CN205867958U - Energy -saving multiple -effect VOCs purified reaction ware - Google Patents
Energy -saving multiple -effect VOCs purified reaction ware Download PDFInfo
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- CN205867958U CN205867958U CN201620886535.8U CN201620886535U CN205867958U CN 205867958 U CN205867958 U CN 205867958U CN 201620886535 U CN201620886535 U CN 201620886535U CN 205867958 U CN205867958 U CN 205867958U
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Abstract
The utility model discloses an energy -saving multiple -effect VOCs purified reaction ware, this VOCs purified reaction ware includes the ware body, the internal tapered hood that has installed of ware, leave the clearance between the inner wall of the tapered hood and the ware body, tapered hood separates the inner chamber of the ware body catalytic oxidation room that sprays the absorption chamber with be located upper portion that becomes to be located the lower part, VOCs intake pipe of sub -unit connection of absorption chamber sprays, the upper portion that sprays the absorption chamber is connected one and is used for to spraying the absorption system that sprays who sprays the medicament in the absorption chamber, the catalytic oxidation indoor location has the ultraviolet lamp, VOCs intake pipe facial make -up is equipped with an ozone VOCs mixing arrangement, this ozone VOCs mixing arrangement connects an ozone generator, the gas vent is installed at the top of the ware body, connect ozone tail gas on -line detector on the pipeline of this gas vent, the entire system operation is controlled through the PLC controller. This VOCs purified reaction ware VOCs handles high -efficiently, thorough, and system energy consumption and equipment running cost are low.
Description
Technical field
This utility model belongs to gas pollutant processing technology field, particularly relates to a kind of energy-saving multi-effect VOCs and purifies anti-
Answer device.
Background technology
Along with quickly propelling of Chinese Urbanization and process of industrialization, the discharge capacity of organic exhaust gas is increasing, and air is dirty
Dye is on the rise, and the volatile organic matter (VOCs) in surrounding air is substantially improved.Volatile organic matter is that China's air is crucial
Pollutant PM2.5 and O3The important as precursors thing formed, easily intercouples with other atmosphere pollution, and the new pollutant formed are difficult
With natural decomposition, it is the most lasting to endanger.Additionally, it can also participate in photochemical reaction, cause photochemical pollution.Organic exhaust gas
Often with stench, not only human body and various sense organ there are is stimulation, and there is certain toxicity, health is caused
Harm greatly.The improvement that eliminates of organic exhaust gas is a urgent and important job, becomes difficult point and the focus of current research.
At present, more technique such as the activated carbon adsorption of TREATMENT OF VOCs application, it is catalyzed burning etc. actually used
During still suffer from certain limitation, it is difficult to the Abgasgesetz and the people that meet increasingly stringent compel improving air quality
Highly necessary ask.As absorption method can not fundamentally eliminate pollutant, its desorption equipment, control system and desorption operating cost are high, inhale
Attached dose saturated after need regeneration or change.Production by Catalytic Combustion Process is generally with noble metal as catalyst, and cost is high；Need to be in hot environment
Under carry out there is potential safety hazard and catalyst easy in inactivation；Organic exhaust gas concentration is relatively low needs outside heat to maintain burning.
Utility model content
Technical problem to be solved in the utility model is, overcomes the deficiency and defect mentioned in background above technology, carries
For a kind of energy-saving multi-effect VOCs purification reactor, this VOCs purification reactor is by spray-absorption technology and compound homogeneous catalysis oxygen
Changing further treatment technique to combine, VOCs processes efficiently, thoroughly.
