CN105439098A - Ozone water machine using raw material water for cooling - Google Patents
Ozone water machine using raw material water for cooling Download PDFInfo
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- CN105439098A CN105439098A CN201510904082.7A CN201510904082A CN105439098A CN 105439098 A CN105439098 A CN 105439098A CN 201510904082 A CN201510904082 A CN 201510904082A CN 105439098 A CN105439098 A CN 105439098A
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/10—Preparation of ozone
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
The invention discloses an ozone water machine using raw material water for cooling. The ozone water machine comprises an oxygen feed system, a water-cooled ozone generation pipe, a gas-liquid mixing pump and an ozone dissolving device. An oxygen output opening of the oxygen feed system is communicated with an oxygen inlet of the water-cooled ozone generation pipe, and a water inlet of the gas-liquid mixing pump is communicated with a raw material water source used for preparing ozone water. The ozone water machine further comprises a backwater preventing device and a flow dividing pipeline, an ozone outlet of the water-cooled ozone generation pipe is communicated with a gas inlet of the backwater preventing device, a gas outlet of the backwater preventing device is communicated with an air suction port of the gas-liquid mixing pump, a water outlet of the gas-liquid mixing pump is divided into two paths through the flow dividing pipeline, one path is communicated with a cooling water inlet of the water-cooled ozone generation pipe, the other path is communicated with a water inlet of the ozone dissolving device, and a cooling water outlet of the water-cooled ozone generation pipe is communicated with a water inlet of the ozone dissolving device. The produced ozone water is high and stable in yield and stable in concentration, the efficiency is high, and the ozone water machine has the advantages of saving energy, being environmentally friendly, low in cost and small in installing space.
Description
Technical field
The present invention relates to one and utilize the water-cooled ozone water apparatus of raw material.
Background technology
Ozone water has extremely strong oxidisability, and it has wide range of applications, and is broad-spectrum bactericide disinfectant, can kill the bacteriophage of body surface, removes fruit-vegetable pesticide residues, and non-secondary pollution.Ozone water is prepared from by being dissolved in raw water by the ozone gas of ozone generating pipe output in production scene, therefore the efficiency of ozone generating pipe output ozone gas is the important restriction factor of ozone water preparation efficiency, the efficiency of ozone generating pipe output ozone gas then with ozone generating pipe temperature negative correlation operationally, namely when ozone generating pipe is operated in specified temperature range, its ozone output efficiency can reach the highest, when ozone generating pipe is operated in higher than rated temperature range, its ozone output efficiency then can reduce along with the rising of temperature.
As shown in Figure 1, application number is in the Chinese invention patent application " ozone water generating device " of 200810081791.X, the type of cooling that ozone generating pipe 2 adopts is the conventional ozone generating pipe type of cooling in the ozone water preparation of prior art, that is: the ozone gas of ozone generating pipe 2 output is tentatively mixed in rear input ozone dissolver 4 by ejector 7 and raw water and mixes further, ozone generating pipe 2 is then by independent of aforementioned ozone water, the liquid circulation loop of preparing outside loop cools, this liquid circulation loop comprises the cooling fluid containing box 5 storing cooling fluid, for the heat exchanger 8 of lowering the temperature to cooling fluid and the water circulating pump driving cooling fluid to circulate between liquid circulation loop and the cooling line of ozone generating pipe 2.The ozone generating pipe type of cooling of this application has the following disadvantages: the first, and the cost using cooling fluid, water circulating pump, heat exchanger to carry out cooling is higher; The second, cooling fluid containing box 5 is set and takes up room greatly.
In prior art, also has the ozone generating pipe type of cooling being reduced ozone water production cost by the cooling fluid using common water coolant to carry out alternative above-mentioned application, but the type of cooling has the following disadvantages equally like this: first, because water coolant works in circulation in the cooling water circulation pipeline closed, and the cooling means of water coolant are difficult to reach the cooling-down effect to cooling fluid, after the ozone generating pipe continuous firing long period, water coolant is serious by temperature rise; And if the mode passing through to introduce cooling water source constantly changes the water coolant in cooling water circulation pipeline, then there is the problem that water resource waste is serious, cost improves; The second, this type of cooling needs to arrange cooling fluid containing box equally, there is the large problem that takes up room.
Summary of the invention
Technical problem to be solved by this invention is: provide one to utilize the water-cooled ozone water apparatus of raw material.
