CN205517129U - Use concentrated purification treatment system of waste gas of incinerator heat recovery - Google Patents
Use concentrated purification treatment system of waste gas of incinerator heat recovery Download PDFInfo
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- CN205517129U CN205517129U CN201620101808.3U CN201620101808U CN205517129U CN 205517129 U CN205517129 U CN 205517129U CN 201620101808 U CN201620101808 U CN 201620101808U CN 205517129 U CN205517129 U CN 205517129U
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- 239000002912 waste gas Substances 0.000 title claims abstract description 146
- 238000000746 purification Methods 0.000 title claims abstract description 45
- 238000011084 recovery Methods 0.000 title description 6
- 239000007789 gas Substances 0.000 claims abstract description 80
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 45
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000010457 zeolite Substances 0.000 claims abstract description 45
- 239000012530 fluid Substances 0.000 claims abstract description 44
- 238000010438 heat treatment Methods 0.000 claims abstract description 27
- 238000001179 sorption measurement Methods 0.000 claims abstract description 21
- 238000003795 desorption Methods 0.000 claims description 46
- 238000005516 engineering process Methods 0.000 claims description 44
- 238000007664 blowing Methods 0.000 claims description 31
- 238000005086 pumping Methods 0.000 claims description 15
- 239000002245 particle Substances 0.000 claims description 9
- 238000010079 rubber tapping Methods 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 23
- 230000008901 benefit Effects 0.000 abstract description 4
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract 2
- 230000001953 sensory effect Effects 0.000 abstract 2
- 206010037660 Pyrexia Diseases 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 16
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 8
- 238000005259 measurement Methods 0.000 description 6
- 238000009825 accumulation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000004575 stone Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 238000005201 scrubbing Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 210000003437 trachea Anatomy 0.000 description 3
- 210000005056 cell body Anatomy 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 238000002336 sorption--desorption measurement Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000009897 systematic effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a wet unit falls in the concentrated purification treatment system by heating of waste gas, entry waste gas sensory unit and regulating unit's configuration, the high -temperature gas by heating that make to burn the device falls the heat exchange of wet unit and carries out the heat exchange with waste gas in the waste gas intake pipe, the preceding temperature rise and the hygrometry that make waste gas get into zeolite runner enrichment facility descend, with the adsorption efficiency of promoting this zeolite runner enrichment facility organic substance in to waste gas, and then in the promotion waste gas organic substance get rid of efficiency, regulating unit can measuration the exhaust gas temperature or the humidity of the entrance of zeolite runner enrichment facility according to entry waste gas sensory unit and come control to be used for the working fluid's of indirect heating waste gas the velocity of flow or flow. The utility model discloses need not additionally to install additional the heat source device and / or the pipeline that are used for the heating, have and reduce power -wasting advantage, and in the reducible system pipeline because of plus the pressure loss that causes of subassembly to reduce system complexity.
Description
Technical field
This utility model relates to a kind of waste gas thickening-purification technology processing system, is used for processing industry manufacturing process and produces
Raw waste gas, makes the organic substance in waste gas reduce or removes.
Background technology
Many industry manufacturing process can produce the waste gas containing organic substance, most volatile organic matter
Confrontation human body produces harm, therefore the waste gas that manufacturing process produces needs purified process and meets waste gas discharge mark
After standard, just can be emitted in external environment.Existing organic exhaust gas purifying system uses zeolite runner to concentrate
Device and incinerator, wherein, this zeolite runner enrichment facility inner area is separated with adsorption zone and desorption district and boils
Stone runner persistently rotates through this adsorption zone and this desorption district, and the waste gas that manufacturing process produces introduces this absorption
Qu Zhong, by the organic substance in this zeolite runner absorption waste gas, the zeolite turned in this desorption district turns
Wheel, is desorbed the organic substance being adsorbed on zeolite runner by the desorption air-flow introduced, and with
The desorption air-flow of the organic substance being desorbed introduces this incinerator and carries out incineration process.So, by boiling
The rotational run of stone runner, makes zeolite runner constantly repeat absorption and the step of desorption, makes by this boiling
After organic substance contained in waste gas after stone runner enrichment facility is reduced to discharge standard, just can be expelled to
In air.
In some manufacturing process (such as spraying manufacturing process), the waste gas that manufacturing process produces is contained within greatly
Amount shot-like particle, therefore in manufacturing process rear end frequently with scrubbing tower or other wash dirt device and carry out scrubbing exhaust gas,
To reduce the shot-like particle in waste gas, therefore, the waste gas finally discharged is low temperature and high humility.
But, owing to zeolite runner has hydrophobic property, the waste gas that the humidity of waste gas is too high is unfavorable for that zeolite turns
The wheel enrichment facility removal efficiency to organic substance, and, the too high or too low for temperature of waste gas also affects boiling
The stone runner enrichment facility removal efficiency to organic substance, specifically, with relative humidity and other conditions
Under Gu Ding, zeolite runner is the lowest to the removal efficiency of organic substance in waste gas, as a example by isopropanol, if useless
Temperature is too high, such as, when reaching more than 45 DEG C, zeolite runner drops to 92% to the removal efficiency of isopropanol
Hereinafter, and removal efficiency with temperature increase and reduce rapidly；And if EGT is too low, for example, 20
Time below DEG C, the wheel face of zeolite runner may be caused because of the dew point temperature less than desorption gas to condense wet
Profit, causes removal efficiency to reduce rapidly；Under fixing with temperature and other conditions, the relative humidity of waste gas is more
Height, zeolite runner is the lowest to the removal efficiency of organic substance in waste gas, as a example by isopropanol or acetone, useless
When the relative humidity of gas reaches more than 85%, the zeolite runner removal efficiency dramatic decrease to isopropanol or acetone
To less than 90%, and removal efficiency increases and rapid reduction with relative humidity.
Accordingly, when existing organic exhaust gas purifying system is applied to the waste gas processing low temperature and high humility, its
The best to organic removal efficiency, and the shortcoming having power consumption.
Utility model content
To having during the waste gas processing low temperature and high humility for solving above-mentioned known waste gas cleaning system to be applied to
The problem that the removal efficiency of machine thing is the best, the utility model proposes a kind of waste gas applying incinerator recuperation of heat
Thickening-purification technology processing system.
