CN207918625U - A kind of composite bactericidal running water system - Google Patents
A kind of composite bactericidal running water system Download PDFInfo
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- CN207918625U CN207918625U CN201721736467.8U CN201721736467U CN207918625U CN 207918625 U CN207918625 U CN 207918625U CN 201721736467 U CN201721736467 U CN 201721736467U CN 207918625 U CN207918625 U CN 207918625U
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Abstract
A kind of composite bactericidal running water system, it is made of pretreating device (A), bioactivity processing unit (B) and water-quality activating system (C), pending water is introduced into pretreating device and is handled, it is handled afterwards into bioactivity processing unit, finally enters water-quality activating system and handled；The pretreating device (A) is made of the first water inlet (1), process tank (2), the first sewage draining exit (3) and the first water outlet (4)；The bioactivity processing unit (B) includes mainly jet pump (6), ejector (7), bioactivity tank (10), ozone generator (18), ORP on-line computing models (19) and anti-water recovery apparatus (21)；The water-quality activating system (C) is mainly made of third valve (13), water-quality activating device (14), the 4th valve (15) and bypath valve (16), and water-quality activating device (14) is mainly made of the second water inlet (24), the second water outlet (29), Main Control Tank (26), shell (28), quartz burner (25), electrode (27) and pedestal (31).
Description
Technical field
The present invention relates to water treatment field more particularly to a kind of composite bactericidal running water systems.
Background technology
Industrial circulating water cultivating due to cultivation health it is controllable, non-hazardous to environment, economize on resources, breeding efficiency height, be
A kind of breeding way with high content of technology, environmentally protective is the developing direction of aquaculture from now on, and is supported in industrial circulating water
It is always an important factor for restricting cultivation success or failure to grow the disinfection of water body and water body aging in process.
At present to the sterilizing of water body mostly only with a kind of independent method for disinfection, such as ultraviolet light irradiation-sterilize sterilization
(referring to document CN101647421A, CN101851015A), ozone sterilization sterilization (referring to document CN101336621A,
CN101767897A) or chloric bactericin method (referring to document CN10212064A, CN1556046A) etc., but the above method is equal
It is unable to reach ideal bactericidal effect, especially in the zoic water body such as industrial circulating water cultivating water body or landscape water body
Sterilizing is carried out, when carrying out sterilizing using single method, the dosage hour such as added can be unable to reach the effect of sterilization
Fruit, and the excessive growth that can influence organism in water of dosage.And for water body problem of aging, current processing method also only has
It is realized by largely changing water, largely changes water both waste water resource and the energy, while also polluting the environment.
Invention content
In view of the deficiencies of the prior art, the object of the present invention is to provide a kind of composite bactericidal running water system, which passes through
Physical filtering, ozone-bioactivity advanced treating and water-quality activating technology ensure the fresh of breeding water body and cleaning.
The present invention adopts the following technical scheme that：
A kind of composite bactericidal running water system, by pretreating device, bioactivity processing unit and water-quality activating system group
At pending water is introduced into pretreating device and is handled, and is handled, is finally entered into bioactivity processing unit afterwards
Water-quality activating system is handled；The pretreating device is by the first water inlet, process tank, the first sewage draining exit and the first water outlet
It forms, the different size of filtrate of multilayer is filled in process tank, to cross the particulate matter in drainage, through the first water outlet stream after processing
Go out, the bioactivity processing unit is mainly supervised including jet pump, ejector, bioactivity tank, ozone generator, ORP online
Instrument and anti-water recovery apparatus are surveyed, the water flowed out through the first water outlet is handled into the bioactivity processing unit, wherein one
Part enters bioactivity tank through by-passing valve, and another part is after the first valve is pressurized by jet pump, from ejector through second
Valve enters bioactivity tank；The water-quality activating system is mainly by third valve, water-quality activating device, the 4th valve and side
Port valve door forms, and water-quality activating device is mainly by the second water inlet, the second water outlet, Main Control Tank, shell, quartz burner, electricity
Pole and pedestal composition, are equipped with quartz burner and electrode inside the shell, and quartz burner compresses spiral shell by the sealing at shell both ends
Mother is fixed on the shell, and the second sewage draining exit is equipped in outer casing bottom.The water of water outlet outflow is through third valve from the second water inlet
Into water-quality activating device, through water-quality activating device, treated that water is flowed out through the 4th valve from system water outlet, water-quality activating
Device is equipped with bypath valve, to facilitate the maintaining of water-quality activating device.