Solve the problems of the technologies described above, the technical solution adopted in the present invention is as follows:
One utilizes the water-cooled ozone water apparatus of raw material, comprise oxygen plenum system, water-cooled ozone-generator tube, gas-liquid mixing pump and ozone dissolver, the oxygen delivery port of described oxygen plenum system is communicated with the oxygen inlet mouth of described water-cooled ozone-generator tube, the water-in of described gas-liquid mixing pump is communicated with the raw material water source for the preparation of ozone water, the ozone of input and raw water can be prepared into preliminary mixing ozone water and export by described gas-liquid mixing pump, the preliminary mixing ozone water of input can be prepared into the ozone water reaching predetermined concentration by described ozone dissolver, it is characterized in that: described ozone water apparatus also comprises anti-water recovery apparatus and distribution pipeline, wherein, described anti-water recovery apparatus is provided with inlet mouth, air outlet and overflow port, the gas inputted from inlet mouth can be exported by air outlet and be discharged by overflow port by the liquid blowed back into from air outlet by described anti-water recovery apparatus, the ozone outlet of described water-cooled ozone-generator tube is communicated with the inlet mouth of described anti-water recovery apparatus, the air outlet of described anti-water recovery apparatus is communicated with the suction opening of described gas-liquid mixing pump, the water outlet of described gas-liquid mixing pump is divided into two-way by described distribution pipeline, one tunnel is communicated with the entrance of cooling water of described water-cooled ozone-generator tube, another road is communicated with the water-in of described ozone dissolver, the cooling water outlet of described water-cooled ozone-generator tube is communicated with the water-in of described ozone dissolver, the ozone water of predetermined concentration is reached described in the water outlet output of described ozone dissolver.
The principle of work of above-mentioned ozone water apparatus is:
The oxygen that oxygen plenum system exports is prepared into ozone gas and exports by water-cooled ozone-generator tube, gas-liquid mixing pump extracts the raw water that raw material water source provides, the ozone gas utilizing the negative pressure pressure produced during its work to be exported by anti-water recovery apparatus suction water-cooled ozone-generator tube on the other hand on the one hand, and this ozone gas and raw water mix and blend are become preliminary mixing ozone water, this tentatively mixes ozone water and is sprayed at a high speed by the water outlet of gas-liquid mixing pump and be divided into two-way by distribution pipeline, the first via is by flowing into ozone dissolver again after the cooling line of water-cooled ozone-generator tube, second tunnel then flows directly into ozone dissolver, conflux in ozone dissolver outside or inside with the preliminary ozone water that mixes on the second tunnel after the heat produced when making the preliminary mixing ozone water of the first via take away rapidly water-cooled ozone-generator tube work, the preliminary mixing ozone water of ozone dissolver to input carries out secondary mixing, export after making tentatively to mix the concentration that ozone water can reach predetermined, and, raw water that gas-liquid mixing pump is refluxed to anti-water recovery apparatus air outlet by suction opening when quitting work (this backflow is produced by the moment positive pressure of gas-liquid mixing pump when quitting work) can be discharged by the overflow port of anti-water recovery apparatus, and avoids raw water to be back in the gas circuit of water-cooled ozone-generator tube causing damage to it.
In order to the stable raw water for the preparation of ozone water supplies, as a modification of the present invention, described ozone water apparatus also comprises the water tank for storing described raw water; The water-in of described gas-liquid mixing pump is by the raw material water source of water tank connection for the preparation of ozone water.
In order to avoid ozone water apparatus supplies lower than continuous firing when preassigned at raw water, as a modification of the present invention, described ozone water apparatus also comprises anhydrous protector; The water-in of described gas-liquid mixing pump to be communicated with the raw material water source for the preparation of ozone water by anhydrous protector successively with described water tank; namely the water-in of described anhydrous protector is communicated with the water outlet of described water tank; described anhydrous protector is provided with lowest water level, and it can at the raw water water level flow through lower than turning off the path that raw water flows through anhydrous protector during described lowest water level.
As one embodiment of the present invention, described oxygen plenum system comprises freezing type drier, air compressor, condenser and oxygenerator; Described cooling driers, air compressor, condenser are connected successively with oxygenerator, and the air outlet of described oxygenerator is the oxygen delivery port of described oxygen plenum system.
