CN105833663A - High-temperature flue gas cooling device - Google Patents
High-temperature flue gas cooling device Download PDFInfo
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- CN105833663A CN105833663A CN201610361296.9A CN201610361296A CN105833663A CN 105833663 A CN105833663 A CN 105833663A CN 201610361296 A CN201610361296 A CN 201610361296A CN 105833663 A CN105833663 A CN 105833663A
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- Prior art keywords
- flue gas
- temperature
- pipe
- water
- condensation bin
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Classifications
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- 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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
- F28D3/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits with tubular conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention relates to a high-temperature flue gas cooling device. The device comprises a cylindrical condensation warehouse, and further comprises a smoke inlet pipe and at least one water inlet pipe, wherein flue gas cooling pipes are arranged in the condensation warehouse, a hot water recovery pipe is communicated at the lower end of the condensation warehouse, one end of the smoke inlet pipe extends from the side wall of the lower part of the condensation warehouse, one end of the water inlet pipe extends from the side wall of the upper part of the condensation warehouse, and a smoke discharge pipe is communicated with the upper end of the condensation warehouse, at least one nozzle is arranged at one end of the water inlet pipe which extends into the condensation warehouse, and the nozzle is located above the upper end ports of the flue gas cooling pipes. The high-temperature flue gas cooling device disclosed by the invention can lower the temperature of a flue gas which enters an adsorption tower, avoid local hot spots of activated carbon or activated coke in the adsorption tower, prolong the service life of equipment and lower the maintenance cost of the equipment. In addition, the energy of the high temperature flue gas is recovered and utilized, and the energy utilization rate is improved.
Description
Technical field
The present invention relates to industry cooling technology and energy regenerating utilizes technical field, particularly relate to a kind of high temperature
Flue gas cooling device.
Background technology
Activated coke or Activated Carbon Flue Gas Desulfurization Technology belong to dry type absorption method sulfur removal technology, rely on activated coke or
Activated carbon is to the absorption of sulfur dioxide and is parsed flue gas desulfurization circulation.Because activated coke or activated carbon have
Spectral adsorption, this technology can remove multiple harmful substances simultaneously.Sweetening process does not consumes
Water, does not has waste water, waste residue to produce, and has the environmental-protecting performance of excellence.Desulfurization product is high concentration titanium dioxide
Sulfur gas, can produce the products such as sulphuric acid, sulfur, sulfur dioxide liquid, chemical fertilizer, can effectively alleviate resource
The problem lacked.
It is fabricated to purpose with metal when the adsorption tower using active Jiao or activated carbon purifies iron-smelter
Iron making and sintering technique, Fossil fuel (coal), coke or the combustion of its compound of steam power plant
In the flue gas produce during burning, discharged, or the flue gas of discharge in industry/life scrap incinerator
In, during contained polluter, owing to flue gas itself has higher temperature, add flue gas and pass through wind
By post bake after machine adiabatic compression, when the flue-gas temperature of entrance adsorption tower is more than 150 DEG C, suction can be made
Activated carbon or activated coke in attached tower produce hot localised points, if flue-gas temperature is continued above 150 DEG C, make
Focus produces fire point, and activated carbon or activated coke may proceed to oxidation, makes activated carbon or activated coke lose efficacy and even fires
Burn, thus cause adsorption tower to damage.For this reason, it may be necessary to a kind of flue-gas-cooling system of exploitation, it is possible to control into
Enter the temperature of the flue gas of adsorption tower, it is to avoid activated carbon or activated coke in adsorption tower produce hot localised points.
Summary of the invention
The technical problem to be solved is for above-mentioned the deficiencies in the prior art, it is provided that a kind of high temperature
Flue gas cooling device.
The technical scheme is that a kind of high-temperature flue gas chiller, bag
Include cylindrical condensation bin, also include smoke-intake pipe road and at least one water inlet pipe.
Being provided with flue gas cooling pipe in described condensation bin, described condensation bin lower end is communicated with Recovery of the hot water pipe
Road, the one end in described smoke-intake pipe road stretches into from the lower sides of described condensation bin, one end of described water inlet pipe
Stretching into from the upper portion side wall of described condensation bin, the upper end of described condensation bin is communicated with smoke discharging pipe；Described enter
Water pipe stretches into one end of described condensation bin at least provided with a shower nozzle, and described shower nozzle is positioned at the cooling of described flue gas
Above the upper port of pipeline.
