CN203307164U - Mariculture bacteria-free process equipment - Google Patents
Mariculture bacteria-free process equipment Download PDFInfo
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- CN203307164U CN203307164U CN2013203406982U CN201320340698U CN203307164U CN 203307164 U CN203307164 U CN 203307164U CN 2013203406982 U CN2013203406982 U CN 2013203406982U CN 201320340698 U CN201320340698 U CN 201320340698U CN 203307164 U CN203307164 U CN 203307164U
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- asepticize
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Abstract
The utility model belongs to the technical field of bacteria-free process equipment, and discloses mariculture bacteria-free process equipment. The main technical feature is that the equipment comprises a tank with a water inlet and a water outlet at two ends, a partition with a liquid port is arranged in the tank, the partition divides the tank into an equipment chamber and a sterilizing chamber, an ozonator and a gas-liquid mixing mechanism are arranged in the equipment chamber, the tank of the equipment chamber is provided with a gas intake pipe, the gas intake pipe is communicated with the ozonator; the gas-liquid mixing mechanism comprises a liquid inlet, a gas inlet and a liquid outlet; the liquid inlet is communicated with the water inlet of the tank, the gas inlet is communicated with the gas outlet pipe of the ozonator, the liquid outlet is communicated with the liquid port, the gas intake pipe is provided with a gas flowmeter and a gas control valve, and a liquid flowmeter and a liquid control valve are arranged at the water inlet, so that pesticide residues are reduced, and the quality of aquaculture products is improved.
Description
Technical field
The utility model belongs to asepticize treatment facility and treatment process technical field, relates to concretely sea farming asepticize treatment facility and method.
Background technology
The marine organisms such as many marine fish, shrimp, shellfish need to be used sea farming, owing in seawater, containing a large amount of bacteriums, virus and algae, in breeding process, the biology of sea farming are easily infected, and in order to kill virus except algae, mainly take at present following two kinds of methods:
One, after culturing pool is put into seawater, in seawater, spray insecticide, to play pesticide-germicide except the algae effect, but there is following defect in the method, 1, spray insecticide after, seawater in pond need to be placed to 40---after 60 days, the cultivation seedling could be put into, avoid agricultural chemicals to damage seedling, culturing time is short; 2, life-time service agricultural chemicals, cause agricultural chemicals residual for a long time in aquaculture organism, causes the pollutions such as fishes and shrimps shellfish, and product quality is poor.
Its two, after cleaning up the pond, lime is sprayed in surrounding in culturing pool and bottom, operation is numerous and diverse, cost is high, and has changed the pH value of former seawater, is unfavorable for seedling early growth.
The utility model content
The technical problem that the utility model solves just be to provide a kind of sterilization except algae is effective, operation is simple, cost is low, safe and convenient to use, to the sea farming asepticize treatment facility of seawater component without change, non agricultural chemical residuum, fishery products quality better.
For solving the problems of the technologies described above, the technical scheme the utility model proposes is: comprise the tank body of two ends with water-in and water outlet, described water outlet is positioned at described tank end near top, in described tank body, be provided with the partition of crossing the liquid mouth, described partition is divided into canyon and sterilizing chamber by tank body; In described canyon, be provided with ozonizer and gas-liquid mixed organization, on the tank body of described canyon, be provided with inlet pipe, this inlet pipe is communicated with ozonizer, described gas-liquid mixed mechanism comprises fluid inlet, inlet mouth and liquid outlet, described fluid inlet is communicated with described tank body water-in, described inlet mouth is communicated with the escape pipe of described ozonizer, and described liquid outlet is communicated with the described liquid mouth of crossing; On described inlet pipe, be provided with gas meter and gas control valve, in described water inlet, be provided with liquid meter and liquid control valve door.
Its additional technical feature is:
Described gas-liquid mixed mechanism is gas-liquid mixing pump;
The volume of described sterilizing chamber is 120-240:1 with the ratio of per second flooding quantity;
On described inlet pipe, instrument air dryer is set;
Described gas-liquid mixed mechanism is the Venturi tube with water pump;
Below described sterilizing chamber, be provided with Draw off valve;
Near both sides, described sterilizing chamber end, be provided with two electrolytic bars, between described two electrolytic bars, be provided with ion separation membrane, described water outlet is two, respectively near described electrolytic bar, on described water outlet, be connected with thrust-augmenting nozzle, be provided with the mixing tank with water port at the other end of two thrust-augmenting nozzles;
The length of described thrust-augmenting nozzle is 4---6 meters, the volume of described mixing tank is 1:2 with the ratio of the volume of described sterilizing chamber.