For reaching above-mentioned purpose and other purposes, this utility model provides a kind of and applies the useless of incinerator recuperation of heat
Gas thickening-purification technology processing system, comprises exhaust inlet pipe, zeolite runner enrichment facility, incinerating apparatus, heat
Switch, heating wet down unit, inlet exhaust gases sensing unit and regulation unit, this exhaust inlet pipe,
For introducing pending waste gas；This zeolite runner enrichment facility includes adsorption section, blowing portion and desorption portion,
This adsorption section has the arrival end connecting this exhaust inlet pipe and the port of export connecting tapping equipment, this blowing
Portion has for inputting the arrival end blowing down air-flow and for exporting the port of export of this blowing air-flow, this desorption
Portion has the arrival end for inputting desorption air-flow and for exporting the port of export of this desorption air-flow；This incineration
Device includes combustor, the first switching pipeline and the second switching pipeline, and this first switching pipeline connects this and takes off
The port of export in attached portion, this second switching pipeline connects this tapping equipment；This heat-exchange device includes heat extraction
Pipeline and add hot pipeline, this heat draws pipeline and connects this combustor and this second switching pipeline, and this adds heat pipe
Linear system connects the port of export in this blowing portion and the arrival end of this desorption portion, and this heat is drawn pipeline and is used for drawing this
High-temperature gas in combustor, shape after the blowing air-flow exported for this blowing portion and high-temperature gas heat exchange
Become this desorption air-flow；This heating wet down unit includes the first heat exchanger, the second heat exchanger, circulation pipe
Line and pumping, it is online that this first heat exchanger is arranged at this second switching pipe, and this second heat exchanger is arranged
On this exhaust inlet pipe, this pipeloop be configured at this first heat exchanger and this second heat exchanger it
Between, it is online that this pumping is arranged at this circulation pipe, is handed over by this first heat with transportation work circular fluidic flow
Parallel operation and this second heat exchanger；This inlet exhaust gases sensing unit includes that the first temperature sensor and humidity pass
Sensor, after this first temperature sensor and this humidity sensor are configured at this second heat exchanger；This tune
Joint unit is arranged at this circulation pipe and online and connects this inlet exhaust gases sensing unit, and this regulation unit is used for depending on
In the temperature recorded according to this inlet exhaust gases sensing unit and humidity, at least one is to control in this pipeloop
The flow velocity of working fluid or flow.
Above-mentioned waste gas thickening-purification technology processing system, wherein this regulation unit includes humidity controller and frequency conversion
Device, this humidity controller connects this humidity sensor, and this converter is arranged in this pumping and to connect this wet
Degree controller.
Above-mentioned waste gas thickening-purification technology processing system, wherein this regulation unit includes temperature controller, this temperature
Degree controller connects this first temperature sensor, and this converter is arranged in this pumping and connects this humidity control
Device processed and this temperature controller.
Above-mentioned waste gas thickening-purification technology processing system, wherein this inlet exhaust gases sensing unit includes the second temperature
Sensor, before this second temperature sensor is configured at this second heat exchanger and connect this temperature control
Device, temperature that this regulation unit can record according to this first temperature sensor, this first temperature sensor with
In temperature difference that this second temperature sensor records and the humidity that this humidity sensor records, at least one comes
Control flow velocity or the flow of working fluid in this pipeloop.
Above-mentioned waste gas thickening-purification technology processing system, wherein this regulation unit includes temperature controller and regulation
Valve, this temperature controller connects this first temperature sensor, and it is online also that this regulation valve is arranged at this circulation pipe
Connect this temperature controller.
Above-mentioned waste gas thickening-purification technology processing system, wherein this regulation unit includes humidity controller, and this is wet
Degree controller connects this humidity sensor, and this regulation valve is arranged at this circulation pipe and online and connects this temperature control
Device processed and this humidity controller.
Above-mentioned waste gas thickening-purification technology processing system, wherein this regulation unit includes flow equilibrium pipeline, should
Regulation valve is three-way valve, and this flow equilibrium pipeline is connected across and is configured at this first heat exchanger import and export both sides
Circulation pipe online, this regulation valve is arranged at this circulation pipe online and wherein port and connects this balance pipeline
One end.
Above-mentioned waste gas thickening-purification technology processing system, wherein this inlet exhaust gases sensing unit includes the second temperature
Sensor, before this second temperature sensor is configured at this second heat exchanger and connect this temperature control
Device, temperature that this regulation unit can record according to this first temperature sensor, this first temperature sensor with
In temperature difference that this second temperature sensor records and the humidity that this humidity sensor records, at least one comes
Control flow velocity or the flow of working fluid in this pipeloop.
Above-mentioned waste gas thickening-purification technology processing system, wherein this first heat exchanger arrangement is in this second switching
After in the gas flow of pipeline, this heat draws the position that pipeline is connected to this second switching pipeline.
Above-mentioned waste gas thickening-purification technology processing system, wherein this first heat exchanger is fin-tube type heat exchanger
Or tube coil type heat exchanger.
Above-mentioned waste gas thickening-purification technology processing system, including particulate filter, this shot-like particle filters
Device is arranged between this exhaust inlet pipe and arrival end of this adsorption section, so that the input of this exhaust inlet pipe
Waste gas by and filter the shot-like particle in waste gas.
Above-mentioned waste gas thickening-purification technology processing system, wherein this incinerating apparatus is dual-trench type heat accumulation type incineration
Stove, three grooved heat accumulating type incinerators or heat accumulating of revolution type incinerator.
Accordingly, waste gas thickening-purification technology processing system of the present utility model enters the concentration of this zeolite runner at waste gas
Before device, make the EGT in this exhaust inlet pipe raise and relative humidity reduces, and can be promoted this
Zeolite runner enrichment facility is to the absorbability of organic substance in waste gas, and promotes organic substance in waste gas
Removal efficiency.Further, organic exhaust gas adsorption desorption thickening-purification technology system of the present utility model utilizes incinerator
Used heat heats the waste gas in this exhaust inlet pipe indirectly, and without additionally installing heater and/or pipeline additional,
Therefore there is the advantage reducing power consumption, additionally, the crushing caused because of additional assembly in systematic pipeline can be reduced,
And system complexity can be reduced.
