CN109772110A - A kind of high efficiency demister with Cooling and Heat Source - Google Patents
A kind of high efficiency demister with Cooling and Heat Source Download PDFInfo
- Publication number
- CN109772110A CN109772110A CN201910163662.3A CN201910163662A CN109772110A CN 109772110 A CN109772110 A CN 109772110A CN 201910163662 A CN201910163662 A CN 201910163662A CN 109772110 A CN109772110 A CN 109772110A
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- Prior art keywords
- gas
- heat source
- filler
- shell
- evaporator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 238000001816 cooling Methods 0.000 title claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 54
- 239000000945 filler Substances 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000002184 metal Substances 0.000 claims description 14
- 229920003023 plastic Polymers 0.000 claims description 11
- 239000004033 plastic Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 9
- 239000000919 ceramic Substances 0.000 claims description 8
- 238000009826 distribution Methods 0.000 claims description 8
- -1 polypropylene Polymers 0.000 claims description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 3
- 239000005977 Ethylene Substances 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 3
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims description 3
- 229920001155 polypropylene Polymers 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 239000010962 carbon steel Substances 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 239000007769 metal material Substances 0.000 claims description 2
- 229920000515 polycarbonate Polymers 0.000 claims description 2
- 239000004417 polycarbonate Substances 0.000 claims description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims 3
- 239000002826 coolant Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 6
- 235000019504 cigarettes Nutrition 0.000 abstract description 3
- 239000007921 spray Substances 0.000 abstract description 3
- 238000003303 reheating Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 83
- 239000011257 shell material Substances 0.000 description 35
- 239000003595 mist Substances 0.000 description 14
- 238000004581 coalescence Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 6
- 239000003507 refrigerant Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- 239000003518 caustics Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000883990 Flabellum Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A kind of high efficiency demister with Cooling and Heat Source, including shell, cold and heat source system, reheater, filler, shell include gas access, gas distributor, discharge outlet, condensed water drainage trough, gas vent, supporter.Cold and heat source system includes compressor, evaporator, condenser, throttle valve, reheating gas bag includes heating source and heating tube, gas distributor, evaporator, condenser, heating tube are located at enclosure interior, it is successively inwardly arranged by gas access, compressor, heating source are located at hull outside, and evaporator, condenser are connected by pipeline with compressor, and throttle valve is equipped between evaporator, condenser, heating source is connected with heating tube, and filler is filled in the remaining space of enclosure interior.High efficiency demister of the present invention can effectively remove the steam carried secretly in the wet processes tail gas treatment device outlet such as water scrubber, spray column, can prevent the white cigarette problem in exhaust emissions, while being convenient for the subsequent processing of tail gas.
Description
Technical field
The invention belongs to gas and liquid separation technology field more particularly to a kind of high efficiency demisters with Cooling and Heat Source.
Background technique
Generate large quantity of exhaust gas in the production process of the industries such as electric power, metallurgy, petrochemical industry, in exhaust gas containing a large amount of acid, alkalinity,
The harmful substances such as stench, VOCs or dust cause seriously to pollute to atmospheric environment.Currently, environment protection field largely use spray column,
The wet processing apparatus such as water scrubber go the harmful substance in removing exhaust gas, in the exhaust gas after the absorption of pickling, alkali cleaning or water, contain
The fine drop that a large amount of partial sizes are 10~60 microns is entrained with solid particulate matter etc. dissolved with inorganic salts in these drops, not only right
Atmosphere also causes more serious corrosion and fouling at pollution to follow-up equipment.Therefore after using wet process to exhaust-gas treatment
Must carry out demisting, but current demister structure is simple, be mounted at the top of wet process waste gas treatment equipment more, using filler,
The components such as silk screen, flabellum, gas and components hit containing mist, mist coalescence drip under the effect of gravity at big drop.It is existing
In some demisters, to the removal effect that biggish droplet has had, but fine mist is not easy coalescence, and removal efficiency is poor, and
Gas flow direction is contrary with drips, is easily broken up by air-flow during drop is low, causes reentrainment, work as gas
When temperature is higher, as temperature reduces gas in the duct after mist removal, vapor is secondary to condense into droplet, arranges with exhaust gas
Out, the generation for causing discharge outlet white cigarette, if exhaust gas carries out subsequent processing, the drop in exhaust gas will cause adverse effect.