The invention has the beneficial effects as follows: a kind of high-temperature flue gas chiller of the present invention, can be lowered into
The temperature of the flue gas of adsorption tower, it is to avoid activated carbon or activated coke in adsorption tower produce hot localised points, extend
Service life of equipment, reduce cost of equipment maintenance.It addition, the energy of high-temperature flue gas is entered simultaneously
Row recycles, and improves capacity usage ratio, reduces the pollution to environment.
On the basis of technique scheme, the present invention can also do and improve as follows:
Further: described flue gas cooling pipe has multiple, multiple described flue gas cooling pipe helical ring windings
Put in described condensation bin, and multiple described flue gas cooling pipe all becomes with the axis direction of described condensation bin
Symmetrically it is arranged in described condensation bin.
Above-mentioned further scheme provides the benefit that: by described flue gas cooling pipe is set to spiral type
High-temperature flue gas stroke in described flue gas cooling pipe can be extended, extend cool time, play more preferably
Cooling effect.
Further: described water inlet pipe is provided with water spraying control valve, described smoke-intake pipe road is provided with flue gas control
Valve.
Above-mentioned further scheme provides the benefit that: by arranging described water spraying control valve and flue gas control valve
Further: to be additionally provided with on described water inlet pipe and detect the effusion meter of discharge in described water inlet pipe.
Above-mentioned further scheme provides the benefit that: can show eaily by arranging described effusion meter
Show the water velocity in described water inlet pipe, can compare according to the water velocity in described water inlet pipe meanwhile
Control the water-jet velocity of described shower nozzle easily.
Further: also to include that temperature-detecting device, described temperature-detecting device include the first temperature sensor
With the second temperature sensor, the detection head of described first temperature sensor is arranged on described Recovery of the hot water pipeline
In, the detection head of described second temperature sensor is arranged in described smoke discharging pipe.
Above-mentioned further scheme provides the benefit that: can monitor institute in real time by described temperature-detecting device
State in Recovery of the hot water pipeline flue-gas temperature in water temperature and smoke discharging pipe, convenient according to cigarette in described smoke discharging pipe
In temperature and Recovery of the hot water pipeline, water temperature control high-temperature flue gas is passed through speed and the water spray of described shower nozzle
Speed.
Further: also to include feed back control system, described feed back control system respectively with described injection water control
Valve processed, injection water stop valve and temperature-detecting device electrical connection, and according to the temperature of temperature-detecting device detection
Degree controls described injection water control valve and the state of injection water stop valve.
Above-mentioned further scheme provides the benefit that: can be according to described row by described feed back control system
In smoke pipeline, in flue-gas temperature and Recovery of the hot water pipeline, described injection water stop valve is controlled by water temperature in real time
System so that the flue gas discharged in described smoke discharging pipe meets the adsorption tower temperature requirements to flue gas.
Further: described shower nozzle is free to rotate by drive mechanism.
Above-mentioned further scheme provides the benefit that: by the way so that described shower nozzle ejection
Water is sprayed in described condensation bin uniformly, and it is real to high-temperature flue gas to enter many described flue gas cooling pipes
The most uniformly cool down, improve cooling effect further.
Further: also include drainage screen, described drainage screen be arranged in described smoke discharging pipe and to condensation after
Flue gas arrange outside and carry out filtration treatment before.
Above-mentioned further scheme provides the benefit that: permissible by arranging drainage screen in described smoke discharging pipe
High-temperature flue gas after cooling is carried out filtration treatment, reduces the impurity such as dust therein, reduce environment
Pollute, the pollutant entering adsorption tower can be reduced simultaneously, reduce the maintenance cost of equipment, extension device
Service life.
Further: also to include that purifier, described purifier are arranged on lower end and the institute of described condensation bin
State between Recovery of the hot water pipeline, and the hot water discharged from described condensation bin is filtered.
Above-mentioned further scheme provides the benefit that: can be to described condensation by arranging described purifier
The hot water that storehouse is discharged filters, and improves the quality discharging hot water, strengthens its purposes, put forward high-octane profit
By rate.
Further: also to include bypassing water pipe, one end of described bypass water pipe is with described Recovery of the hot water pipeline even
Logical, the other end connects with described purifier, and makes to enter described Recovery of the hot water pipe by controlling valve
The hot water in road returns to described purifier and carries out secondary filter process.
Above-mentioned further scheme provides the benefit that: by arranging described bypass water pipe, and coordinate control valve
Door forms other tube loop and the hot water entering described Recovery of the hot water pipeline is carried out secondary filter process, improves
Discharge the quality of hot water, to strengthen its purposes.
Accompanying drawing explanation
Fig. 1 is a kind of high-temperature flue gas chiller structural representation of the present invention.
