CN202328303U - Waste heat recovery system for condensing anti-corrosion gas/fuel boiler - Google Patents
Waste heat recovery system for condensing anti-corrosion gas/fuel boiler Download PDFInfo
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- CN202328303U CN202328303U CN2011204577062U CN201120457706U CN202328303U CN 202328303 U CN202328303 U CN 202328303U CN 2011204577062 U CN2011204577062 U CN 2011204577062U CN 201120457706 U CN201120457706 U CN 201120457706U CN 202328303 U CN202328303 U CN 202328303U
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- heat exchanger
- exchanger body
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- flue gas
- condensing
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Abstract
The utility model discloses a waste heat recovery system for a condensing anti-corrosion gas/fuel boiler. The waste heat recovery system can be used for effectively recovering the physical heat energy of boiler flue gas, and not only recovering a great amount of sensible heat, but also recovering gasification latent heat emitted by condensation of water vapor. The waste heat recovery system structurally comprises a common heat pipe exchanger body and a solution spraying device. Heat is transferred to the other side from the flue gas side by the heat pipe exchanger through the oscillation transmission of a heat pipe and is used for heating the air or water; and a solution sprayed by a spray nozzle is uniformly dispersed on the inner walls of a heat exchange pipe and a heat exchanger at the flue gas side so as to eliminate the corrosion of the weakly acidic solution formed by condensation of the water vapor in the boiler flue gas.
Description
Technical field
The utility model relates to a kind of residual neat recovering system, and sensible heat and steam gasification latent heat and the heat exchanger body that especially can reclaim combustion gas/oil burning boiler flue gas can be by the residual neat recovering systems of faintly acid gas attack.
Background technology
Contain considerable protium in natural gas or the fuel oil, the steam vapour amount that burning produces is very big, and wherein steam volume composition is generally 15%-19% in the gas fired-boiler flue gas, and steam volume composition is 10%-12% in the flue gas that oil burning boiler produces.The exhaust gas temperature of gas fired-boiler is generally at 120-250 ℃, has sensible heat and 11% the latent heat of 7%-15% not to be utilized in the flue gas and just directly is discharged in the atmosphere, and this not only causes a large amount of energy wastes also to aggravate the thermal pollution of environment.In order to make full use of the energy, reclaim the physics heat energy of flue gas, often carry out the waste heat recovery of flue gas through the method that reduces exhaust gas temperature; And when the heat exchanger wall surface temperature is lower than the dew-point temperature of flue gas, the water vapour in the flue gas will be condensed, the recyclable a large amount of steam latent heat of this process; Meanwhile; The sour gas that contains in the flue gas forms weak acid solution, and heat exchanging wall face causes sour corrosion easily, therefore for preventing the corrosion of heat exchanger; Residual heat from boiler fume is generally just drained into atmosphere on dew-point temperature; Promptly only reclaimed a part of sensible heat, latent heat is not basically by effective recycling, and this is the basic reason that combustion gas/oil burning boiler flue gas waste heat recovery rate is low.Some one Chinese patent application file (as 200420049576,200910048782,200910238452,2009102617842,201010225079X) has been mentioned the recovery of boiler smoke latent heat; But do not consider the corrosion of weakly acidic condensed water heat exchanging device body; With the service life that has a strong impact on heat exchanger, overall economic benefit is not obvious.
The utility model content
The purpose of the utility model is for overcoming the deficiency of above-mentioned prior art; A kind of residual neat recovering system of condensing anticorrosion combustion gas/oil burning boiler is provided, and this system can not cause sensible heat and most of steam gasification latent heat of the situation recover boiler smoke of corrosion at heat exchanging device body.
For realizing above-mentioned purpose, the utility model adopts following technical proposals:
A kind of residual neat recovering system of condensing anticorrosion combustion gas/oil burning boiler; It comprises that a heat exchanger body and a part are arranged at the spray solution device in the heat exchanger body; One end of said heat exchanger body flue gas one side links to each other with the exhaust opening of combustion gas/oil burning boiler; The other end is provided with the low-temperature flue gas evacuation port, and heat exchanger body opposite side one end is provided with air or water inlet, air or water out after the heating that the other end is with hot user links to each other.