Summary of the invention
In order to solve the above technical problems, the present invention develops a kind of high efficiency demister with Cooling and Heat Source, can effectively remove
The steam carried secretly in the wet processes tail gas treatment device outlet such as water scrubber, spray column, can prevent the white cigarette problem in exhaust emissions, together
When convenient for tail gas subsequent processing.
Technical solution of the present invention: a kind of high efficiency demister with Cooling and Heat Source, including shell, cold and heat source system, reheater,
Filler, shell include gas access, gas distributor, discharge outlet, condensed water drainage trough, gas vent, supporter, described cold and hot
Source system includes compressor, evaporator, condenser, throttle valve, and the reheater includes heating source and heating tube, the gas point
Cloth device, evaporator, condenser, heating tube are located at enclosure interior；By gas access successively inwardly horizontally arranged, compressor, heating
Source is located at hull outside；Compressor, throttle valve, between evaporator is to circuit sequentially connection at condenser；Heating source and heating tube phase
Even, the filler is filled in the remaining space of enclosure interior.
Further shell material is metal or plastics, and metal material is carbon steel, stainless steel or alloy, and plastic material is
Polypropylene, ABS plastic, polycarbonate, polyformaldehyde.
Further gas distributor is AND DEWATERING FOR ORIFICE STRUCTURE, pitch of holes 1-5cm, aperture 2-10cm, aperture on orifice plate by
It is gradually reduced upwards down.
Further discharge outlet is located at housing bottom, between gas access and gas distributor.
Further condensed water drainage trough is located at the intracorporal bottom of shell, condensed water drain front of the slot be located at evaporator with it is cold
Between condenser, end is connected with discharge outlet, and front end level height is greater than end.
The compressor of further cold and heat source system is located at the outside of shell, the refrigerant in compressor be sky gas and water,
One of alcohol, freon, ethylene.
Further heating source is power supply, hot-air, hot water, and cooperation delivery pump makes when heating source is hot water or hot-air
With.
Further filler subsection filling in the intracorporal space of shell, filler material are metal, ceramics or plastics.
The three sections of fillings of further filler point, first segment are filled in the space where gas distribution grid and evaporator, fill out
Expect that type is plastics or ceramics, second segment is filled in the space where condenser, and filling kind is that ceramics or metal, third section are filled out
It fills in the space where heating tube, filling kind is metal.
The utility model has the advantages that the high efficiency demister of the present invention with Cooling and Heat Source, by traditional demister droplet collision type coalescence
It is changed to droplet pre-cooling coalescence, is first cooled down to the exhaust gas of discharge wet waste gas processing equipment first using cold and heat source system, water
In evaporator coalescence at big drips, the exhaust gas after demisting heats up mist by condenser, reduces the relative humidity of exhaust gas, passes through
Demister is discharged after crossing reheater secondary temperature elevation, while the mist carried secretly in effectively removing gas, reduces the opposite of exhaust gas
Humidity, vapor condenses caused by reducing after preventing exhaust gas from entering subsequent processing device because of temperature, corrodes follow-up equipment or to subsequent
Treatment process impacts.After condenser is placed in evaporator by the present invention, refrigerant under compressor effect in evaporator and
It being recycled between condenser, the heat exhaust gas for making full use of condenser to distribute tentatively is heated up, subsequent reheater energy consumption is saved, this
Outside, coalescence drips direction is vertical with gas flow in the present invention, can reduce influence of the gas flowing to drips, prevent
Reentrainment.Filler is filled in shell, increases the heat exchange area of exhaust gas and Cooling and Heat Source, enhances fine mist coalescence effect, filler
Subsection filling fills ceramics or plastics filler in condenser zone, can prevent the salt in mist from generating corrosion etc. to material unfavorable
It influences, subsequent condensation device and heating tube area filling metal packing can enhance heat-transfer effect, increase exhaust gas discharge temperature, this hair
Bright special gas distributor, aperture are gradually reduced from bottom to top on orifice plate, can prevent exhaust gas from forming short circuit at the top of equipment,
Gas is distributed more uniform.
Detailed description of the invention
Fig. 1 is the high efficiency demister structural schematic diagram of the present invention with Cooling and Heat Source.
Wherein: 1- shell, 2- cold and heat source system, 3- reheater, 4- filler, the gas access 101-, 102- gas distributor,
103- discharge outlet, 104- condensed water drainage trough, 105- gas vent, 106- supporter, 201- compressor, 202- evaporator,
203- condenser, 204- throttle valve, 301- heating source, 302- heating tube.