Concentrate for the ease of operator and manipulate ozone water apparatus, as one embodiment of the present invention, described ozone water apparatus also comprises the control circuit board for controlling ozone water apparatus work; Described control circuit board is electrically connected with the control end of described freezing type drier, air compressor, condenser, oxygenerator, water-cooled ozone-generator tube, gas-liquid mixing pump and anhydrous protector respectively.
In order to reduce the space taken needed for ozone water apparatus further, as a kind of preferred implementation of the present invention, described ozone water apparatus also comprises vertical chassis, described vertical chassis is provided with upper and lower two sheaf spaces, described air compressor, condenser, oxygenerator, water-cooled ozone-generator tube, anti-water recovery apparatus and control circuit board are installed in the upper sheaf space of described vertical chassis, wherein, described control circuit board is arranged on the left part forward position of described upper sheaf space, described air compressor and condenser are all arranged on the left part rearward position of described upper sheaf space, and condenser is positioned at the top position of air compressor, described water-cooled ozone-generator tube is arranged on the right part position of described upper sheaf space, described anti-water recovery apparatus and oxygenerator are separately positioned on middle part forward position and the middle part rearward position of described upper sheaf space, described freezing type drier, gas-liquid mixing pump, anhydrous protector and ozone dissolver are installed in the lower layer space of described vertical chassis, wherein, described freezing type drier and gas-liquid mixing pump are arranged on the left part position of described lower layer space, described freezing type drier is positioned at the top position of gas-liquid mixing pump, described anhydrous protector and ozone dissolver are arranged on the right part position of described lower layer space, and described anhydrous protector is positioned at the anterior position of ozone dissolver, the water-in of the overflow port of described anti-water recovery apparatus, the water outlet of ozone dissolver, anhydrous protector, the condensate drain outlet of freezing type drier all expose at the right tank wall lower position of described vertical chassis, described water tank is arranged on the outside of vertical chassis.
Preliminary mixing ozone water water flow in order to ensure the cooling line flowing through water-cooled ozone-generator tube can reach and enable water-cooled ozone-generator tube keep more than the minimum cooling water flow of stabilized operating temperature scope, as one embodiment of the present invention, described ozone dissolver is provided with the first water-in and the second water-in, described distribution pipeline comprises the first Y-junction, described first Y-junction has the straight-through water-in that caliber adapts to the water outlet of described gas-liquid mixing pump, caliber adapts to the bypass water outlet that the straight-through water outlet mouth of the entrance of cooling water of described water-cooled ozone-generator tube and caliber adapt to the first water-in of described ozone dissolver, the entrance of cooling water that the straight-through water-in of described first Y-junction is communicated with the water outlet of described gas-liquid mixing pump, straight-through water outlet mouth is communicated with described water-cooled ozone-generator tube, bypass water outlet are communicated with the first water-in of described ozone dissolver, and the cooling water outlet of described water-cooled ozone-generator tube is communicated with the second water-in of described ozone dissolver.
As a kind of preferred implementation of the present invention, described distribution pipeline also comprises first flow variable valve; The straight-through water outlet mouth of described first Y-junction is communicated with the entrance of cooling water of described water-cooled ozone-generator tube by first flow variable valve.
In order to the preliminary mixing ozone water water flow in the cooling line of water-cooled ozone-generator tube can be regulated, as one embodiment of the present invention, described ozone dissolver is provided with the first water-in and the second water-in, described distribution pipeline comprises the second Y-junction and second adjustable valve, described second Y-junction has the straight-through water-in that caliber adapts to the water outlet of described gas-liquid mixing pump, caliber adapt to the first water-in of described ozone dissolver straight-through water outlet mouth and caliber adapt to the bypass water outlet of the entrance of cooling water of described water-cooled ozone-generator tube, the straight-through water-in of described first Y-junction is communicated with the water outlet of described gas-liquid mixing pump, straight-through water outlet mouth by the entrance of cooling water that second adjustable valve is communicated with the first water-in of described ozone dissolver, bypass water outlet is communicated with described water-cooled ozone-generator tube, and the cooling water outlet of described water-cooled ozone-generator tube is communicated with the second water-in of described ozone dissolver.
In order to be convenient to the ozone water output flow regulating ozone water apparatus, as one embodiment of the present invention, the water outlet of described ozone dissolver is connected with pressure regulator valve.
