CN111450693A - Coal fired power plant exhaust gas purification system - Google Patents
Coal fired power plant exhaust gas purification system Download PDFInfo
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- CN111450693A CN111450693A CN202010392698.1A CN202010392698A CN111450693A CN 111450693 A CN111450693 A CN 111450693A CN 202010392698 A CN202010392698 A CN 202010392698A CN 111450693 A CN111450693 A CN 111450693A
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- power plant
- waste gas
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- 238000000746 purification Methods 0.000 title claims abstract description 44
- 239000003245 coal Substances 0.000 title claims description 16
- 239000002912 waste gas Substances 0.000 claims abstract description 79
- 239000007789 gas Substances 0.000 claims abstract description 73
- 239000007788 liquid Substances 0.000 claims abstract description 70
- 239000012535 impurity Substances 0.000 claims abstract description 39
- 238000005507 spraying Methods 0.000 claims abstract description 31
- 239000007921 spray Substances 0.000 claims abstract description 20
- 238000001179 sorption measurement Methods 0.000 claims description 24
- 238000007789 sealing Methods 0.000 claims description 12
- 239000010908 plant waste Substances 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 6
- 239000005341 toughened glass Substances 0.000 claims description 6
- 238000011049 filling Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 21
- 239000003795 chemical substances by application Substances 0.000 description 16
- 230000003472 neutralizing effect Effects 0.000 description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000000243 solution Substances 0.000 description 11
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- 239000003344 environmental pollutant Substances 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 4
- 235000017491 Bambusa tulda Nutrition 0.000 description 4
- 241001330002 Bambuseae Species 0.000 description 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 4
- 239000011425 bamboo Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/79—Injecting reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/88—Replacing filter elements
-
- 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
- B01D53/04—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 with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/52—Hydrogen sulfide
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40084—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by exchanging used adsorbents with fresh adsorbents
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention provides a waste gas purification system of a coal-fired power plant. The waste gas purification system for the coal-fired power plant comprises a shell, a gas inlet pipe and a gas exhaust pipe, wherein a liquid storage area, a spraying area and an impurity removal area are sequentially arranged in the shell from bottom to top, a spiral gas guide piece and a plurality of spray heads are arranged in the spraying area, the gas inlet pipe is arranged at the gas inlet end of the spiral gas guide piece, the spray heads are communicated with the liquid storage area through liquid conveying pipes, an impurity removal assembly for removing impurities from waste gas is arranged in the impurity removal area, and the gas exhaust pipe is arranged above the impurity removal area. When the waste gas purification system of the coal-fired power plant is used for purifying waste gas, the waste gas has high flowing speed, high treatment efficiency and good purification effect.
Description
Technical Field
The invention relates to the technical field of waste gas treatment, in particular to a waste gas purification system of a coal-fired power plant.
Background
The waste gas of the vacuum power industry is mainly concentrated in a coal-fired power plant, the waste gas generated after coal combustion in the coal-fired power plant contains a large amount of harmful gases and solids, and main pollutants in the harmful gases comprise nitrogen oxides, sulfur dioxide, carbon monoxide, smoke dust and the like. In order to protect the environment, the electric waste gas needs to be purified before being discharged.
In order to improve the treatment effect of the electric exhaust gas, the existing exhaust gas purification system usually needs to treat the exhaust gas for many times. For example, chinese patent publication No. CN 108421376a discloses a flue gas purification apparatus, which includes a flue gas dust collecting hood, a bag-type dust collector, a cooling tower, a spray tower, a dispersion purification tower, a tail gas drying tower, and an exhaust fan, which are sequentially disposed from left to right. Above-mentioned equipment carries out a lot of through setting up a plurality of independent devices and handles waste gas, though can improve the waste gas treatment effect to a certain extent, nevertheless has that area is big, the structure is complicated relatively, gas flow speed is slow etc. defects, and waste gas treatment's efficiency and effect all await improvement.
In view of this, the invention is particularly proposed.
Disclosure of Invention
The invention provides a waste gas purification system of a coal-fired power plant, which has the advantages of high flow speed of waste gas, high treatment efficiency and good purification effect when being used for purifying the waste gas.
The invention provides a waste gas purification system of a coal-fired power plant, which comprises a shell, a gas inlet pipe and a gas exhaust pipe, wherein a liquid storage area, a spraying area and an impurity removal area are sequentially arranged in the shell from bottom to top, a spiral gas guide piece and a plurality of spray heads are arranged in the spraying area, the gas inlet pipe is arranged at the gas inlet end of the spiral gas guide piece, the spray heads are communicated with the liquid storage area through liquid conveying pipes, an impurity removal component for removing impurities from waste gas is arranged in the impurity removal area, and the gas exhaust pipe is arranged above the impurity removal area.
According to the coal-fired power plant waste gas purification system, the spiral air guide piece is arranged to enable waste gas to flow spirally, so that the retention time of the waste gas in the spraying area is prolonged, and the waste gas can fully react with a neutralizer from the liquid storage area; simultaneously, the helical air guide piece has small blocking effect on waste gas, the loss of gas flow velocity is small, the waste gas can be purified under the condition of rapid flow, and the treatment efficiency and treatment effect of the waste gas are obviously improved.