For solving above-mentioned technical problem, the technical scheme that the utility model proposes is:
A kind of energy-saving multi-effect VOCs purification reactor, including body, is equiped with cone-shaped hood, described taper in described body
Leaving gap between cover and the inwall of body, the inner chamber of body is separated into and is positioned at the spray-absorption room of bottom and is positioned at by cone-shaped hood
The catalysis oxidizing chamber on top, the bottom of described spray-absorption room connects a VOCs air inlet pipe, and the top of spray-absorption room connects one
Uviol lamp, VOCs air inlet pipe are installed in the spray-absorption system of spray-absorption household sprays medicament, described catalysis oxidizing chamber
On be equiped with an ozone VOCs mixing arrangement, this ozone VOCs mixing arrangement connects an ozonator.
Above-mentioned energy-saving multi-effect VOCs purification reactor a, it is preferred that air vent is offered at the top of described body, this row
Connect an ozone tail gas monitor, described ozone tail gas monitor and a PLC at QI KOU to connect.
Above-mentioned energy-saving multi-effect VOCs purification reactor, it is preferred that described spray-absorption system includes being installed in described
The shower nozzle on top, spray-absorption room and the spray liquid liquid storage tank being connected with described shower nozzle by pipeline, shower nozzle and spray liquid liquid storage tank
On the pipeline connected, a spray pump is installed.
Above-mentioned energy-saving multi-effect VOCs purification reactor, it is preferred that the bottom of described body connects a spray liquid and reclaims
Pipe, the other end of described spray liquid recovery tube connects a spray liquid to reclaiming and carries out oil, water, the three-phase of solid three phase separation
Separator, the outlet of described three phase separator connects with spray liquid liquid storage tank.
Above-mentioned energy-saving multi-effect VOCs purification reactor, it is preferred that be equiped with for examining on described spray liquid liquid storage tank
The liquidometer of liquid level in survey pond, this liquidometer and spray pump are all connected with PLC.
Above-mentioned energy-saving multi-effect VOCs purification reactor, it is preferred that described cone-shaped hood is hollow structure, under cone-shaped hood
Side, portion offers the cooling water inlet of the inner space with cone-shaped hood, and opposite side offers the cold of the inner space with cone-shaped hood
But water out.
Above-mentioned energy-saving multi-effect VOCs purification reactor, it is preferred that described uviol lamp is microwave electrodeless lamp, ultraviolet
Lamp is multiple, and multiple uviol lamps are arranged on the top of described catalysis oxidizing chamber.
Compared with prior art, the utility model has the advantage of:
(1) spray-absorption technology is combined by this utility model with compound homogeneous catalysis oxidation depth treatment technology, the most right
VOCs carries out absorbing, oxidoreduction pretreatment, removes oil droplet therein, solid matter and major part VOCs, passes through light the most again
Catalytic reaction carries out advanced treating, and VOCs processes highly efficient, thorough.
(2) use cone-shaped hood can realize the cyclonic separation of oil droplet, float, enhance oil, dust from fluid-mechanics point of view
Separate, removal effect, ozone and VOCs mixed gas at the spiral of cone-shaped hood pretreatment chamber, sinking, limited away from
From the interior flow velocity increasing gas to greatest extent, strengthen its turbulent condition, beneficially gas-liquid mixed, strengthen assimilation effect, compare
In traditional spray-absorption technique, purification reactor of the present utility model is higher to exhaust emission absorption efficiency, compared to biography
The ozone oxidation tower of system, operating cost is lower, and removal effect is more preferable.
(3) the ozone tail gas concentration in expellant gas is carried out by being located at the ozone tail gas monitor of exhaust ports
Line is monitored, detection signal feedback PLC, and discharge power and the oxygen amount of including in by PLC control ozonator are to smelly
The intake of oxygen is adjusted, it is ensured that VOCs can reduce system energy consumption simultaneously with qualified discharge, saved equipment after treatment
Operating cost.
(4), after the drop after spray-absorption crashes into the bottom of purification reactor, three-phase is entered by spray liquid recovery tube
Separator, separates the oil in recovered liquid, water and solid, and will wherein include water the going out from three phase separator of medicament
The mouth of a river enters spray liquid liquid storage tank after discharging, it is achieved that recycling spray liquid, the operation that reduce further equipment becomes
This.