Specific embodiment
Embodiment 1
A kind of high efficiency demister with Cooling and Heat Source, including shell 1, cold and heat source system 2, reheater 3, filler 4.Shell 1 includes gas
Body entrance 101, gas distributor 102, discharge outlet 103, condensed water drainage trough 104, gas vent 105, supporter 106.It is cold and hot
Source system 2 includes compressor 201) evaporator 202, condenser 203, throttle valve 204.The reheater include heating source 301 and
Heating tube 302.The gas distributor 102, evaporator 202, condenser 203, heating tube 302 are located inside shell 1, by gas
Entrance 101 is successively inwardly horizontally arranged.Compressor 201, heating source 301 are located at outside shell 1.Compressor 201, condenser 203,
It is to circuit sequentially connection between throttle valve 204, evaporator 202.Heating source 301 is connected with heating tube 302.The filler 4 is filled
In in the 1 remaining space in inside of shell.1 material of shell be ABS plastic, gas distributor 102 be AND DEWATERING FOR ORIFICE STRUCTURE, pitch of holes 1cm,
Aperture 2cm, aperture are gradually reduced from bottom to top on orifice plate, and discharge outlet 103 is located at 1 bottom of shell, gas access 101 and gas
Between distributor 102.Condensed water drainage trough 104 is located at the bottom in shell 1, and 104 front end of condensed water drainage trough is located at evaporator
Between 202 and condenser 203, end is connected with discharge outlet 103, and front end level height is greater than end.The pressure of cold and heat source system
Contracting machine 201 is located at the outside of shell 1, and the refrigerant in compressor is freon.Heating source 301 is power supply, and filler 4 divides three sections to fill out
It fills, first segment is filled in the space where gas distribution grid 102 and evaporator 202, and 4 type of filler is plastics, second segment filling
In the space where condenser 203,4 type of filler is ceramics, and third section is filled in the space where heating tube 302,4 kinds of filler
Class is metal.
After the present apparatus is installed on the caustic wash tower of acid waste gas, the mist for taking caustic wash tower out of enters demister with gas, big
Drop directly drips under self gravity, droplet and evaporator 202 of the fine mist after the distribution of gas distributor 102 in gas
And filler 4 contacts, drop to the cold after coalescence at big drips enter condensed water drainage trough 104, final liquid is from drainage hole 103
It is discharged, the gas after demisting continues flow forward, contacts after condenser 203 tentatively preheating with heating tube 302, gas sufficiently rises
Demister is discharged after temperature.
Embodiment 2
A kind of high efficiency demister with Cooling and Heat Source, including shell 1, cold and heat source system 2, reheater 3, filler 4.Shell 1 includes gas
Body entrance 101, gas distributor 102, discharge outlet 103, condensed water drainage trough 104, gas vent 105, supporter 106.It is cold and hot
Source system 2 includes compressor 201, evaporator 202, condenser 203, throttle valve 204.The reheater include heating source 301 and
Heating tube 302.The gas distributor 102, evaporator 202, condenser 203, heating tube 302 are located inside shell 1, by gas
Entrance 101 is successively inwardly horizontally arranged.Compressor 201, heating source 301 are located at outside shell 1.Compressor 201, condenser 203,
It is to circuit sequentially connection between throttle valve 204, evaporator 202.Heating source 301 is connected with heating tube 302.The filler 4 is filled
In in the 1 remaining space in inside of shell.1 material of shell is stainless steel.Body distributor 102 is AND DEWATERING FOR ORIFICE STRUCTURE, pitch of holes 5cm, hole
Diameter 10cm, aperture are gradually reduced from bottom to top on orifice plate, and discharge outlet 103 is located at 1 bottom of shell, gas access 101 and gas
Between distributor 102.Condensed water drainage trough 104 is located at the bottom in shell 1, and 104 front end of condensed water drainage trough is located at evaporator
Between 202 and condenser 203, end is connected with discharge outlet 103, and front end level height is greater than end.The pressure of cold and heat source system
Contracting machine 201 is located at the outside of shell 1, and the refrigerant in compressor is water.Heating source 301 is hot-air, and cooperation delivery pump uses.