The sea farming asepticize treatment facility that the utility model provides and this sea farming asepticize treatment facility of use are processed the method for seawater, compared with the existing technology have the following advantages: one, owing to comprising the tank body of two ends with water-in and water outlet, described water outlet is positioned at described tank end near top, in described tank body, be provided with the partition of crossing the liquid mouth, described partition is divided into canyon and sterilizing chamber by tank body; In described canyon, be provided with ozonizer and gas-liquid mixed organization, on the tank body of described canyon, be provided with inlet pipe, this inlet pipe is communicated with ozonizer, described gas-liquid mixed mechanism comprises fluid inlet, inlet mouth and liquid outlet, described fluid inlet is communicated with described tank body water-in, described inlet mouth is communicated with the escape pipe of described ozonizer, and described liquid outlet is communicated with the described liquid mouth of crossing; On described inlet pipe, be provided with gas meter and gas control valve, in described water inlet, be provided with liquid meter and liquid control valve door, ozonizer and gas-liquid mixed organization are opened, by observing gas meter and liquid meter, adjust gas control valve and liquid control valve door, if adopting air is the source of the gas of ozonizer, making gas-liquid volume ratio is 1:9, if adopting oxygen is the source of the gas of ozonizer, gas-liquid volume ratio is 1:12-16, like this, for ozone concn now, reach optimum germicidal effect; They are two years old, because the volume of described sterilizing chamber is 120-240:1 with the ratio of per second flooding quantity, make the water that ozone concn is high in tank body, stop 2-4 minute, like this, the germ in seawater, marine alga etc. almost all are killed, and stop long, cause time waste, stop too shortly, cause sterilization not thorough, affect culture efficiency; Its three, owing on described inlet pipe, instrument air dryer being set, when with air, during as ozone gas source, by instrument air dryer, improving the amount that generates ozone; Its four, owing to below described sterilizing chamber, being provided with Draw off valve, after after water injection, by Draw off valve, the seawater in sterilizing chamber is all discharged; They are five years old, owing near both sides, described sterilizing chamber end, being provided with two electrolytic bars, between described two electrolytic bars, be provided with ion separation membrane, described water outlet is two, respectively near described electrolytic bar, on described water outlet, be connected with thrust-augmenting nozzle, be provided with the mixing tank with water port at the other end of two thrust-augmenting nozzles; Seawater after ozone sterilizing is in the electrolysis of process electrolytic bar, make the water in two thrust-augmenting nozzles present highly basic or strong acid type, further utilize strong oxidized water and strong alkaline water to the seawater sterilization and disinfection, and then mix through mixing tank, change hardly the potential of hydrogen of seawater, be conducive to cultivate the growth of seedling; Its six, because the length of described thrust-augmenting nozzle is 4---6 meters, the volume of described mixing tank is 1:2 with the ratio of the volume of described sterilizing chamber, like this, strong basicity seawater and strongly-acid seawater are through 4---the sterilization of 6 meters, and sterilization effect is better, and again through 1---seawater can fully mix in 2 minutes.
The accompanying drawing explanation
Fig. 1 is the structural representation of sea farming asepticize treatment facility;
Fig. 2 is that gas-liquid mixed mechanism is the structural representation of the sea farming asepticize treatment facility of Venturi tube;
Fig. 3 is the cross-sectional view with the sea farming asepticize treatment facility of electrolysis mechanism.
Embodiment
Below in conjunction with the drawings and specific embodiments, sea farming asepticize treatment facility and the treatment process that the utility model proposes is described further.
As shown in Figure 1, be the structural representation of sea farming asepticize treatment facility.Its structure comprises the tank body 3 of two ends with water-in 1 and water outlet 2, and water outlet 2 is positioned at the end of tank body 3 near top, in tank body 3, is provided with and cuts off 4, cutting off 4 with crossing liquid mouth 5, cuts off 4 tank body 3 is divided into to canyon 6 and sterilizing chamber 7;
In canyon 6, be provided with ozonizer 8 and gas-liquid mixed organization 9, on the tank body 3 of canyon 7, be provided with inlet pipe 10, this inlet pipe 10 is communicated with ozonizer 8, gas-liquid mixed mechanism 9 comprises fluid inlet 91, inlet mouth 92 and liquid outlet 93, fluid inlet 91 is communicated with the water-in 1 of tank body 3, inlet mouth 92 is communicated with the escape pipe 81 of ozonizer 8, and liquid outlet 93 is communicated with mistake liquid mouth 5; On inlet pipe 10, be provided with gas meter 11 and gas control valve 12, be provided with liquid meter 13 and liquid control valve door 14 at water-in 1 place.
Ozonizer 8 and gas-liquid mixed organization 9 are opened, by observing gas meter 11 and liquid meter 13, adjust gas control valve 12 and liquid control valve door 14, if adopting air is the source of the gas of ozonizer 8, making gas-liquid volume ratio is 1:9, is the source of the gas of ozonizer 8 if adopt oxygen, and gas-liquid volume ratio is 1:12-16, like this, for ozone concn now, reach optimum germicidal effect.
The volume of sterilizing chamber is 120-240:1 with the ratio of per second flooding quantity, makes the water that ozone concn is high in tank body, stop 2-4 minute, because be not easy volatilization and decompose at the sterilization indoor ozone, like this, the germ in seawater, marine alga etc. almost all are killed.If stop longly, can cause time waste, stop too shortly, cause sterilization not thorough, affect culture efficiency.