(5) on spray liquid liquid storage tank, it is provided for the liquidometer of liquid level in detection cell, and by spray pump and should
Liquidometer is connected with PLC, and PLC receives liquid level signal and controls spray pump according to this liquid level signal
Medicament is sprayed, it is achieved that the automated job of this spray-absorption system in purification reactor.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is this
Some embodiments of utility model, for those of ordinary skill in the art, on the premise of not paying creative work, also
Other accompanying drawing can be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of this utility model VOC purification reactor.
Marginal data:
1, body；2, cone-shaped hood；3, spray-absorption room；4, catalysis oxidizing chamber；5, VOCs air inlet pipe；6, uviol lamp；7, smelly
Oxygen VOCs mixing arrangement；8, ozonator；9, air vent；10, ozone tail gas monitor；11, PLC；12, shower nozzle；
13, spray liquid liquid storage tank；14, spray pump；15, spray liquid recovery tube；16, three phase separator；17, liquidometer；18, cooling water enters
Mouthful；19, coolant outlet.
Detailed description of the invention
For the ease of understanding this utility model, below in conjunction with Figure of description and preferred embodiment to this utility model
Make more comprehensively, describe meticulously, but protection domain of the present utility model is not limited to embodiment in detail below.
It should be strongly noted that when a certain element is described as on " be connected to or be communicated in " another element, it can
Being to be directly connected to or connect on another element, it is also possible to be to be indirectly connected with by other intermediate connectors or connect at another
On element.
Unless otherwise defined, the implication that all technical term used hereinafter is generally understood that with those skilled in the art
Identical.Technical term used herein is intended merely to describe the purpose of specific embodiment, is not intended to limit this practicality
Novel protection domain.
Unless otherwise specified, the various raw materials used in this utility model, reagent, instrument and equipment etc. all can lead to
Cross market to be commercially available or can be prepared by existing method.
Embodiment
A kind of embodiment of this utility model energy-saving multi-effect VOCs purification reactor, this VOCs purification reactor passes through will
Spray-absorption technology combines with compound homogeneous catalysis oxidation depth treatment technology, removes the volatilization in gas thoroughly, efficiently
Property Organic substance (VOCs).As it is shown in figure 1, as seen from Figure 1, it mainly includes body 1 to the structure of this VOCs purification reactor, this device
Being equiped with the cone-shaped hood 2 of in body 1, the vertex of a cone of this cone-shaped hood 2 upward, leaves gap between the inwall of cone-shaped hood 2 and body 1,
Air-flow can enter the top of purification reactor from the gap between cone-shaped hood 2 and wall.The inner chamber of body 1 is separated by cone-shaped hood 2
Becoming to be positioned at the spray-absorption room 3 of bottom and superposed catalysis oxidizing chamber 4, the bottom of spray-absorption room 3 connects a VOCs and enters
Trachea 5, the dusty gas containing VOCs enters in spray-absorption room 3 from this VOCs air inlet pipe 5.The top of spray-absorption room 3 connects
Spray-absorption system, this spray-absorption system absorbs medicament (spray liquid) for spraying in spray-absorption room 3.VOCs air inlet pipe
Being equiped with ozone VOCs mixing arrangement 7 on 5, this ozone VOCs mixing arrangement 7 connects an ozonator 8, and ozonator 8 produces
Ozone is also mixed with VOCs air-flow at VOCs air inlet pipe 5 by raw ozone by ozone VOCs mixing arrangement 7.Containing ozone