Compared with prior art, the present invention has following beneficial effect:
First, the present invention utilizes gas-liquid mixing pump ozone gas and raw water to be prepared into tentatively mix ozone water and this is tentatively mixed ozone water high speed and sprays, make the cooling line of leading up to ozone generating pipe in the preliminary mixing ozone water current of at a high speed ejection, thus the heat produced when taking away ozone generating pipe work fast, that guarantees that ozone generating pipe can continue is operated in specified temperature range and keeps high-level efficiency, the ozone gas output of high stability, and, preliminary mixing ozone water after lowering the temperature to ozone generating pipe can also be input to the ozone water being prepared into further in ozone dissolver and reaching predetermined concentration, thus avoid the waste of water resources,
What gas-liquid mixing pump exported is then directly inputted to except for the preliminary mixing ozone water current except cooling the ozone water being prepared into further in ozone dissolver and reaching predetermined concentration to ozone generating pipe, ozone generating pipe cooling water flow is avoided to limit the bottleneck becoming ozone water apparatus output ozone water, and, because the preliminary mixing ozone water heated up by ozone generating pipe cooling line is mixed with the preliminary ozone water that mixes directly entered in ozone dissolver, the ozone water that ozone dissolver is prepared into is very little relative to the temperature rise of raw water;
In addition, the present invention is without the need to independently arranging cooling water tank and being communicated with cooling water source, only need to be communicated with raw material water source and can meet the supply of preparation ozone water raw water and the supply of ozone generating pipe water coolant, reduce and space needed for ozone water apparatus is installed and the cost reducing ozone water apparatus, and, only needing, gas-liquid mixing pump is set and can drive ozone, raw water, the flowing of preliminary mixing ozone water in respective gas circuit and water route, save and water circulating pump is set, provide cost savings further and space, and make the installation of ozone water apparatus more easy;
Therefore, the output of ozone water apparatus output ozone water of the present invention is high, efficiency is high, concentration stabilize, stable yield, and, there is energy-conserving and environment-protective, cost is low, installing space is little advantage.
Second, the present invention can improve the stability of raw water supply by setting up water tank, to exist because of the hydraulic pressure of water supply pipe, instability of flow and easily cause the phenomenons that get muddled such as pump working output pressure, flow, mixed effect to make the problem of ozone water apparatus cisco unity malfunction to solve using water supply pipe as raw material water source.
3rd, the present invention can avoid ozone water apparatus to supply lower than continuous firing when preassigned at raw water by setting up anhydrous protector, adds the job security of ozone water apparatus.
4th; air compressor, condenser, oxygenerator, water-cooled ozone-generator tube, anti-water recovery apparatus, control circuit board, freezing type drier, gas-liquid mixing pump, anhydrous protector and ozone dissolver are arranged in the levels space of vertical chassis by the present invention respectively; and the volume minimization of ozone water apparatus is made by rational spatial arrangement, reduce the space taken needed for ozone water apparatus further.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is described in further detail:
Fig. 1 is the system chart of ozone water generating device of the prior art;
Fig. 2 is the system chart of the ozone water apparatus of the embodiment of the present invention one;
Fig. 3 is the front view of vertical chassis in the embodiment of the present invention one;
Fig. 4 is the rear view of vertical chassis in the embodiment of the present invention one;
Fig. 5 is the left view of vertical chassis in the embodiment of the present invention one;
Fig. 6 is the right view of vertical chassis in the embodiment of the present invention one;
Fig. 7 is that the master of the ozone water apparatus of the embodiment of the present invention one looks internal structure schematic diagram;
Fig. 8 is the backsight internal structure schematic diagram of the ozone water apparatus of the embodiment of the present invention one;
Fig. 9 is the system chart of the ozone water apparatus of the embodiment of the present invention two.
Embodiment
Embodiment one
As shown in Fig. 2 to Fig. 8, the ozone water apparatus of the embodiment of the present invention one, comprise oxygen plenum system, water-cooled ozone-generator tube 4, anti-water recovery apparatus 5, gas-liquid mixing pump 6, for the water tank 7 of storage of raw materials water, anhydrous protector 8, distribution pipeline, ozone dissolver 10, for controlling control circuit board 12 and the vertical chassis 13 of ozone water apparatus work, wherein, anti-water recovery apparatus 5 is provided with inlet mouth, air outlet and overflow port 5a, the gas inputted from inlet mouth can be exported by air outlet and be discharged by overflow port by the liquid blowed back into from air outlet by anti-water recovery apparatus 5, ozone dissolver 10 is provided with the first water-in and the second water-in.
