CN207462990U - It is desorbed the recycling of steam organic matter and fixed gas purifying integration device - Google Patents
It is desorbed the recycling of steam organic matter and fixed gas purifying integration device Download PDFInfo
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- CN207462990U CN207462990U CN201721314315.9U CN201721314315U CN207462990U CN 207462990 U CN207462990 U CN 207462990U CN 201721314315 U CN201721314315 U CN 201721314315U CN 207462990 U CN207462990 U CN 207462990U
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- fluid
- condensing plant
- subsequent purification
- housing
- catch box
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Abstract
A kind of desorption steam organic matter recycling and fixed gas purifying integration device, it is characterized in that, subsequent purification device including condensing plant and condensing plant downstream, wherein, the condensing plant includes condensing plant housing, condensing plant housing is equipped with fluid inlet and fluid outlet, is equipped with gas channel and the condensed fluid pipeline in condensing plant housing, and condensed fluid is exchanged heat by your cold fluid line with air-flow；Subsequent purification device is equipped with spray washing device, ultraviolet photolysis device, demister successively.The utility model device is suitable for the industries volatile organic matters (VOCs) such as organic chemical industry, medication chemistry, coating and printing ink product, rubber plastic product, textile printing and dyeing and is administered using the cleaning of absorbing process desorption steam.The organic efficiency of VOCs reaches more than 70%, and condensed fixed gas purification efficiency reaches more than 90%.
Description
Technical field
The utility model discloses a kind of desorption steam organic solvent recycling and fixed gas purifying integration device, available for having
The recycling of solvent, while purified treatment is carried out to fixed gas, belong to volatile organic matter pollution control technology field.
Background technology
The discharge of control volatile organic compounds (VOCs) is to improve the major tasks of China's atmosphere quality.Big portion
VOCs is divided not only itself to there is stronger toxicity, but also is important as precursors object and the participation for influencing China's regional atmospheric combined pollution
Object.Fine particle (PM2.5) and ozone (O3), are also tied in a hundred and one ways with VOCs.For this purpose, country has formulated the relevant technologies
Policy control VOCs pollutions, to improve atmosphere quality, safeguard health of people and improve the quality of living.
When middle low concentration VOCs exhaust gas has recovery value, adsorption technology recovery processing is most common process program.It is common
Method to be VOCs exhaust gas first adsorbed using activated carbon or carbon fiber, gas is purified；Activated carbon or carbon fiber reach
Saturation or during close to saturation, is purged using 130-140 DEG C of low pressure saturated vapor；Organic matter is parsed by stripping, living
Property charcoal or carbon fiber restore absorption property, complete regeneration；It is 130-140 DEG C that 20 are obtained simultaneously to temperature, is had containing a large amount of volatility
The desorption steam of machine object.Steam is desorbed generally using shell and tube condenser and spiral heat exchanger is exchanged heat and organic solvent
Recycling；Shell and tube condenser has the shortcomings that internal incrustation is serious, it is inconvenient to safeguard, is used for a long time, it may appear that condensation effect is bad
The phenomenon that；Spiral heat exchanger requirement welding quality is high, and maintenance is relatively difficult.Fixed gas when organic solvent recycles still contains
The VOCs compositions of higher concentration, still need to purified treatment.
Utility model content
For defect in the prior art, the purpose of this utility model is to provide a kind of desorption steam organic matter recycling
With fixed gas purifying integration device.In order to achieve the above objectives, the utility model adopts the following technical scheme：
A kind of desorption steam organic matter recycling and fixed gas purifying integration device, set including condensing plant and condensation
The subsequent purification device in standby downstream, wherein, the condensing plant includes condensing plant housing, condensing plant housing be equipped with fluid into
Mouthful and fluid outlet, be equipped with gas channel and the condensed fluid pipeline in condensing plant housing, condensed fluid by it is cold you flow
Body pipeline exchanges heat with air-flow；Fluid inlet and fluid outlet are located at gas channel both ends.
In a kind of more preferred embodiment, oil trap is additionally provided in the condensing plant housing, is divided after being condensed for storage
From organic matter.The subsequent purification device includes subsequent purification device for housing, and subsequent purification device case is equipped with and condensation
The air inlet of apparatus casing fluid outlet connection, subsequent purification device case are additionally provided with gas outlet, and enclosure interior has accommodating cavity,
Accommodating cavity is between air inlet and gas outlet.
The fluid line is preferably gravity assisted heat pipe (i.e. two-phase closed type hot siphon).
