CN110882611A - Boiler flue gas whitening system - Google Patents
Boiler flue gas whitening system Download PDFInfo
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- CN110882611A CN110882611A CN201911308365.XA CN201911308365A CN110882611A CN 110882611 A CN110882611 A CN 110882611A CN 201911308365 A CN201911308365 A CN 201911308365A CN 110882611 A CN110882611 A CN 110882611A
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 219
- 239000003546 flue gas Substances 0.000 title claims abstract description 218
- 230000002087 whitening effect Effects 0.000 title claims abstract description 34
- 238000002156 mixing Methods 0.000 claims abstract description 54
- 238000001816 cooling Methods 0.000 claims abstract description 39
- 238000009833 condensation Methods 0.000 claims abstract description 9
- 230000005494 condensation Effects 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims 1
- 239000003517 fume Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 230000009467 reduction Effects 0.000 abstract description 2
- 239000003570 air Substances 0.000 description 76
- 239000000779 smoke Substances 0.000 description 27
- 238000010438 heat treatment Methods 0.000 description 13
- 230000006872 improvement Effects 0.000 description 10
- 239000000428 dust Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 4
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000007791 dehumidification Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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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
- B01D53/005—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 heat treatment
-
- 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
- B01D53/26—Drying gases or vapours
-
- 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
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
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- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chimneys And Flues (AREA)
Abstract
The invention discloses a boiler flue gas whitening system, and belongs to the technical field of environmental protection. According to the boiler flue gas whitening system, the cooling tower and the vortex tube are arranged between the flue gas condenser and the flue gas heater, and the cooling tower separates the flue gas condenser from the vortex tube, so that the reduction of flue gas condensation efficiency and heat exchange efficiency caused by the mixing of cold and hot air flows can be prevented; the outer shunting chamber of the flue gas heater is arranged along the circumferential direction of the inner mixing chamber, the mixing chamber is communicated with the shunting chamber through a diversion pipe arranged on the surface of the mixing chamber, and hot air flows are uniformly and stably shunted after being shunted by the diversion pipe, so that flue gas in the mixing chamber can be uniformly heated; and the hot shunting can not press the flue gas into the flue pipe because of overlarge air pressure, thereby effectively preventing the flue gas from flowing back and improving the whitening effect.
Description
Technical Field
The invention belongs to the technical field of environmental protection, and particularly relates to a boiler flue gas whitening system.
Background
At present, more than 90% of units of coal-fired power plants in China adopt limestone-gypsum wet desulphurization modes, and most of the desulphurization processes remove sulfur dioxide by spray washing. The method comprises the following steps of treating boiler flue gas by processes such as denitration and dust removal, enabling the treated boiler flue gas to enter a desulfurization tower, controlling the temperature to be 45-55 ℃ through wet desulfurization reaction, enabling the flue gas discharged from a desulfurization absorption tower to be called clean flue gas, enabling the flue gas just discharged from the desulfurization tower to be wet saturated flue gas, and enabling the dew point temperature of the flue gas to be close to that of water. If the flue gas is directly discharged to the ambient air with low temperature and humidity in a wet saturation state, white smoke is generated, which contains a large amount of water vapor and some pollutants. According to the mechanism of white smoke formation and dissipation, the current mainstream treatment method is as follows: the flue gas heating technology, the flue gas condensing technology, the condensing and reheating composite technology and the like are mostly applied, but in the application of the technology, as the process is complex, the number of matched equipment is large, and the flue gas condensing and heating are included, a large amount of electric energy is consumed by the applied electric equipment in the operation process.
