CN108069567A - A kind of composite bactericidal running water system - Google Patents
A kind of composite bactericidal running water system Download PDFInfo
- Publication number
- CN108069567A CN108069567A CN201711331387.9A CN201711331387A CN108069567A CN 108069567 A CN108069567 A CN 108069567A CN 201711331387 A CN201711331387 A CN 201711331387A CN 108069567 A CN108069567 A CN 108069567A
- Authority
- CN
- China
- Prior art keywords
- water
- valve
- bioactivity
- tank
- quality activating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 127
- 230000000844 anti-bacterial effect Effects 0.000 title claims abstract description 13
- 239000002131 composite material Substances 0.000 title claims abstract description 12
- 230000003213 activating effect Effects 0.000 claims abstract description 38
- 238000000034 method Methods 0.000 claims abstract description 15
- 239000010865 sewage Substances 0.000 claims abstract description 9
- 239000010453 quartz Substances 0.000 claims abstract description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 7
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000013618 particulate matter Substances 0.000 claims abstract description 5
- 238000007789 sealing Methods 0.000 claims abstract description 5
- 230000002070 germicidal effect Effects 0.000 claims abstract description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 40
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 238000011084 recovery Methods 0.000 claims description 12
- 230000000694 effects Effects 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 230000005672 electromagnetic field Effects 0.000 claims description 9
- 229910052760 oxygen Inorganic materials 0.000 claims description 9
- 239000001301 oxygen Substances 0.000 claims description 9
- 244000005700 microbiome Species 0.000 claims description 6
- 239000000706 filtrate Substances 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 description 13
- 238000004659 sterilization and disinfection Methods 0.000 description 6
- 238000009395 breeding Methods 0.000 description 5
- 230000001488 breeding effect Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 230000032683 aging Effects 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 230000000593 degrading effect Effects 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009432 framing Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000037081 physical activity Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/487—Treatment of water, waste water, or sewage with magnetic or electric fields using high frequency electromagnetic fields, e.g. pulsed electromagnetic fields
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
A kind of composite bactericidal running water system, it is made of pretreating device, bioactivity processing unit and water-quality activating system, pending water is introduced into pretreating device and is handled, and is handled afterwards into bioactivity processing unit, finally enters water-quality activating system and handled；The pretreating device is made of water inlet, process tank, sewage draining exit and water outlet, process tank crosses the particulate matter in drainage, it is flowed out after processing through water outlet, the water that the bioactivity processing unit is flowed out through water outlet is handled into the bioactivity processing unit；The water-quality activating system is mainly made of the first valve, water-quality activating device, the second valve and bypath valve, water-quality activating device is mainly made of water inlet, water outlet, Main Control Tank, shell, quartz burner, electrode and pedestal, quartz burner and electrode are housed inside the shell, ultraviolet germicidal lamp is fixed on the shell by the sealing clamp nut at shell both ends, and sewage draining exit is equipped in outer casing bottom.
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
Preferable bactericidal effect is unable to reach, particularly 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 effect of sterilization can be unable to reach when the dosage such as added is small
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 pollute the environment.
The content of the invention
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
Into pending water is introduced into pretreating device and is handled, and is handled, finally entered into bioactivity processing unit afterwards
Water-quality activating system is handled；The pretreating device is made of water inlet, process tank, sewage draining exit and water outlet, process tank
The different size of filtrate of multilayer is inside filled with, to cross the particulate matter in drainage, is flowed out after processing through water outlet, the bioactivity
Processing unit mainly includes jet pump, ejector, bioactivity tank, ozone generator, ORP on-line computing models and anti-return water dress
Put, through the water outlet flow out water handled into the bioactivity processing unit, a portion through by-passing valve into
Enter bioactivity tank, another part enters bioactivity tank after valve is pressurized by jet pump, from ejector through valve；It is described
Water-quality activating system is mainly made of the first valve, water-quality activating device, the second valve and bypath valve, water-quality activating device master
It to be made of water inlet, water outlet, Main Control Tank, shell, quartz burner, electrode and pedestal, inside the shell equipped with ultraviolet radiator
Pipe and electrode, ultraviolet germicidal lamp are fixed on the shell by the sealing clamp nut at shell both ends, and row is equipped in outer casing bottom
Dirty mouth.The water of water outlet outflow enters water-quality activating device through the first valve from water inlet, and through water-quality activating device, treated
Water is flowed out through the second valve from system water outlet, and water-quality activating device is equipped with bypath valve, to facilitate the dimension of water-quality activating device
Shield maintenance.