Along air inlet to gas outlet direction, it is equipped with spray washing device successively in the accommodating cavity, ultraviolet photolysis fills
It puts, demister；It is closed between the spray washing device, ultraviolet photolysis device, demister and accommodating cavity inner wall.
In an advantageous embodiment, the spray washing device, ultraviolet photolysis device, demister be successively from the bottom to top
Setting.In an advantageous embodiment, the spray washing device includes pump, packing area, the fluid pumped out is sent into packing area
Pipeline, spray into packing area the nozzle of fluid, the nozzle is connected on pipeline.In more preferred embodiment, the pipeline
Including internal pipeline and external pipe, internal pipeline is located above packing area, the internally positioned pipeline of nozzle, and nozzle and filler
There are gaps between area.
In an advantageous embodiment, the spray washing device can be level-one or multi-stage spray wash mill, at different levels
Spray washing apparatus structure can be identical or different, and preferably identical.It is highly preferred that spray washing devices at different levels can be point
It She Zhi not pump, partial common one pumps or all shares a pump.
In an advantageous embodiment, the ultraviolet photolysis device includes ultra violet light emitter, the ultra violet light emitter
The ultraviolet light of 185nm and/or 254nm can at least be emitted.In more preferred embodiment, the ultraviolet photolysis device includes ultraviolet
Optical transmitting set and photocatalyst bed, the photocatalyst such as titanium dioxide.The photocatalyst can be raw under ultraviolet light generator irradiation
Into the active material of decomposing organic matter.
Wherein, it is highly preferred that at least partially uv optical transmitting set is to photocatalyst bed emitting ultraviolet light.In a kind of more preferable reality
It applies in example, at least one or more described ultraviolet light generator is equipped with below the photocatalyst bed.More preferably implement a kind of
In example, the ultraviolet photolysis device includes multilayer optical catalyst bed, and every layer of photocatalyst bed above and or below is equipped with ultraviolet light emission
Device, the ultra violet light emitter can be tubulose and/or laminated structure, extend along photocatalyst bed surface.
In an advantageous embodiment, the demister includes multiple baffle plates, and gap is formed between each baffle plate.
Each baffle plate can be laminated or be arranged side by side, and be preferably arranged side by side.
Wherein, the baffle plate can be preferably at least part and be corrugated sheet, can also be at least part surface equipped with convex
The texture or the two for playing baffle or protrusion exist simultaneously.
In a kind of more preferred embodiment, the demister further includes bottom diversion trench, for collecting baffle plate trapping
Liquid.
In an advantageous embodiment, the subsequent purification device further includes catch box, it is preferable that the catch box is located at
Housing bottom, and it is at least partly open at the top of catch box, and top is the packing area.
Wherein, the opening can be realized by modes such as hole, hole, windows.
In a kind of more preferred embodiment, the catch box be equipped with the air inlet, and pass through the air inlet with it is described
The fluid outlet connection of condensing unit.
It is highly preferred that catch box connection demister leakage fluid dram, for example, diversion trench connection catch box or
The catch box is directly connected below baffle plate.
It is highly preferred that the pump connection catch box, pipeline is pumped by the fluid in catch box.
In a kind of more preferred embodiment, the catch box further includes liquid supplementation pipe and/or drain pipe.
Wherein, the drain pipe preferably comprises overflow pipe and blow-off pipe, and the overflow pipe is located above default liquid level, institute
Blow-off pipe is stated to be located at below default liquid level, and be preferably located at catch box bottom.
It is highly preferred that the catch box further includes liquid level gauge.
In more preferred embodiment, the catch box further includes purifier, such as filter, absorber, sterilizer, derusting
Device etc..
In a kind of preferred embodiment of the utility model, the desorption steam organic matter recycling is integrated with fixed gas purification
Device further includes PLC control system, and the PLC control system connects and controls condensing unit, spray washing device, ultraviolet photolysis
Any one in valve on device, catch box liquid supplementation pipe and/or drain pipe or several working conditions.
As PLC system can control condensed fluid working condition, pump working condition, spray washing install pipes it is upper each
The working condition of valve, working condition, catch box liquid supplementation pipe valve working state, and/or the liquid collecting for controlling ultra violet light emitter
Working condition of case drain tube valve etc..
Relative to the prior art, the technical solution of the utility model has the advantages that：
1) recycling of the utility model desorption steam organic matter and fixed gas purifying integration device, first drop high-temp waste gas
Temperature, organic matter are precipitated, organic matter are separated and recovered.
