臭氧水携带少量臭氧气一起流 过高压混合桶下盖 6-11上的出水孔 6-13, 从第三级高压混合桶上盖 8-3上的进气 口 8-2流入到第三级高压混合桶 8-10, 同吋第三级进水电磁阀 7开启, 自来水进入 第三级混合桶 8, 水从第三级高压混合桶 8-10上的高压混合桶上盖 8-3上的进水孔 8-1流入, 在第三级高压混合桶 8-10内进行第三级混合。 第三级高压混合桶 8-10 内装有气水分离网 8-8。 气水分离网 8-8 (参见图 4) 由 100目或 100目以上的微孔 钛板网或其他耐臭氧的网状材质制成。 当臭氧水携带臭氧气泡流经第三级混合 桶 8内的气水分离网 8-8吋, 臭氧水中夹带的臭氧气泡被打散成许多微气泡, 微气 泡浮起, 与喷入混合桶内的水雾再溶合为臭氧水, 避免了臭氧气泡被臭氧水带 走, 更进一步提高了臭氧气和水的混合效率, 臭氧水携带少量臭氧气一起流过 高压混合桶下盖 8-11上的出水孔 8-13进入气水分离装置。 多级高压混合装置内部 的压力是由喷水刀口 4-7、 6-7、 8-7和压力调节阀 11调整到 0.3~7.0kg/cm2, 以满 足高效混合的需求。 如果三级混合桶的混合效率未达到理想效果, 还可以另外 增加混合桶的数量以增加混合的次数, 如第 4级混合桶、 第 5级混合桶 ......, 来 达到更高的需求。 依次经过多级混合, 还有极少量的臭氧气混在臭氧水中流经 第一级气水分离装置 9和第二级气水分离装置 10吋, 臭氧水和未溶于水的臭氧气 分离。 压力为 0.3~7.0kg/cm2的高压臭氧水经过出水电磁阀 11、 压力调节阀 12从 出水口 13流出。 臭氧气经还原装置 14还原成氧气从排气口 15排出。 [18] Using 吋, when the first stage water inlet solenoid valve 3 is opened, tap water with a pressure of 1.5 to 9.0 kg/cm2 is fed from the water inlet 1 through the first stage water inlet solenoid valve 3 into the first stage mixing tank 4, water from The water inlet hole 4-1 on the upper cover 4-3 of the high pressure mixing tank flows in, and the nozzle 4-5 in the nozzle nut 4-6 enables the water to spray and effectively atomize, forming an extremely easy to be dissolved with ozone gas. Water mist, the flow rate is adjusted by the small hole in the water jet knife edge 4-7. The high-pressure ozone gas with a pressure of 0.35~9.0kg/cm2 enters the first-stage mixing tank 4 through the air inlet 2, and the ozone gas enters from the air inlet hole 4-2 on the upper cover 4-3 of the high-pressure mixing barrel, and meets the water mist. The gas and water are dissolved in the ozone water, and the crucible is subjected to the first stage high pressure mixing in the barrel. Ozone water and part of the water-insoluble ozone gas flow together through the water outlet holes 4-13 on the lower lid of the high-pressure mixing tank 4-11, through the high-pressure connecting pipe and the intake air on the upper cover 6-3 of the second high-pressure mixing barrel The hole 6-2 enters the second stage high pressure mixing barrel 6-10, the second stage water inlet solenoid valve 5 is opened, the tap water enters the second stage mixing barrel 6, and the water is pressurized from the second stage high pressure mixing barrel 6-10. The water inlet hole 6-1 on the mixing tank upper cover 6-3 flows in, and the water-insoluble ozone gas carried by the ozone water sprays the atomized water in the second-stage high-pressure mixing barrel 6-10 with the nozzle 6-5. The mist is mixed in the second stage, and the ozone gas which is not dissolved in water is mixed into ozone water, which can be effectively treated by the two-stage high pressure mixing. Improve the mixing efficiency, but there is still a small amount of ozone gas which is not soluble in water. Ozone water carries a small amount of ozone gas together and flows through the water outlet hole 6-13 on the lower cover 6-11 of the high pressure mixing tank, and is covered from the third stage high pressure mixing barrel. The air inlet 8-2 on the 8-3 flows into the third stage high pressure mixing barrel 8-10, and the third stage water inlet solenoid valve 7 is opened, the tap water enters the third stage mixing barrel 8, and the water is discharged from the third stage high pressure. The water inlet hole 8-1 on the upper lid 8-3 of the high pressure mixing tank on the mixing tank 8-10 flows in, and the third stage mixing is performed in the third stage high pressure mixing tank 8-10. The third-stage high-pressure mixing tank 8-10 is equipped with a gas-water separation net 8-8. The gas-water separation net 8-8 (see Fig. 4) is made of a 100-mesh or 100-mesh microporous titanium mesh or other ozone-resistant mesh material. When the ozone water carries the ozone bubbles flowing through the gas-water separation net 8-8 in the third-stage mixing tank 8, the ozone bubbles entrained in the ozone water are broken up into a plurality