VOCs gas formed after VOCs air inlet pipe 5 enters spray-absorption room 3 along cone-shaped hood 2 rise outward turning VOCs air-flow, should
VOCs air-flow does spiral-flow type ascending motion along cone-shaped hood 2, forms conical cyclone, and its tangential velocity is gradually increased from inside to outside, can
Effectively realize Oil-gas Separation.Condensing after the inwall of droplets contact cone-shaped hood 2, the inwall along cone-shaped hood 2 flows down, and enters spray liquid storage
Liquid pool 13, separates eventually through three phase separator 16.After rotating the top of the VOCs air-flow arrival cone-shaped hood 2 risen then along cone
The axle center of shape cover 2 is downward, forms downward interior rotational gas flow, and air-flow runs at the top of cone-shaped hood 2 and sprays from spray-absorption system
The medicament gone out, VOCs therein absorbs with medicament generation and crashes into the bottom of purification reactor after redox reaction with medicament,
Complete the pretreatment to VOCs gas.Subsequently, VOCs air-flow is along the catalysis oxygen on the entrance top, gap between cone-shaped hood 2 and wall
Changing in room 4, be provided with uviol lamp 6 in this catalysis oxidizing chamber 4, by the irradiation of this uviol lamp 6, the VOCs in catalysis gas is with smelly
Oxygen generation light-catalyzed reaction, removes the VOCs in gas further, VOCs gas is carried out advanced treating, and this uviol lamp 6 is preferred
Using microwave electrodeless lamp, this microwave electrodeless lamp excites ultraviolet light by variable frequency microwave, and its radiation wavelength can be with
Time fluctuation, microwave frequency can reach 3000MHz so that the ultraviolet light that uviol lamp sends fluctuates near 200nm high-amplitude wave, thus
Produce mixing light intensity ultraviolet radiation, enhance the catalysis efficiency of ozone.This VOCs purification reactor uses cone-shaped hood 2 to lead
Stream so that the VOCs air-flow entered in spray-absorption room 3 flows in the way of eddy flow mixing, strengthens air-liquid mass-transfer efficiency, by force
Change pretreating effect；Cone-shaped hood 2 uses the vertex of a cone to arrange upward, make use of ascending air in the flow velocity difference at bottom and top,
Strengthening VOCs air-flow and the mixing of spray liquid, further enhancing spray-absorption effect；This purification reactor is by spray-absorption skill
Art combines with compound homogeneous catalysis oxidation depth treatment technology, VOCs air-flow first carries out in spray-absorption room 3 spray and inhales
Receipts, oxidoreduction pretreatment, carry out photochemical catalytic oxidation advanced treating in then entering back into catalysis oxidizing chamber 4, substantially increase
VOCs treatment efficiency.
In the present embodiment, the top of body 1 is provided with an air vent 9, connects an ozone tail gas monitor at this air vent 9
10, ozone tail gas monitor 10 is connected with a PLC 11, and PLC 11 is connected with ozonator 8.At catalysis oxygen
Change the interior gas after photocatalysis removes VOCs in room 4 to discharge from air vent 9, be located at the ozone tail gas monitor 10 at air vent 9
Ozone tail gas concentration in expellant gas is carried out on-line monitoring, ozone tail gas monitor 10 generates ozone tail gas concentration letter
Number and by this ozone tail gas concentration signal send to PLC 11, PLC 11 is according to the ozone tail gas concentration received
Signal adjusts discharge frequency (power) and the oxygen amount of including in of ozonator 8, and then to the ozone being passed through in purification reactor
Amount (ozone dosage) is adjusted, and makes VOCs with qualified discharge, and can reduce system energy consumption after treatment, saves and set
Standby operating cost.
