CN108786365A - The white vapour processing unit of chimney and method - Google Patents
The white vapour processing unit of chimney and method Download PDFInfo
- Publication number
- CN108786365A CN108786365A CN201810877919.7A CN201810877919A CN108786365A CN 108786365 A CN108786365 A CN 108786365A CN 201810877919 A CN201810877919 A CN 201810877919A CN 108786365 A CN108786365 A CN 108786365A
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- room
- heat absorption
- absorption material
- chamber
- air guide
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- 238000000034 method Methods 0.000 title claims abstract description 41
- 239000000463 material Substances 0.000 claims abstract description 67
- 238000010521 absorption reaction Methods 0.000 claims abstract description 66
- 238000003860 storage Methods 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 230000008569 process Effects 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000005192 partition Methods 0.000 claims abstract description 25
- 238000009833 condensation Methods 0.000 claims abstract description 4
- 230000005494 condensation Effects 0.000 claims abstract description 4
- 238000010926 purge Methods 0.000 claims description 13
- 239000000498 cooling water Substances 0.000 claims description 8
- 238000003672 processing method Methods 0.000 claims description 2
- 238000007664 blowing Methods 0.000 claims 2
- 238000000926 separation method Methods 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 5
- 231100000719 pollutant Toxicity 0.000 abstract description 5
- 230000000505 pernicious effect Effects 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 28
- 238000005260 corrosion Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 241000219112 Cucumis Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
Abstract
The invention discloses a kind of white vapour processing units of chimney and method, device to include：Driving motor,Air guide room,Process chamber and separate and collect room,Driving motor is mounted on the top of air guide room,Air guide room is mounted on the top of process chamber,The inside of air guide room and inner treatment chamber unicom,It separates and collects room and is fixedly mounted on process chamber bottom end,The bottom end for separating and collecting room is installed with drainpipe,It is provided with air inlet and exhaust outlet on the side wall of air guide room,Air guide chamber interior is provided with switching valve,Switching valve connects driving motor and axis,Axis is disposed longitudinally in process chamber,Heat absorption material and liquid distributor are socketed on the centre position of axis,Multiple partition boards are installed on axis,Partition room forms storage chamber,Liquid distributor bottom end is installed with water inlet pipe,By being cooled down to heat absorption material,Make the white vapour condensation for encountering heat absorption material,Droplet is detached by gravity with gas,Detach the moisture content and pernicious gas in white vapour,Reach the steam and pollutant removed in white vapour,The purpose preserved the ecological environment.
Description
Technical field
The present invention relates to the Steam treatment technical fields in white vapour, and in particular to a kind of white vapour processing unit of chimney and side
Method.
Background technology
With the improvement of Environmental pollution, it is both needed to handle exhaust gas before exhaust gas discharge, but smoke stack emission goes out
White vapour in still along with steam, these steam all also can still contain Sox, NOx with harmful substance such as power plant,
Some other has oil smoke, and organic substance, the pollutant of front end is related therewith.These are with the harmful substance meeting in steam
It is dispersed into air, air can be polluted and be inhaled into human respiratory tract, ground, pollution building, melon and fruit vegetable are returned in a manner of rain, snow etc.
Dish, livestock, clothing, are finally detrimental to health.
Invention content
In order to solve the above technical problems, the present invention proposes a kind of white vapour processing unit of chimney and method, to reach removal
Steam and pollutant in white vapour, the purpose preserved the ecological environment.