In one preferred embodiment, the size for flowing through the water of the ejector is controlled by valve and by-passing valve,
The inlet end of ejector is connected through check-valves and anti-water recovery apparatus with the ozone outlet of ozone generator, the size of ozone dosage
It is controlled by ORP on-line computing models, ORP electrodes are located on the pipeline before system water outlet, and valve is equipped with before ORP electrodes, with convenient
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, activated carbon is provided 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 ozone is put into, 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 the operation of system realization big flow can be made, 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 effectively protect the safe operation of ozone generator, and ozone after jet mixing directly into
Enter bioactivity tank, reduce 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 ultraviolet radiator in device C and the collective effect of electromagnetic field of high frequency are activated, 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 water inlet, at 2
Manage tank, 3 sewage draining exits, 4 water outlets, 5 valves, 6 jet pumps, 7 ejectors, 8 valves, 9 by-passing valves, 10 bioactivity tanks, 11 blowdowns
Mouthful, 12 water outlets, 13 first valves, 14 water-quality activating devices, 15 second valves, 16 bypath valves, 17 water outlets, 18 ozone hair
Raw device, 19ORP on-line computing models, 20 check-valves, 21 anti-water recovery apparatuses, 22ORP electrodes, 23 valves, 24 water inlets, 25 ultraviolet lights
Fluorescent tube, 26 Main Control Tanks, 27 electrodes, 28 shells, 29 water outlets, 30 sealing clamp nuts, 31 pedestals, 32 sewage draining exits
Specific embodiment
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 is introduced into pretreating device A processing, afterwards into bioactivity
Processing unit B processing finally enters water-quality activating system C processing.
As Figure 2-3, pretreating device A is made of water inlet 1, process tank 2, sewage draining exit 3 and water outlet 4, pending
Water handled by water inlet 1 into process tank 2, the different size of filtrate of multilayer is filled in process tank 2, to cross in drainage
Particulate matter, especially greater than 20 microns of particulate matter flows out after processing through water outlet 4.By the way that pre-procesor is set to go
Except the particle more than 20 microns, water quality is not only improved, 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 the water outlet 4 outflow enter the bioactivity processing unit B
It is handled, through by-passing valve 9 into bioactivity tank 10, another part is pressurized a portion through valve 5 by jet pump 6
Afterwards, bioactivity tank 10 is entered from ejector 7 through valve 8；By adding in ozone on bioactivity tank, make in bioactivity tank
Activated carbon on enriched gaseous oxygen, condensed organic, microorganism, form biomembrane, the biomembrane of activated carbon has good degradation water
The effect of middle organic matter.
Water-quality activating system C is mainly by 16 groups of the first valve 13, water-quality activating device 14, the second valve 15 and bypath valve
Into water-quality activating device 14 is mainly by water inlet 24, water outlet 29, Main Control Tank 26, shell 28, quartz burner 25, electrode 27
It is formed with pedestal 31, passes through 28 both ends of shell equipped with quartz burner 25 and electrode 27, ultraviolet germicidal lamp 25 in shell 28
Sealing clamp nut 30 be fixed on shell 28,28 bottom of shell be equipped with sewage draining exit 32.The water that water outlet 12 flows out is through the
One valve 13 is from water inlet 24 into water-quality activating device 14, through water-quality activating device treated water through the second valve 15 from being
System water outlet 17 flows out, and water-quality activating device 14 is equipped with bypath valve 16, to facilitate the maintaining of water-quality activating device 14.
In a specific embodiment, the size for flowing through the water of the ejector 7 is controlled by valve 8 and by-passing valve 9
System, the inlet end of ejector 7 are connected through check-valves 20 and anti-water recovery apparatus 21 with the ozone outlet of ozone generator 18, and ozone is thrown
The size of 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 electrodes
Valve 23 is equipped with before 22, to facilitate the maintaining of ORP electrodes；Through bioactivity tank 10, treated that water is flowed through water outlet 12
Go out.Ejector 7 and the connecting line of ozone generator 18 are equipped with check-valves 20 and anti-water recovery apparatus 21, pass through 20 He of check-valves
The duplicate protection of anti-water recovery apparatus 21 can effectively protect the safe operation of ozone generator, and ozone is direct after jet mixing
Into bioactivity tank, reduce the use of ozone mixing column, saved investment and operating cost.