In the present embodiment, spray-absorption system includes the multiple shower nozzles 12 being installed in top, spray-absorption room 3 and by pipe
The spray liquid liquid storage tank 13 that road is connected with shower nozzle 12, the pipeline that this shower nozzle 12 is connected with spray liquid liquid storage tank 13 is provided with a spray
Drenching pump 14, this spray pump 14 is interior to spray-absorption room 3 for the spray liquid in spray liquid liquid storage tank 13 is pressed into spray-absorption room 3
Interior VOCs carries out spray-absorption.The bottom of body 1 connects a spray liquid recovery tube 15, the other end of this spray liquid recovery tube 15
Being connected with an oil, water, solid three phase separator 16, the outlet of this three phase separator 16 connects with spray liquid liquid storage tank 13.Right
Medicine after VOCs carries out absorption and redox reaction drips the bottom crashing into purification reactor, via the leakage fluid dram of purification reactor
Enter spray liquid recovery tube 15 after discharge, then through three phase separator 16, oil, water and the solid in the spray liquid of recovery is carried out
Separate.Isolated Oil Recovery utilizes, and solid matter is recyclable or does final disposal, wherein includes the water of medicament from three-phase
The outlet of separator 16 enters spray liquid liquid storage tank 13 after discharging, it is achieved that recycles spray liquid, reduces further
The operating cost of equipment.
In the present embodiment, spray liquid liquid storage tank 13 is equiped with liquidometer 17, spray pump 14 and this liquidometer 17 all with
PLC 11 connects, and liquidometer 17, for detecting the liquid level in spray liquid liquid storage tank 13, generates liquid level signal also
Being sent by this liquid level signal to PLC 11, PLC 11 controls spray according to the liquid level signal received
Pump 14 sprays medicament in purification reactor, it is achieved that the automated job of this spray-absorption system.
In the present embodiment, cone-shaped hood 2 is hollow structure, and the side, bottom of cone-shaped hood 2 offers cooling water inlet 18, another
Side offers coolant outlet 19, this cooling water inlet 18 and coolant outlet 19 all with the inner space of cone-shaped hood 2.This purification
When reactor runs, it is passed through cooling water from cooling water inlet 18 and VOCs air-flow is cooled down.This cone-shaped hood 2 uses hollow to set
Meter, utilizes convection type cooling medium endless form, and the VOCs air-flow containing colloid or oil droplet encounters taper in eddy flow uphill process
The wall of cover 2 condenses rapidly, and oil droplet therein or colloidal substance import the end of purification reactor along the wall of cone-shaped hood 2
Portion, separates through oil, water, solid three phase separator 16.
The operation principle of this VOCs purification reactor is: VOCs air-flow in VOCs air inlet pipe 5 enters spray-absorption room 3,
VOCs gas mixes with ozone beforehand through ozone VOCs mixing arrangement 7 in VOCs air inlet pipe 5, containing the VOCs of ozone
Gas forms the outward turning VOCs air-flow of rising under the effect of cone-shaped hood 2, forms conical cyclone, its tangential velocity from inside to outside by
Cumulative greatly, it is achieved Oil-gas Separation.In cone-shaped hood 2, constantly it is passed through condensed water from cooling water inlet 18, VOCs air-flow is carried out cold
But, the VOCs air-flow containing colloid or oil droplet condenses rapidly after encountering the wall of cone-shaped hood 2 in eddy flow uphill process, oil therein
Drip or colloidal substance flows into the bottom of purification reactor along the wall of cone-shaped hood 2, then enter through oil, water, solid three phase separator 16
Row separates, and cooling water is discharged from the coolant outlet 19 being positioned at cone-shaped hood 2 opposite side.Rotate the VOCs air-flow risen and arrive cone
The axle center of the top tailing edge cone-shaped hood 2 of shape cover 2 then downwards, form the interior rotational gas flow declined, beneficially ozone, spray liquid,
VOCs and effective mixing of middle catabolite.Air-flow runs into the spray liquid from shower nozzle 12 ejection at the top of cone-shaped hood 2, wherein
VOCs and spray liquid, ozone occurs to absorb and after redox reaction, drip the bottom crashing into purification reactor with medicine.Ozone with
After the mixing of VOCs gas, reacted with VOCs by modes such as electrophilic addition, oxygen-derived free radicals oxidations, thus by the Organic substance in waste gas