In order to achieve the above objectives, technical scheme is as follows：A kind of white vapour processing unit of chimney, described device packet
It includes：Driving motor, air guide room, process chamber and room is separated and collected, the driving motor is fixedly mounted on the top of air guide room, described
Air guide room is fixedly mounted on the top of process chamber, and inside and the inner treatment chamber unicom of the air guide room are described to separate and collect room
It is fixedly mounted on process chamber bottom end, the room of separating and collecting is the hollow body of falling from power opened up and down, the bottom for separating and collecting room
End is installed with drainpipe, and air inlet and exhaust outlet, the air guide chamber interior setting are provided on the side wall of the air guide room
It is useful for separating the baffle of air inlet and exhaust outlet, the air guide chamber interior is additionally provided with switching valve, the top of the switching valve
It is connect with driving motor, axis is vertically arranged in the process chamber, the top of the axis is connect with the switching valve, described
Heat absorption material and liquid distributor are socketed on the centre position of axis, the liquid distributor is arranged in the lower section of heat absorption material and is pasted with heat absorption material
It closes, multiple partition boards is installed on the axis, are both provided on the heat absorption material and liquid distributor preset with partition board quantity Matching
Slot, the partition board are evenly distributed in the presetting slot of the surrounding of axis, the middle position of the heat absorption material and liquid distributor setting partition board
It sets, the liquid distributor bottom end is installed with water inlet pipe, and one end of the water inlet pipe is connected to liquid distributor bottom, the water inlet pipe
The other end extend to outside device.
Further, steam baffle is socketed on the axis, the steam baffle is arranged in the top of axis, the steam baffle
Area be less than the area of heat absorption material upper surface.
Further, the thickness range of the heat absorption material is between 0.3 meter to 1.5 meters.
Further, the one side that the heat absorption material is contacted with gas is arranged in parallel with axis.
Further, the water inlet pipe is fixedly mounted on the bottom of liquid distributor by screw.
Further, multiple manholes are provided on the side wall of the process chamber, the manhole is used for service personnel couple
Device is overhauled.
Further, purging motor is provided in the process chamber, the purging motor is used for will part not reaction completely
White vapour blow into the storage chamber of process chamber.
Further, the storage chamber of the partition room further includes having purging room and rest chamber, and the purging room is used for will be not complete
The white vapour handled entirely blows into other storage chambers；The rest chamber is for the storage chamber of heat absorption and exothermic storage chamber to be spaced apart.
Further, liquid distributor road is distributed in the lower section of heat absorption material, to required gas to be processed after heat absorption material heat absorption
It further touches and cools down with extraneous colder water.
A kind of white vapour processing method of chimney, steps are as follows for the method：By water inlet pipe by cooling water import liquid distributor from
And reduce the temperature of gas；White vapour is entered in process chamber by air inlet in the storage chamber of a part of partition room；Store up indoor white vapour
It is entered below heat absorption material across heat absorption material；The heat that the heat absorption material of storage chamber bottom absorbs white vapour makes the moisture content in white vapour condense,
Heat is stored on heat absorption material simultaneously；Condensed liquid is together with cooling water from the drainpipe row separated and collected below room
Go out；Heat absorption material heat release below storage chamber of the gas through another part partition room, to enter after making remaining gas temperature be promoted
It is discharged by exhaust outlet after storage chamber.
The invention has the advantages that：
(1) the present invention makes the white vapour condensation for encountering heat absorption material, detaches the water in white vapour by being cooled down to heat absorption material
Part and pernicious gas, preserve the ecological environment.
(2) material that absorbs heat in the present invention can absorb heat also can heat release, reduce part energy consumption, save device operating cost, fill
Divide the energy being utilized in processing steam, is that tradition takes off the 30%~50% of white energy consumption.
(3) what the present invention used is all direct heat transfer mode, breaches the de- white indirect heat exchange mode of tradition；
(4) breakthrough improvement, traditional heat exchange use common metal not at corrosion-resistant aspect in present invention heat exchange material
It is acid to be resistant to burn into, again very high using corrosion resistant metal price, using corrosion resistant plastics, heat-conducting system is at a fairly low, heat transfer
Efficiency is low, and it is big to make volume.
(5) apparatus of the present invention are particularly suitable for, in chimney end, it is short increasing this equipment downtime transformation time；
(6) what the present invention used is de- white, be really by gas to be processed moisture content and be partially soluble in the pollutant of water
Removal, prevents from being discharged into air, and can decide whether Treated sewage reusing production according to the water quality condensed out or enter sewage system
System is further processed.