In one preferred embodiment, the size of the water of the ejector is flowed through by the second valve and by-passing valve control
System, the inlet end of ejector are connected through check-valves and anti-water recovery apparatus with the ozone outlet of ozone generator, ozone dosage
Size is controlled by ORP on-line computing models, and ORP electrodes are located on the pipeline before system water outlet, and the 5th valve is equipped with before ORP electrodes
Door, to facilitate the maintaining of ORP electrodes；Through bioactivity tank, treated that water is flowed out through water outlet.
In one preferred embodiment, by-passing valve is arranged in ejector.
In one preferred embodiment, it is provided with activated carbon in bioactivity tank or the biology of other strong adsorptions is filled out
Material forms biomembrane with enriched gaseous oxygen, condensed organic, microorganism.
In one preferred embodiment, electrode generates electromagnetic field of high frequency.
Beneficial technique effect caused by the present invention：
The system of the present invention is provided with preprocessor before putting into ozone, and particle of the removal more than 20 microns has improved
Water quality, and can reduce the dosage of follow-up ozone, by-passing valve is provided in ejector in addition, can effectively ensure jet stream
The stable operation of device, and system can be made to realize the operation of big flow, greatly reduce the energy consumption of system operation；Further, originally
The ejector of the system of invention and the connecting line of ozone generator are equipped with check-valves and anti-water recovery apparatus, by check-valves and
The duplicate protection of anti-water recovery apparatus, can effective protection ozone generator safe operation, and ozone after jet mixing directly into
Enter bioactivity tank, reduces the use of ozone mixing column, saved investment and operating cost；In addition, by bioactivity
Ozone is added on tank, makes enriched gaseous oxygen, condensed organic, microorganism on the activated carbon in bioactivity tank, forms biomembrane, it is living
The biomembrane of property charcoal plays the role of Organic substance in water of degrading well, and system end is provided with water-quality activating device C, passes through water quality
The collective effect for activating the ultraviolet radiator and electromagnetic field of high frequency in device C can quickly destroy what bioactivity processing unit B came out
Residual ozone in water, while the germ in speed killing water is interrogated, and also the product after ozone destruction is oxygen, in electromagnetic field of high frequency
The lower activity for increasing water body of effect.Sterilizing is carried out by the system, sterilizing rate is up to 100%, and no chemical residues, energy
In the case of online sterilizing, ensure safety biological in breeding water body.
Description of the drawings
Fig. 1 is the structural framing figure of the present invention；
Fig. 2 is the structure chart of the system of the present invention；
Fig. 3 is the structure chart of the water-quality activating device of the present invention.
Reference sign：A pretreating devices, B bioactivity processing units, C water-quality activating systems, 1 first water inlet,
2 process tanks, 3 first sewage draining exits, 4 first water outlets, 5 first valves, 6 jet pumps, 7 ejectors, 8 second valves, 9 by-passing valves,
10 bioactivity tanks, 11 sewage draining exits, 12 water outlets, 13 third valves, 14 water-quality activating devices, 15 the 4th valves, 16 by-passing valves
Door, 17 system water outlets, 18 ozone generators, 19ORP on-line computing models, 20 check-valves, 21 anti-water recovery apparatus, 22ORP electricity
Pole, 23 the 5th valves, 24 second water inlets, 25 quartz burners, 26 Main Control Tanks, 27 electrodes, 28 shells, 29 second water outlets,
30 sealing clamp nuts, 31 pedestals, 32 second sewage draining exits
Specific implementation mode
Hereinafter, by attached drawing, the present invention is described in detail.Hereinafter, same component uses same symbol.
As shown in Figure 1, the present invention provides a kind of composite bactericidal running water system, by pretreating device A, bioactivity processing
Device B and water-quality activating system C compositions, pending water are introduced into pretreating device A processing, enter bioactivity afterwards
Processing unit B processing finally enters water-quality activating system C processing.
As Figure 2-3, pretreating device A is by the first water inlet 1, process tank 2, the first sewage draining exit 3 and the first water outlet
4 compositions, pending water are handled by the first water inlet 1 into process tank 2, and multilayer different size is filled in process tank 2
Filtrate, with cross drainage in particulate matter, especially greater than 20 microns of particulate matter, after processing through the first water outlet 4 flow out.It is logical
Particle of the setting pre-procesor removal more than 20 microns is crossed, not only improves water quality, but also the dosage of follow-up ozone can be reduced.