2) the utility model becomes the mass transfer surfaces that continuously contact with of gas-liquid using filler wetting surface, using gas-liquid two-phase it
Between double films effect absorption removal is carried out to methanol waste gas；
3) recycling of the utility model desorption steam organic matter and fixed gas purifying integration device are smelly using ultraviolet photogenerated
Oxygen has extremely strong oxidation, in addition, ultraviolet light can be with Direct Pyrolysis methanol to methanol；The utility model can be with auxiliary
With catalyst, catalyst generates reactive group under ultraviolet light, and methanol is continued to decompose, and improves the ability for decomposing methanol；
4) in the utility model, baffle plate and catch box can use the liquid circulation of trapping, can save ejecting liquid
Use；
5) the utility model subsequent purification device preferably uses upright type of design, and floor space is small；And spray washing liquid
The partial impurities in exhaust gas can further be adsorbed during decline, and realize that cross-flow sprays, may further be exhaust gas drop
Temperature；Spray washing liquid after decline is fallen directly into catch box, reduces liquid conveying pressure；
6) the utility model device is suitable for organic chemical industry, medication chemistry, coating and printing ink product, rubber plastic product, spinning
The industries volatile organic matters (VOCs) such as printing and dyeing are knitted to administer using the cleaning of absorbing process desorption steam.The organic efficiency of VOCs reaches
To more than 70%, condensed fixed gas purification efficiency reaches more than 90%.
Description of the drawings
Fig. 1 is the desorption steam organic matter recycling of the utility model and the structural representation of fixed gas purifying integration device
Figure.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model part of the embodiment, instead of all the embodiments.Based on the embodiment in the utility model, sheet
Field those of ordinary skill all other embodiments obtained without making creative work, belong to this practicality
Novel protected range.
In the description of the present invention, it should be noted that term " " center ", " on ", " under ", " left side ",.It is " right side ", " perpendicular
Directly ", the orientation of the instructions such as " level ", " interior ", " outer " or position relationship are based on orientation shown in the drawings or position relationship, are only
The utility model must have specific with the device or element for simplifying description rather than instruction or hint meaning for ease of description
Orientation, with specific azimuth configuration and operation, therefore it is not intended that limitation to the utility model.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or integrally
Connection；Can be mechanical connection or electrical connection；It can be directly connected, can also be indirectly connected by intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, can above-mentioned art be understood with concrete condition
Concrete meaning of the language in the utility model.
With reference to Fig. 1, the recycling of desorption steam organic matter and fixed gas purifying integration device of the utility model include condensation
The subsequent purification device in 2 downstream of device 2 and condensing unit.
Condensing unit is equipped with fluid inlet 1, i.e. exhaust gas inlet, condensing unit is internally provided with gas passage, leads to for exhaust gas
It crosses, is additionally provided with gravity assisted heat pipe as heat transfer unit, gravity assisted heat pipe is in direct contact with gas passage, and high-temp waste gas passes through heat exchanger
Heat absorbing side releases heat, which is quickly transmitted to the cold side of heat exchanger through heat pipe, and exhaust gas temperature is reduced.Cooling water leads to
Heat is absorbed during the cold side for crossing heat exchanger, the heat of hot water is the thermal energy for recycling high-temperature gas, is achieved in waste heat and returns
The purpose of receipts.After exhaust gas temperature declines simultaneously, the partial organic substances matter in exhaust gas is condensed and is removed；Condensate liquid enters condensation
The oil trap 21 of 2 lower section of device, can concentrate separating-purifying, so as to recycle the organic matter that condensation obtains.Condensing unit 2 leads in gas
Road downstream is equipped with fluid outlet 22, and the exhaust gas after cooling is sent to the subsequent purification device in downstream.
Sensing TT＆C system can be set, and the cooling effect, recuperation of heat effect, organic substance yield to exhaust gas carry out real
When monitor and record, and feed back to PLC control system, the intelligent control for product provides data.
Subsequent purification bottom of device is catch box 6, and catch box 6 is equipped with air inlet, and air inlet is connected with fluid outlet 22,
6 top of catch box is at least partly open, also, is purifier housing 8 at the top of catch box, in the accommodating cavity in housing 8, by
Under it is supreme successively be equipped with spray washing device 3, ultraviolet photolysis device 4, demister 5.Exhaust gas after cooling passes through catch box liquid
Space above face enters housing 8.