Accompanying drawing explanation
Fig. 1 is the configuration schematic diagram of the waste gas thickening-purification technology processing system of this utility model first embodiment；
Fig. 2 is the configuration schematic diagram of the waste gas thickening-purification technology processing system of this utility model the second embodiment.
[symbol description]
1 waste gas adsorption desorption thickening-purification technology system
2 tapping equipments
100 exhaust inlet pipes
200 zeolite runner enrichment facilities
201 zeolite runners
210 adsorption sections
211 arrival ends
212 ports of export
220 blowing portions
221 arrival ends
222 ports of export
230 desorption portion
231 arrival ends
232 ports of export
300 heat accumulation type incineration devices
310 combustor
320 first switching pipelines
330 second switching pipelines
340A, 340B, 340C regenerator
350 promote valve
350A, 350B, 350C valve group
351A, 351B, 351C valve group
400 heat-exchange devices
410 heat draw pipeline
410A the first line sections
410B the second line sections
420 add hot pipeline
420A the 3rd line sections
420B the 4th line sections
500 heating wet down unit
510 first heat exchangers
520 second heat exchangers
530 pipeloops
540 pumpings
550 flow equilibrium pipelines
600 inlet exhaust gases sensing unit
610 first temperature sensors
620 second temperature sensors
630 humidity sensors
700 regulation unit
710 humidity controllers
720 converters
730 temperature controllers
740 regulation valves
800 particulate filters
Detailed description of the invention
It is for being fully understood by the purpose of this utility model, feature and effect, existing by following specific embodiment,
And coordinate accompanying drawing, this utility model is described in further details, is described as follows:
Waste gas thickening-purification technology processing system of the present utility model is used for processing in industry manufacturing process is discharged
Waste gas, be preferably applicable to such as to spray the industry manufacturing process such as manufacturing process, manufacturing process of spraying paint,
Containing substantial amounts of shot-like particle and Organic substance, therefore, above-mentioned work in the waste gas that above-mentioned industry manufacturing process produces
Industry manufacturing process would generally make waste gas carry out washing dirt process by scrubbing tower before waste gas discharges, and makes waste gas
Middle shot-like particle content is greatly reduced, but, the temperature through the waste gas of this scrubbing tower can drop to 10-30
DEG C and humidity can rise to more than 90%, and such inlet exhaust gases be unfavorable for that most waste gas concentrates
The adsorption cleaning efficiency of processing means (such as hydrophobic zeolite runner enrichment facility), therefore this utility model
The technical scheme of waste gas thickening-purification technology processing system there is at least one feature be: enter useless at inlet exhaust gases
Before gas concentration device, make the temperature of waste gas raise and humidity reduces.
Refer to Fig. 1, the waste gas of the application incinerator recuperation of heat of this utility model first embodiment concentrates clean
Change the waste gas that processing system 1 produces after processing manufacturing process, be preferably used for processing low temperature and (be less than
30 DEG C) and high humility (more than 90%) containing organic compounds, this waste gas thickening-purification technology processing system 1 comprises
Exhaust inlet pipe 100, zeolite runner enrichment facility 200, incinerating apparatus 300, heat-exchange device 400,
Heating wet down unit 500, inlet exhaust gases sensing unit 600 and regulation unit 700.
This exhaust inlet pipe 100 is connected to the discharge pipe line of industry manufacturing process, for introduction to waste gas.
This zeolite runner enrichment facility 200 includes adsorption section 210, blowing portion 220 and desorption portion 230,
Wherein, this adsorption section 210, this blowing portion 220 and this desorption portion 230 are included in cell body and separate formation
Compartment, zeolite runner 201 be arranged in this cell body and rotatable the most sequentially through this adsorption section 210, should
Desorption portion 230 and this blowing portion 220, in this adsorption section 210, this zeolite runner 201 adsorbs waste gas
In organic substance；In this desorption portion 230, will be adsorbed on zeolite runner 134 by desorption air-flow
Organic substance be desorbed；In this blowing portion 220, by blowing down air-flow, the zeolite after desorption is turned
Wheel 230 cools down and dehumidifies.This adsorption section 210 has the arrival end 211 connecting this exhaust inlet pipe 100
And the port of export 212 of connection tapping equipment, for the waste gas introduced by this exhaust inlet pipe 100 by being somebody's turn to do
Zeolite runner 201 in adsorption section 210；This blowing portion 220 has for inputting the entrance blowing down air-flow
Hold 221 and for exporting the port of export 222 of this blowing air-flow, for blow-out gas stream by this blowing portion 220
In zeolite runner；This desorption portion 230 has the arrival end 231 for inputting desorption air-flow and for defeated
Go out the port of export 232 of this desorption air-flow, for desorption air-flow by the zeolite runner in this desorption portion 230
201。
This incinerating apparatus 300 includes that combustor 310, first switches pipeline 320 and the second switching pipeline
330, this first switching pipeline 320 connects the port of export 232 of this desorption portion 230, this second switching pipe
Line 330 connects this tapping equipment 2, is provided with burner or electro-thermic heater in this combustor 310, with
Make the burned process of gas of the desorption air-flow entered via the first switching pipeline 320.
This heat-exchange device 400 includes that heat is drawn pipeline 410 and adds hot pipeline 420, and this heat draws pipeline
410 connect this combustor 310 and with this second switching pipeline 330, and wherein this heat extraction pipeline 410 is
Connect this combustor 310 with the first line sections 410A and connect this with the second line sections 410B and second cut
Changing pipeline 330, this adds hot pipeline 420 and connects the port of export 222 and this desorption portion 230 in this blowing portion 220
Arrival end 231, wherein this adds hot pipeline 420 and connects this blowing portion 220 with the 3rd line sections 420A
The port of export 222 and connect the arrival end 231 of this desorption portion 230 with the 4th line sections 420B, should
Heat is drawn the first line sections 420A of pipeline 420 and is come for the high-temperature gas drawing in this combustor 310
As heat source, the blowing via the 3rd line sections 420A conveying for this blowing portion 220 exports
Forming this desorption air-flow after degasification stream and high-temperature gas heat exchange, desorption air-flow is again via the 4th line sections
420B inputs the arrival end to this desorption portion 230.