As in patent application No.: 2018222521809, filing date: in 2018, 12 and 29 months, the invention and creation name is: a wet desulphurization flue gas de-whitening device comprises a cooling device, a desulphurization tower, a de-whitening device and a chimney, wherein the cooling device is connected with the desulphurization tower, the desulphurization tower is connected with the de-whitening device, and the de-whitening device is connected with the chimney through flues; the bottom end of the cooling device is provided with a first cooling part, the top end of the cooling device is provided with a second cooling part, an air induction port is arranged on a shell of the cooling device between the first cooling part and the second cooling part, a fan is arranged at the air induction port, and a drain pipe is arranged at the bottom of the cooling device; the white-removing device comprises a steam inlet valve and a heat exchange tube, the heat exchange tube is arranged in the flue, and a dehydrator is arranged in front of the chimney. The device has simple structure and convenient control, but has poor whitening effect under extreme conditions such as winter.
Again as in patent application No.: 2018222521809, filing date: in 2018, 12 and 29 months, the invention and creation name is: a boiler flue gas de-whitening device adopts a de-whitening technical route for reducing humidity and dust, and adopts high-temperature hot air to adjust the suction force of a chimney and reduce the relative humidity of the flue gas. The device adopts high-efficiency condensing cooling tower equipment to carry out dust removal, cooling, condensing and dehumidifying treatment on the desulfurized clean flue gas after the wet desulphurization device; meanwhile, ambient air is introduced by adopting a gas heat exchanger to exchange heat with high-temperature flue gas, the temperature of the flue gas and the suction force of a chimney are adjusted by using high-temperature hot air, and the relative humidity of the flue gas is reduced; the gas heat exchanger is adopted to exchange heat between cold clean flue gas and hot flue gas to improve the exhaust temperature of the cold clean flue gas, the treated clean flue gas can be smoothly sent into a chimney, and white smoke can not appear even if the temperature of the flue gas is rapidly reduced to the ambient temperature when the flue gas is exhausted from a chimney opening. However, the device is complex in structure, for example, two heat exchangers are required to be used for heat exchange, a blender is required to be arranged for mixing flue gas, a plurality of flue pipelines are provided, and the device is worthy of further improvement.
To the above-mentioned problem that takes off white system flue to arrange complicacy and take off white efficiency not good, there has been the disclosure of relevant technical scheme, for example patent application number: 2018114747066, filing date: 12 and 4 in 2018, the name of the invention is: a kind of hot wet flue gas de-whiting dust-collecting equipment and de-whiting dust-collecting method to utilize it, the hot wet flue gas de-whiting dust-collecting equipment includes the suction chamber, mixing chamber, diffusion chamber demisting dust remover communicated sequentially, the hot wet flue gas de-whiting dust-collecting equipment also includes the first air blower and vortex tube, wherein, the suction chamber is used for sucking hot wet flue gas and pressurized cold air, the mixing chamber is used for mixing hot wet flue gas and cold air; the first fan is communicated with the vortex tube and used for pressurizing cold air and sending the cold air into the vortex tube; the cold airflow interface of the vortex tube is connected with the diffusion chamber, and the hot airflow interface of the vortex tube is connected to the rear of the demisting dust remover. The device utilizes vortex tube refrigeration principle, directly mixes low temperature air current and supersaturation wet flue gas, has further improved the degree of supersaturation of flue gas, has increased and has separated out the condensate water yield and droplet particle size to more easily by the capture of defroster, get rid of white dust removal processing to hot wet flue gas and have important using value.
However, the device controls the mixed heat exchange of the flue gas by adjusting the flow rate of the flue gas and the flow rate of the cold and hot airflow separated by the vortex tube, the air pressure of the airflow is not easy to control, and the flue gas backflow phenomenon can be caused, so that the system needs to be further optimized to improve the whitening efficiency and quality.
Disclosure of Invention
1. Technical problem to be solved by the invention
The invention aims to overcome the defect of uneven heating of flue gas caused by improper control of airflow partial pressure of a vortex tube in the existing de-whitening system, and provides a boiler flue gas de-whitening system.