Gas-liquid mixed mechanism 9 can be gas-liquid mixing pump as shown in Figure 1; Also can be the Venturi tube with water pump 15 16 as shown in Figure 2.
Instrument air dryer 17 is set on inlet pipe 10, when using air as ozone gas source, by instrument air dryer 17, can improves the amount that generates ozone.
Below sterilizing chamber 7, be provided with Draw off valve 18, after after water injection, by Draw off valve 18, the seawater in sterilizing chamber all discharged.
As shown in Figure 3, in the both sides near sterilizing chamber 7 ends, be provided with two electrolytic bars 19, between two electrolytic bars 19, be provided with ion separation membrane 20, water outlet 2 is two, respectively near electrolytic bar 19, on water outlet 2, be connected with thrust-augmenting nozzle 21, be provided with the mixing tank 23 with water port 22 at the other end of two thrust-augmenting nozzles 21.Seawater after ozone sterilizing is in 19 electrolysis of process electrolytic bar, make the water in two thrust-augmenting nozzles 21 present highly basic or strong acid type, further utilize strong oxidized water and strong alkaline water to the seawater sterilization and disinfection, and then mix through mixing tank 23, change hardly the potential of hydrogen of seawater, be conducive to cultivate the growth of seedling.
The length of thrust-augmenting nozzle 21 is 4---6 meters, the volume of mixing tank 23 is 1:2 with the ratio of the volume of sterilizing chamber 7, and like this, strong basicity seawater and strongly-acid seawater are through 4---the sterilization of 6 meters, sterilization effect is better, and again through 1---seawater can fully mix in 2 minutes.
Protection domain of the present utility model not only is confined to above-described embodiment, as long as structure is identical with the utility model sea farming asepticize treatment facility structure, just drops on the scope of the utility model protection.
Claims (8)
1. sea farming asepticize treatment facility, comprise the tank body of two ends with water-in and water outlet, described water outlet is positioned at described tank end near top, it is characterized in that: in described tank body, be provided with the partition of crossing the liquid mouth, described partition is divided into canyon and sterilizing chamber by tank body;
In described canyon, be provided with ozonizer and gas-liquid mixed organization, on the tank body of described canyon, be provided with inlet pipe, this inlet pipe is communicated with ozonizer, described gas-liquid mixed mechanism comprises fluid inlet, inlet mouth and liquid outlet, described fluid inlet is communicated with described tank body water-in, described inlet mouth is communicated with the escape pipe of described ozonizer, and described liquid outlet is communicated with the described liquid mouth of crossing;
On described inlet pipe, be provided with gas meter and gas control valve, in described water inlet, be provided with liquid meter and liquid control valve door.
2. sea farming asepticize treatment facility according to claim 1 is characterized in that: described gas-liquid mixed mechanism is gas-liquid mixing pump.
3. sea farming asepticize treatment facility according to claim 1, it is characterized in that: the volume of described sterilizing chamber is 120-240:1 with the ratio of per second flooding quantity.
4. sea farming asepticize treatment facility according to claim 1, is characterized in that: on described inlet pipe, instrument air dryer is set.
5. sea farming asepticize treatment facility according to claim 1 is characterized in that: described gas-liquid mixed mechanism is the Venturi tube with water pump.
6. sea farming asepticize treatment facility according to claim 1, is characterized in that: be provided with Draw off valve below described sterilizing chamber.
7. sea farming asepticize treatment facility according to claim 1, it is characterized in that: be provided with two electrolytic bars near both sides, described sterilizing chamber end, between described two electrolytic bars, be provided with ion separation membrane, described water outlet is two, respectively near described electrolytic bar, on described water outlet, be connected with thrust-augmenting nozzle, be provided with the mixing tank with water port at the other end of two thrust-augmenting nozzles.
8. sea farming asepticize treatment facility according to claim 7, it is characterized in that: the length of described thrust-augmenting nozzle is 4---6 meters, the volume of described mixing tank is 1:2 with the ratio of the volume of described sterilizing chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203406982U CN203307164U (en) | 2013-06-14 | 2013-06-14 | Mariculture bacteria-free process equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203406982U CN203307164U (en) | 2013-06-14 | 2013-06-14 | Mariculture bacteria-free process equipment |
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| Publication Number | Publication Date |
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| CN203307164U true CN203307164U (en) | 2013-11-27 |
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| CN2013203406982U Expired - Fee Related CN203307164U (en) | 2013-06-14 | 2013-06-14 | Mariculture bacteria-free process equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103262824A (en) * | 2013-06-14 | 2013-08-28 | 河北正通玻璃钢有限公司 | Mariculture aseptic treatment equipment and method |
-
2013
- 2013-06-14 CN CN2013203406982U patent/CN203307164U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103262824A (en) * | 2013-06-14 | 2013-08-28 | 河北正通玻璃钢有限公司 | Mariculture aseptic treatment equipment and method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131127 Termination date: 20140614 |
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| EXPY | Termination of patent right or utility model |