Bioactivity processing unit B mainly include jet pump 6, ejector 7, bioactivity tank 10, ozone generator 18,
ORP on-line computing models 19 and anti-water recovery apparatus 21, the water through first water outlet 4 outflow enter bioactivity processing dress
B processing is set, a portion enters bioactivity tank 10 through by-passing valve 9, and another part passes through jet pump through the first valve 5
After 6 superchargings, enter bioactivity tank 10 from ejector 7 through the second valve 8；By the way that ozone is added on bioactivity tank, make life
Enriched gaseous oxygen, condensed organic, microorganism on activated carbon in object activity tank, form biomembrane, and the biomembrane of activated carbon has very
The effect of good degradation Organic substance in water.
Water-quality activating system C is mainly by 16 groups of third valve 13, water-quality activating device 14, the 4th valve 15 and bypath valve
At water-quality activating device 14 is mainly by the second water inlet 24, the second water outlet 29, Main Control Tank 26, shell 28, quartz burner
25, electrode 27 and pedestal 31 form, and quartz burner 25 and electrode 27 are housed in shell 28, and quartz burner 25 passes through outer
The sealing clamp nut 30 at 28 both ends of shell is fixed on shell 28, and the second sewage draining exit 32 is equipped in 28 bottom of shell.Water outlet 12
The water of outflow enters water-quality activating device 14 through third valve 13 from the second water inlet 24, through water-quality activating device treated water
It is flowed out from system water outlet 17 through the 4th valve 15, water-quality activating device 14 is equipped with bypath valve 16, to facilitate water-quality activating to fill
Set 14 maintaining.
In a specific embodiment, the size of the water of the ejector 7 is flowed through by the second valve 8 and by-passing valve
9 controls, the inlet end of ejector 7 is connected through check-valves 20 and anti-water recovery apparatus 21 with the ozone outlet of ozone generator 18, smelly
The size of oxygen dosage is controlled by setting ORP on-line computing models 19, and ORP electrodes 22 are located on the pipeline before system water outlet 17, ORP
Valve 23 is equipped with before electrode 22, to facilitate the maintaining of ORP electrodes；Through treated the water of bioactivity tank 10 through water outlet 12
Outflow.Ejector 7 and the connecting line of ozone generator 18 are equipped with check-valves 20 and anti-water recovery apparatus 21, pass through check-valves
20 and anti-water recovery apparatus 21 duplicate protection, can effective protection ozone generator safe operation, and ozone is after jet mixing
It is directly entered bioactivity tank, reduces the use of ozone mixing column, has saved investment and operating cost.
In a specific embodiment, by-passing valve 9 is arranged in ejector 7, by-passing valve is arranged in ejector, both
It can effectively ensure the stable operation of ejector, and system can be made to realize the operation of big flow, greatly reduce system operation
Energy consumption.
In a specific embodiment, activated carbon or the biology of other strong adsorptions are provided in bioactivity tank 10
Filler forms biomembrane with enriched gaseous oxygen, condensed organic, microorganism.
Preferably, electrode 27 can generate electromagnetic field of high frequency.Pass through the quartz burner and height in water-quality activating device 14
The collective effect of frequency electromagnetic field can quickly destroy residual ozone in the water that bioactivity processing unit B comes out, while quickly kill
Germ in water, and the product after ozone destruction is oxygen, increases the activity of water body under the action of electromagnetic field of high frequency.
The system of the present invention is provided with preprocessor before putting into ozone, and particle of the removal more than 20 microns has improved
Water quality, and can reduce the dosage of follow-up ozone, by-passing valve is provided in ejector in addition, can effectively ensure jet stream
The stable operation of device, and system can be made to realize the operation of big flow, greatly reduce the energy consumption of system operation；Further, originally
The ejector of the system of invention and the connecting line of ozone generator are equipped with check-valves and anti-water recovery apparatus, by check-valves and
The duplicate protection of anti-water recovery apparatus, can effective protection ozone generator safe operation, and ozone after jet mixing directly into
Enter bioactivity tank, reduces the use of ozone mixing column, saved investment and operating cost；In addition, by bioactivity
Ozone is added on tank, makes enriched gaseous oxygen, condensed organic, microorganism on the activated carbon in bioactivity tank, forms biomembrane, it is living
The biomembrane of property charcoal plays the role of Organic substance in water of degrading well, and system end is provided with water-quality activating device C, passes through water quality
The collective effect for activating the ultraviolet radiator and electromagnetic field of high frequency in device C can quickly destroy what bioactivity processing unit B came out
Residual ozone in water, while the germ in speed killing water is interrogated, and also the product after ozone destruction is oxygen, in electromagnetic field of high frequency
The lower activity for increasing water body of effect.Sterilizing is carried out by the system, sterilizing rate is up to 100%, and no chemical residues, energy
In the case of online sterilizing, ensure safety biological in breeding water body.