In accompanying drawing, the list of parts representated by each label is as follows:
1, condensation bin, 2, smoke-intake pipe road, 3, water inlet pipe, 4, flue gas cooling pipe, 5, hot water returns
Closed tube road, 6, smoke discharging pipe, 7, shower nozzle, 8, water spraying control valve, 9, flue gas control valve, 10, stream
Gauge, the 11, first temperature sensor, the 12, second temperature sensor, 13, feed back control system, 14,
Purifier, 15, bypass water pipe, 16, back-water valve (BWV).
Detailed description of the invention
Being described principle and the feature of the present invention below in conjunction with accompanying drawing, example is served only for explaining this
Invention, is not intended to limit the scope of the present invention.
As it is shown in figure 1, a kind of high-temperature flue gas chiller structural representation, including cylindrical condensation bin
1, also include smoke-intake pipe road 2 and at least one water inlet pipe 3.
Being provided with flue gas cooling pipe 4 in described condensation bin 1, described condensation bin 1 lower end is communicated with hot water and returns
Closed tube road 5, the one end in described smoke-intake pipe road 2 stretches into from the lower sides of described condensation bin 1, described in enter
One end of water pipe 3 is stretched into from the upper portion side wall of described condensation bin 1, and the upper end of described condensation bin 1 is communicated with
Smoke discharging pipe 6.
Described water inlet pipe 3 stretches into one end of described condensation bin 1 at least provided with a shower nozzle 7, described shower nozzle
Above 7 upper port being positioned at described flue gas cooling pipe 4.
In the present embodiment, described flue gas cooling pipe 4 has multiple, multiple described flue gas cooling pipe 4 spiral shells
Rotation is circumferentially positioned in described condensation bin 1, and multiple described flue gas cooling pipe 4 is all with described condensation bin
The axis direction of 1 is arranged in described condensation bin 1 in a center of symmetryly.By by described flue gas cooling tube
Road 4 is set to spiral type can extend high-temperature flue gas stroke in described flue gas cooling pipe 4, extends
Cool time, play more preferable cooling effect.
Preferably, described water inlet pipe 3 is provided with water spraying control valve 9, and described smoke-intake pipe road 2 is provided with cigarette
Gas control valve 8.Can be the most right by arranging described water spraying control valve 9 and flue gas control valve 8
The high-temperature flue gas being passed through and the speed of condensed water are controlled, to meet the cooling need of different flue-gas temperatures
Ask.
Preferably, described water inlet pipe 3 is additionally provided with detects the effusion meter 10 of discharge in described water inlet pipe 3.
The water velocity in described water inlet pipe 3 can be shown eaily by arranging described effusion meter 10,
Meanwhile, the spray of described shower nozzle 7 can be controlled eaily according to the water velocity in described water inlet pipe 3
Water speed.
Preferably, a kind of high-temperature flue gas chiller of the present invention also includes temperature-detecting device, described temperature
Degree detection device includes that the first temperature sensor 11 and the second temperature sensor 12, described first temperature pass
The detection head of sensor 11 is arranged in described Recovery of the hot water pipeline 5, described second temperature sensor 12
Detection head is arranged in described smoke discharging pipe 6；Detect water temperature and row in described Recovery of the hot water pipeline 5 respectively
The temperature of flue-gas temperature in smoke pipeline 6.Described hot water can be monitored in real time by described temperature-detecting device
Flue-gas temperature in water temperature and smoke discharging pipe 6 in recovery channel 5, convenient according to cigarette in described smoke discharging pipe 6
In temperature and Recovery of the hot water pipeline 5, water temperature control high-temperature flue gas is passed through speed and the spray of described shower nozzle 7
Water speed.
Preferably, a kind of high-temperature flue gas chiller of the present invention also includes feed back control system 13, described
Feed back control system 13 fills with described injection water control valve 8, injection water stop valve 9 and temperature detection respectively
Put electrical connection, and control described injection water control valve 8 and injection according to the temperature of temperature-detecting device detection
The state of water stop valve 9.Can be according in described smoke discharging pipe 6 by described feed back control system 13
In flue-gas temperature and Recovery of the hot water pipeline 5, described injection water stop valve 9 is controlled by water temperature in real time, makes
The flue gas must discharged in described smoke discharging pipe 6 meets the adsorption tower temperature requirements to flue gas.
In the present embodiment, described shower nozzle 7 is free to rotate by drive mechanism.The most permissible
The water that described shower nozzle 7 is sprayed is sprayed in described condensation bin 1 uniformly, and enters many described cigarettes
Air cooling pipeline 4 realizes uniformly cooling to high-temperature flue gas, improves cooling effect further.