(7) present invention can be suitably applied to any tail vapour and need de- white situation, for there is corrosion to have acid gas, advantage
It is particularly evident.
Description of the drawings
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technology description to be briefly described.
Fig. 1 is the white vapour processing device structure diagram of chimney disclosed by the embodiments of the present invention；
Fig. 2 is heat absorption material disclosed by the embodiments of the present invention and liquid distributor structural schematic diagram；
Number and the corresponding component title represented by letter in figure：
1, driving motor；2, air guide room；3, process chamber；4, room is separated and collected；5, drainpipe；6, air inlet；7, exhaust outlet；
8, switching valve；9, axis；10, absorb heat material；11, liquid distributor；12, partition board；13, water inlet pipe；14, steam baffle.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes.
The present invention provides a kind of white vapour processing unit of chimney and method, operation principle is cold by being carried out to heat absorption material
But, the white vapour condensation for encountering heat absorption material, steam is made to be condensed again through cooling water is further cooling, droplet divides after by gravity with gas
From detaching the moisture content and pernicious gas in white vapour, to reach the steam and pollutant that remove in white vapour, the gas after being dehydrated is again
It absorbs heat material heat release, adjusts relative humidity, achieve the purpose that preserve the ecological environment, vision can't see white vapour.
With reference to embodiment and specific implementation mode, the present invention is described in further detail.
As depicted in figs. 1 and 2, a kind of white vapour processing unit of chimney, described device include：Driving motor 1, air guide room 2, place
It manages room 3 and separates and collects room 4, the driving motor 1 is fixedly mounted on the top of air guide room 2, and the air guide room 2 is fixedly mounted on
The top of process chamber 3, inside and the 3 inside unicom of process chamber of the air guide room 2, the room 4 that separates and collects is fixedly mounted on place
3 bottom end of room is managed, the hollow body of falling from power for separating and collecting room 4 and being open up and down, the bottom end for separating and collecting room 4 is fixedly mounted
There is drainpipe 5, air inlet 6 and exhaust outlet 7 are provided on the side wall of the air guide room 2, the air guide room 2, which is internally provided with, to be used for
The baffle for separating air inlet 6 and exhaust outlet 7, is additionally provided with switching valve 8 inside the air guide room 2, the top of the switching valve 8 with
Driving motor 1 connects, and axis 9 is vertically arranged in the process chamber 3, and the top of the axis 9 is connect with the switching valve 8,
It is socketed with heat absorption material 10 on the centre position of the axis 9 and liquid distributor 11, the liquid distributor 11 are arranged under the material 10 that absorbs heat
It just and with heat absorption material 10 is bonded, multiple partition boards 12 is installed on the axis 9, are respectively provided on the heat absorption material 10 and liquid distributor 11
There are the presetting slot with 12 quantity Matching of partition board, the partition board 12 to be evenly distributed in the presetting slot of the surrounding of axis 9, the heat absorption
Material 10 and liquid distributor 11 are arranged the medium position of partition board 12, and 11 bottom end of the liquid distributor is installed with water inlet pipe 13, it is described into
One end of water pipe 13 is connected to 11 bottom of liquid distributor, and the other end of the water inlet pipe 13 extends to outside device.
Wherein, there is heat absorption material 10 corrosion-resistant, acid and alkali-resistance performance, switching valve 8 to be made of resistant material, process chamber
3 shells and separate and collect that 4 shell of room makes of steel plate and the one side that contact with gas is by preservative treatment.
Wherein, steam baffle 14 is socketed on the axis 9, the steam baffle 14 is arranged in the top of axis 9, the gear vapour
The area of plate 14 is less than the area of 10 upper surface of heat absorption material, and the time that steam baffle 14 makes white vapour be detained in storage chamber is elongated, makes suction
The heat absorption of hot material 10 is more abundant.