Said heat exchanger body is gravity heat pipe heat exchanger or oscillating flow heat pipe heat exchanger; Said heat exchanger body comprises housing and the oscillating flow heat pipe or the gravity assisted heat pipe that are arranged in the housing.
Said spray solution device is arranged on flue gas one side of heat exchanger body; Said spray solution device comprises the some acidity-basicity sensors that are arranged at the outside solution pump of heat exchanger body and are arranged at heat exchanger body inside; Solution pump links to each other through solution conveyor tube road some shower nozzles inner with being arranged at heat exchanger body, and said acidity-basicity sensor links to each other with solution pump through microcircuit.
Said some acidity-basicity sensors are arranged at oscillatory flow or gravity assisted heat pipe outer wall, heat exchanger body fume side inwall and condensate inlet place.
Said some shower nozzles are arranged on the inner inwall of heat exchanger body, and shower nozzle towards corresponding with oscillatory flow or gravity assisted heat pipe.
The bottom of said heat exchanger body flue gas one side is provided with a steam trap, can in time get rid of the condensed water ponding in the heat exchanger.
The import and export of air or water are equipped with the pressure and temperature sensor on the import of the flue gas on the said heat exchanger body, low-temperature flue gas evacuation port and the heat exchanger body, can appropriateness adjustment flow.
Low-temperature flue gas evacuation port place on the said heat exchanger body is provided with the flue gas acquisition port, but timing sampling is analyzed the flue gas composition.
The utility model is provided with a heat pipe or oscillating flow heat pipe heat exchanger at the afterbody of boiler exhaust gas system, and working medium transfers to the air side with heat by fume side in the heat exchanger, in order to add function such as hot-air.The heat pipe start-up temperature is low; Heat pipe still can operate as normal in the time of 60-70 ℃ for flue gas; Therefore can flue-gas temperature be reduced to below 60 ℃, flue gas can discharge a large amount of sensible heats and steam gasification latent heat, and the inwall that steam condenses in heat pipe outer wall or heat exchanger body is combined into the faintly acid droplet; The faintly acid droplet is neutral with the alkaline solution that comes the spray solution device is miscible, and the collecting system that flow to fume side is discharged through drain port.This process reclaims the sensible heat and the steam gasification latent heat of oil and gas boiler to greatest extent, and can reduce the pollution of high-temperature flue gas to atmospheric environment, really realizes energy-saving and emission-reduction.
The course of work of the utility model is: the high-temperature flue gas from boiler gets into the heat exchanger fume side; High-temperature flue gas heating heat pipe; The heat pipe startup transfers to opposite side with heat and heats new air or water; The fume side temperature is reduced to below the dew point, and steam condensed and discharged a large amount of gasification latent heats this moment, can reclaim sensible heat and a large amount of gasification latent heats simultaneously; Steam forms droplet and assembles in heat pipe outer wall; This moment, solution pump work was sprayed alkaline solution by shower nozzle to the heat pipe outside wall surface; The weak acid solution neutralization that control solution concentration and solution amount are lucky and boiler smoke condenses and forms; Form neutral drop and flow down along heat pipe, compile after steam trap discharge to do in water with or drain into municipal sewage pipe network.Heat pipe outer wall, heat exchanger fume side inwall and condensate inlet place are equipped with acidity-basicity sensor; Feed back to solution pump through the microcircuit transmission and adjust liquid inventory and lift through the frequency conversion mode, when solution is faintly acid, sensor feedback solution pump enlargement discharge; Otherwise turn flow down; All be neutral in the liquid film of final control fume side or alkalescence slightly, heat exchanging device body non-corrosiveness has prolonged heat exchanger service life.
The anticorrosion condensing flue gas waste heat recovery system that the utility model relates to does not need preparatory desulfurization processing, the heat exchanger body of flue gas not to need special anti-anti-corrosion material, and native system is simple and reliable; Heat recovery efficiency is high, and the common cost of heat exchanger material is low, and maintenance cost is few; Assembling is simple, and is easy to operate.Can reduce exhaust gas temperature effectively, the range of decrease can reach more than 100 ℃.Realize that the solar term rate of boiler can reach 10% after the fume afterheat condensing and recycling.