Above-mentioned oxygen plenum system comprises freezing type drier 1, air compressor 2a, condenser 2b and oxygenerator 3; Cooling driers 1, air compressor 2a, condenser 2b are connected successively with oxygenerator 3, and the air outlet of oxygenerator 3 is the oxygen delivery port of oxygen plenum system.The oxygen delivery port of oxygen plenum system is communicated with the oxygen inlet mouth of water-cooled ozone-generator tube 4, and the oxygen making water-cooled ozone-generator tube 4 that oxygen plenum system can be utilized to input prepares ozone; The ozone outlet of water-cooled ozone-generator tube 4 is communicated with the inlet mouth of anti-water recovery apparatus 5, and the air outlet of anti-water recovery apparatus 5 is communicated with the suction opening of gas-liquid mixing pump 6.
The water-in of gas-liquid mixing pump 6 to be communicated with the raw material water source for the preparation of ozone water by anhydrous protector 8 successively with water tank 7; namely the water-in of water tank 7 is communicated with raw material water source, the water outlet of water-in 8a joining water box 7 of anhydrous protector 8, the water-in of water outlet connection gas-liquid mixing pump 6; wherein; anhydrous protector 8 is provided with lowest water level, and it can at the raw water water level flow through lower than turning off the path that raw water flows through anhydrous protector 8 during lowest water level.
The ozone inputted by suction opening and the raw water inputted by water-in can be prepared into preliminary mixing ozone water and export by above-mentioned gas-liquid mixing pump 6; Above-mentioned distribution pipeline comprises the first Y-junction 9a, and the first Y-junction 9a has the bypass water outlet that caliber adapts to the straight-through water-in of the water outlet of gas-liquid mixing pump 6, caliber adapts to the entrance of cooling water of water-cooled ozone-generator tube 4 straight-through water outlet mouth and caliber adapt to the first water-in of ozone dissolver 10; The straight-through water-in of the first Y-junction 9a is communicated with water outlet, the entrance of cooling water of straight-through water outlet mouth connection water-cooled ozone-generator tube 4, first water-in of bypass water outlet connection ozone dissolver 10 of gas-liquid mixing pump 6, and the cooling water outlet of water-cooled ozone-generator tube 4 is communicated with the second water-in of ozone dissolver 10; Thus make the water outlet of gas-liquid mixing pump 6 be divided into two-way by distribution pipeline, a road is communicated with the entrance of cooling water of water-cooled ozone-generator tube 4, the first water-in of another road connection ozone dissolver 10.
The cooling water outlet of above-mentioned water-cooled ozone-generator tube 4 is communicated with the second water-in of ozone dissolver 10, the preliminary mixing ozone water inputted by the first and second water-ins can be prepared into the ozone water reaching predetermined concentration by ozone dissolver 10, and the water outlet 10a of ozone dissolver 10 exports the ozone water that this reaches predetermined concentration; The water outlet 10a of ozone dissolver 10 is connected with pressure regulator valve 11, thus controls the output flow of ozone water.
Above-mentioned control circuit board 12 is electrically connected with the control end of freezing type drier 1, air compressor 2a, condenser 2b, oxygenerator 3, water-cooled ozone-generator tube 4, gas-liquid mixing pump 6 and anhydrous protector 8 respectively; thus user can easily by this running of control circuit board 12 centralized Control.
Above-mentioned vertical chassis 13 is provided with upper and lower two sheaf spaces, air compressor 2a, condenser 2b, oxygenerator 3, water-cooled ozone-generator tube 4, anti-water recovery apparatus 5 and control circuit board 12 are installed in the upper sheaf space of vertical chassis 13, wherein, control circuit board 12 is arranged on the left part forward position of sheaf space, air compressor 2a and condenser 2b is all arranged on the left part rearward position of sheaf space, and condenser 2b is positioned at the top position of air compressor 2a, water-cooled ozone-generator tube 4 is arranged on the right part position of sheaf space, anti-water recovery apparatus 5 and oxygenerator 3 are separately positioned on middle part forward position and the middle part rearward position of sheaf space, freezing type drier 1, gas-liquid mixing pump 6, anhydrous protector 8 and ozone dissolver 10 are installed in the lower layer space of vertical chassis 13, wherein, freezing type drier 1 and gas-liquid mixing pump 6 are arranged on the left part position of lower layer space, freezing type drier 1 is positioned at the top position of gas-liquid mixing pump 6, anhydrous protector 8 and ozone dissolver 10 are arranged on the right part position of lower layer space, and anhydrous protector 8 is positioned at the anterior position of ozone dissolver 10, the water-in 8a of the overflow port 5a of anti-water recovery apparatus 5, the water outlet 10a of ozone dissolver 10, anhydrous protector 8, the condensate drain outlet 1a of freezing type drier 1 all expose at the right tank wall lower position of vertical chassis 13, water tank 7 is arranged on the outside of vertical chassis 13.In addition, for the ozone dissolver 10 with ozone tail gas overflow port 10b, its ozone tail gas overflow port 10b also exposes at the right tank wall lower position of vertical chassis 13.