This heating wet down unit 500 includes first heat exchanger the 510, second heat exchanger 520, circulation
Pipeline 530 and pumping 540, this first heat exchanger 510 is arranged on this second switching pipeline 330,
This second heat exchanger 520 is arranged on this exhaust inlet pipe 100, and this pipeloop 530 is configured at this
Between first heat exchanger 510 and this second heat exchanger 520, this pumping 540 is arranged at this circulation pipe
On line 530, handed over by this first heat exchanger 510 and this second heat with transportation work circular fluidic flow
Parallel operation 520.
This inlet exhaust gases sensing unit 600 includes the first temperature sensor 610, humidity sensor 630,
This first temperature sensor 610 and this humidity sensor 630 be configured at this second heat exchanger 520 it
After, to sense the temperature after waste gas heats and humidity.In the present embodiment, this first temperature sensor 610
And this humidity sensor 630 is arranged at the entrance of this adsorption section 210 in this zeolite runner enrichment facility 200
Hold at 211.
This regulation unit 700 is arranged on this pipeloop 530 and connects this inlet exhaust gases sensing unit
600, this regulation unit 700 is for the temperature recorded according to this inlet exhaust gases sensing unit 600 and humidity
In at least one flow velocity controlling working fluid in this pipeloop 530 or flow, and then control enter
To this second heat exchanger 520 as the temperature of the working fluid of high temperature side.
Working fluid in the present embodiment, in this first heat exchanger 510, in this pipeloop 530
With this second switching pipeline 330 in high-temperature gas heat exchange, by this first heat exchanger after heat exchange
The working fluid of 510 outlets heats up.In this second heat exchanger 520, in this pipeloop 530
Working fluid carries out heat exchange with the waste gas in this exhaust inlet pipe 100, makes waste gas enter this zeolite runner
Before the adsorption section 210 of enrichment facility 200, the temperature of this waste gas heats up, due to the temperature characterisitic of gas
Being associated with relative humidity characteristic, the temperature of this waste gas is increased to 20-40 DEG C and relative humidity is reduced to
80%RH, it is preferred that the temperature of this waste gas is increased to 30-40 DEG C and relative humidity is less than 75%RH.
In this utility model first embodiment, this regulation unit 700 is for single according to this inlet exhaust gases sensing
In first 600 temperature recorded and humidity, at least one is to control the stream of working fluid in this pipeloop 530
Amount, enters into this second heat exchanger 520 temperature as the working fluid of high temperature side using control.
For example, this regulation unit 700 can include humidity controller 710 and converter 720, and this is wet
Degree controller 710 connects this humidity sensor 630, and this converter 720 is arranged in this pumping 540 also
Connecting this humidity controller 710, this humidity controller 710 is surveyed according to this inlet exhaust gases sensing unit 600
The humidity obtained transmits control signal and gives this converter 720, and this converter 720 is based on this control signal control
Make the rotating speed of this pumping 540, and then control the flow velocity of working fluid in this pipeloop 530, therefore depend on
The efficiency of heat exchange is changed according to the humidity of waste gas.
As illustrating, when this inlet exhaust gases senses the wet of humidity sensor 630 measurement of unit 600
When degree is higher than predetermined value (such as 80%RH), this regulation unit 700 controls to make work in this pipeloop 530
The flow velocity making fluid increases, and to promote the heat exchanger effectiveness of the second heat exchanger 520, and makes this waste gas enter
The heating rate of the relatively low temperature waste gas of trachea 100 increases, and makes the wet down speed of waste gas increase.
It addition, this regulation unit 700 may also include temperature controller 730, this temperature controller 730 is even
Connecing this first temperature sensor 610, this converter 720 is arranged in this pumping 540 and connects this humidity
Controller 710 and this temperature controller 730.Accordingly, this temperature controller 730 can give up according to this entrance
The temperature that gas sensing unit 600 records transmits control signal and gives this converter 720, and this converter 720 depends on
Control the rotating speed of this pumping 540 according to this control signal, and then control working fluid in this pipeloop 530
Flow velocity, therefore change the efficiency of heat exchange according to the humidity of waste gas or temperature.
As illustrating, when this inlet exhaust gases senses the wet of humidity sensor 630 measurement of unit 600
Degree is less than predetermined higher than the temperature that predetermined value (such as 80%RH) or this first temperature sensor 610 measure
During value (such as 20 DEG C), this regulation unit 700 controls to make the flow velocity of working fluid in this pipeloop 530
Increase, to promote the heat exchanger effectiveness of the second heat exchanger 520, and make this exhaust inlet pipe 100 relatively
The heating rate of low temperature waste gas increases, and makes the heating rate of waste gas increase with wet down speed.And when this
When the temperature that one temperature sensor 610 measures is higher than predetermined value (such as 40 DEG C), this regulation unit 700 is controlled
System makes the flow velocity of working fluid in this pipeloop 530 reduce, and makes the waste gas of this exhaust inlet pipe 100
Temperature increase rate slows down.And when the temperature of this first temperature sensor 610 measurement is predetermined temperature range
Time interior (such as 20-40 DEG C), this regulation unit 700 maintains the stream of working fluid in this pipeloop 530
Speed, and make the EGT of this exhaust inlet pipe 100 be maintained in this predetermined temperature range.
Additionally, this inlet exhaust gases sensing unit 600 may also include the second temperature sensor 620, this is second years old
Before temperature sensor 620 is configured at this second heat exchanger 520 and connect this temperature controller 730 and (be
Avoid connection excessively mixed and disorderly, thus graphic not shown in this second temperature sensor 620 and this temperature control
Connection line between device 730 processed), this regulation unit 700 except the most above-mentioned can be according to this first temperature
Temperature that sensor 610 records or the humidity that this humidity sensor 630 records are to control this pipeloop
In 530 outside the flow velocity of working fluid or flow, this regulation unit 700 can also be with this first temperature sensing
The temperature difference that device 610 and this second temperature sensor 620 record controls as foundation, and makes this waste gas
The waste gas of air inlet pipe 100 is maintained at predetermined temperature difference scope by the temperature difference of this second heat exchanger 520
In.
