CN109081423A - A kind of container-type oxidative system and method - Google Patents
A kind of container-type oxidative system and method Download PDFInfo
- Publication number
- CN109081423A CN109081423A CN201811291865.2A CN201811291865A CN109081423A CN 109081423 A CN109081423 A CN 109081423A CN 201811291865 A CN201811291865 A CN 201811291865A CN 109081423 A CN109081423 A CN 109081423A
- Authority
- CN
- China
- Prior art keywords
- oxygenerator
- ejector
- ozone generator
- ozone
- container
- 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
- 230000001590 oxidative effect Effects 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 17
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 72
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000010865 sewage Substances 0.000 claims abstract description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 230000003647 oxidation Effects 0.000 claims abstract description 9
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 9
- 230000008569 process Effects 0.000 claims abstract description 7
- 239000000284 extract Substances 0.000 claims abstract description 4
- 239000000498 cooling water Substances 0.000 claims description 19
- 238000001816 cooling Methods 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000003044 adaptive effect Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- -1 industrial oxidation Substances 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009423 ventilation Methods 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
- 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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/782—Ozone generators
-
- 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
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/784—Diffusers or nozzles for ozonation
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)
Abstract
The present invention relates to a kind of container-type oxidative system and methods, the system includes screw air compressor, oxygenerator, ozone generator, water pump, ejector and haptoreaction pond, screw air compressor, oxygenerator, ozone generator, water pump, ejector and haptoreaction pond are sequentially connected by pipeline, screw air compressor compresses air, and is conveyed to oxygenerator；Oxygenerator generates oxygen, and is conveyed to ozone generator；Ozone generator generates ozone, and is conveyed to ejector；Water pump extracts sewage to be treated, and squeezes into ejector；Ejector forms negative pressure by sewage flow at high speed, sucks ozone, is sufficiently mixed sewage and ozone, is conveyed to haptoreaction pond；Haptoreaction pond is used for oxidation processes.Using technical solution of the present invention, oxygenerator and the integrated function of ozone generator and haptoreaction pond can be realized, to solve the large volume in prior art, low concentration, the disadvantage that transport is cumbersome, stability is low.
Description
Technical field
The present invention relates to water-treatment technology field more particularly to a kind of container-type oxidative systems and method.
Background technique
According to demand currently on the market, drinking water, sewage, urban river water, denitrating flue gas, industrial oxidation, petroleum and petrochemical industry,
The industries such as industrial bleaching, foodstuff preservation, animal husbandry disinfection are all being equipped at catalytic ozonation even depth using ozone generator
Reason technology is handled.
Industry uses panel type ozone producer at present, panel type ozone producer be by electric discharge chamber system, air supply system,
Cooling water system, power-supply system are constituted.The air supply system of ozone generator is oxygen making set system, and oxygen making set system is inhaled using transformation
Attached method prepares oxygen, and ozone generator can effectively improve ozone output using source of oxygen.
With the development in market, it can be seen that demand of the ozone generator in environmental protection industry (epi) sharply increases, thus right
Required by the equipment room of ozone generator just has, and traditional equipment can not meet the demand of existing market.
Summary of the invention
To solve problems of the prior art, the embodiment of the present invention provides a kind of container-type oxidative system and side
Method can be realized oxygenerator and the integrated function of ozone generator and haptoreaction pond, to solve in prior art
Large volume, low concentration, the disadvantage that transport is cumbersome, stability is low.
One side according to an embodiment of the present invention provides a kind of container-type oxidative system, including screw air compressor, oxygen processed
Machine, ozone generator, water pump, ejector and haptoreaction pond, the screw air compressor, oxygenerator, ozone generator, water pump,
Ejector and haptoreaction pond are sequentially connected by pipeline, wherein
Screw air compressor is conveyed to oxygenerator for compressing air；
Oxygenerator is conveyed to ozone generator for generating oxygen；
Ozone generator is conveyed to ejector for generating ozone；
Water pump squeezes into ejector for extracting sewage to be treated；
Ejector sucks ozone, is sufficiently mixed sewage and ozone, is conveyed to contact for allowing sewage flow at high speed to form negative pressure
Reaction tank；
Haptoreaction pond is used for oxidation processes.
