CN108002583A - A kind of big instant water treatment facilities of scale of construction plasma gas-liquid - Google Patents
A kind of big instant water treatment facilities of scale of construction plasma gas-liquid Download PDFInfo
- Publication number
- CN108002583A CN108002583A CN201711214117.XA CN201711214117A CN108002583A CN 108002583 A CN108002583 A CN 108002583A CN 201711214117 A CN201711214117 A CN 201711214117A CN 108002583 A CN108002583 A CN 108002583A
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- Prior art keywords
- plasma
- housing
- aeration
- micro
- nano bubble
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- 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.)
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Links
- 210000002381 Plasma Anatomy 0.000 title claims abstract description 57
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000010276 construction Methods 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 title claims abstract description 15
- 239000002101 nanobubble Substances 0.000 claims abstract description 32
- 239000001301 oxygen Substances 0.000 claims abstract description 25
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 25
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000007906 compression Methods 0.000 claims abstract description 15
- 239000002808 molecular sieve Substances 0.000 claims abstract description 8
- 238000005273 aeration Methods 0.000 claims description 46
- 238000004146 energy storage Methods 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 12
- 230000000007 visual effect Effects 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 27
- 241001282153 Scopelogadus mizolepis Species 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 238000005260 corrosion Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 230000001954 sterilising Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000276438 Gadus morhua Species 0.000 description 1
- 244000052616 bacterial pathogens Species 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 235000019516 cod Nutrition 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000000593 degrading Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000000249 desinfective Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000005055 memory storage Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 239000003403 water pollutant 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- C02F1/722—Oxidation by peroxides
-
- 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
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/005—Processes using a programmable logic controller [PLC]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- 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
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- 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
- C02F2303/02—Odour removal or prevention of malodour
-
- 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
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
Abstract
The invention discloses a kind of big instant water treatment facilities of scale of construction plasma gas-liquid, include base, the housing being arranged on base, it is arranged in housing and air pump, compression cooling driers, air filter, oxygen molecular sieve processed, oxygen tank and plasma generator connected in sequence, it is arranged at the plasma electrical source being connected in housing and with plasma generator, and the micro-nano bubble generator and controller being arranged in housing；Wherein, air pump, compression cooling driers, air filter, plasma generator, plasma electrical source, micro-nano bubble generator are electrically connected with the controller.The present invention is directly connected with treatment tank, the sewage of the big scale of construction quickly can be handled, treated sewage is efficient；Equipment conveniently moving, installation is simple, saves space；Equipment realizes PLC remote controls, fully automatic operation, and use cost is low.
Description
Technical field
The present invention relates to field of sewage treatment equipment, a kind of specific big instant water treatment facilities of scale of construction plasma gas-liquid.
Background technology
The main function of sewage disposal device be can effective treated sewage, avoid sewage and pollutant from flowing directly into waters,
It is of great significance to improving the ecological environment, being lifted city taste and promote economic development.Currently on the market at general sewage
Reason equipment uses several frequently seen technique, and a part of equipment is usually realized using core part is replaced；Another part equipment passes through
Persistently add medicament to realize, right such method is required for troublesome operation and there are follow-up expense；On the other hand, the latter is also easy to produce two
Secondary pollution；Also there is the shortcomings of processing assembly line is long in most equipment.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of big instant water treatment facilities of scale of construction plasma gas-liquid, directly
Connect, the sewage of the big scale of construction can quickly be handled, treated sewage is efficient with treatment tank；Equipment conveniently moving, peace
Dress is simple, saves space；Equipment realizes PLC controls, fully automatic operation, and use cost is low.
The technical scheme is that：
A kind of big instant water treatment facilities of scale of construction plasma gas-liquid, include base, the housing being arranged on base, is arranged at
In housing and air pump, compression cooling driers, air filter, oxygen molecular sieve processed, oxygen tank and plasma connected in sequence
Generator, is arranged at the plasma electrical source being connected in housing and with plasma generator, and is arranged at micro- in housing
Nano-bubble generating apparatus and controller；The air pump, compression cooling driers, air filter, plasma generator,
Plasma electrical source, micro-nano bubble generator are electrically connected with the controller；Be provided with the housing aeration water inlet,
Aeration outlet, plasma gas exports and power interface, and the micro-nano reached outside housing is connected with the aeration water inlet
Rice bubble aeration water inlet pipe, aeration are connected with the micro-nano bubble aeration outlet pipe reached outside housing, micro-nano gas in outlet
Generating apparatus be soaked respectively by micro-nano bubble aeration water inlet pipe, micro-nano bubble aeration outlet pipe and the sewage disposal outside housing
Pond connects, and the plasma exhaust pipe reached outside housing is connected with plasma gas outlet, and plasma occurs
Device is connected by plasma exhaust pipe with the treatment tank outside housing, the air pump, compression cooling driers, air mistake
Filter, plasma electrical source, micro-nano bubble generator, the power input of controller are connected with power interface.