Wherein, the thickness range of the heat absorption material 10 is between 0.3 meter to 1.5 meters, heat absorption material 10 top contact at first into
The gas entered finally contacts the gas of discharge, so 10 temperature of heat absorption material on upper layer is higher and higher, 10 temperature of heat absorption material of lower layer
It is lower and lower.
Wherein, the action for controlling switching valve 8 allows different time sections control air inlet to pass through different heat absorption materials 10 from outlet,
The heat absorption material of low temperature absorbs heat, the heat absorption material heat release of high temperature.
Wherein, the heat absorption material 10 put in process chamber 3, which divides, 4-36 lattice, wherein the heat absorption material of each lattice is all to experiencing suction
Heat, blowback, heat release, standing, then absorb heat, the process of so one cycle repeatedly.
Wherein, the one side that the heat absorption material 10 is contacted with gas is arranged in parallel with axis 9.
Wherein, the water inlet pipe 13 is fixedly mounted on the bottom of liquid distributor 11 by screw, further by water inlet pipe 13
It is connect with liquid distributor 11.
Wherein, multiple manholes 10 are provided on the side wall of the process chamber, the manhole 10 is used for service personnel couple
Device is overhauled.
Wherein, purging motor is provided in the process chamber 3, the purging motor is used for white by what is partly do not reacted completely
Vapour is blown into the storage chamber of process chamber.
Wherein, the storage chamber between the partition board 12 further includes having purging room and rest chamber, and the purging room is used for will not completely
The white vapour of processing blows into other storage chambers；The rest chamber is for the storage chamber of heat absorption and exothermic storage chamber to be spaced apart.
Wherein, 11 pipeline of liquid distributor is distributed in the lower section of heat absorption material 10, is inhaled through the material 10 that absorbs heat to required gas to be processed
It further touches and cools down with extraneous colder water after heat.
Steps are as follows for the method：Cooling water is imported into liquid distributor 11 to reduce the temperature of gas by water inlet pipe 13；
White vapour is entered by air inlet 6 in the storage chamber in process chamber 3 between a part of partition board 12；Storing up indoor white vapour passes through heat absorption material to enter
10 sides under to heat absorption material；The heat that the heat absorption material 10 of storage chamber bottom absorbs white vapour makes the moisture content in white vapour condense, while by heat
It is stored on heat absorption material 10；Condensed liquid is discharged together with cooling water from the drainpipe 5 for separating and collecting 4 lower section of room；Gas
Through 10 heat release of heat absorption material below the storage chamber between another part partition board 12, to enter storage chamber after so that remaining gas temperature is promoted
It is discharged afterwards by exhaust outlet 7.
It is uniformly arranged around axis using 12 pieces of partition boards in the present invention, forms the white vapour processing unit of 12 storage chambers, chimney
After out white vapour is drawn by pipeline, be sent into white vapour processing unit by former cooking fume control equipment main air blower, gas first from 1,2,
3,4,5 storage chambers enter (1,2,3,4,5 storage chambers are heat absorption area at this time), and under the action of cooling water, gas temperature is dropped by 45 DEG C
As low as 30 DEG C or so, under the action of low temperature, the moisture in gas is condensed into liquid, reduces steam in exhaust and reaches de- white mesh
, while partial organic substances are removed with condensed water.Gas after condensed drying is discharged (at this time from 7,8,9,10,11 storage chambers
7,8,9,10,11 be heat release zone), and cold is recycled, Room the 6th purges at this time, and Room the 12nd is stood；After a certain period of time, gas is cut
Change to 2,3,4,5,6 storage chamber air inlets (at this time 2,3,4,5,6 storage chambers be heat absorption area), the exhaust of 8,9,10,11,12 storage chambers (8,9,10,
11,12 be heat release zone), the purging of Room the 7th, Room the 1st is stood, 12 such accumulation of heat cycle operations.Gas after taking off in vain is discharged into chimney,
High altitude discharge.The steam and harmful substance in gas are efficiently separated, is preserved the ecological environment.