2. Technical scheme
In order to achieve the purpose, the technical scheme provided by the invention is as follows:
the invention discloses a boiler flue gas whitening system, which comprises a flue gas condenser, a cooling tower, a vortex tube and a flue gas heater which are sequentially connected, wherein the vortex tube is used for separating cold and hot air flows, the generated cold air flows are used for cooling circulating water by the cooling tower, the flue gas heater is of a double-layer structure and comprises an outer-layer flow dividing chamber and an inner-layer mixing chamber, flue gas condensed by the flue gas condenser is introduced into the mixing chamber, the mixing chamber is communicated with the flow dividing chamber through a flow guide pipe arranged on the surface of the mixing chamber, and hot air flows generated by the vortex tube are introduced into the flow dividing chamber and enter the mixing chamber along the flow guide pipe to realize mixed heat exchange with the.
As a further improvement of the invention, the bottom wall of the shunting chamber comprises end horizontal sections at two ends and a middle extended section, the middle extended section is provided with a flue gas inlet communicated with the mixing chamber, and the end horizontal section is provided with an air inlet communicated with the shunting chamber.
As a further improvement of the present invention, the air inlet includes a first air inlet and a second air inlet, which are respectively disposed on the end horizontal sections on both sides of the middle protruding section.
As a further improvement of the invention, the top wall of the mixing chamber is provided with a flue gas outlet which is communicated with a chimney through a smoke exhaust pipe.
As a further improvement of the invention, the ratio of the height of the middle extending section to the height of the flue gas heater is 1/6-1/4.
As a further improvement of the invention, the draft tube is horizontally arranged or obliquely arranged along the wall surface towards the direction of the flue gas inlet.
As a further improvement of the invention, the wall surface of the side wall of the mixing chamber is also provided with a flue gas baffle plate, the flue gas baffle plate is provided with a shunting hole, and the flue gas baffle plate and the diversion pipe are alternately arranged.
As a further improvement of the invention, the cooling tower is communicated with the flue gas condenser through a circulating pipe.
As a further improvement of the invention, a demister is arranged between the flue gas condenser and the flue gas heater, and the demister is communicated with the flue gas inlet of the mixing chamber through the flue gas inlet pipe.
As a further improvement of the invention, a pressure gauge is also arranged on a hot airflow pipe communicated between the vortex pipe and the flue gas heater.
3. Advantageous effects
Compared with the prior art, the technical scheme provided by the invention has the following remarkable effects:
(1) according to the boiler flue gas whitening system, the cooling tower and the vortex tube are arranged between the flue gas condenser and the flue gas heater, and the cooling tower separates the flue gas condenser from the vortex tube, so that the reduction of flue gas condensation efficiency and heat exchange efficiency caused by the mixing of cold and hot air flows can be prevented; the outer shunting chamber of the flue gas heater is arranged along the circumferential direction of the inner mixing chamber, the mixing chamber is communicated with the shunting chamber through a diversion pipe arranged on the surface of the mixing chamber, and hot air flows are uniformly and stably shunted after being shunted by the diversion pipe, so that flue gas in the mixing chamber can be uniformly heated; and the hot shunting can not press the flue gas into the flue pipe because of overlarge air pressure, thereby effectively preventing the flue gas from flowing back and improving the whitening effect.
(2) According to the boiler flue gas whitening system, the bottom wall of the shunting chamber is of a three-section structure, the flue gas inlet is arranged at the middle extending section, the heat flow inlets are arranged at the end horizontal sections at two sides, the guide pipes are obliquely arranged along the wall of the mixing chamber in the direction facing the flue gas inlet, and the sub-air flows at the bottom and the side wall are matched to form a peripheral hot air flow layer, so that flue gas disturbance is fully promoted, the flue gas is uniformly heated, and local white smoke is prevented from being formed.
(3) According to the boiler flue gas whitening system, the pressure gauge is further arranged on the hot gas flow pipe communicated between the vortex tube and the flue gas heater to monitor the pressure of hot gas flow generated by the vortex tube, and workers can adjust the power of the vortex tube according to the pressure gauge, so that the adjustment of sub-gas flow in the mixing chamber is realized, the flue gas can be better subjected to heat exchange, and the flue gas whitening is realized.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention, and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic structural diagram of a boiler flue gas whitening system according to the present invention;
FIG. 2 is a schematic view of the flue gas heater of the present invention;
FIG. 3 is a schematic view of a flue gas heater according to embodiment 3;
fig. 4 is a schematic structural view of a flue gas heater in embodiment 4.