The booster pump that the micro-nano bubble generator includes energy storage canister and is connected with controller, the electricity of booster pump
Source input terminal is connected with power interface, and the import of booster pump is connected with aeration water inlet, the outlet of booster pump and energy storage canister into
Mouth connection, outlet and the aeration outlet of energy storage canister connect.
Cooling device, cooling device and the cooling cycle being arranged on housing are provided with the plasma generator
Water out is connected with entrance.
Multilayer rack, the air pump, compression cooling driers, air filter, system are provided with the housing
Oxygen molecular sieve, oxygen tank, plasma generator, plasma electrical source, micro-nano bubble generator, controller are set respectively
In on the bottom plate of housing or on multilayer rack.
The controller includes display control panel and programmable logic controller (PLC), is provided with display control panel
Display screen, operational and controlled key button, aeration pressure gauge and the aeration flowmeter being connected with programmable logic controller (PLC)；The aeration pressure
Table and aeration flowmeter are connected with micro-nano bubble generator.
Oxygen flow rate adjusting valve is provided with the oxygen tank and the connecting line of plasma generator.
The cabinet door with visual window, multiple radiator windows and exhaust fan, the cabinet door direction are provided with the housing
The display control panel of controller.
Advantages of the present invention：
（1）, the present invention using sequentially connected air pump, compression cooling driers, air filter, oxygen molecular sieve processed, oxygen tank
Low temperature plasma is produced with plasma generator, makes the hydrone in high-concentration sewage that excitation cracking and ionization occur, it is raw
Into carboxyl free radical OH, O3、H2O2, carboxyl free radical OH, O3、H2O2 Bombard high-concentration sewage in organic matter C-C keys and
Unsaturated bond, makes organic matter scission of link and open loop in high-concentration sewage, and macromolecular becomes small molecule, rapid oxidation and decomposes in water
Pollutant, so as to reach the purpose of decoloration, deodorization, sterilization, algae removal.
（2）, the present invention in micro-nano bubble aeration exit, the grade of micro-nano bubble and plasma exhaust pipe discharge from
Daughter mixes, the solution-air suspension jet for including a large amount of micro-nano bubbles of generation, plasma microbubble air supporting coagulation process
The dissolving mass-transfer efficiency of plasma in water is improved, extends the time of contact of plasma and sewage.The present invention realizes
The high-efficient purification of high-concentration sewage, water outlet reach discharging standards.
（3）, the present invention using the working gas that air is plasma generator, using physical method treated sewage, no
Need to add medicine, non-secondary pollution；It is high to the pathogenic microorganisms, the killing rate such as bacterium that contain in sewage, it can remove at the same time
Color, smelly, taste in sewage, biochemical substances of degrading.
（4）, the present invention be integration apparatus, conveniently moving, installation is simple, floor space is small.
（5）, the present invention be connected with treatment tank after sewage therein is quickly handled, realize intelligentized control method,
Power saving, noiseless, operating cost is low, fully automatic operation, is safeguarded without personal management.
Brief description of the drawings
Fig. 1 is the front view inside inventive shell.
Fig. 2 is the rearview inside inventive shell.
Fig. 3 is the left view inside inventive shell.
Fig. 4 is the right view inside inventive shell.
Fig. 5 is the mounting structure schematic diagram of the present invention.
Fig. 6 is the fundamental diagram of the present invention, and " --- " connects for pipeline, "-- " connected for signal.
Fig. 7 is the structure diagram in cesspool.
Embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other without making creative work
Embodiment, belongs to the scope of protection of the invention.