It further, further include cooling-water machine, the cooling-water machine is for carrying out cooling heat ozone generator.
Further, the screw air compressor, oxygenerator, ozone generator, water pump, ejector and cooling-water machine are mounted on 6
In rice container, the haptoreaction pond is mounted on the bottom plate of 3 meters of containers, 6 meters of containers and 3 meters of containers
Bottom plate weld together.
It further, further include programmable logic controller (PLC), the programmable logic controller (PLC) and the screw air compressor,
Oxygenerator, ozone generator, water pump, ejector and cooling-water machine are electrically connected, and control the screw rod sky for exporting electric signal
Press, oxygenerator, ozone generator, water pump, ejector and cooling-water machine.
Further, the oxygenerator further comprises a cooling driers, two adsorption towers, an air reservoir, one
Oxygen storage tank and an oxygenerator control cabinet, the oxygenerator control cabinet is connect with the programmable logic controller (PLC), for connecing
By the PLC controls, to control the start and stop of oxygenerator.
Further, the ozone generator further comprises arc chamber, power supply box, transformer and strong and weak electric unit.
Further, the soaked cover of gas-tight is provided in the haptoreaction pond, the soaked cover of gas-tight is for preventing water pump
It is pumped into gas.
It further, further include exhaust hood, the exhaust hood is used to arrange the screw air compressor, oxygenerator and cooling-water machine
Air quantity out is drawn out to the exhaust outlet of container.
Further, the ozone generator is 1kg/h panel type ozone producer.
The other side of the embodiment of the present invention additionally provides a kind of container-type method for oxidation, comprising the following steps:
Screw air compressor passes through pipeline to oxygenerator after compressing air；
Oxygenerator generates oxygen, and by pipeline to ozone generator；
Ozone generator generates ozone, and gives ejector air inlet by pipeline；
The water inlet of water pump extracts sewage outside container, and the water outlet of water pump is docked with ejector water inlet, by sewage transport
To ejector；
The sewage of ejector high speed flowing forms negative pressure, sucks ozone, then export the mixing of sewage and ozone from ejector
Liquid is transported to haptoreaction pond；
Haptoreaction pond carries out oxidation processes to the mixture of ozone and water.
The technical solution that the embodiment of the present invention provides, can effectively improve the utilization rate of product, realize oxygenerator with it is smelly
The integrated function of Oxygen Generator and haptoreaction pond, thus solve the large volume in prior art, low concentration, transport it is numerous
Disadvantage trivial, stability is low facilitates installation, maintains easily, is moved easily, saving space and shorten debugging cycle.
It should be understood that above general description and following detailed description be only it is exemplary and explanatory, not
It can the limitation present invention.
Detailed description of the invention
The drawings herein are incorporated into the specification and forms part of this specification, and shows and meets implementation of the invention
Example, and be used to explain the principle of the present invention together with specification.
Fig. 1 is the schematic diagram of internal structure of container-type oxidative system in the embodiment of the present invention.
Fig. 2 is the outside schematic diagram of container-type oxidative system in the embodiment of the present invention.
Specific embodiment
Example embodiments are described in detail here, and the example is illustrated in the accompanying drawings.Following description is related to
When attached drawing, unless otherwise indicated, the same numbers in different drawings indicate the same or similar elements.Following exemplary embodiment
Described in embodiment do not represent all embodiments consistented with the present invention.On the contrary, they be only with it is such as appended
The example of system and related application, method being described in detail in claims, some aspects of the invention are consistent.
Fig. 1 is the schematic diagram of internal structure of container-type oxidative system in the embodiment of the present invention.Fig. 2 is reality of the invention
Apply the outside schematic diagram of container-type oxidative system in example.As depicted in figs. 1 and 2, which includes screw rod
Air compressor machine 1, oxygenerator 2, ozone generator 3, cooling-water machine 4, water pump 5, ejector 7 and haptoreaction pond 6 and programmable logic
Controller.Wherein ozone generator is 1kg/h panel type ozone producer, and water pump is horizontal pump.
Screw air compressor, oxygenerator, ozone generator, water pump, ejector and cooling-water machine are mounted in 6 meters of containers, are connect
Touching reaction tank is mounted on the bottom plate of 3 meters of containers, and the bottom plate of 6 meters of containers and 3 meters of containers welds together, whole system
Outer dimension be 9 × 2.4 × 2.9 meters.6 meters of internal containers do heat preservation noise reduction, illumination and ventilation Air exhaust.