In a specific embodiment, by-passing valve 9 is arranged in ejector 7, by-passing valve is set 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 ultraviolet radiator and high frequency in water-quality activating device 14
The collective effect of electromagnetic field can quickly destroy residual ozone in the water that bioactivity processing unit B comes out, while quickly kill water
In germ, and ozone destroy after product be oxygen, under the action of electromagnetic field of high frequency increase water body activity.
The system of the present invention is provided with preprocessor before ozone is put into, 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 the operation of system realization big flow can be made, 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 effectively protect the safe operation of ozone generator, and ozone after jet mixing directly into
Enter bioactivity tank, reduce 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 ultraviolet radiator in device C and the collective effect of electromagnetic field of high frequency are activated, 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 scope 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 scope.
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) form, 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 made of water inlet (1), process tank (2), sewage draining exit (3) and water outlet (4), process tank (2)
The different size of filtrate of multilayer is inside filled with, to cross the particulate matter in drainage, is flowed out after processing through water outlet (4)；
The bioactivity processing unit (B) mainly includes jet pump (6), ejector (7), bioactivity tank (10), ozone hair
Raw device (18), ORP on-line computing models (19) and anti-water recovery apparatus (21), the water through the water outlet (4) outflow enter the life
Object activity processing unit (B) is handled, and through by-passing valve (9) into bioactivity tank (10), another part passes through a portion
After valve (5) is pressurized by jet pump (6), enter bioactivity tank (10) from ejector (7) through valve (8)；
The water-quality activating system (C) is mainly by the first valve (13), water-quality activating device (14), the second valve (15) and bypass
Valve (16) form, water-quality activating device (14) mainly by water inlet (24), water outlet (29), Main Control Tank (26), shell (28),
Quartz burner (25), electrode (27) and pedestal (31) composition, are equipped with quartz burner (25) and electrode in shell (28)
(27), ultraviolet germicidal lamp (25) is fixed on by the sealing clamp nut (30) at shell (28) both ends on shell (28), outside
Shell (28) bottom is equipped with sewage draining exit (32), and the water of water outlet (12) outflow enters water quality through the first valve (13) from water inlet (24)
Device (14) is activated, is flowed out through water-quality activating device (14) treated water through the second valve (15) from system water outlet (17),
Water-quality activating device (14) is equipped with bypath valve (16), to facilitate the maintaining of water-quality activating device.
2. composite bactericidal running water system as described in claim 1 flows through the size of water of the ejector (7) by valve
(8) controlled with by-passing valve (9), the inlet end of ejector (7) is through check-valves (20) and anti-water recovery apparatus (21) and ozone generator
(18) ozone outlet is connected, and the size of ozone dosage is controlled by ORP on-line computing models (19), and ORP electrodes (22), which are located at, is
On pipeline before system water outlet (17), valve (23) is equipped with before ORP electrodes (22), to facilitate the maintaining of ORP electrodes (22)；
It is flowed out through bioactivity tank (10) treated water through water outlet (12).
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 or
The biologic packing material of other strong adsorptions forms biomembrane with enriched gaseous oxygen, condensed organic, microorganism.
5. composite bactericidal running water system as claimed in claim 1 or 2, the electrode (27) generates electromagnetic field of high frequency.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711331387.9A CN108069567A (en) | 2017-12-13 | 2017-12-13 | A kind of composite bactericidal running water system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711331387.9A CN108069567A (en) | 2017-12-13 | 2017-12-13 | A kind of composite bactericidal running water system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108069567A true CN108069567A (en) | 2018-05-25 |
Family
ID=62158490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711331387.9A Pending CN108069567A (en) | 2017-12-13 | 2017-12-13 | A kind of composite bactericidal running water system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108069567A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112811682A (en) * | 2020-12-31 | 2021-05-18 | 上海砼仁环保技术发展有限公司 | Integrated water body disinfection device |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2394441Y (en) * | 1999-11-18 | 2000-09-06 | 赵博林 | Sterilizing and oxygen feeding machine for aquaculture |