Hydroxylating, strengthens its water solublity, thus strengthens the spray-absorption preprocessing process removal effect to VOCs.Spray liquid uses alkalescence
Liquid and add the oxidizing liquid of hydroxyl, can be strengthened organic absorption by hydrogen bond action, meanwhile, spray process
Middle spray liquid and the ozone contact in VOCs gas, it is achieved heterocatalysis aoxidizes, and strengthening absorbs.By spray-absorption pretreatment
After, the VOCs concentration in VOCs air-flow can reduce by more than 80%.Subsequently, gas is along between the inwall of cone-shaped hood 2 and body 1
Gap ascends into the catalysis oxidizing chamber 4 being positioned at top, spray-absorption room 3.VOCs air-flow after pretreatment is at catalysis oxidizing chamber
By the irradiation of microwave electrodeless lamp 6 in 4, there is light-catalyzed reaction with VOCs, to air-flow in the ozone contained in catalysis gas
In VOCs carry out advanced treating, the gas after light-catalyzed reaction is discharged from the air vent 9 being positioned at body 1 top.The row of being located at
Ozone tail gas concentration in ozone tail gas monitor 10 on-line monitoring expellant gas at QI KOU 9 generates ozone tail gas concentration letter
Number, PLC 11 adjusts power and the oxygen amount of including in of ozonator 8 according to this ozone tail gas concentration signal, and then right
The ozone amount being passed through in purification reactor is adjusted.Crash at the bottom of purification reactor after spray-absorption in spray-absorption room 3
The liquid in portion enters in three phase separator 16, after separating the oil in liquid, water and solid by spray liquid recovery tube 15
Discharging respectively, wherein, the water containing medicament enters in entering spray liquid liquid storage tank 13 after the outlet of three phase separator 16 is discharged
Row recycles.It is high that liquid level in pond is detected and generate liquid level by the liquidometer 17 being located in spray liquid liquid storage tank 13
Degree signal, PLC 11 controls spray pump 14 according to the liquid level signal received and sprays medicament in purification reactor.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model, for this
For the technical staff in field, this utility model can have various modifications and variations.All in spirit of the present utility model and principle
Within, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (7)
1. an energy-saving multi-effect VOCs purification reactor, including body (1), it is characterised in that: described body is equiped with in (1)
Cone-shaped hood (2), leaves gap between the inwall of described cone-shaped hood (2) and body (1), the inner chamber of body (1) is divided by cone-shaped hood (2)
It is divided into spray-absorption room (3) and the superposed catalysis oxidizing chamber (4) being positioned at bottom, the bottom of described spray-absorption room (3)
Connect a VOCs air inlet pipe (5), top connection one spray of spraying agent in spray-absorption room (3) of spray-absorption room (3)
Absorption system, is provided with uviol lamp (6) in described catalysis oxidizing chamber (4), VOCs air inlet pipe (5) is equiped with an ozone VOCs and mixes
Locking device (7), this ozone VOCs mixing arrangement (7) connects an ozonator (8).
Energy-saving multi-effect VOCs purification reactor the most according to claim 1, it is characterised in that: the top of described body (1)
Portion offers an air vent (9), and this air vent (9) place connects an ozone tail gas monitor (10), described ozone tail gas monitor
(10) it is connected with a PLC (11).
Energy-saving multi-effect VOCs purification reactor the most according to claim 2, it is characterised in that: described spray-absorption system
Including the shower nozzle (12) being installed in described spray-absorption room (3) top and the spray liquid being connected with described shower nozzle (12) by pipeline
Liquid storage tank (13), the pipeline that shower nozzle (12) is connected with spray liquid liquid storage tank (13) is provided with a spray pump (14).
Energy-saving multi-effect VOCs purification reactor the most according to claim 3, it is characterised in that: the end of described body (1)
Portion connects a spray liquid recovery tube (15), and the other end of described spray liquid recovery tube (15) connects a spray liquid to reclaiming and enters
Row oil, water, the three phase separator (16) of solid three phase separation, the outlet of described three phase separator (16) and spray liquid liquid storage tank
(13) connection.