100. A flue gas condenser; 110. a cooling tube; 111. a dehumidification pipe; 112. a circulation pipe;
200. a demister;
300. a cooling tower; 310. a water outlet pipe; 311. a water tank;
400. a vortex tube; 410. an eddy nozzle; 411. a cold air end; 412. a hot gas end; 413. a vortex chamber; 420. a cold air pipe; 421. a hot gas pipe; 422. a first intake pipe; 423. a second intake pipe;
500. a flue gas heater; 510. a shunting chamber; 511. a first air inlet; 512. a second air inlet; 520. a mixing chamber; 521. a flue gas inlet; 522. a flue gas outlet; 523. a flow guide port; 524. a flue gas baffle; 525. a shunt hole;
600. a chimney; 610. a smoke exhaust pipe.
Detailed Description
For a further understanding of the invention, reference should be made to the following detailed description taken in conjunction with the accompanying drawings and examples.
The boiler flue gas whitening effect is related to the temperature and the humidity of the discharged flue gas, so that a flue gas condensing device and a flue gas heating device are often arranged in the existing flue gas whitening system to improve the temperature and the humidity of the discharged flue gas and reduce the content of the generated white smoke. The vortex tube is characterized in that the introduced high-pressure air can be divided to obtain low-temperature cold air flow and high-temperature hot air flow, and the vortex tube is of a pure mechanical structure and cannot generate chemical pollution. The structure of the vortex tube is well known in the art and will not be described in detail herein.
The inventor summarizes the working principle as follows: after high-pressure air is introduced into the vortex tube, the airflow rotates at a very high speed to flow to a hot airflow outlet of the vortex tube, a part of the airflow flows out through the control valve, and after the rest of the air is blocked, the air reversely rotates at the same speed in the original airflow ring and flows to a cold airflow outlet of the vortex tube, and finally the air is separated into cold airflow and hot airflow. Wherein the cold air flow enters the condensing equipment through the pipeline to realize the cooling of the flue gas, and the hot air flow enters the heating equipment through the pipeline to exchange heat with the flue gas.
It should be noted that, under normal conditions, one end of the flue gas heating device in the flue gas whitening system is communicated with the flue gas inlet pipe, and the other end is communicated with the flue gas exhaust pipe, but because the high-speed generated airflow in the vortex pipe is unstable, the problem exists when the high-speed generated airflow is directly introduced into the flue gas heating device: when the air pressure of hot air flow generated by the vortex tube is larger than the air pressure of flue gas introduced into the flue gas heating equipment, the high-pressure air flow can press the flue gas in the flue gas heating equipment into a flue gas inlet pipeline, so that the flue gas backflow phenomenon is caused, at the moment, the heat exchange efficiency of the flue gas heating equipment on the flue gas is greatly reduced, and the whitening effect of the whole system is greatly reduced, so that how to fully utilize cold and hot air flow generated by the vortex tube and prevent the flue gas backflow is realized, the heat exchange efficiency of the flue gas heating equipment is improved, and the problem to be solved is that the vortex tube is applied to a.
Example 1
With reference to fig. 1 and fig. 2, the boiler flue gas whitening system of the present embodiment includes a flue gas condenser 100, a cooling tower 300, a vortex tube 400 and a flue gas heater 500, which are connected in sequence, wherein the vortex tube 400 is used for separating cold and hot air flows, the generated cold air flows are used for cooling circulating water by the cooling tower 300, the flue gas heater 500 is a double-layer structure and includes an outer-layer diversion chamber 510 and an inner-layer mixing chamber 520, flue gas condensed by the flue gas condenser 100 is introduced into the mixing chamber 520, the mixing chamber 520 is communicated with the diversion chamber 510 through a diversion tube 523 arranged on a surface thereof, and hot air flows generated by the vortex tube 400 are introduced into the diversion chamber 510 and enter the mixing chamber 520 along the diversion tube 523 to realize mixed heat exchange with the flue gas.