| US6685825B1 (en) * | 2002-11-14 | 2004-02-03 | Senno Technology Inc. | Water treatment system combining ozone injection and monitoring apparatuses |
| CN101200338A (en) * | 2006-12-12 | 2008-06-18 | 上海水产大学 | Method for removing organics and ammonia nitrogen from aquaculture water |
| CN101602562A (en) * | 2008-06-12 | 2009-12-16 | 中国科学院生态环境研究中心 | A kind of high-safety regenerated water deep treatment system |
| WO2013173857A1 (en) * | 2012-05-23 | 2013-11-28 | Abouloukme Ali | Water disinfection apparatus |
| CN203319807U (en) * | 2013-06-26 | 2013-12-04 | 徐雨顺 | Water treatment system for fish and shrimp farming |
| CN205556337U (en) * | 2016-04-07 | 2016-09-07 | 北京市水产技术推广站 | A water ultraviolet ray disinfection device that is used for running water breeding field seed hatching workshop |
| CN205838795U (en) * | 2016-06-17 | 2016-12-28 | 恩那社工程有限公司 | Dyeing waste water Treated sewage reusing device |
| CN207918625U (en) * | 2017-12-13 | 2018-09-28 | 广州畅驰机电设备有限公司 | A kind of composite bactericidal running water system |
-
2017
- 2017-12-13 CN CN201711331387.9A patent/CN108069567A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2394441Y (en) * | 1999-11-18 | 2000-09-06 | 赵博林 | Sterilizing and oxygen feeding machine for aquaculture |
| US6685825B1 (en) * | 2002-11-14 | 2004-02-03 | Senno Technology Inc. | Water treatment system combining ozone injection and monitoring apparatuses |
| CN101200338A (en) * | 2006-12-12 | 2008-06-18 | 上海水产大学 | Method for removing organics and ammonia nitrogen from aquaculture water |
| CN101602562A (en) * | 2008-06-12 | 2009-12-16 | 中国科学院生态环境研究中心 | A kind of high-safety regenerated water deep treatment system |
| WO2013173857A1 (en) * | 2012-05-23 | 2013-11-28 | Abouloukme Ali | Water disinfection apparatus |
| CN203319807U (en) * | 2013-06-26 | 2013-12-04 | 徐雨顺 | Water treatment system for fish and shrimp farming |
| CN205556337U (en) * | 2016-04-07 | 2016-09-07 | 北京市水产技术推广站 | A water ultraviolet ray disinfection device that is used for running water breeding field seed hatching workshop |
| CN205838795U (en) * | 2016-06-17 | 2016-12-28 | 恩那社工程有限公司 | Dyeing waste water Treated sewage reusing device |
| CN207918625U (en) * | 2017-12-13 | 2018-09-28 | 广州畅驰机电设备有限公司 | A kind of composite bactericidal running water system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112811682A (en) * | 2020-12-31 | 2021-05-18 | 上海砼仁环保技术发展有限公司 | Integrated water body disinfection device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| NZ597220A (en) | Fluid treatment apparatus | |
| CN107079869A (en) | A kind of industrial circulating water cultivating system | |
| CN103845754A (en) | Sterilization and disinfection purification device and method for air in livestock shed | |
| CN203898789U (en) | Sterilization, disinfection and purification device for air in livestock breeding shed | |
| CN106621789A (en) | Purification device and process of sludge drying and granulation waste gas | |
| CN103644604A (en) | Air PM dedusting sterilizer | |
| CN207918625U (en) | A kind of composite bactericidal running water system | |
| CN108069567A (en) | A kind of composite bactericidal running water system | |
| CN202799901U (en) | Factory farming water purification circulatory system | |
| CN206089267U (en) | Novel heterogeneous micro -nano bubble ozone sewage treatment device | |
| CN106882911A (en) | A kind of purifying processing device of aquiculture sewerage | |
| CN207774978U (en) | A kind of ultraviolet sterilization forward type water treatment facilities | |
| CN215798962U (en) | Ultrapure water device for laboratory | |
| KR102368131B1 (en) | Photocatalytic oxidation of OH radical hydroxyl group to remove odor, improve water quality, and regenerate filter media | |
| CN206279049U (en) | A kind of multi-stage sewage treatment device with recycling function | |
| CN108947053A (en) | A kind of water filter purification system | |
| CN205398325U (en) | Antibiotic waste water processing apparatus | |
| CN108706681A (en) | A kind of water route sterilizing unit and apply its Intelligent toilet cover | |
| KR101249733B1 (en) | Sea water supplying appratus for fishery farming and sea water supplying method | |
| CN203269693U (en) | Recirculating water treatment system | |
| CN209292134U (en) | A kind of Potable water equipment | |
| CN207671873U (en) | A kind of aquaculture sewage purifier | |
| CN104528996A (en) | High-efficiency sterilization device and method and swimming pool water treatment circulating system with sterilization device | |
| CN206395999U (en) | Hot spring water circulation treatment device | |
| CN206337051U (en) | Movable type water purification device with high-effective disinfecting effect |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180525 |
|
| WD01 | Invention patent application deemed withdrawn after publication |