For example, with the temperature difference that records between 2-6 DEG C for predetermined temperature difference scope, when the temperature recorded
When degree difference is less than 2 DEG C, this regulation unit 700 controls to make the flow velocity of working fluid in this pipeloop 530
Increase, to promote the heat exchanger effectiveness of the second heat exchanger 520, and make this exhaust inlet pipe 100 relatively
The heating rate of low temperature waste gas increases；When the temperature difference recorded is higher than 6 DEG C, and this regulation unit 700 controls
The flow velocity making working fluid in this pipeloop 530 reduces, and makes the waste gas temperature of this exhaust inlet pipe 100
Degree increase rate slows down.And when the temperature difference recorded is in the predetermined temperature range of 2-6 DEG C, this tune
Joint unit 700 maintains the flow velocity of working fluid in this pipeloop 530.
Accordingly, in this utility model embodiment, this regulation unit 700 can be according to this first temperature sensing
Temperature, this first temperature sensor 610 that device 610 records record with this second temperature sensor 620
In the humidity that temperature difference and this humidity sensor 630 record, at least one is to control this pipeloop 530
The flow velocity of middle working fluid.
In the present embodiment, this first heat exchanger 510 is configured at the gas stream of this second switching pipeline 330
After upwards this heat draws the position that pipeline 410 is connected to this second switching pipeline 330, therefore this heat is drawn
The high-temperature gas drawn by this combustor 310 in pipeline 410 first converges into this second switching pipeline 330,
And mix with processed gas after the burning exported by this incinerating apparatus 300 in this second switching pipeline 330
Afterwards, in this second switching pipeline 330 mixed gas of high-temperature gas and processed gas again through this
One heat exchanger 510, so as to making the temperature of the high temperature side of this first heat exchanger 510 improve, and can lead to
During excessively this heat draws pipeline 410 and this second switching pipeline 330, at least one configuration control valve controls
Adjust flow, and then control the temperature of the high temperature side for this first heat exchanger 510.For example,
The flow being configured to the processed gas in this second switching pipeline 330 with pipeline flow is that this heat is drawn
Nine times of the flow of the high-temperature gas in pipeline 410 as example, this heat is drawn in pipeline 410 by this combustion
Burn room 310 draw and be about 230 DEG C by the temperature of the high-temperature gas of this heat-exchange device 400, should
After the burning exported by this incinerating apparatus 300 in second switching pipeline 330, the temperature of processed gas is about
100 DEG C, high-temperature gas and the mixed mixed gas of processed gas are about 113 DEG C, using as this
The high temperature side of one heat exchanger 510.The mixed gas of 113 DEG C is handed over through this first heat exchanger 510 heat
After alternatively, temperature is down to about 53 DEG C.
In the present embodiment, this first heat exchanger 510 can be fin-tube type heat exchanger or coiled heat exchange
Device.This working fluid can for example, water or heating agent.
In the present embodiment, this incinerating apparatus 300 example is dual-trench type heat accumulating type incinerator, as it can be seen,
This combustor 310 connects two regenerator 340A, 340B, above-mentioned regenerator 340A, 340B with this first
The intake and exhaust of switching pipeline 320 and this second switching pipeline 330 controls, can be by such as promoting valve
350 or the valve group of other forms switch, this lifting valve 350 incinerates cycle period according to accumulation of heat and distinguishes
Corresponding switching is communicated to this first switching pipeline 320 and the above-mentioned regenerator of this second switching pipeline 330
340A,340B.Wherein, the kind of this incinerating apparatus 300 and the relevant pipeline configuration of intake and exhaust are not limited to
The present embodiment and graphic, separately, this incinerating apparatus 300 is alternatively three grooved heat accumulating type incinerators or rotary-type
Heat accumulating type incinerator.
Additionally, this waste gas thickening-purification technology processing system 1 can further include particulate filter 800, should
Before particulate filter 800 is arranged at the arrival end 211 of this adsorption section 210, give up by this for filtering
Shot-like particle in the waste gas of gas air inlet pipe 100 input, to reduce shot-like particle obstruction pipeline, the boiling in waste gas
Stone runner 201 and other can contact the assembly of waste gas.
In this utility model first embodiment, can be by the high-temperature gas of this incinerating apparatus 300 be added with this
The wet unit of heat drop 500 carries out heat exchange and indirectly heats the waste gas in this exhaust inlet pipe 100, and passes through
This regulation unit 700 is according in the temperature measured in exhaust inlet pipe and humidity, at least one controls this
The heat exchanger effectiveness between waste gas in heating wet down unit 500 and this exhaust inlet pipe 100, and make waste gas
Temperature and relative humidity obtain control.Therefore, the waste gas making this zeolite runner enrichment facility of entrance can rise
Temperature, in the preset range of such as 20-40 DEG C and humidity is decreased below the preset range of 80%, therefore increases
Enter this zeolite runner enrichment facility 200 absorbability to the organic substance in waste gas.
Accordingly, the waste gas thickening-purification technology processing system 1 of this utility model first embodiment adds heat drop by this
Wet unit 500, this inlet exhaust gases sensing unit 600 and the configuration of this regulation unit 700, make this incineration
The high-temperature gas of device 300 is indirectly heated this waste gas entered by the heat exchange of this heating wet down unit 500
Waste gas in trachea 100, and make the waste gas in this exhaust inlet pipe 100 enter the concentration of this zeolite runner
Temperature before device 200 rises and relative humidity declines, to promote this zeolite runner enrichment facility 200
To the absorbability of organic substance in waste gas, and then promote the removal efficiency of organic substance in waste gas, wherein
This heating wet down unit 500 and giving up in this exhaust inlet pipe 100 can be controlled by this regulation unit 700
Heat exchanger effectiveness between gas.Additionally, the waste gas thickening-purification technology processing system of this utility model first embodiment
1 high-temperature gas utilizing this incinerating apparatus 300 to draw heats this blowing air-flow with the desorption gas as high temperature
Stream, draws this high-temperature gas more simultaneously and indirectly heats the waste gas in this exhaust inlet pipe 100, and without
Additionally install heater and/or pipeline additional, therefore there is the advantage reducing power consumption, additionally, system can be reduced
The crushing caused because of additional assembly in pipeline, and system complexity can be reduced.