In order to make full use of cold and hot air flows generated by the vortex tube in the prior art, the vortex tube is usually directly arranged on a pipeline communicated between a condenser and a heat exchanger, and the cold and hot air flows are simultaneously flowed to the same pipeline, so that the cold and hot air flows are easily mixed, and the condensation efficiency and the heat exchange efficiency of flue gas are reduced. In order to solve the problem, a cooling tower 300 is arranged between the flue gas condenser 100 and the vortex tube 400, and the flue gas condenser 100 is separated from the vortex tube 400 by the cooling tower 300 so as to prevent the cold and hot gas flows from mixing.
Specifically in this embodiment, be equipped with the water pump between flue gas condenser 100 and the cooling tower 300 and both are connected through cooling tube 110, and outlet pipe 310 and water tank 311 intercommunication are passed through to cooling tower 300 bottom, and the cooling water in the water pump drive water tank 311 flows to flue gas condenser 100 to the realization is to the condensation cooling of clean flue gas, and the moisture in the heat transfer back flue gas is saturated after the temperature reduces and is appeared, and moisture condenses and is discharged by the drain, and the flue gas then gets into flue gas heater 500. The vortex tube 400 is connected with an air compressor, the air compressor presses high-pressure air into a vortex chamber 413 along a vortex nozzle 410, cold air flow generated in the vortex chamber 413 is discharged into the cooling tower 300 through a cold air tube 420 connected with a cold air end 411, so that further cooling of cooling water is realized, and the heat transfer efficiency of the flue gas condenser 100 is improved. In this embodiment, the circulating water is used as a cooling medium in the flue gas condenser 100, and after the flue gas is condensed by the cooling water, the smoke dust and soluble pollutants in the flue gas are reduced.
Further, in this embodiment, the hot air flow generated in the swirl chamber 413 is discharged into the flue gas heater 500 through the hot air pipe 421 connected to the hot air end 412, so as to realize mixed heat exchange of flue gas, the temperature of the flue gas is increased after the flue gas is heated in the flue gas heater 500, diffusion of flue gas moisture can be completed when no moisture is separated out, and the smoke plume phenomenon can be effectively solved.
Further, in order to prevent the smoke from generating the backflow phenomenon, the smoke heater 500 is designed to be a double-layer structure, and specifically comprises an outer-layer diversion chamber 510 and an inner-layer mixing chamber 520, the mixing chamber 520 is communicated with the diversion chamber 510 through a diversion pipe 523 arranged on the surface of the mixing chamber 520, the smoke is introduced into the mixing chamber 520, and hot air is introduced into the diversion chamber 510. Because the outer diversion chamber 510 is arranged along the circumference of the inner mixing chamber 520, the flue gas in the mixing chamber 520 can be uniformly heated; in addition, after the hot air flow generated by the vortex tube 400 passes through the shunting action of the flow guide tube 523, the generated heat is uniformly and stably shunted, and the smoke is not pressed into the smoke inlet pipeline due to overlarge air pressure, so that the smoke is effectively prevented from flowing back, the mixed heat exchange of the smoke is facilitated, and the whitening effect is improved.
Example 2
The structure of the boiler flue gas whitening system of the present embodiment is substantially the same as that of embodiment 1, further, the bottom wall of the flow dividing chamber 510 includes end horizontal sections 530 at both ends and a middle extended section 531, the middle extended section 531 is provided with a flue gas inlet 521 communicated with the mixing chamber 520, and the end horizontal section 530 is provided with an air inlet communicated with the flow dividing chamber 510. Preferably, the ratio of the height of the middle protruding section 531 to the height of the flue gas heater 500 is 1/6-1/4.