of micro-bubbles, and the micro-bubbles float and are sprayed into the mixing barrel. The water mist is then dissolved into ozone water, which avoids the ozone bubbles being carried away by the ozone water, further improving the mixing efficiency of ozone gas and water. The ozone water carries a small amount of ozone gas together and flows through the high pressure mixing barrel under the cover 8-11. The water outlet holes 8-13 enter the gas water separation device. The pressure inside the multistage high pressure mixing device is adjusted to 0.3 to 7.0 kg/cm2 by the water jet blades 4-7, 6-7, 8-7 and the pressure regulating valve 11 to meet the demand for efficient mixing. If the mixing efficiency of the three-stage mixing tank does not achieve the desired effect, the number of mixing barrels can be additionally increased to increase the number of mixing, such as the fourth-stage mixing barrel, the fifth-stage mixing barrel, etc., to achieve higher Demand. After multiple stages of mixing, a very small amount of ozone gas is mixed in the ozone water to flow through the first-stage gas-water separation device 9 and the second-stage gas-water separation device 10, and the ozone water and the water-insoluble ozone gas are separated. The high-pressure ozone water having a pressure of 0.3 to 7.0 kg/cm2 flows out of the water outlet 13 through the water discharge solenoid valve 11 and the pressure regulating valve 12. The ozone gas is reduced to oxygen by the reduction device 14 and is discharged from the exhaust port 15.

Claims

权利要求书 Claim
[1] 1.一种制造高压力臭氧水的多级高压混合装置, 它具有进水口 (1) , 其特 征在于进水口 (1) 分别连接至少两级高压混合桶, 每级高压混合桶均设有 进水孔、 出水孔及进气孔, 进水口 (1) 与高压混合桶的进水孔之间设有进 水电磁阀, 进气口 (2) 通过高压管与第一级高压混合桶的进气孔相连, 前一级高压混合桶的出水孔通过高压管连接下一级高压混合桶的进气孔, 最后一级高压混合桶的出水孔通过高压管连接第一级气水分离装置 (9) , 每级高压混合桶均设有与进水孔相连的喷淋雾化装置, 最后一级高压混合 桶的内部设有高压混合桶网架 (8-9) , 高压混合桶网架 (8-9) 上设有气 水分离网 (8-8) ,第一级气水分离装置 (9) 的出水口连接第二级气水分离 装置 (10) 的进水口, 第二级气水分离装置 (10) 的出水口通过出水电磁 阀 (11) 、 压力调节阀 (12) 连接出水口 (13) , 第一级气水分离装置 (9 ) 和第二级气水分离装置 (10) 的出气口连接还原装置 (14) , 还原装置 (14) 连接排气口 (15) 。  [1] 1. A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water, which has a water inlet (1), characterized in that the water inlet (1) is respectively connected to at least two stages of high-pressure mixing barrels, and each stage of high-pressure mixing barrels is There is a water inlet hole, a water outlet hole and an air inlet hole, and a water inlet solenoid valve is arranged between the water inlet (1) and the water inlet hole of the high pressure mixing barrel, and the air inlet port (2) is mixed with the first stage high pressure through the high pressure tube. The air inlet holes of the barrel are connected, and the water outlet hole of the high-pressure mixing barrel of the first stage is connected to the air inlet hole of the lower-stage high-pressure mixing barrel through the high-pressure pipe, and the water outlet hole of the first-stage high-pressure mixing barrel is connected to the first-stage gas-water separation through the high-pressure pipe. The device (9) has a spray atomizing device connected to the water inlet hole in each high-pressure mixing barrel, and a high-pressure mixing barrel net (8-9) is arranged inside the high-pressure mixing barrel of the first stage, and the high-pressure mixing barrel net A gas-water separation network (8-8) is arranged on the frame (8-9), and the water outlet of the first-stage gas-water separation device (9) is connected to the water inlet of the second-stage gas-water separation device (10), the second stage The water outlet of the gas-water separation device (10) passes through the water discharge solenoid valve (11), pressure The regulating valve (12) is connected to the water outlet (13), the first-stage gas-water separation device (9) and the second-stage gas-water separation device (10) are connected to the outlet device (14), and the reducing device (14) is connected to the row. Air port (15).