Preferably, a kind of high-temperature flue gas chiller of the present invention also includes drainage screen, described drainage screen
In being arranged on described smoke discharging pipe 6 and condensed flue gas is arranged outside and carry out filtration treatment before.Pass through
Drainage screen is set in described smoke discharging pipe 6 and the high-temperature flue gas after cooling can be carried out filtration treatment, fall
The impurity such as low dust therein, reduce the pollution to environment, can reduce the pollution entering adsorption tower simultaneously
Thing, reduces the maintenance cost of equipment, the service life of extension device.
Preferably, a kind of high-temperature flue gas chiller of the present invention also includes purifier 14, described water purification
Device 14 is arranged between the lower end of described condensation bin 1 and described Recovery of the hot water pipeline 5, and to from institute
The hot water stating condensation bin 1 discharge filters.Can be to described cold by arranging described purifier 14
The hot water that solidifying storehouse 1 is discharged filters, and improves the quality discharging hot water, strengthens its purposes, improves energy
Utilization rate.
Preferably, a kind of high-temperature flue gas chiller of the present invention also includes bypassing water pipe 15, described bypass
One end of water pipe 15 connects with described Recovery of the hot water pipeline 5, and the other end connects with described purifier 14,
And make the hot water entering described Recovery of the hot water pipeline 5 return to described purifier 14 by controlling valve
Carry out secondary filter process.By arranging described bypass water pipe 15, and control valve is coordinated to form other pipe back
Road also carries out secondary filter process to the hot water entering described Recovery of the hot water pipeline 5, improves and discharges hot water
Quality, to strengthen its purposes.
Here, described bypass water pipe 15 arranges a back-water valve (BWV) 16, described by opening or closing
Back-water valve (BWV) 16 can realize bypassing opening or closing of water pipe 15, thus can realize the hot water discharged
Secondary filter processes, very convenient.Preferably, here can be real by described feed back control system 13
Now automatically controlling described back-water valve (BWV) 16.
In like manner, we can also arrange bypass cigarette between described smoke discharging pipe 6 and described smoke-intake pipe road 2
Pipe, one end of described bypass smoke pipe connects with described smoke discharging pipe 6, the other end and described smoke-intake pipe road 2
Connection, carries out cooling twice process with by control valve to the flue gas entered in described smoke discharging pipe 6.
So can improve cooling effect and the filter effect of flue gas.
A kind of high-temperature flue gas chiller of the present invention, can be lowered into the temperature of the flue gas of adsorption tower,
Avoid the activated carbon in adsorption tower or activated coke to produce hot localised points, extend the service life of equipment, fall
Low cost of equipment maintenance.It addition, the energy of high-temperature flue gas is recycled simultaneously, improve energy
Amount utilization rate, reduces the pollution to environment.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all in the present invention
Spirit and principle within, any modification, equivalent substitution and improvement etc. made, should be included in this
Within bright protection domain.
Claims (10)
1. a high-temperature flue gas chiller, including cylindrical condensation bin (1), it is characterised in that:
Also include smoke-intake pipe road (2) and at least one water inlet pipe (3)；
Being provided with flue gas cooling pipe (4) in described condensation bin (1), described condensation bin (1) lower end is even
Being connected with Recovery of the hot water pipeline (5), one end of described smoke-intake pipe road (2) is from described condensation bin (1)
Lower sides stretches into, and one end of described water inlet pipe (3) is stretched into from the upper portion side wall of described condensation bin (1),
The upper end of described condensation bin (1) is communicated with smoke discharging pipe (6)；
Described water inlet pipe (3) stretches into one end of described condensation bin (1) at least provided with a shower nozzle (7),
Described shower nozzle (7) is positioned at above the upper port of described flue gas cooling pipe (4).
A kind of high-temperature flue gas chiller, it is characterised in that: described cigarette
Air cooling pipeline (4) has multiple, and multiple described flue gas cooling pipe (4) spiral surroundings are arranged on described
In condensation bin (1), and multiple described flue gas cooling pipe (4) is all with the axle of described condensation bin (1)
Line direction is arranged in described condensation bin (1) in a center of symmetryly.
A kind of high-temperature flue gas chiller, it is characterised in that enter described in:
Water pipe (3) is provided with water spraying control valve (9), and described smoke-intake pipe road (2) is provided with flue gas control valve
(8)。
A kind of high-temperature flue gas chiller, it is characterised in that enter described in:
The effusion meter (10) of detection described water inlet pipe (3) interior discharge it is additionally provided with on water pipe (3).