A kind of big instant water treatment facilities of scale of construction plasma gas-liquid, include base 1, the housing being arranged on base 1
2, the multilayer rack 3 being arranged in housing, is arranged on the bottom plate of housing 2 or on multilayer rack 3 and connected in sequence
Air pump 4, compression cooling driers 5, air filter 6, oxygen molecular sieve processed 7, oxygen tank 8 and plasma generator 9, are arranged at
The plasma electrical source 10 being connected on multilayer rack 3 and with plasma generator 9, is arranged at oxygen tank 8 and plasma
Oxygen flow rate adjusting valve 11 on the connecting line of generator 9, and be arranged on multilayer rack 3 energy storage canister 12, supercharging
Pump 13 and controller；Energy storage canister 12 and booster pump 13 form micro-nano bubble generator；
Controller includes display control panel and programmable logic controller (PLC) 19, is provided with and may be programmed on display control panel
Display screen 20, operational and controlled key button 21, aeration pressure gauge 22 and the aeration flowmeter 23 that logic controller 19 connects；It is aerated pressure gauge 22
It is connected with aeration flowmeter 23 with the inside of energy storage canister 12 of micro-nano bubble generator；
Aeration water inlet 14, aeration outlet 15, plasma gas outlet 16, power interface 17, cooling cycle are provided with housing 2
Water out and entrance 18, the import of booster pump 13 are connected with aeration water inlet 14, the outlet of booster pump 13 and energy storage canister 12 into
Mouth connection, the outlet and aeration outlet 15 of energy storage canister 12 are connected, are aerated on water inlet 14 and are connected with the micro-nano reached outside housing 2
Rice bubble aeration water inlet pipe 24, aeration exports and is connected with the micro-nano bubble aeration outlet pipe 25 reached outside housing 2 on 15, micro-
Nano bubble aeration water inlet pipe 24, micro-nano bubble aeration outlet pipe 25 are connected with the treatment tank 30 outside housing 2, plasma
The plasma exhaust pipe 26 reached outside housing 2 is connected with gas vent 16, plasma generator 9 passes through plasma
Exhaust pipe 26 is connected with the treatment tank 30 outside housing 2；Air pump 4, compression cooling driers 5, air filter 6, plasma
Body power supply 10, booster pump 13, the power input of programmable logic controller (PLC) 19 are connected with power interface 17；Plasma is sent out
The cooling device set on raw device 9 is connected plasma generator 9 with cooling cycle water out and entrance 18 and radiates；
Air pump 4, compression cooling driers 5, air filter 6, plasma generator 9, plasma electrical source 10, booster pump 13
It is electrically connected with the programmable logic controller (PLC) 19 of controller；
Wherein, see Fig. 1,2 and 5, the cabinet door 27 with visual window, multiple radiator windows 28 and exhaust fan 29, cabinet are provided with housing 2
Display control panel of the door 27 towards controller.
The operation principle of the present invention：
See Fig. 6, outside air is entered in compression cooling driers 5 by air pump 4 first is compressed the cold of dry generation drying
Air, then cold air enter nitrogen therein after entering 6 impurity screening of air filter and partial moisture in oxygen molecular sieve 7 processed
Gas is separated, and remaining oxygen enters 8 memory storage of oxygen tank；When preparing plasma, the oxygen in oxygen tank 8 enters
Plasma is generated in plasma generator, plasma is successively by plasma gas outlet 16, plasma exhaust pipe 26
Enter progress plasma sewage disposal in the sewage for the treatment of tank；The micro-nano gas that energy storage canister 12 and booster pump 13 form
The generating apparatus that is soaked produces micro-nano bubble, successively by being arranged after aeration outlet 15, micro-nano bubble aeration outlet pipe 25 with gas ions
The plasma that tracheae 26 is discharged is entered in the corrosion-resistant micro-nano aeration tube 30 of cesspool after completing coagulation, improves plasma
The dissolving mass-transfer efficiency of body in water, accelerates the rate of climb of water body dissolved ozone concentration, improves the peak concentration of dissolved ozone,
And the time of contact of plasma and sewage is extended, reduce and react required concentration threshold, shorten the reaction time, improve dirty
Water treatment efficiency, realizes the purification of high-concentration sewage, is finally reached efficient sterilizing, disinfection, the effect for reducing COD, and water outlet reaches
Discharging standards.
See Fig. 5, liquid level sensor 32 is both provided with treatment tank 31, recirculated water is additionally provided with treatment tank 31
Pump 33, makes the effluent cycle in treatment tank 31, speed up processing, the dirt after the interior processing of last treatment tank 31
Arranged outside water.