Ozone water apparatus principle of work of the present invention is:
The oxygen that oxygen plenum system exports is prepared into ozone gas and exports by water-cooled ozone-generator tube 4, the raw water that extraction raw material water source, gas-liquid mixing pump 6 one aspect provides, another aspect utilize the negative pressure pressure produced during its work to be sucked the ozone gas of water-cooled ozone-generator tube 4 output by anti-water recovery apparatus 5, and this ozone gas and raw water mix and blend are become preliminary mixing ozone water, this tentatively mixes ozone water and is sprayed at a high speed by the water outlet of gas-liquid mixing pump 6 and be divided into two-way by distribution pipeline, the first via is by flowing into ozone dissolver 10 again after the cooling line of water-cooled ozone-generator tube 4, second tunnel then flows directly into ozone dissolver 10, conflux in ozone dissolver 10 outside or inside with the preliminary ozone water that mixes on the second tunnel after making the preliminary mixing ozone water of the first via take away rapidly the heat produced when water-cooled ozone-generator tube 4 works, the preliminary mixing ozone water of ozone dissolver 10 to input carries out secondary mixing, export after making tentatively to mix the concentration that ozone water can reach predetermined, and, raw water that gas-liquid mixing pump 6 is refluxed to anti-water recovery apparatus 5 air outlet by suction opening when quitting work (this backflow is produced by the moment positive pressure of gas-liquid mixing pump 6 when quitting work) can be discharged by the overflow port of anti-water recovery apparatus 5, and avoids raw water to be back in the gas circuit of water-cooled ozone-generator tube 4 causing damage to it.
In addition, above-mentioned distribution pipeline is communicated with gas-liquid mixing pump 6 and ozone dissolver 10 owing to utilizing the straight-through pipeline connection gas-liquid mixing pump 6 of the first Y-junction 9a with water-cooled ozone-generator tube 4, by-pass line, the preliminary mixing ozone water current that gas-liquid mixing pump 6 is exported preferentially flow in the cooling line of water-cooled ozone-generator tube 4, ensure that in the cooling line of water-cooled ozone-generator tube 4 and have enough current to cool water-cooled ozone-generator tube 4.And when the preliminary mixing ozone water current that gas-liquid mixing pump 6 exports are very large, the load of the cooling line of water-cooled ozone-generator tube 4 is exceeded in order to avoid excessive current, can by setting up first flow variable valve 9b in above-mentioned distribution pipeline, make the straight-through water outlet mouth of the first Y-junction 9a be communicated with the entrance of cooling water of water-cooled ozone-generator tube 4 by first flow variable valve 9b, thus the preliminary mixing ozone water water flow in the cooling line of water-cooled ozone-generator tube 4 can be regulated.
Embodiment two
As shown in Figure 9, the ozone water apparatus of the embodiment of the present invention two is substantially identical with embodiment one, their difference is: in the present embodiment two, ozone dissolver 10 is provided with the first water-in and the second water-in, distribution pipeline comprises the second Y-junction 9c and second adjustable valve 9d, and the straight-through water outlet mouth that the second Y-junction 9c has that caliber adapts to the straight-through water-in of the water outlet of gas-liquid mixing pump 6, caliber adapts to the first water-in of ozone dissolver 10 and caliber adapt to the bypass water outlet of the entrance of cooling water of water-cooled ozone-generator tube 4; The straight-through water-in of the first Y-junction 9a is communicated with water outlet, first water-in of straight-through water outlet mouth by second adjustable valve 9d connection ozone dissolver 10, the entrance of cooling water of bypass water outlet connection water-cooled ozone-generator tube 4 of gas-liquid mixing pump 6, the cooling water outlet of water-cooled ozone-generator tube 4 is communicated with the second water-in of ozone dissolver 10, thus can regulate the preliminary mixing ozone water water flow in the cooling line of water-cooled ozone-generator tube 4.