Screw air compressor, oxygenerator, ozone generator, water pump, ejector and haptoreaction pond are sequentially connected by pipeline.
Programmable logic controller (PLC) and screw air compressor, oxygenerator, ozone generator, water pump, ejector and cooling-water machine point
It is not electrically connected, output electric signal control screw air compressor, oxygenerator, ozone generator, water pump, ejector and cooling-water machine.
Oxygenerator includes a cooling driers, two adsorption towers, an air reservoir, an oxygen storage tank and an oxygenerator
Control cabinet, oxygenerator control cabinet are connect with programmable logic controller (PLC), receive PLC controls, to control oxygen processed
The start and stop of machine.
Ozone generator includes arc chamber, power supply box, transformer and strong and weak electric unit.Cooling-water machine carries out ozone generator
Cooling heat dissipation, i.e., the type of cooling of interior recirculated water is to give cooling heat dissipation by cooling-water machine module in Ozone generator module.
The soaked cover of gas-tight is provided in haptoreaction pond, the soaked cover of gas-tight can prevent water pump to be pumped into gas, to influence
Reaction effect.
Exhaust hood is additionally included, which can draw the air quantity that screw air compressor, oxygenerator and cooling-water machine are discharged
The exhaust outlet of container is arrived out.
The operating process of the container-type oxidative system is described below:
First screw air compressor air is compressed after by pipeline to oxygenerator, the cooling driers in oxygenerator are cooling by air
It is dry, then deliver air in two adsorption towers of oxygenerator, it is handed over by two adsorption towers of PLC controls
Oxygen is produced for absorption, the oxygen that oxygenerator generates is pipelined to ozone generator, the cooling of screw air compressor and oxygenerator
Mode is air-cooled.
35mg/l~150mg/l ozone that ozone generator generates gives ejector air inlet by pipeline.
The water inlet of water pump extracts sewage outside container, and the water outlet of water pump is docked with ejector water inlet, by sewage
It is conveyed to ejector.
The sewage of ejector high speed flowing forms negative pressure, sucks ozone, then from ejector outlet by sewage and ozone
Mixing liquid is transported to haptoreaction pond；
Haptoreaction pond carries out oxidation processes to the mixture of ozone and water, to realize processing sewage.
Using the technical solution in above-described embodiment, the utilization rate of product can be effectively improved, realize oxygenerator with it is smelly
The integrated function of Oxygen Generator and haptoreaction pond, thus solve the large volume in prior art, low concentration, transport it is numerous
Disadvantage trivial, stability is low facilitates installation, maintains easily, is moved easily, and saves space and shortens debugging cycle.
Those skilled in the art after considering the specification and implementing the invention disclosed here, will readily occur to of the invention its
Its embodiment.This application is intended to cover any variations, uses, or adaptations of the invention, these modifications, purposes or
Person's adaptive change follows general principle of the invention and including the undocumented common knowledge in the art of the present invention
Or conventional techniques.
It should be understood that the present invention is not limited to the precise structure already described above and shown in the accompanying drawings, and
And various modifications and changes may be made without departing from the scope thereof.The scope of the present invention is limited only by the attached claims.
Claims (10)
1. a kind of container-type oxidative system, which is characterized in that including screw air compressor, oxygenerator, ozone generator, water pump,
Ejector and haptoreaction pond, the screw air compressor, oxygenerator, ozone generator, water pump, ejector and haptoreaction pond are logical
Piping is sequentially connected, wherein
Screw air compressor is conveyed to oxygenerator for compressing air；
Oxygenerator is conveyed to ozone generator for generating oxygen；
Ozone generator is conveyed to ejector for generating ozone；
Water pump squeezes into ejector for extracting sewage to be treated；
Ejector sucks ozone, is sufficiently mixed sewage and ozone, is conveyed to contact for allowing sewage flow at high speed to form negative pressure
Reaction tank；
Haptoreaction pond is used for oxidation processes.
2. container-type oxidative system according to claim 1, which is characterized in that it further include cooling-water machine, the cooling-water machine
For being carried out cooling heat to ozone generator.