Above-mentioned detailed description is illustrating for one of the present invention practicable embodiment, which is not to limit
The patented technology range of the present invention is made, all equivalence enforcements or change without departing from carried out by the present invention are intended to be limited solely by the special of this case
In sharp range.
Claims (5)
1. a kind of composite bactericidal running water system, by pretreating device (A), bioactivity processing unit (B) and water-quality activating system
(C) it forms, pending water is introduced into pretreating device and is handled, handled afterwards into bioactivity processing unit, most
It is handled afterwards into water-quality activating system；
The pretreating device (A) is by the first water inlet (1), process tank (2), the first sewage draining exit (3) and the first water outlet (4) group
At process tank (2) is interior to be filled with the different size of filtrate of multilayer, to cross the particulate matter in drainage, through the first water outlet after processing
(4) it flows out；The bioactivity processing unit (B) includes mainly jet pump (6), ejector (7), bioactivity tank (10), smelly
Oxygen Generator (18), ORP on-line computing models (19) and anti-water recovery apparatus (21), through first water outlet (4) outflow water into
Enter the bioactivity processing unit (B) to be handled, a portion enters bioactivity tank (10) through by-passing valve (9), separately
A part enters bioactivity tank after the first valve (5) is pressurized by jet pump (6), from ejector (7) through the second valve (8)
(10)；
The water-quality activating system (C) is mainly by third valve (13), water-quality activating device (14), the 4th valve (15) and bypass
Valve (16) form, water-quality activating device (14) mainly by the second water inlet (24), the second water outlet (29), Main Control Tank (26),
Shell (28), quartz burner (25), electrode (27) and pedestal (31) composition, are equipped with quartz burner (25) in shell (28)
With electrode (27), quartz burner (25) is fixed on by the sealing clamp nut (30) at shell (28) both ends on shell (28),
It is equipped with the second sewage draining exit (32) in shell (28) bottom, the water of water outlet (12) outflow is through third valve (13) from the second water inlet
(24) enter water-quality activating device (14), be discharged from system through the 4th valve (15) through water-quality activating device (14) treated water
Mouth (17) outflow, water-quality activating device (14) is equipped with bypath valve (16), to facilitate the maintaining of water-quality activating device (14).
2. composite bactericidal running water system as described in claim 1 flows through the size of the water of the ejector (7) by the second valve
The inlet end of door (8) and by-passing valve (9) control, ejector (7) occurs through check-valves (20) and anti-water recovery apparatus (21) with ozone
The ozone outlet of device (18) is connected, and the size of ozone dosage is controlled by ORP on-line computing models (19), and ORP electrodes (22) are located at
On pipeline before system water outlet (17), the 5th valve (23) is equipped with before ORP electrodes (22), to facilitate the dimension of ORP electrodes (22)
Shield maintenance；It is flowed out through water outlet (12) through bioactivity tank (10) treated water.
3. composite bactericidal running water system as claimed in claim 1 or 2, the by-passing valve (9) is arranged in ejector (7).
4. composite bactericidal running water system as claimed in claim 1 or 2, be provided in the bioactivity tank (10) activated carbon with
Enriched gaseous oxygen, condensed organic, microorganism form biomembrane.
5. composite bactericidal running water system as claimed in claim 1 or 2, the electrode (27) generates electromagnetic field of high frequency.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721736467.8U CN207918625U (en) | 2017-12-13 | 2017-12-13 | A kind of composite bactericidal running water system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721736467.8U CN207918625U (en) | 2017-12-13 | 2017-12-13 | A kind of composite bactericidal running water system |
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| CN207918625U true CN207918625U (en) | 2018-09-28 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108069567A (en) * | 2017-12-13 | 2018-05-25 | 广州畅驰机电设备有限公司 | A kind of composite bactericidal running water system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108069567A (en) * | 2017-12-13 | 2018-05-25 | 广州畅驰机电设备有限公司 | A kind of composite bactericidal running water system |
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Address after: 510530 Room 628, 81 Dongyi Second Street, Luogang District, Guangzhou City, Guangdong Province Patentee after: Guangzhou Changchi Environmental Technology Co., Ltd. Address before: 510530 Room 628, 81 Dongyi Second Street, Luogang District, Guangzhou City, Guangdong Province Patentee before: GUANGZHOU CHANG CHI MECHANICAL AND ELECTRICAL EQUIPMENT CO., LTD. |
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