It under special operating mode, needs to increase compression refrigerating system, refrigerant coil pipe is placed in the lower section of heat absorption material, simultaneously will
The heat dissipation of compressibility is placed in the outlet of equipment, makes full use of the heat exchange of refrigerant compression, is also not limited to certainly with compression refrigeration
System further includes various forms of coolings, heating mode.
Above-described is only the preferred embodiment of a kind of white vapour processing unit of chimney disclosed in this invention and method,
It should be pointed out that for those of ordinary skill in the art, without departing from the concept of the premise of the invention, can also do
Go out several modifications and improvements, these are all within the scope of protection of the present invention.
Claims (9)
1. a kind of white vapour processing unit of chimney, which is characterized in that described device includes：Driving motor, air guide room, process chamber and point
From collecting chamber, the driving motor is fixedly mounted on the top of air guide room, and the air guide room is fixedly mounted on the top of process chamber,
The inside of the air guide room and inner treatment chamber unicom, the room of separating and collecting is fixedly mounted on process chamber bottom end, the separation
Collecting chamber is the hollow body of falling from power opened up and down, and the bottom end for separating and collecting room is installed with drainpipe, the air guide room
Side wall on be provided with air inlet and exhaust outlet, the air guide chamber interior is provided with the gear for separating air inlet and exhaust outlet
Plate, the air guide chamber interior are additionally provided with switching valve, and the top of the switching valve is connect with driving motor, are indulged in the process chamber
To axis is provided with, the top of the axis is connect with the switching valve, and heat absorption material is socketed on the centre position of the axis
And liquid distributor, the liquid distributor are arranged in the lower section of heat absorption material and are bonded with heat absorption material, and multiple partition boards are equipped on the axis,
The presetting slot with partition board quantity Matching is both provided on the heat absorption material and liquid distributor, the partition board is evenly distributed on the four of axis
Week presetting slot in, it is described heat absorption material and liquid distributor setting partition board medium position, the liquid distributor bottom end be installed with into
One end of water pipe, the water inlet pipe is connected to liquid distributor bottom, and the other end of the water inlet pipe extends to outside device.
2. the white vapour processing unit of chimney according to claim 1, which is characterized in that it is socketed with steam baffle on the axis,
The steam baffle is arranged at the top of axis, and the area of the steam baffle is less than the area of heat absorption material upper surface.
3. the white vapour processing unit of chimney according to claim 1 or 2, which is characterized in that the thickness range of the heat absorption material
Between 0.3 meter to 1.5 meters.
4. the white vapour processing unit of chimney according to claim 3, which is characterized in that it is described heat absorption material contacted with gas one
Face is arranged in parallel with axis.
5. the white vapour processing unit of chimney according to claim 4, which is characterized in that the water inlet pipe is fixed by screw pacifies
Mounted in the bottom of liquid distributor.
6. the white vapour processing unit of chimney according to claim 5, which is characterized in that be provided on the side wall of the process chamber
Multiple manholes, the manhole overhaul device for service personnel.
7. the white vapour processing unit of chimney according to claim 6, which is characterized in that be provided with purging wind in the process chamber
Machine, the purging motor is for blowing into the white vapour partly not reacted completely in the storage chamber of process chamber.
8. the white vapour processing unit of chimney according to claim 7, which is characterized in that the storage chamber of the partition room further includes having
Room and rest chamber are purged, the purging room is used to incompletely processed white vapour blowing into other storage chambers；The rest chamber is used for will
The storage chamber of heat absorption and exothermic storage chamber are spaced apart.