See Fig. 7, be provided with multiple vertical clapboards 34 in treatment tank 31, the bottom of vertical clapboard 34 and cesspool 31
Bottom of pond closing connection, cesspool 31 is interior to be equipped with corrosion-resistant micro-nano aeration tube by the space bottom that vertical clapboard 34 is split
30, sewage deep all-in-one machine of the corrosion-resistant micro-nano aeration tube 30 with the present invention is connected, and the sewage in former pond initially enters
In the space of 31 high order end for the treatment of tank, then sequentially overflow in adjacent sewage pool space and repeatedly handled, then
Discharged by delivery pipe, flowmeter 35 is provided with delivery pipe, for calculating sewage load.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of changes, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (7)
- A kind of 1. big instant water treatment facilities of scale of construction plasma gas-liquid, it is characterised in that：Include base, be arranged on base Housing, be arranged in housing and air pump connected in sequence, compression cooling driers, air filter, oxygen molecular sieve processed, oxygen Tank and plasma generator, are arranged at the plasma electrical source being connected in housing and with plasma generator, and set In micro-nano bubble generator and controller in housing；The air pump, compression cooling driers, air filter, etc. Plasma generator, plasma electrical source, micro-nano bubble generator are electrically connected with the controller；Set on the housing There are aeration water inlet, aeration outlet, plasma gas outlet and power interface, be connected with and reach on the aeration water inlet Micro-nano bubble aeration water inlet pipe outside housing, aeration are connected with the micro-nano bubble aeration water outlet reached outside housing in outlet Pipe, micro-nano bubble generator pass through micro-nano bubble aeration water inlet pipe, micro-nano bubble aeration outlet pipe and housing respectively Outer treatment tank connection, the plasma gas are connected with the plasma exhaust pipe reached outside housing in outlet, Plasma generator is connected by plasma exhaust pipe with the treatment tank outside housing, the air pump, compression Cooling driers, air filter, plasma electrical source, micro-nano bubble generator, controller power input and power supply Interface connects.
- A kind of 2. big instant water treatment facilities of scale of construction plasma gas-liquid according to claim 1, it is characterised in that：It is described Micro-nano bubble generator include energy storage canister and the booster pump being connected with controller, power input and the electricity of booster pump Source interface connects, and the import of booster pump is connected with aeration water inlet, and the outlet of booster pump and the import of energy storage canister connect, energy storage canister Outlet with aeration outlet connection.
- A kind of 3. big instant water treatment facilities of scale of construction plasma gas-liquid according to claim 1, it is characterised in that：It is described Plasma generator on be provided with cooling device, cooling device and the cooling cycle water out and entrance that are arranged on housing Connection.
- A kind of 4. big instant water treatment facilities of scale of construction plasma gas-liquid according to claim 1, it is characterised in that：It is described Housing in be provided with multilayer rack, the air pump, compression cooling driers, air filter, oxygen molecular sieve processed, oxygen Tank, plasma generator, plasma electrical source, micro-nano bubble generator, controller are respectively arranged at the bottom plate of housing On upper or multilayer rack.
- A kind of 5. big instant water treatment facilities of scale of construction plasma gas-liquid according to claim 1, it is characterised in that：It is described Controller include display control panel and programmable logic controller (PLC), remote communication module, set on display control panel There are the display screen being connected with programmable logic controller (PLC), operational and controlled key button, aeration pressure gauge and aeration flowmeter；The aeration pressure Power table and aeration flowmeter are connected with micro-nano bubble generator.
- 6. according to a kind of big instant water treatment facilities of scale of construction plasma gas-liquid described in claim 1, it is characterised in that：Described Oxygen flow rate adjusting valve is provided with the connecting line of oxygen tank and plasma generator.
- A kind of 7. big instant water treatment facilities of scale of construction plasma gas-liquid according to claim 5, it is characterised in that：It is described Housing on be provided with the cabinet door with visual window, multiple radiator windows and exhaust fan, display of the cabinet door towards controller Control panel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711214117.XA CN108002583A (en) | 2017-11-28 | 2017-11-28 | A kind of big instant water treatment facilities of scale of construction plasma gas-liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711214117.XA CN108002583A (en) | 2017-11-28 | 2017-11-28 | A kind of big instant water treatment facilities of scale of construction plasma gas-liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108002583A true CN108002583A (en) | 2018-05-08 |
Family
ID=62054180
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711214117.XA Withdrawn CN108002583A (en) | 2017-11-28 | 2017-11-28 | A kind of big instant water treatment facilities of scale of construction plasma gas-liquid |
Country Status (1)
| Country | Link |
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| CN (1) | CN108002583A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110759541A (en) * | 2019-11-26 | 2020-02-07 | 南京师范大学 | System and method for treating algal toxins and odor substances in high-algae sediment dehydration filtrate |
| CN110980915A (en) * | 2019-12-23 | 2020-04-10 | 解冰 | Nano oxygen radical water for directionally repairing variant cells and preparation method thereof |
-
2017
- 2017-11-28 CN CN201711214117.XA patent/CN108002583A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110759541A (en) * | 2019-11-26 | 2020-02-07 | 南京师范大学 | System and method for treating algal toxins and odor substances in high-algae sediment dehydration filtrate |
| CN110759541B (en) * | 2019-11-26 | 2022-06-28 | 南京师范大学 | System for treating algal toxins and odor substances in high algae bottom mud dehydration filtrate and removing method |
| CN110980915A (en) * | 2019-12-23 | 2020-04-10 | 解冰 | Nano oxygen radical water for directionally repairing variant cells and preparation method thereof |
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Application publication date: 20180508 |