In order to promote the uniform mixing of the flue gas and the hot gas flow, the bottom wall of the flow dividing chamber 510 is provided with a three-segment structure, wherein the middle protruding section 531 is protruded, and the flue gas inlet 521 is arranged on the middle protruding section 531, so as to send the flue gas into the middle position of the flow dividing chamber 510. Specifically, in the present embodiment, the duct 523 is disposed horizontally or obliquely along the wall toward the flue gas inlet 521.
Preferably, the air inlets in this embodiment include a first air inlet 511 and a second air inlet 512, and the first air inlet 511 and the second air inlet 512 are respectively disposed on the end horizontal section 530 of the bottom wall of the diverging chamber 510. On one hand, the two air inlets can divide hot air flow generated by the vortex tube 400 into two sub-air flows, the length of an air flow inlet path is prolonged, the pressure of the fluid is dispersed, and the backflow of smoke gas caused by concentrated pressure of the hot air flow is prevented; on the other hand, the flow guide pipe 523 is obliquely arranged along the wall surface towards the direction of the flue gas inlet 521, and is matched with the sub-flow at the bottom to form a peripheral hot air flow layer, so that the disturbance of the flue gas can be fully promoted, and the uniform heating of the flue gas is realized.
Specifically, in this embodiment, a flue gas outlet 522 is disposed on the top wall of the mixing chamber 520, the flue gas outlet 522 is communicated with the chimney 600 through the smoke exhaust pipe 610, flue gas with uniform temperature distribution is formed at the top of the mixing chamber 520 after being fully mixed and heat exchanged, and is exhausted along the chimney 600, and finally exhausted to the high altitude through the chimney 600. Because the moisture, smoke dust and soluble pollutants in the smoke are removed in the condensation and crystallization process of the front smoke condensation equipment, and the temperature of the smoke is stably raised by the rear smoke heating equipment, the smoke can be well diffused when being discharged from the chimney 600, the phenomenon of 'white smoke' caused by condensation and separation of the moisture can not be generated, the emission of the pollutants can be reduced, the visual influence of the 'white smoke' can be eliminated, and the smoke condensation and crystallization equipment has multiple benefits of environmental protection and the like.
Example 3
With reference to fig. 3, the structure of the boiler flue gas whitening system of this embodiment is substantially the same as that of embodiment 2, and further, in this embodiment, a flue gas baffle 524 is horizontally disposed on a wall surface of a side wall of the mixing chamber 520, a flow guide hole 525 is formed in the flue gas baffle 524, and the flue gas baffle 524 and the flow guide pipe 523 are alternately disposed. The flue gas baffle 524 in this embodiment is communicated with the inner side wall of the mixing chamber 520, and the flue gas baffle 524 is provided with the diversion holes 525, so that the flue gas can be dispersed, and the hot air flow can be further promoted to uniformly mix and heat the flue gas.
Example 4
Referring to fig. 4, the structure of the boiler flue gas whitening system of the present embodiment is substantially the same as that of embodiment 2, except that: in this embodiment, the flue gas baffles 524 are obliquely arranged along the wall surface towards the flue gas outlet 522, and the flue gas baffles 524 and the flow guide pipes 523 are alternately arranged. The flue gas baffle 524 in this embodiment is disposed to be inclined upward, so as to prevent the flue gas from being discharged to the flue gas outlet 522, and prolong the residence time of the flue gas in the mixing chamber 520, so that the hot air flow can sufficiently disturb and heat the flue gas.
Example 5
The structure of the boiler flue gas whitening system of this embodiment is substantially the same as that of embodiment 2, and preferably, a demister 200 is further disposed between the flue gas condenser 100 and the flue gas heater 500 in this embodiment, and the demister 200 is communicated with the flue gas inlet 521 of the mixing chamber 520 through the flue gas inlet pipe 111 to achieve dehumidification of the flue gas. In this embodiment, the cooling tower 300 is communicated with the flue gas condenser 100 through the circulating pipe 112, so as to realize the recycling of cooling water and save energy. Particularly, in this embodiment, the heat exchange elements in the flue gas condenser 100 are finned tubes, so that the heat exchange efficiency is high, circulating water flows in the tubes, flue gas exchanges heat with the flue gas outside the tubes, and a drain outlet is formed in the bottom of the flue gas condenser, so that condensate can be conveniently discharged and treated.