Refer to Fig. 2, it is shown as the waste gas thickening-purification technology processing system of this utility model the second embodiment
Configuration schematic diagram.This utility model the second embodiment is roughly the same with first embodiment, the figure of the present embodiment
Identical element numbers continued to use by assembly identical with this first embodiment effect and function in formula.
In this utility model the second embodiment, this regulation unit 700 is for single according to this inlet exhaust gases sensing
In first 600 temperature recorded and humidity, at least one is to control the stream of working fluid in this pipeloop 530
Amount.
For example, this regulation unit 700 can include temperature controller 730 and regulation valve 740, this temperature
Degree controller 730 connects this first temperature sensor 610, and this regulation valve 740 is arranged at this pipeloop
On 530 and connect this temperature controller 730, this regulation valve 740 controls the stream in this pipeloop 530
Amount.This temperature controller 730 transmits according to the temperature that this inlet exhaust gases sensing unit 600 records and controls news
Number giving this regulation valve 740, this regulation valve 740 controls its valve opening, and then control according to this control signal
Make this pipeloop 530 and enter the flow of the working fluid in this first heat exchanger 510, therefore foundation
The temperature of waste gas changes the efficiency of heat exchange.
Wherein, this regulation unit 700 can include flow equilibrium pipeline 550, and this regulation valve 740 is threeway
Valve, this flow equilibrium pipeline 550 is connected across and is configured at this first heat exchanger 510 and imports and exports following of both sides
Endless tube is online, and this regulation valve 740 is arranged on this pipeloop 530 and wherein a port connects this balance
One end of pipeline 550.
Accordingly, when this regulation valve 740 aperture diminishes, by the workflow of this first heat exchanger 510
The flow of body diminishes, and becomes big by the flow of the working fluid of this flow equilibrium pipeline 550；On the contrary,
When this regulation valve 740 aperture becomes big, become by the flow of the working fluid of this first heat exchanger 510
Greatly, diminished by the flow of the working fluid of this flow equilibrium pipeline 550.
Additionally, this regulation unit 700 may also include humidity controller 710, this humidity controller 710 is even
Connecing this humidity sensor 630, this regulation valve 740 is arranged on this pipeloop 530 and connects this temperature
Controller 730 and this humidity controller 710.
As illustrating, when this inlet exhaust gases senses the wet of humidity sensor 630 measurement of unit 600
Degree is less than predetermined higher than the temperature that predetermined value (such as 80%RH) or this first temperature sensor 610 measure
During value (such as 20 DEG C), this regulation unit 700 controls to make this pipeloop 530 enter this first heat exchange
The flow of the working fluid in device 510 increases, so that as the work of this second heat exchanger 520 high temperature side
The temperature making fluid raises, and makes the heating rate of the relatively low temperature waste gas of this exhaust inlet pipe 100 increase,
And make the heating rate of waste gas increase with wet down speed.And when the temperature of this first temperature sensor 610 measurement
When degree is higher than predetermined value (such as 40 DEG C), this regulation unit 700 controls to make this pipeloop 530 enter should
The flow-reduction of the working fluid in the first heat exchanger 510, so that as this second heat exchanger 520
The temperature of the working fluid of high temperature side reduces, and makes the waste gas heating rate of this exhaust inlet pipe 100 subtract
Slow.And when the temperature of this first temperature sensor 610 measurement is interior (the such as 20-40 of predetermined temperature range
DEG C) time, this regulation unit 700 maintains this pipeloop 530 to enter work in this first heat exchanger 510
Make the flow of fluid, and make the EGT of this exhaust inlet pipe 100 be maintained at this predetermined temperature range
In.
Additionally, this inlet exhaust gases sensing unit 600 may also include the second temperature sensor 620, this is second years old
Before temperature sensor 620 is configured at this second heat exchanger 520 and connect this temperature controller 730 and (be
Avoid connection excessively mixed and disorderly, thus graphic not shown in this second temperature sensor 620 and this temperature control
Connection line between device 730 processed), this regulation unit 700 except the most above-mentioned can be according to this first temperature
Temperature that sensor 610 records or the humidity that this humidity sensor 630 records are to control this pipeloop
In 530 outside the flow velocity of working fluid or flow, this regulation unit 700 can also be with this first temperature sensing
The temperature difference that device 610 and this second temperature sensor 620 record controls as foundation, and makes this waste gas
The waste gas of air inlet pipe 100 maintains predetermined temperature difference scope by the temperature difference of this second heat exchanger 520
In.
For example, with the temperature difference that records between 2-6 DEG C for predetermined temperature difference scope, when the temperature recorded
When degree difference is less than 2 DEG C, this regulation unit 700 controls to make this pipeloop 530 enter this first heat exchange
The flow of the working fluid in device 510 increases, so that as the work of this second heat exchanger 520 high temperature side
The temperature making fluid raises, and makes the heating rate of the waste gas of this exhaust inlet pipe 100 increase；When recording
Temperature difference higher than 6 DEG C, this regulation unit 700 controls to make the stream of working fluid in this pipeloop 530
Prompt drop is low, so that the temperature as the working fluid of this second heat exchanger 520 high temperature side reduces, and makes
The waste gas heating rate of this exhaust inlet pipe 100 slows down.And when the temperature difference that record is pre-at 2-6 DEG C
Time in the range of fixed temperature, this regulation unit 700 maintains this pipeloop 530 to enter this first heat exchanger
The flow of working fluid in 510.
Accordingly, in the present embodiment, this regulation unit 700 can record according to this first temperature sensor 610
Temperature, the temperature difference that records with this second temperature sensor 620 of this first temperature sensor 610 and
In the humidity that this humidity sensor 630 records at least one to control this pipeloop 530 enter this first
The flow of the working fluid in heat exchanger 510.