A kind of high-temperature flue gas chiller, it is characterised in that: also include
Temperature-detecting device, described temperature-detecting device includes that the first temperature sensor (11) and the second temperature pass
Sensor (12), the detection head of described first temperature sensor (11) is arranged on described Recovery of the hot water pipeline
(5), in, the detection head of described second temperature sensor (12) is arranged in described smoke discharging pipe (6).
A kind of high-temperature flue gas chiller, it is characterised in that: also include
Feed back control system (13), described feed back control system (13) respectively with described injection water control valve (8),
Injection water stop valve (9) and temperature-detecting device electrical connection, and according to the temperature of temperature-detecting device detection
Degree controls described injection water control valve (8) and the state of injection water stop valve (9).
7., according to high-temperature flue gas chiller a kind of described in any one of claim 1 to 6, its feature exists
In: described shower nozzle (7) is free to rotate by drive mechanism.
8., according to high-temperature flue gas chiller a kind of described in any one of claim 1 to 6, its feature exists
In: also include that drainage screen, described drainage screen are arranged in described smoke discharging pipe (6) and to condensed
Flue gas is arranged outside and is carried out filtration treatment before.
9., according to high-temperature flue gas chiller a kind of described in any one of claim 1 to 6, its feature exists
In: also include that purifier (14), described purifier (14) are arranged on described condensation bin (1)
Lower end and described Recovery of the hot water pipeline (5) between, and to the hot water discharged from described condensation bin (1)
Filter.
A kind of high-temperature flue gas chiller, it is characterised in that: also include
Bypass water pipe (15), one end of described bypass water pipe (15) is with described Recovery of the hot water pipeline (5) even
Logical, the other end connects with described purifier (14), and makes to enter described hot water by controlling valve
The hot water of recovery channel (5) returns to described purifier (14) and carries out secondary filter process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610361296.9A CN105833663A (en) | 2016-05-26 | 2016-05-26 | High-temperature flue gas cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610361296.9A CN105833663A (en) | 2016-05-26 | 2016-05-26 | High-temperature flue gas cooling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105833663A true CN105833663A (en) | 2016-08-10 |
Family
ID=56595581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610361296.9A Pending CN105833663A (en) | 2016-05-26 | 2016-05-26 | High-temperature flue gas cooling device |
Country Status (1)
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| CN (1) | CN105833663A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106958822A (en) * | 2017-05-08 | 2017-07-18 | 宜兴福鼎环保工程有限公司 | A kind of RKS turns round grate furnace CIU |
| CN109297776A (en) * | 2017-07-24 | 2019-02-01 | 深圳国技仪器有限公司 | Nitrogen condensed flue gas processor |
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| CN87200905U (en) * | 1987-01-26 | 1988-04-13 | 陈海儒 | Apparatus for removing smoke and dust with water-mixed |
| CN201832550U (en) * | 2010-08-27 | 2011-05-18 | 深圳市翔宇环保科技有限公司 | Wet cyclonic flue gas processor |
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| CN104236094A (en) * | 2013-12-31 | 2014-12-24 | 赵淑霞 | Condensation heat exchange hot water unit |
| CN204637858U (en) * | 2015-05-29 | 2015-09-16 | 湖州环清环保科技有限公司 | Shell and tube tail gas environment-friendly processing unit |
| CN205174418U (en) * | 2015-11-24 | 2016-04-20 | 浙江春晖环保能源有限公司 | Biomass boiler flue gas cooling device |
| CN205683794U (en) * | 2016-05-26 | 2016-11-16 | 武汉珂普尔节能科技有限公司 | A kind of high-temperature flue gas chiller |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87200905U (en) * | 1987-01-26 | 1988-04-13 | 陈海儒 | Apparatus for removing smoke and dust with water-mixed |
| CN201832550U (en) * | 2010-08-27 | 2011-05-18 | 深圳市翔宇环保科技有限公司 | Wet cyclonic flue gas processor |
| CN104236094A (en) * | 2013-12-31 | 2014-12-24 | 赵淑霞 | Condensation heat exchange hot water unit |
| CN204007180U (en) * | 2014-08-23 | 2014-12-10 | 中国化学工程第六建设有限公司 | A kind of waste gas residual heat recycling and processing device |
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| CN205174418U (en) * | 2015-11-24 | 2016-04-20 | 浙江春晖环保能源有限公司 | Biomass boiler flue gas cooling device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106958822A (en) * | 2017-05-08 | 2017-07-18 | 宜兴福鼎环保工程有限公司 | A kind of RKS turns round grate furnace CIU |
| CN109297776A (en) * | 2017-07-24 | 2019-02-01 | 深圳国技仪器有限公司 | Nitrogen condensed flue gas processor |
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Application publication date: 20160810 |