Preferably, in this embodiment, a pressure gauge is further disposed on the hot air flow pipe 421 communicated between the vortex tube 400 and the flue gas heater 500 to monitor the pressure of the hot air flow generated by the vortex tube 400, and a worker can adjust the power of the vortex tube 400 according to the pressure gauge, so as to adjust the sub-air flow in the mixing chamber 520, so as to better exchange heat with the flue gas and realize white removal of the flue gas.
The above examples are only intended to illustrate the technical solution of the present invention, but not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and such modifications or substitutions do not depart from the spirit and scope of the corresponding technical solutions of the embodiments of the present invention.
Claims (10)
1. The utility model provides a boiler flue gas takes off white system which characterized in that: including flue gas condenser (100), cooling tower (300), vortex tube (400) and flue gas heater (500) that connect gradually, vortex tube (400) are used for separating cold and hot air current, and the cold air current of its production is used for cooling tower (300) to carry out cooling to the circulating water, flue gas heater (500) are bilayer structure, and it includes outer shunting chamber (510) and inlayer mixing chamber (520), flue gas behind flue gas condenser (100) condensation lets in mixing chamber (520), mixing chamber (520) through honeycomb duct (523) that its surface arranged with shunting chamber (510) intercommunication, the hot gas flow that vortex tube (400) produced lets in shunting chamber (510) and gets into mixing chamber (520) along honeycomb duct (523) in order to realize with the mixed heat transfer of flue gas.
2. The boiler flue gas whitening system according to claim 1, characterized in that: the bottom wall of the shunting chamber (510) comprises end part horizontal sections (530) at two ends and a middle extending section (531), a flue gas inlet (521) communicated with the mixing chamber (520) is formed in the middle extending section (531), and an air inlet communicated with the shunting chamber (510) is formed in the end part horizontal section (530).
3. The boiler flue gas whitening system according to claim 2, characterized in that: the air inlets include a first air inlet (511) and a second air inlet (512), and the first air inlet (511) and the second air inlet (512) are respectively arranged on the end horizontal sections (530) at both sides of the middle protruding section (531).
4. The boiler flue gas whitening system according to claim 2, characterized in that: be equipped with exhanst gas outlet (522) on the roof of mixing chamber (520), exhanst gas outlet (522) are through discharging fume pipe (610) and chimney (600) intercommunication.
5. The boiler flue gas whitening system according to claim 2, characterized in that: the ratio of the height of the middle extending section (531) to the height of the flue gas heater (500) is 1/6-1/4.
6. The boiler flue gas whitening system according to any one of claims 2 to 5, characterized in that: the draft tube (523) is horizontally arranged or obliquely arranged along the direction of the wall surface towards the flue gas inlet (521).
7. The boiler flue gas whitening system according to claim 6, characterized in that: still be equipped with flue gas baffle (524) on the lateral wall of mixing chamber (520), be equipped with reposition of redundant personnel hole (525) on flue gas baffle (524), just flue gas baffle (524) with honeycomb duct (523) set up in turn.
8. The boiler flue gas whitening system according to any one of claims 1 to 7, characterized in that: the cooling tower (300) is communicated with the flue gas condenser (100) through a circulating pipe (112).
9. The boiler flue gas whitening system according to claim 8, characterized in that: a demister (200) is further arranged between the flue gas condenser (100) and the flue gas heater (500), and the demister (200) is communicated with a flue gas inlet (521) of the mixing chamber (520) through a flue gas inlet pipe (111).
10. The boiler flue gas whitening system according to claim 8, characterized in that: and a pressure gauge is also arranged on a hot airflow pipe (421) communicated between the vortex pipe (400) and the flue gas heater (500).
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