In the present embodiment, this incinerating apparatus 300 example is three grooved heat accumulating type incinerators, as figure be,
This combustor 310 connects three regenerator 340A, 340B, 340C, above-mentioned regenerator 340A, 340B, 340C
Control to pass through valve group with the intake and exhaust of this first switching pipeline 320 and this second switching pipeline 330
350A, 350B, 350C switch, and respectively this regenerator 340A, and 340B, 340C connect recovery line,
Being provided with valve group 351A, 351B, 351C online in this recovery tube, this recovery line is connected to the first switching
Pipeline 320, above-mentioned valve group 350A, 350B, 350C respectively with above-mentioned regenerator 340A, 340B, 340C are even
Logical, and each valve group 350A, 350B, 350C connect this first switching pipeline 320 and this second switching pipeline
330, each valve group 350A, 350B, 350C carry out corresponding switching respectively according to accumulation of heat incineration cycle period and are communicated to
This first switching pipeline 320 and above-mentioned regenerator 340A of this second switching pipeline 330,340B, 340C,
And by valve group 351A in this recovery line and its, 351B, 351C control respectively this regenerator
One corresponding accumulation of heat of 340A, 340B, 340C incinerate cycle period make waste gas recovery therein return this
One switching pipeline 320.Wherein, the kind of this incinerating apparatus 300 and the relevant pipeline of intake and exhaust configure not
Being limited to the present embodiment and graphic, this incinerating apparatus 300 is alternatively dual-trench type heat accumulating type incinerator or rotary-type
Heat accumulating type incinerator.
When the waste gas thickening-purification technology processing system of above-mentioned first and second embodiment of this utility model operates, useless
Gas introduces this zeolite runner enrichment facility 200 via this exhaust inlet pipe 100, and wherein this zeolite runner is dense
Compression apparatus 200 at least has this adsorption section 210, this blowing portion 220 and this desorption portion 230, this absorption
The arrival end 211 in portion 210 connects this exhaust inlet pipe 100 and the port of export 212 is connected to this tapping equipment
2, the arrival end 231 input desorption air-flow of this desorption portion 230 and the port of export 232 are connected to this incineration dress
Putting 300, this incinerating apparatus is used for the incineration process desorption air-flow from this desorption portion 230.
In this utility model the second embodiment, can be by the high-temperature gas of this incinerating apparatus 300 be added with this
The wet unit of heat drop 500 carries out heat exchange and indirectly heats the waste gas in this exhaust inlet pipe 100, and passes through
This regulation unit 700 is according in the temperature measured in exhaust inlet pipe and humidity, at least one controls this
The heat exchanger effectiveness between waste gas in heating wet down unit 500 and this exhaust inlet pipe 100, and make waste gas
Temperature and relative humidity obtain control.Therefore, the waste gas making this zeolite runner enrichment facility of entrance can rise
The preset range of temperature to such as 20-40 DEG C and humidity are decreased below the preset range of 80%, therefore promote
This zeolite runner enrichment facility 200 absorbability to the organic substance in waste gas.
Accordingly, the waste gas thickening-purification technology processing system 1 of this utility model the second embodiment adds heat drop by this
Wet unit 500, this inlet exhaust gases sensing unit 600 and the configuration of this regulation unit 700, make this incineration
The high-temperature gas of device 300 is indirectly heated this waste gas entered by the heat exchange of this heating wet down unit 500
Waste gas in trachea 100, and make the waste gas in this exhaust inlet pipe 100 enter the concentration of this zeolite runner
Temperature before device 200 rises and relative humidity declines, to promote this zeolite runner enrichment facility 200
To the absorbability of organic substance in waste gas, and then promote the removal efficiency of organic substance in waste gas, wherein
This heating wet down unit 500 and giving up in this exhaust inlet pipe 100 can be controlled by this regulation unit 700
Heat exchanger effectiveness between gas.Incinerate additionally, the waste gas thickening-purification technology processing system 1 of above-described embodiment utilizes
The high-temperature gas that device 300 is drawn heats this blowing air-flow with the desorption air-flow as high temperature, draws simultaneously again
Go out this high-temperature gas and indirectly heat the waste gas in this exhaust inlet pipe 100, and without additionally installing heating additional
Device and/or pipeline, therefore there is the advantage reducing power consumption, additionally, can reduce in systematic pipeline because of additional
The crushing that assembly causes, and system complexity can be reduced.
This utility model is disclosed by preferred embodiment the most, but is familiar with those skilled in the art
It should be understood that this embodiment is only used for describing this utility model, and it is new to be not construed as limiting this practicality
The scope of type.It should be noted that every change equivalent with this embodiment and displacement, all should be set to contain
In category of the present utility model.Therefore, protection domain of the present utility model should be with claims institute
Define in the range of standard.
Claims (13)
1. the waste gas thickening-purification technology processing system applying incinerator recuperation of heat, it is characterised in that comprise:
Exhaust inlet pipe, is used for introducing pending waste gas；
Zeolite runner enrichment facility, including adsorption section, blowing portion and desorption portion, this adsorption section has the arrival end connecting this exhaust inlet pipe and the port of export connecting tapping equipment, this blowing portion has for inputting the arrival end blowing down air-flow and for exporting the port of export of this blowing air-flow, and this desorption portion has the arrival end for inputting desorption air-flow and for exporting the port of export of this desorption air-flow；
Incinerating apparatus, including combustor, the first switching pipeline and the second switching pipeline, this first switching pipeline connects the port of export of this desorption portion, and this second switching pipeline connects this tapping equipment；
Heat-exchange device, draw pipeline including heat and add hot pipeline, this heat is drawn pipeline and is connected this combustor and this second switching pipeline, this adds hot pipeline and connects the port of export in this blowing portion and the arrival end of this desorption portion, this heat is drawn pipeline and is used for drawing the high-temperature gas in this combustor, and the blowing air-flow for the outlet of this blowing portion forms this desorption air-flow after high-temperature gas heat exchange；
Heating wet down unit, including the first heat exchanger, the second heat exchanger, pipeloop and pumping, it is online that this first heat exchanger is arranged at this second switching pipe, this second heat exchanger is arranged on this exhaust inlet pipe, this pipeloop is configured between this first heat exchanger and this second heat exchanger, it is online that this pumping is arranged at this circulation pipe, with transportation work circular fluidic flow by this first heat exchanger and this second heat exchanger；
Inlet exhaust gases sensing unit, including the first temperature sensor and humidity sensor, after this first temperature sensor and this humidity sensor are configured at this second heat exchanger；And
Regulation unit, is arranged at this circulation pipe and online and connects this inlet exhaust gases sensing unit, this regulation unit for according in this inlet exhaust gases sensing temperature of recording of unit and humidity at least one to control flow velocity or the flow of working fluid in this pipeloop.