The utility model is preventing to reclaim the latent heat of flue gas in a large number under the prerequisite that heat exchanger body is corroded, and improves heat recovery efficiency, and the utility model not only can be the new type heat exchanger design technical support is provided, and also helps existing Modification of Heat Exchanger work.
The beneficial effect of the utility model is:
1. this heat exchanger system adopts gravity assisted heat pipe or oscillating flow heat pipe, and start-up temperature is low, can the boiler smoke temperature be reduced to 60 ℃-70 ℃, recyclable a large amount of sensible heat and steam gasification latent heat, and heat recovery efficiency improves greatly;
2. this heat exchanger does not have specific (special) requirements to material, can use ordinary carbon steel or stainless steel to make, and the heat exchanger inner surface also need not preservative treatment, does not fear corrosion;
3. system cost is low, does not need the out of stock large-scale plant that waits of the sort of desulfurization of large-size thermal power plant, and cost is extremely low;
4. condensate liquid is neutral, can drain into the urban sewage system, and is pollution-free;
5. most of faintly acid gas is absorbed in the boiler smoke after waste heat recovery, and temperature is lower, drains into the atmosphere environmentally safe.
6. this heat exchanger can be processed into modularization, and according to boiler installed power or exhaust gas volumn size adjustment heat exchanger size, easy to operate flexibly, assembling splits simple, and maintenance cost is little.
The heat of the enforcement of the utility model in can the high efficiente callback low-temperature flue gas; Efficiently solve the cold end corrosion problem, increase service life greatly; Well realized the energy-saving and emission-reduction consumption reduction,
Description of drawings
Fig. 1 is the utility model structural representation;
1. heat exchanger bodies wherein, 2. heat pipe tube bank, 3. acidity-basicity sensor, 4. shower nozzle, 5. steam trap, 6. solution pump, 7. low-temperature flue gas evacuation port, 8. air or water inlet, 9. air or water out.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further specified.
Among Fig. 1; A kind of residual neat recovering system of condensing anticorrosion combustion gas/oil burning boiler; It comprises that a heat exchanger body and a part are arranged at the spray solution device in the heat exchanger body; One end of said heat exchanger body flue gas one side links to each other with the exhaust opening of combustion gas/oil burning boiler, receives the high-temperature flue gas from the oil and gas boiler; The other end is provided with low-temperature flue gas evacuation port 7, and heat exchanger body opposite side one end is provided with air or water inlet 8, air or water out 9 after the heating that the other end is with hot user links to each other.
Heat exchange of heat pipe body 1 and the two cooperating of spray solution device.Wherein heat exchanger body 1 is assembled by housing and heat pipe tube bank 2 (oscillating flow heat pipe or gravity assisted heat pipes), and heat exchanger body 1 is gravity heat pipe heat exchanger or oscillating flow heat pipe heat exchanger; Heat exchanger body 1 comprises housing and the oscillating flow heat pipe or the gravity assisted heat pipe that are arranged in the housing.
The spray solution device is cooperating when the flue gas condensing heat exchange, in the weakly acidic solution that produces when condensing with steam.The spray solution device is arranged on flue gas one side of heat exchanger body 1; Said spray solution device comprises the some acidity-basicity sensors 3 that are arranged at the outside solution pump of heat exchanger body 6 and are arranged at heat exchanger body 1 inside; Solution pump 6 links to each other with the some shower nozzles 4 that are arranged at heat exchanger body 1 inside through the solution conveyor tube road, and said acidity-basicity sensor 3 links to each other with solution pump 6 through microcircuit.
Some acidity-basicity sensors 3 are arranged at oscillatory flow or gravity assisted heat pipe outer wall, heat exchanger body fume side inwall and condensate inlet place.Some shower nozzles 4 are arranged on the heat exchanger body 1 inner inwall, and shower nozzle 4 towards corresponding with oscillatory flow or gravity assisted heat pipe.The bottom of heat exchanger body 1 flue gas one side is provided with a steam trap 5, can in time get rid of the condensed water ponding in the heat exchanger.The import and export of air or water are equipped with the pressure and temperature sensor on the import of the flue gas on the heat exchanger body, low-temperature flue gas evacuation port and the heat exchanger body 1, can appropriateness adjustment flow.Low-temperature flue gas evacuation port place on the heat exchanger body is provided with the flue gas acquisition port, but timing sampling is analyzed the flue gas composition.