[2] 2.根据权利要求 1所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的每级高压混合桶均具有桶体, 桶体的上、 下端分别连接高压 混合桶上盖、 高压混合桶下盖, 高压混合桶的进水孔、 进气孔设在高压混 合桶上盖上,高压混合桶的出水孔设在高压混合桶下盖上。  [2] 2. A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water according to claim 1, wherein each of the high-pressure mixing barrels has a barrel body, and the upper and lower ends of the barrel are respectively connected. The upper cover of the high-pressure mixing barrel and the lower cover of the high-pressure mixing barrel, the water inlet hole and the air inlet hole of the high-pressure mixing barrel are disposed on the upper cover of the high-pressure mixing barrel, and the water outlet hole of the high-pressure mixing barrel is disposed on the lower cover of the high-pressure mixing barrel.
[3] 3.根据权利要求 1所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的喷淋雾化装置是在高压混合桶上盖下端进水孔的下方连接喷 嘴, 喷嘴外连接喷嘴螺帽, 喷嘴螺帽内喷嘴的下端设有喷水刀口。  [3] 3. A multistage high pressure mixing device for manufacturing high pressure ozone water according to claim 1, wherein said spray atomizing device is below the water inlet hole of the lower end of the high pressure mixing barrel. The nozzle is connected, and the nozzle nut is connected outside the nozzle, and the lower end of the nozzle in the nozzle nut is provided with a water jet knife edge.
[4] 4.根据权利要求 2所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的桶体与高压混合桶上盖、 高压混合桶下盖之间由 0型密封圏 密封。  [4] 4. A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water according to claim 2, wherein the barrel is separated from the upper lid of the high-pressure mixing barrel and the lower lid of the high-pressure mixing barrel. Sealed seal.
[5] 5.根据权利要求 1所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的高压混合桶为 2 - 10级, 即高压混合桶的数量为 2 - 10个。  [5] 5. A multi-stage high-pressure mixing device for manufacturing high-pressure ozone water according to claim 1, wherein said high-pressure mixing barrel is 2 - 10, that is, the number of high-pressure mixing barrels is 2 - 10.
[6] 6.根据权利要求 1所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的气水分离网用耐臭氧的网状材质制成。 [6] 6. A multistage high pressure mixing device for producing high pressure ozone water according to claim 1, wherein said gas water separation mesh is made of an ozone resistant mesh material.
7.根据权利要求 6所述的一种制造高压力臭氧水的多级高压混合装置, 其特 征在于所述的气水分离网 (8-8) 用 100目或 100目以上的微孔钛板网或耐臭 氧的网状材质制成。 The multi-stage high-pressure mixing device for manufacturing high-pressure ozone water according to claim 6, characterized in that the gas-water separation net (8-8) is made of a microporous titanium plate of 100 mesh or more. Made of mesh or ozone resistant mesh material.
PCT/CN2008/072968 2008-09-22 2008-11-06 An apparatus for making high pressure ozonated water WO2010031227A1 (en)

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