2. waste gas thickening-purification technology processing system as claimed in claim 1, it is characterised in that this regulation unit includes humidity controller and converter, and this humidity controller connects this humidity sensor, and this converter is arranged in this pumping and connects this humidity controller.
3. waste gas thickening-purification technology processing system as claimed in claim 2, it is characterized in that, this regulation unit includes temperature controller, and this temperature controller connects this first temperature sensor, and this converter is arranged in this pumping and connects this humidity controller and this temperature controller.
4. waste gas thickening-purification technology processing system as claimed in claim 3, it is characterized in that, this inlet exhaust gases sensing unit includes the second temperature sensor, before this second temperature sensor is configured at this second heat exchanger and connect this temperature controller, in temperature difference that this regulation unit can record with this second temperature sensor according to the temperature that this first temperature sensor records, this first temperature sensor and the humidity that this humidity sensor records, at least one is to control flow velocity or the flow of working fluid in this pipeloop.
5. waste gas thickening-purification technology processing system as claimed in claim 1, it is characterized in that, this regulation unit includes temperature controller and regulation valve, and this temperature controller connects this first temperature sensor, and this regulation valve is arranged at this circulation pipe and online and connects this temperature controller.
6. waste gas thickening-purification technology processing system as claimed in claim 5, it is characterized in that, this regulation unit includes humidity controller, and this humidity controller connects this humidity sensor, and this regulation valve is arranged at this circulation pipe and online and connects this temperature controller and this humidity controller.
7. waste gas thickening-purification technology processing system as claimed in claim 6, it is characterized in that, this regulation unit includes flow equilibrium pipeline, this regulation valve is three-way valve, this flow equilibrium pipeline is connected across and is configured at this first heat exchanger to import and export the circulation pipe of both sides online, and this regulation valve is arranged at this circulation pipe online and wherein port and connects one end of this balance pipeline.
8. waste gas thickening-purification technology processing system as claimed in claim 7, it is characterized in that, this inlet exhaust gases sensing unit includes the second temperature sensor, before this second temperature sensor is configured at this second heat exchanger and connect this temperature controller, in temperature difference that this regulation unit can record with this second temperature sensor according to the temperature that this first temperature sensor records, this first temperature sensor and the humidity that this humidity sensor records, at least one is to control flow velocity or the flow of working fluid in this pipeloop.
9. waste gas thickening-purification technology processing system as claimed in claim 6, it is characterized in that, this inlet exhaust gases sensing unit includes the second temperature sensor, this second temperature sensor connects this temperature controller, and in temperature difference that this regulation unit can record with this second temperature sensor according to the temperature that this first temperature sensor records, this first temperature sensor and the humidity that this humidity sensor records, at least one is to control flow velocity or the flow of working fluid in this pipeloop.
10. as claimed in any one of claims 1-9 wherein waste gas thickening-purification technology processing system, it is characterised in that this first heat exchanger arrangement this heat in the gas flow of this second switching pipeline is drawn after pipeline is connected to this second position switching pipeline.
11. waste gas thickening-purification technology processing systems as claimed in claim 10, it is characterised in that this first heat exchanger is fin-tube type heat exchanger or tube coil type heat exchanger.
12. waste gas thickening-purification technology processing systems as claimed in claim 10, it is characterized in that, including particulate filter, this particulate filter is arranged between this exhaust inlet pipe and arrival end of this adsorption section so that this exhaust inlet pipe input waste gas by and filter the shot-like particle in waste gas.
13. waste gas thickening-purification technology processing systems as claimed in claim 10, it is characterised in that this incinerating apparatus is dual-trench type heat accumulating type incinerator, three grooved heat accumulating type incinerators or heat accumulating of revolution type incinerator.
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| CN201620101808.3U CN205517129U (en) | 2016-02-01 | 2016-02-01 | Use concentrated purification treatment system of waste gas of incinerator heat recovery |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620101808.3U CN205517129U (en) | 2016-02-01 | 2016-02-01 | Use concentrated purification treatment system of waste gas of incinerator heat recovery |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107854953A (en) * | 2017-11-24 | 2018-03-30 | 何平 | A kind of intelligence presses interior cycle industrial gas sampling processing system and method |
| CN109985488A (en) * | 2019-04-30 | 2019-07-09 | 厦门冉能环保科技有限公司 | A kind of rotating cylinder Adsorption Concentration device |
| CN112344352A (en) * | 2019-08-07 | 2021-02-09 | 华懋科技股份有限公司 | Heat accumulation backflow high-efficiency organic waste gas treatment system and method |
| CN112999805A (en) * | 2021-03-02 | 2021-06-22 | 机械工业第九设计研究院有限公司 | Novel wet-type paint spraying chamber VOC waste gas heating and humidity reducing technical scheme |
| TWI811690B (en) * | 2021-05-28 | 2023-08-11 | 華懋科技股份有限公司 | Rotor system with heat medium oil and method thereof |
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2016
- 2016-02-01 CN CN201620101808.3U patent/CN205517129U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107854953A (en) * | 2017-11-24 | 2018-03-30 | 何平 | A kind of intelligence presses interior cycle industrial gas sampling processing system and method |
| CN109985488A (en) * | 2019-04-30 | 2019-07-09 | 厦门冉能环保科技有限公司 | A kind of rotating cylinder Adsorption Concentration device |
| CN112344352A (en) * | 2019-08-07 | 2021-02-09 | 华懋科技股份有限公司 | Heat accumulation backflow high-efficiency organic waste gas treatment system and method |
| CN112999805A (en) * | 2021-03-02 | 2021-06-22 | 机械工业第九设计研究院有限公司 | Novel wet-type paint spraying chamber VOC waste gas heating and humidity reducing technical scheme |
| TWI811690B (en) * | 2021-05-28 | 2023-08-11 | 華懋科技股份有限公司 | Rotor system with heat medium oil and method thereof |
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