As shown in Figure 1, spray washing device includes packing area 31, pump 9 and pipeline, pipeline includes external pipe 33 and interior
Portion's pipeline 32, internal pipeline 32 are located at the top of packing area 31.The nozzle of internal pipeline 32 can be one or more, and direction
Packing area 31.Each nozzle has gap with 31 surface of packing area, in favor of expanding spray area.Pump connection catch box 6, will collect
Liquid in liquid case 6 is pumped by external pipe 33, internal pipeline 32 to nozzle.
Filler is high-efficient purification filler, and ejecting liquid sprays at the top of filler in spray washing device, the table of filler wetting
Face becomes the mass transfer surfaces that gas-liquid continuously contacts with, and the organic waste in removal gas is absorbed using double films effect between gas-liquid two-phase
Gas.Meanwhile spray washing fluid is cooled down twice exhaust gas.Spray washing device sprays (i.e. for cross-flow in the utility model
Ejecting liquid flowing is opposite with gas flow direction).Spray washing fluid is flowed down from packing area 31, falls into the catch box of lower section
It is interior, realize cycle.
The spray washing device is connected with PLC control system, is controlled by PLC control system.
Gas after spray washing enters ultraviolet photolysis device, and ultraviolet photolysis device includes ultraviolet light generator 41 (such as
Electrodeless UV lamp pipe), 185nm and 254nm ultraviolet lights can be sent out, can be cracked using the high-energy of 185 nanometers of short wave ultraviolets
Organic exhaust gas.
Ultraviolet photolysis device can also include photocatalyst of titanium dioxide 42, it is preferable that have at least one or more ultraviolet light
Generator 41 is located at 42 lower section of photocatalyst bed.It is cracked in this way, organic exhaust gas first passes around ultraviolet light.Photocatalyst bed 42
Can be that multilayer is set, surface is equipped with one or more ultraviolet light generators 41 above and/or under each layer of photocatalyst bed 41, utilizes
254 nanometer ultraviolet rays irradiation titanium deoxide catalyst generates the active secondary oxidant such as hydroxyl to aoxidize organic exhaust gas.It is organic
Under the synergistic effect of photocatalyst and ultraviolet light oxygenolysis persistently occurs for exhaust gas, ultimately generates carbon dioxide and water.
The ultraviolet photolysis device is connected with PLC control system, is controlled by PLC control system.
The demister 5 uses baffle type mist eliminator, including baffle plate arranged side by side.
It is for gas to pass through that gap is formed between baffle plate, when the gap between the gas containing water mist enters baffle plate,
Since the inertial impaction of gas acts on, water mist collides with baffle plate and is attached to surface.The diffusion of baffling plate surface water mist
Water mist is made to form larger drop and moves forward to baffle plate turning with air-flow with gravitational settling, due to turn to centrifugal force and
The surface tension of rubbing action, suction-operated and liquid with baffle plate so that drop is increasing, until the drop gathered is big
To its own generation gravity be more than gas climbing power and surface tension of liquid resultant force when, drop is divided from baffling plate surface
From getting off.
Baffle plate can be at least partially corrugated sheet, can also be that at least part surface is equipped with raised baffle or protrusion
Texture or the two exist simultaneously, and this being folded to structure increases the chance that water mist is captured more, and the water mist not being removed is under
One turning is captured through phase same-action, and such repeated action greatly improves efficiency.
Exhaust gas after demisting is discharged by the gas outlet 7 at 8 top of housing.
Catch box 6 includes water tank, liquid level gauge, water supply solenoid valve, drain solenoid valve and (is equipped with overflow port, lower water at upper water level
Sewage draining exit is equipped at position).The fluid level controller, water supply solenoid valve, drain solenoid valve are connected with PLC control system.Liquid collecting
There can also be filtering and cleaning device in case 6.
In catch box fluid low or it is excessively high when, liquid level gauge sends a signal to PLC control system, PLC control system moisturizing
Solenoid valve, drain solenoid valve work.