The present invention is not limited to above-mentioned embodiment; according to foregoing; according to ordinary technical knowledge and the customary means of this area; do not departing under the present invention's above-mentioned basic fundamental thought prerequisite; the present invention can also make the equivalent modifications of other various ways, replacement or change, all drops among protection scope of the present invention.Such as, ozone dissolver 10 also only can have a water-in, and for this situation, the first water-in of above-mentioned ozone dissolver 10 and the second water-in can be formed by connecting tee joint on the water-in of this ozone dissolver 10.
Claims (10)
1. one kind utilizes the water-cooled ozone water apparatus of raw material, comprise oxygen plenum system, water-cooled ozone-generator tube (4), gas-liquid mixing pump (6) and ozone dissolver (10), the oxygen delivery port of described oxygen plenum system is communicated with the oxygen inlet mouth of described water-cooled ozone-generator tube (4), the water-in of described gas-liquid mixing pump (6) is communicated with the raw material water source for the preparation of ozone water, the ozone of input and raw water can be prepared into preliminary mixing ozone water and export by described gas-liquid mixing pump (6), the preliminary mixing ozone water of input can be prepared into the ozone water reaching predetermined concentration by described ozone dissolver (10), it is characterized in that: described ozone water apparatus also comprises anti-water recovery apparatus (5) and distribution pipeline, wherein, described anti-water recovery apparatus (5) is provided with inlet mouth, air outlet and overflow port (5a), the gas inputted from inlet mouth can be exported by air outlet and be discharged by overflow port by the liquid blowed back into from air outlet by described anti-water recovery apparatus (5), the ozone outlet of described water-cooled ozone-generator tube (4) is communicated with the inlet mouth of described anti-water recovery apparatus (5), the air outlet of described anti-water recovery apparatus (5) is communicated with the suction opening of described gas-liquid mixing pump (6), the water outlet of described gas-liquid mixing pump (6) is divided into two-way by described distribution pipeline, one tunnel is communicated with the entrance of cooling water of described water-cooled ozone-generator tube (4), another road is communicated with the water-in of described ozone dissolver (10), the cooling water outlet of described water-cooled ozone-generator tube (4) is communicated with the water-in of described ozone dissolver (10), the ozone water of predetermined concentration is reached described in water outlet (10a) output of described ozone dissolver (10).
2. ozone water apparatus according to claim 1, is characterized in that: described ozone water apparatus also comprises the water tank (7) for storing described raw water; The water-in of described gas-liquid mixing pump (6) is by the raw material water source of water tank (7) connection for the preparation of ozone water.
3. ozone water apparatus according to claim 2, is characterized in that: described ozone water apparatus also comprises anhydrous protector (8); The water-in of described gas-liquid mixing pump (6) to be communicated with the raw material water source for the preparation of ozone water by anhydrous protector (8) successively with described water tank (7); namely the water-in (8a) of described anhydrous protector (8) is communicated with the water outlet of described water tank (7); described anhydrous protector (8) is provided with lowest water level, and it can at the raw water water level flow through lower than turning off the path that raw water flows through anhydrous protector (8) during described lowest water level.
4. ozone water apparatus according to claim 3, is characterized in that: described oxygen plenum system comprises freezing type drier (1), air compressor (2a), condenser (2b) and oxygenerator (3); Described cooling driers (1), air compressor (2a), condenser (2b) are connected successively with oxygenerator (3), and the air outlet of described oxygenerator (3) is the oxygen delivery port of described oxygen plenum system.
5. ozone water apparatus according to claim 4, is characterized in that: described ozone water apparatus also comprises the control circuit board (12) for controlling ozone water apparatus work; Described control circuit board (12) is electrically connected with the control end of described freezing type drier (1), air compressor (2a), condenser (2b), oxygenerator (3), water-cooled ozone-generator tube (4), gas-liquid mixing pump (6) and anhydrous protector (8) respectively.