Energy-saving multi-effect VOCs purification reactor the most according to claim 4, it is characterised in that: described spray liquid liquid storage tank
(13) liquidometer (17) of liquid level in detection cell, this liquidometer (17) and spray pump (14) it are equiped with on all and PLC
Controller (11) connects.
Energy-saving multi-effect VOCs purification reactor the most according to claim 1, it is characterised in that: described cone-shaped hood (2) is
Hollow structure, the side, bottom of cone-shaped hood (2) offers the cooling water inlet (18) of the inner space with cone-shaped hood (2), another
Side offers the coolant outlet (19) of the inner space with cone-shaped hood (2).
7. according to the energy-saving multi-effect VOCs purification reactor according to any one of claim 1-6, it is characterised in that: described purple
Outer lamp (6) is microwave electrodeless lamp, and uviol lamp (6) is multiple, and multiple uviol lamps (6) are arranged on described catalysis oxidizing chamber (4)
Top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620886535.8U CN205867958U (en) | 2016-08-16 | 2016-08-16 | Energy -saving multiple -effect VOCs purified reaction ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620886535.8U CN205867958U (en) | 2016-08-16 | 2016-08-16 | Energy -saving multiple -effect VOCs purified reaction ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205867958U true CN205867958U (en) | 2017-01-11 |
Family
ID=57703341
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620886535.8U Withdrawn - After Issue CN205867958U (en) | 2016-08-16 | 2016-08-16 | Energy -saving multiple -effect VOCs purified reaction ware |
Country Status (1)
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| CN (1) | CN205867958U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106039956A (en) * | 2016-08-16 | 2016-10-26 | 长沙威保特环保科技股份有限公司 | Energy-saving multi-effect VOCs purification reactor and VOCs purification treatment method |
| CN108479796A (en) * | 2018-03-22 | 2018-09-04 | 广东工业大学 | A kind of cleaning equipment and its purification method of photochemical catalyst and volatile organic matter |
| WO2020083171A1 (en) * | 2018-10-22 | 2020-04-30 | 上海必修福企业管理有限公司 | Ozone purification system and method for engine exhaust gas |
| CN111569625A (en) * | 2020-05-08 | 2020-08-25 | 北京建工环境修复股份有限公司 | System and method for in-situ removing and purifying peculiar smell in pesticide polluted site |
-
2016
- 2016-08-16 CN CN201620886535.8U patent/CN205867958U/en not_active Withdrawn - After Issue
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106039956A (en) * | 2016-08-16 | 2016-10-26 | 长沙威保特环保科技股份有限公司 | Energy-saving multi-effect VOCs purification reactor and VOCs purification treatment method |
| CN106039956B (en) * | 2016-08-16 | 2018-05-08 | 长沙威保特环保科技股份有限公司 | A kind of energy-saving multi-effect VOCs purification reactors and VOCs purifying treatment methods |
| CN108479796A (en) * | 2018-03-22 | 2018-09-04 | 广东工业大学 | A kind of cleaning equipment and its purification method of photochemical catalyst and volatile organic matter |
| WO2020083171A1 (en) * | 2018-10-22 | 2020-04-30 | 上海必修福企业管理有限公司 | Ozone purification system and method for engine exhaust gas |
| WO2020083164A1 (en) * | 2018-10-22 | 2020-04-30 | 上海必修福企业管理有限公司 | Engine tail gas ozone purifying system and method |
| WO2020083169A1 (en) * | 2018-10-22 | 2020-04-30 | 上海必修福企业管理有限公司 | Engine exhaust ozone purification system and method |
| WO2020083167A1 (en) * | 2018-10-22 | 2020-04-30 | 上海必修福企业管理有限公司 | Engine exhaust ozone purification system and method |
| CN111569625A (en) * | 2020-05-08 | 2020-08-25 | 北京建工环境修复股份有限公司 | System and method for in-situ removing and purifying peculiar smell in pesticide polluted site |
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