3. container-type oxidative system according to claim 2, which is characterized in that the screw air compressor, oxygenerator, smelly
Oxygen Generator, water pump, ejector and cooling-water machine are mounted in 6 meters of containers, and the haptoreaction pond is mounted on 3 meters of containers
On bottom plate, the bottom plate of 6 meters of containers and 3 meters of containers welds together.
4. container-type oxidative system according to claim 2, which is characterized in that it further include programmable logic controller (PLC),
The programmable logic controller (PLC) and the screw air compressor, oxygenerator, ozone generator, water pump, ejector and cooling-water machine point
It is not electrically connected, controls the screw air compressor, oxygenerator, ozone generator, water pump, ejector and cold water for exporting electric signal
Machine.
5. container-type oxidative system according to claim 4, which is characterized in that the oxygenerator further comprises one
Cooling driers, two adsorption towers, an air reservoir, an oxygen storage tank and an oxygenerator control cabinet, the oxygenerator control
Case is connect with the programmable logic controller (PLC), for receiving the PLC controls, to control oxygenerator
Start and stop.
6. container-type oxidative system according to claim 1, which is characterized in that the ozone generator further comprises
Arc chamber, power supply box, transformer and strong and weak electric unit.
7. container-type oxidative system according to claim 1, which is characterized in that be provided in the haptoreaction pond anti-
Air-bubble cover, the soaked cover of gas-tight is for preventing water pump to be pumped into gas.
8. container-type oxidative system according to claim 3, which is characterized in that it further include exhaust hood, the exhaust hood
Air quantity for the screw air compressor, oxygenerator and cooling-water machine to be discharged is drawn out to the exhaust outlet of container.
9. container-type oxidative system according to claim 1, which is characterized in that the ozone generator is 1kg/h plate
Formula ozone generator.
10. a kind of container-type method for oxidation, which comprises the following steps:
Screw air compressor passes through pipeline to oxygenerator after compressing air；
Oxygenerator generates oxygen, and by pipeline to ozone generator；
Ozone generator generates ozone, and gives ejector air inlet by pipeline；
The water inlet of water pump extracts sewage outside container, and the water outlet of water pump is docked with ejector water inlet, by sewage transport
To ejector；
The sewage of ejector high speed flowing forms negative pressure, sucks ozone, then export the mixing of sewage and ozone from ejector
Liquid is transported to haptoreaction pond；
Haptoreaction pond carries out oxidation processes to the mixture of ozone and water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811291865.2A CN109081423A (en) | 2018-10-31 | 2018-10-31 | A kind of container-type oxidative system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811291865.2A CN109081423A (en) | 2018-10-31 | 2018-10-31 | A kind of container-type oxidative system and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109081423A true CN109081423A (en) | 2018-12-25 |
Family
ID=64844602
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811291865.2A Pending CN109081423A (en) | 2018-10-31 | 2018-10-31 | A kind of container-type oxidative system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109081423A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111056715A (en) * | 2020-01-10 | 2020-04-24 | 中际晟丰环境工程技术集团有限公司 | Container type ozone advanced oxidation combined system for treating refractory organic wastewater |
| CN111099714A (en) * | 2019-12-29 | 2020-05-05 | 广州易能克科技有限公司 | Micro-bubble sewage treatment device produced by ozone jet friction |
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| CL2007003681A1 (en) * | 2006-12-29 | 2008-05-30 | Purfresh Inc | CONTAINER FOR SHIPMENT FOR THE TRANSPORTATION OF PERECIBLE PRODUCTS THAT INCLUDES AN ADAPTED TRANSPORT ENVIRONMENT, GAS CIRCULATION MEDIA, A COOLING UNIT, AN OZONE GENERATOR, AN OZONE INJECTOR, SENSOR MEDIA AND A MED |
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2018
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111099714A (en) * | 2019-12-29 | 2020-05-05 | 广州易能克科技有限公司 | Micro-bubble sewage treatment device produced by ozone jet friction |
| CN111056715A (en) * | 2020-01-10 | 2020-04-24 | 中际晟丰环境工程技术集团有限公司 | Container type ozone advanced oxidation combined system for treating refractory organic wastewater |
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181225 |
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