6. ozone water apparatus according to claim 5, is characterized in that: described ozone water apparatus also comprises vertical chassis (13), described vertical chassis (13) is provided with upper and lower two sheaf spaces, described air compressor (2a), condenser (2b), oxygenerator (3), water-cooled ozone-generator tube (4), anti-water recovery apparatus (5) and control circuit board (12) are installed in the upper sheaf space of described vertical chassis (13), wherein, described control circuit board (12) is arranged on the left part forward position of described upper sheaf space, described air compressor (2a) and condenser (2b) are all arranged on the left part rearward position of described upper sheaf space, and condenser (2b) is positioned at the top position of air compressor (2a), described water-cooled ozone-generator tube (4) is arranged on the right part position of described upper sheaf space, described anti-water recovery apparatus (5) and oxygenerator (3) are separately positioned on middle part forward position and the middle part rearward position of described upper sheaf space, described freezing type drier (1), gas-liquid mixing pump (6), anhydrous protector (8) and ozone dissolver (10) are installed in the lower layer space of described vertical chassis (13), wherein, described freezing type drier (1) and gas-liquid mixing pump (6) are arranged on the left part position of described lower layer space, described freezing type drier (1) is positioned at the top position of gas-liquid mixing pump (6), described anhydrous protector (8) and ozone dissolver (10) are arranged on the right part position of described lower layer space, described anhydrous protector (8) is positioned at the anterior position of ozone dissolver (10), the overflow port (5a) of described anti-water recovery apparatus (5), the water outlet (10a) of ozone dissolver (10), the water-in (8a) of anhydrous protector (8), the condensate drain outlet (1a) of freezing type drier (1) all expose at the right tank wall lower position of described vertical chassis (13), described water tank (7) is arranged on the outside of vertical chassis (13).
7. the ozone water apparatus according to claim 1 to 6 any one, it is characterized in that: described ozone dissolver (10) is provided with the first water-in and the second water-in, described distribution pipeline comprises the first Y-junction (9a), described first Y-junction (9a) has the straight-through water-in that caliber adapts to the water outlet of described gas-liquid mixing pump (6), caliber adapts to the bypass water outlet that the straight-through water outlet mouth of the entrance of cooling water of described water-cooled ozone-generator tube (4) and caliber adapt to the first water-in of described ozone dissolver (10), the entrance of cooling water that the straight-through water-in of described first Y-junction (9a) is communicated with the water outlet of described gas-liquid mixing pump (6), straight-through water outlet mouth is communicated with described water-cooled ozone-generator tube (4), bypass water outlet are communicated with the first water-in of described ozone dissolver (10), and the cooling water outlet of described water-cooled ozone-generator tube (4) is communicated with the second water-in of described ozone dissolver (10).
8. ozone water apparatus according to claim 7, is characterized in that: described distribution pipeline also comprises first flow variable valve (9b); The straight-through water outlet mouth of described first Y-junction (9a) is communicated with the entrance of cooling water of described water-cooled ozone-generator tube (4) by first flow variable valve (9b).
9. the ozone water apparatus according to claim 1 to 6 any one, it is characterized in that: described ozone dissolver (10) is provided with the first water-in and the second water-in, described distribution pipeline comprises the second Y-junction (9c) and second adjustable valve (9d), described second Y-junction (9c) has the straight-through water-in that caliber adapts to the water outlet of described gas-liquid mixing pump (6), caliber adapt to the first water-in of described ozone dissolver (10) straight-through water outlet mouth and caliber adapt to the bypass water outlet of the entrance of cooling water of described water-cooled ozone-generator tube (4), the straight-through water-in of described first Y-junction (9a) is communicated with the water outlet of described gas-liquid mixing pump (6), straight-through water outlet mouth by the entrance of cooling water that second adjustable valve (9d) is communicated with the first water-in of described ozone dissolver (10), bypass water outlet is communicated with described water-cooled ozone-generator tube (4), and the cooling water outlet of described water-cooled ozone-generator tube (4) is communicated with the second water-in of described ozone dissolver (10).
10. ozone water apparatus according to claim 1, is characterized in that: the water outlet (10a) of described ozone dissolver (10) is connected with pressure regulator valve (11).
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| CN105413506A (en) * | 2015-11-27 | 2016-03-23 | 张旭 | Backwater-prevention device of gas-liquid mixing system |
| CN108211701A (en) * | 2018-01-12 | 2018-06-29 | 刘克诚 | Garbage house deodorization and sterilization equipment and its implementation |
| CN110526384A (en) * | 2019-09-23 | 2019-12-03 | 广州创环臭氧电器设备有限公司 | A kind of high efficiency ozone water apparatus |
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| CN105439098B (en) | 2017-09-22 |
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