Filler 4 divides three sections of fillings, and first segment is filled in the space where gas distribution grid 102 and evaporator 202, and 4 type of filler is pottery
Porcelain, second segment are filled in the space where condenser 203, and 4 type of filler is metal, and third section is filled in where heating tube 302
Space, 4 type of filler be metal.
After the present apparatus is installed on the water scrubber of foul waste gas, the mist for taking water scrubber out of enters demister with gas, big
Drop directly drips under self gravity, droplet and evaporator 202 of the fine mist after the distribution of gas distributor 102 in gas
And filler 4 contacts, drop to the cold after coalescence at big drips enter condensed water drainage trough 104, final liquid is from drainage hole 103
It is discharged, the gas after demisting continues flow forward, contacts after condenser 203 tentatively preheating with heating tube 302, gas sufficiently rises
Demister is discharged after temperature.
Embodiment 3
A kind of high efficiency demister with Cooling and Heat Source, including shell 1, cold and heat source system 2, reheater 3, filler 4.Shell 1 includes gas
Body entrance 101, gas distributor 102, discharge outlet 103, condensed water drainage trough 104, gas vent 105, supporter 106. are cold and hot
Source system 2 includes compressor 201, evaporator 202, condenser 203, throttle valve 204.The reheater include heating source 301 and
Heating tube 302.The gas distributor 102, evaporator 202, condenser 203, heating tube 302 are located inside shell 1, by gas
Entrance 101 is successively inwardly horizontally arranged.Compressor 201, heating source 301 are located at outside shell 1.Compressor 201, condenser 203,
It is to circuit sequentially connection between throttle valve 204, evaporator 202.Heating source 301 is connected with heating tube 302.The filler 4 is filled
In in the 1 remaining space in inside of shell.1 material of shell is polypropylene.Body distributor 102 is AND DEWATERING FOR ORIFICE STRUCTURE, pitch of holes 3cm, hole
Diameter 10cm, aperture are gradually reduced from bottom to top on orifice plate, and discharge outlet 103 is located at 1 bottom of shell, gas access 101 and gas
Between distributor 102.Condensed water drainage trough 104 is located at the bottom in shell 1, and 104 front end of condensed water drainage trough is located at evaporator
Between 202 and condenser 203, end is connected with discharge outlet 103, and front end level height is greater than end.The pressure of cold and heat source system
Contracting machine 201 is located at the outside of shell 1, and the refrigerant in compressor is ethylene.Heating source 301 is hot water, and heating source 301 cooperates defeated
Pump is sent to use.Filler 4 divides three sections of fillings, and first segment is filled in the space where gas distribution grid 102 and evaporator 202, filler 4
Type is plastics, and second segment is filled in the space where condenser 203, and 4 type of filler is metal, and third section is filled in heating tube
Space where 302,4 type of filler are metal.
After the present apparatus is installed on the pickling tower of alkaline exhaust gas, the mist for taking caustic wash tower out of enters demister with gas, big
Drop directly drips under self gravity, droplet and evaporator 202 of the fine mist after the distribution of gas distributor 102 in gas
And filler 4 contacts, drop to the cold after coalescence at big drips enter condensed water drainage trough 104, final liquid is from drainage hole 103
It is discharged, the gas after demisting continues flow forward, contacts after condenser 203 tentatively preheating with heating tube 302, gas sufficiently rises
Demister is discharged after temperature.
Claims (9)
1. a kind of high efficiency demister with Cooling and Heat Source, which is characterized in that including shell (1), cold and heat source system (2), reheater
(3), filler (4), the shell (1) include that gas access (101), gas distributor (102), discharge outlet (103), condensed water draw
Chute (104), gas vent (105), supporter (106), the cold and heat source system (2) include compressor (201), evaporator
(202), condenser (203), throttle valve (204), the reheater (3) include heating source (301) and heating tube (302)；It is described
Gas distributor (102), evaporator (202), condenser (203), heating tube (302) are located at shell (1) inside, by gas access
(101) successively inwardly horizontally arranged；It is external that compressor (201), heating source (301) are located at shell (1)；Compressor (201), condensation
Device (203), throttle valve (204) between evaporator (202) are to circuit sequentially connection, heating source (301) and heating tube (302) phase
Even, the filler (4) is filled in the internal remaining space of shell (1).
2. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, which is characterized in that shell (1) material
For metal or plastics, metal material is carbon steel, stainless steel or alloy, and plastic material is polypropylene, ABS plastic, polycarbonate, gathers
Formaldehyde.
3. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, which is characterized in that the gas distributor
It (102) is AND DEWATERING FOR ORIFICE STRUCTURE, pitch of holes 1-5cm, aperture 2-10cm, aperture is gradually reduced from bottom to top on orifice plate.
4. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, which is characterized in that the discharge outlet (103)
Positioned at shell (1) bottom, between gas access (101) and gas distributor (102).
5. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, it is characterised in that, the condensed water drainage
Slot (104) is located at the bottom in shell (1), and condensed water drainage trough (104) front end is located at evaporator (202) and condenser (203)
Between, end is connected with discharge outlet (103), and front end level height is greater than end.
6. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, it is characterised in that, the compressor
(201) interior circularly cooling agent is one of empty gas and water, alcohol, freon, ethylene.
7. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, it is characterised in that, the heating source (301)
For power supply, hot-air, hot water, cooperation delivery pump is used when heating source (301) is hot water or hot-air.
8. a kind of high efficiency demister with Cooling and Heat Source according to claim 1, it is characterised in that, the filler (4) is in shell
Subsection filling in intracorporal space, filler material are metal, ceramics or plastics.
9. a kind of high efficiency demister with Cooling and Heat Source according to claim 8, it is characterised in that, the filler (4) point three
Section filling, first segment are filled in gas distribution grid (102) and the space where evaporator (202), filler (4) type be plastics or
Ceramics, second segment are filled in the space where condenser (203), and filler (4) type is ceramics or metal, and third section, which is filled in, to be added
Space where heat pipe (302), filler (4) type are metal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910163662.3A CN109772110B (en) | 2019-03-05 | 2019-03-05 | Efficient demister with cold and heat sources |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910163662.3A CN109772110B (en) | 2019-03-05 | 2019-03-05 | Efficient demister with cold and heat sources |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109772110A true CN109772110A (en) | 2019-05-21 |
| CN109772110B CN109772110B (en) | 2024-08-16 |
Family
ID=66486308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910163662.3A Active CN109772110B (en) | 2019-03-05 | 2019-03-05 | Efficient demister with cold and heat sources |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109772110B (en) |
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|---|---|---|---|---|
| FI20115125A0 (en) * | 2011-02-09 | 2011-02-09 | Vahterus Oy | Device for separating drops |
| CN202666453U (en) * | 2012-07-27 | 2013-01-16 | 温州亚光天宜科技有限公司 | Solvent waste gas recovery device |
| US20140000461A1 (en) * | 2012-06-25 | 2014-01-02 | National Engineering Research Center of Drying Technology and Equipment | Dehumidifying tower for exhaust gas |
| CA2829396A1 (en) * | 2012-12-04 | 2014-06-04 | General Electric Company | Exhaust gas recirculation system with condensate removal |
| CN203907779U (en) * | 2014-05-30 | 2014-10-29 | 邯郸美的制冷设备有限公司 | Dehumidifier |
| US20150114817A1 (en) * | 2012-04-04 | 2015-04-30 | Vahterus Oy | Apparatus for vapourising a medium and separating droplets as well as for condensing the medium |
| CN105032087A (en) * | 2015-04-08 | 2015-11-11 | 华南理工大学 | Windmill-tubular condensing-type demister and demisting method thereof |
| CN106215594A (en) * | 2016-08-30 | 2016-12-14 | 广州雅创环保科技有限公司 | A kind of device for processing organic exhaust gas |
| CN209791241U (en) * | 2019-03-05 | 2019-12-17 | 江苏久朗高科技股份有限公司 | Efficient demister with cold and heat sources |
-
2019
- 2019-03-05 CN CN201910163662.3A patent/CN109772110B/en active Active
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|---|---|---|---|---|
| FI20115125A0 (en) * | 2011-02-09 | 2011-02-09 | Vahterus Oy | Device for separating drops |
| US20150114817A1 (en) * | 2012-04-04 | 2015-04-30 | Vahterus Oy | Apparatus for vapourising a medium and separating droplets as well as for condensing the medium |
| US20140000461A1 (en) * | 2012-06-25 | 2014-01-02 | National Engineering Research Center of Drying Technology and Equipment | Dehumidifying tower for exhaust gas |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN109772110B (en) | 2024-08-16 |
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