Finally it should be noted that：The above various embodiments is only to illustrate the technical solution of the utility model rather than it is limited
System；Although the utility model is described in detail with reference to foregoing embodiments, those of ordinary skill in the art should
Understand：It can still modify to the technical solution recorded in foregoing embodiments either to which part or whole
Technical characteristic carries out equivalent replacement；And these modifications or replacement, this practicality that it does not separate the essence of the corresponding technical solution are new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of desorption steam organic matter recycling and fixed gas purifying integration device, which is characterized in that including condensing plant, with
And the subsequent purification device in condensing plant downstream, wherein, the condensing plant includes condensing plant housing, and condensing plant housing is set
There are fluid inlet and fluid outlet, be equipped with gas channel in condensing plant housing and the condensed fluid pipeline, condensed fluid are led to
Your fluid line is subcooled to exchange heat with air-flow；Fluid inlet and fluid outlet are located at gas channel both ends；
The subsequent purification device includes subsequent purification device for housing, and subsequent purification device case is equipped with and condensing plant housing
The air inlet of fluid outlet connection, subsequent purification device case are additionally provided with gas outlet, and enclosure interior has accommodating cavity, accommodating cavity
Between air inlet and gas outlet；Along air inlet to gas outlet direction, it is equipped with spray washing successively in the accommodating cavity
Device, ultraviolet photolysis device, demister；In the spray washing device, ultraviolet photolysis device, demister and accommodating cavity
It is closed between wall.
2. the apparatus according to claim 1, which is characterized in that be additionally provided with oil trap in the condensing plant housing, be used for
The organic matter detached after storage condensation.
3. the apparatus according to claim 1, which is characterized in that the fluid line is gravity assisted heat pipe.
4. the apparatus according to claim 1, which is characterized in that the spray washing device, ultraviolet photolysis device, demisting dress
It puts and sets from the bottom to top successively.
5. device according to claim 4, which is characterized in that the spray washing device includes pump, packing area, will pump out
Fluid be sent into the pipeline of packing area, the nozzle of fluid sprayed into packing area, the nozzle is connected on pipeline.
6. device according to claim 5, which is characterized in that the subsequent purification device further includes catch box, the collection
Liquid case is located at housing bottom, and at least partly open at the top of catch box, and top is the packing area；The catch box is set
There is the air inlet, and pass through the air inlet and connected with the fluid outlet of the condensing unit；The pump connection catch box, will
Fluid in catch box is pumped into pipeline.
7. device according to claim 4, which is characterized in that the ultraviolet photolysis device includes ultra violet light emitter, institute
The ultraviolet light of 185nm and/or 254nm can at least be emitted by stating ultra violet light emitter.
8. device according to claim 7, which is characterized in that the ultraviolet photolysis device further includes photocatalyst bed, described
Photocatalyst can generate the active material of decomposing organic matter under ultraviolet light generator irradiation.
9. device according to claim 7, which is characterized in that at least one or more ultra violet light emitter is located at photocatalyst
Bed lower section.
10. the apparatus according to claim 1, which is characterized in that the demister includes multiple baffle plates, each baffling
Gap is formed between plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721314315.9U CN207462990U (en) | 2017-10-12 | 2017-10-12 | It is desorbed the recycling of steam organic matter and fixed gas purifying integration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721314315.9U CN207462990U (en) | 2017-10-12 | 2017-10-12 | It is desorbed the recycling of steam organic matter and fixed gas purifying integration device |
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| Publication Number | Publication Date |
|---|---|
| CN207462990U true CN207462990U (en) | 2018-06-08 |
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ID=62266671
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721314315.9U Expired - Fee Related CN207462990U (en) | 2017-10-12 | 2017-10-12 | It is desorbed the recycling of steam organic matter and fixed gas purifying integration device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107774119A (en) * | 2017-10-12 | 2018-03-09 | 上海履诚环境科技有限公司 | It is desorbed the recovery of steam organic matter and fixed gas purifying integration device |
| CN111197513A (en) * | 2018-11-16 | 2020-05-26 | 彭斯干 | Method for increasing energy efficiency of ship and synergistic ship |
| CN111672320A (en) * | 2020-07-22 | 2020-09-18 | 常州兰迪科技有限公司 | A device integrating the functions of chemical cleaning of chemical fiber spinnerets and environmental protection waste gas purification |
-
2017
- 2017-10-12 CN CN201721314315.9U patent/CN207462990U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107774119A (en) * | 2017-10-12 | 2018-03-09 | 上海履诚环境科技有限公司 | It is desorbed the recovery of steam organic matter and fixed gas purifying integration device |
| CN111197513A (en) * | 2018-11-16 | 2020-05-26 | 彭斯干 | Method for increasing energy efficiency of ship and synergistic ship |
| CN111672320A (en) * | 2020-07-22 | 2020-09-18 | 常州兰迪科技有限公司 | A device integrating the functions of chemical cleaning of chemical fiber spinnerets and environmental protection waste gas purification |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180608 Termination date: 20201012 |
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| CF01 | Termination of patent right due to non-payment of annual fee |