The utility model is provided with a heat pipe or oscillating flow heat pipe heat exchanger at the afterbody of boiler exhaust gas system, and working medium transfers to the air side with heat by fume side in the heat exchanger, in order to add function such as hot-air.The heat pipe start-up temperature is low; Heat pipe still can operate as normal in the time of 60-70 ℃ for flue gas; Therefore can flue-gas temperature be reduced to below 60 ℃, flue gas can discharge a large amount of sensible heats and steam gasification latent heat, and the inwall that steam condenses in heat pipe outer wall or heat exchanger body is combined into the faintly acid droplet; The faintly acid droplet is neutral with the alkaline solution that comes the spray solution device is miscible, and the collecting system that flow to fume side is discharged through drain port.This process reclaims the sensible heat and the steam gasification latent heat of oil and gas boiler to greatest extent, and can reduce the pollution of high-temperature flue gas to atmospheric environment, really realizes energy-saving and emission-reduction.
The course of work of the utility model is: the high-temperature flue gas from boiler gets into the heat exchanger fume side; High-temperature flue gas heating heat pipe; The heat pipe startup transfers to opposite side with heat and heats new air or water; The fume side temperature is reduced to below the dew point, and steam condensed and discharged a large amount of gasification latent heats this moment, can reclaim sensible heat and a large amount of gasification latent heats simultaneously; Steam forms droplet and assembles in heat pipe outer wall; This moment, solution pump 6 work were sprayed alkaline solution by shower nozzle 4 to the heat pipe outside wall surface; The weak acid solution neutralization that control solution concentration and solution amount are lucky and boiler smoke condenses and forms; Form neutral drop and flow down along heat pipe, compile after steam trap 5 discharge do in water with or drain into municipal sewage pipe network.Heat pipe outer wall, heat exchanger fume side inwall and condensate inlet place are equipped with acidity-basicity sensor 3; Feed back to solution pump 6 through the microcircuit transmission and adjust liquid inventory and lift through the frequency conversion mode, when solution is faintly acid, sensor feedback solution pump enlargement discharge; Otherwise turn flow down; All be neutral in the liquid film of final control fume side or alkalescence slightly, heat exchanging device body non-corrosiveness has prolonged heat exchanger service life.
Though the above-mentioned accompanying drawing that combines is described the specific embodiment of the utility model; But be not restriction to the utility model protection domain; One of ordinary skill in the art should be understood that; On the basis of the technical scheme of the utility model, those skilled in the art need not pay various modifications that creative work can make or distortion still in the utility model protection domain.
Claims (8)
1. the residual neat recovering system of a condensing anticorrosion combustion gas/oil burning boiler; It is characterized in that; It comprises that a heat exchanger body and a part are arranged at the spray solution device in the heat exchanger body, and an end of said heat exchanger body flue gas one side links to each other with the exhaust opening of combustion gas/oil burning boiler, and the other end is provided with the low-temperature flue gas evacuation port; Heat exchanger body opposite side one end is provided with air or water inlet, air or water out after the heating that the other end is with hot user links to each other.
2. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1 is characterized in that, said heat exchanger body is gravity heat pipe heat exchanger or oscillating flow heat pipe heat exchanger; Said heat exchanger body comprises housing and the oscillating flow heat pipe or the gravity assisted heat pipe that are arranged in the housing.
3. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1; It is characterized in that; Said spray solution device is arranged on flue gas one side of heat exchanger body; Said spray solution device comprises the some acidity-basicity sensors that are arranged at the outside solution pump of heat exchanger body and are arranged at heat exchanger body inside; Solution pump links to each other through solution conveyor tube road some shower nozzles inner with being arranged at heat exchanger body, and said acidity-basicity sensor links to each other with solution pump through microcircuit.
4. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1 is characterized in that, said some acidity-basicity sensors are arranged at oscillatory flow or gravity assisted heat pipe outer wall, heat exchanger body fume side inwall and condensate inlet place.
5. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1 is characterized in that, said some shower nozzles are arranged on the inner inwall of heat exchanger body, and shower nozzle towards corresponding with oscillatory flow or gravity assisted heat pipe.
6. the residual neat recovering system of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1 is characterized in that, the bottom of said heat exchanger body flue gas one side is provided with a steam trap.
7. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1; It is characterized in that the air on the gas approach on the said heat exchanger body, low-temperature flue gas evacuation port and the heat exchanger body or the import and export of water are equipped with the pressure and temperature sensor.
8. the residual neat recovering system of a kind of condensing anticorrosion combustion gas/oil burning boiler as claimed in claim 1 is characterized in that, the low-temperature flue gas evacuation port place on the said heat exchanger body is provided with the flue gas acquisition port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204577062U CN202328303U (en) | 2011-11-17 | 2011-11-17 | Waste heat recovery system for condensing anti-corrosion gas/fuel boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204577062U CN202328303U (en) | 2011-11-17 | 2011-11-17 | Waste heat recovery system for condensing anti-corrosion gas/fuel boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202328303U true CN202328303U (en) | 2012-07-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204577062U Expired - Lifetime CN202328303U (en) | 2011-11-17 | 2011-11-17 | Waste heat recovery system for condensing anti-corrosion gas/fuel boiler |
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| CN (1) | CN202328303U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102410550A (en) * | 2011-11-17 | 2012-04-11 | 山东天力干燥股份有限公司 | Waste heat recovery for condensing type anti-corrosive gas/oil-fired boiler |
| CN102878839A (en) * | 2012-09-27 | 2013-01-16 | 林德工程（杭州）有限公司 | Air-bath type vaporizer on basis of gravity type heat tubes and waste heat utilization |
| CN102913941A (en) * | 2012-11-08 | 2013-02-06 | 江苏双良新能源装备有限公司 | Two-stage fuel gas boiler flue gas heat energy recovery system |
| CN107036113A (en) * | 2017-04-13 | 2017-08-11 | 保定清科节能技术推广有限公司 | A kind of flue gas heat recovery system |
| CN107747750A (en) * | 2017-10-25 | 2018-03-02 | 南京师范大学 | Dining room waste heat recovery lampblack absorber based on oscillating heat pipe |
| CN110567288A (en) * | 2019-08-16 | 2019-12-13 | 新疆金禾山能源科技有限公司 | Condensation heat exchanger for flue gas dehumidification and whitening |
-
2011
- 2011-11-17 CN CN2011204577062U patent/CN202328303U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102410550A (en) * | 2011-11-17 | 2012-04-11 | 山东天力干燥股份有限公司 | Waste heat recovery for condensing type anti-corrosive gas/oil-fired boiler |
| CN102878839A (en) * | 2012-09-27 | 2013-01-16 | 林德工程（杭州）有限公司 | Air-bath type vaporizer on basis of gravity type heat tubes and waste heat utilization |
| CN102913941A (en) * | 2012-11-08 | 2013-02-06 | 江苏双良新能源装备有限公司 | Two-stage fuel gas boiler flue gas heat energy recovery system |
| CN107036113A (en) * | 2017-04-13 | 2017-08-11 | 保定清科节能技术推广有限公司 | A kind of flue gas heat recovery system |
| CN107747750A (en) * | 2017-10-25 | 2018-03-02 | 南京师范大学 | Dining room waste heat recovery lampblack absorber based on oscillating heat pipe |
| CN110567288A (en) * | 2019-08-16 | 2019-12-13 | 新疆金禾山能源科技有限公司 | Condensation heat exchanger for flue gas dehumidification and whitening |
| CN110567288B (en) * | 2019-08-16 | 2020-11-20 | 新疆金禾山能源科技有限公司 | Condensation heat exchanger for flue gas dehumidification and whitening |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120711 |
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| CX01 | Expiry of patent term |