9. a kind of white vapour processing method of chimney, which is characterized in that steps are as follows for the method：Cooling water is imported by water inlet pipe
Liquid distributor is to reduce the temperature of gas；White vapour is entered in process chamber by air inlet in the storage chamber of a part of partition room；Storage chamber
Interior white vapour passes through heat absorption material to enter below heat absorption material；The heat that the heat absorption material of storage chamber bottom absorbs white vapour makes water in white vapour
Part condensation, while heat being stored on heat absorption material；Condensed liquid is together with cooling water from the row separated and collected below room
Water pipe is discharged；Heat absorption material heat release below storage chamber of the gas through another part partition room, to make remaining gas temperature be promoted
It is discharged by exhaust outlet after entering storage chamber afterwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810877919.7A CN108786365A (en) | 2018-08-03 | 2018-08-03 | The white vapour processing unit of chimney and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810877919.7A CN108786365A (en) | 2018-08-03 | 2018-08-03 | The white vapour processing unit of chimney and method |
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| Publication Number | Publication Date |
|---|---|
| CN108786365A true CN108786365A (en) | 2018-11-13 |
Family
ID=64079293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810877919.7A Pending CN108786365A (en) | 2018-08-03 | 2018-08-03 | The white vapour processing unit of chimney and method |
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| Country | Link |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4491093A (en) * | 1984-03-26 | 1985-01-01 | Hoekstra I Arthur | Energy and water recovery from flue gases |
| WO2014048089A1 (en) * | 2012-09-26 | 2014-04-03 | 上海伏波环保设备有限公司 | Natural circulation indirect type flue gas reheater |
| CN105709573A (en) * | 2016-03-01 | 2016-06-29 | 上海锅炉厂有限公司 | Exhaust gas water recycling and white smoke eliminating system through condensation method |
| CN205699539U (en) * | 2016-04-29 | 2016-11-23 | 王育波 | Gravity heat-pipe type condensation receives liquid integrated device except mist dedusting |
| CN106334419A (en) * | 2016-08-26 | 2017-01-18 | 中国化学工程第六建设有限公司 | Device for removing white smoke through refrigerating and heating method |
| CN107101216A (en) * | 2017-04-20 | 2017-08-29 | 华电电力科学研究院 | One kind, which is returned, takes out the former neat stress back-heating type heat-exchange system of Anti-leakage type and its method of work |
| CN207146416U (en) * | 2017-08-03 | 2018-03-27 | 上海荣普环境科技有限公司 | A kind of rotary heat-accumulation combustion exhaust treatment system |
| CN208660730U (en) * | 2018-08-03 | 2019-03-29 | 周裕 | The white vapour processing unit of chimney |
-
2018
- 2018-08-03 CN CN201810877919.7A patent/CN108786365A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4491093A (en) * | 1984-03-26 | 1985-01-01 | Hoekstra I Arthur | Energy and water recovery from flue gases |
| WO2014048089A1 (en) * | 2012-09-26 | 2014-04-03 | 上海伏波环保设备有限公司 | Natural circulation indirect type flue gas reheater |
| CN105709573A (en) * | 2016-03-01 | 2016-06-29 | 上海锅炉厂有限公司 | Exhaust gas water recycling and white smoke eliminating system through condensation method |
| CN205699539U (en) * | 2016-04-29 | 2016-11-23 | 王育波 | Gravity heat-pipe type condensation receives liquid integrated device except mist dedusting |
| CN106334419A (en) * | 2016-08-26 | 2017-01-18 | 中国化学工程第六建设有限公司 | Device for removing white smoke through refrigerating and heating method |
| CN107101216A (en) * | 2017-04-20 | 2017-08-29 | 华电电力科学研究院 | One kind, which is returned, takes out the former neat stress back-heating type heat-exchange system of Anti-leakage type and its method of work |
| CN207146416U (en) * | 2017-08-03 | 2018-03-27 | 上海荣普环境科技有限公司 | A kind of rotary heat-accumulation combustion exhaust treatment system |
| CN208660730U (en) * | 2018-08-03 | 2019-03-29 | 周裕 | The white vapour processing unit of chimney |
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Application publication date: 20181113 |
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| RJ01 | Rejection of invention patent application after publication |