In one embodiment, a liquid storage cylinder is axially arranged in the spraying area, the spiral air guide member is annularly arranged outside the liquid storage cylinder, the plurality of spray heads are distributed on the outer wall of the liquid storage cylinder, and the liquid storage cylinder is communicated with the liquid sending pipe through a connecting pipe.
Above-mentioned coal fired power plant exhaust gas purification system through set up the axial liquid section of thick bamboo of depositing in the district that sprays to set up a plurality of shower nozzles dispersion on the outer wall of depositing the liquid section of thick bamboo, thereby make shower nozzle spun neutralizer can fully distribute in the district that sprays, and then realize waste gas and neutralizer and in the abundant contact in the district that sprays, show and improve the exhaust-gas treatment effect, waste gas can discharge to reach standard.
In an embodiment, the edulcoration subassembly includes the adsorption component that is used for adsorbing the edulcoration to waste gas, the adsorption component includes the cylinder mould that is used for filling adsorption media, the cylinder mould is detachably installed in the edulcoration district.
According to the coal power plant waste gas purification system, the adsorption medium is filled by arranging the mesh cage, so that harmful substances in waste gas can be adsorbed, and the purification effect of the waste gas is improved; in addition, set up the cylinder mould as detachable, be convenient for change the adsorption medium who loads in the cylinder mould, be favorable to guaranteeing the exhaust-gas treatment effect.
Further, the edulcoration subassembly is still including being used for filtering the filtering component of edulcoration to waste gas, filtering component includes that detachably installs the filter bag in edulcoration district, the open end orientation of filter bag the inlet end in edulcoration district.
Furthermore, the open end and the closed end of the filter bag are detachably arranged at the bottom end and the top end of the mesh cage respectively, and the adsorption medium is filled between the filter bag and the mesh cage.
On one hand, the waste gas purification system of the coal power plant removes solid impurities in waste gas by arranging the filter bag, so that the waste gas purification effect is further improved; on the other hand, through setting the filter bag to detachable, be convenient for clear up the filter bag to improve the exhaust-gas treatment effect.
In one embodiment, an exhaust assembly for increasing the flow rate of exhaust gas is provided at the outlet end of the exhaust pipe.
The exhaust assembly is used for improving the gas flow rate reduced due to blockage of the impurity removal assembly, so that the gas flow rate of the whole coal-fired power plant waste gas purification system is ensured, more waste gas can be treated in unit time by the arrangement mode, and the waste gas treatment efficiency is further improved.
In an embodiment, the casing is including being located the first casing in liquid storage district, being located the second casing in spraying the district and being located the third casing in edulcoration district, the bottom and the top of second casing respectively with first casing and third casing are sealed and detachable the connection.
Further, a first access opening is formed in the second shell, and a sealing door is hinged and hermetically arranged at the first access opening.
According to the invention, the first access hole is formed in the second shell, so that the parts in the spraying area can be conveniently overhauled.
In addition, be equipped with the second access hole on the third casing second access hole department is articulated and sealed is provided with the toughened glass door.
According to the invention, the second access hole is formed in the third shell, so that each part of the impurity removing area can be conveniently overhauled; simultaneously, set up the inside situation in toughened glass door be convenient for observe edulcoration district to in time change the adsorption media in the cylinder mould and clear up the filter bag.
In one embodiment, a liquid sending pump is disposed on the liquid sending pipe, and the liquid sending pump is electrically connected to an external power source.
Compared with the prior art, the invention has the beneficial effects that at least:
1. the spiral air guide piece is arranged to enable the waste gas to flow spirally, so that the waste gas is long in residence time in the spraying area, low in flow velocity loss and more sufficient in reaction with the neutralizer, the waste gas can be purified under the condition of fast flow, and the treatment efficiency and treatment effect of the waste gas are obviously improved;
2. according to the impurity removing component, the adsorption component is arranged to adsorb harmful substances in the waste gas, and the filtering component is arranged to filter solid impurities in the waste gas, so that the purification treatment effect of the waste gas is good; in addition, the adsorption component and the filter component are convenient to disassemble, assemble and replace, and are convenient for actual operation;
3. the exhaust assembly is arranged at the gas outlet end of the exhaust pipe to improve the flowing speed of gas, so that the gas flow rate of the whole coal-fired power plant waste gas purification system is ensured, more waste gas can be treated in unit time, and the waste gas treatment efficiency is further improved.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and other drawings can be obtained by those skilled in the art without creative efforts.
FIG. 1 is a schematic configuration diagram of a coal fired power plant exhaust gas purification system of the present invention;
FIG. 2 is a schematic structural view of a spray zone of the exhaust gas purification system of a coal-fired power plant according to the present invention;
FIG. 3 is a schematic view of the structure of the impurity removal zone of the waste gas purification system of a coal-fired power plant according to the present invention;
fig. 4 is a schematic structural view of the gas outlet end of the waste gas purification system of the coal-fired power plant of the present invention.
Description of reference numerals:
1. a first housing; 2. an air inlet pipe;
3. a spraying area; 301. a second housing; 302. a support plate; 303. a liquid storage cylinder; 304. a helical air guide; 305. a spray head; 306. a connecting pipe; 307. a first access opening; 308. a sealing door; 309. a liquid feeding pump;
4. an impurity removal area; 401. a third housing; 402. a support ring; 403. a cylinder mould; 404. a filter bag; 405. an adsorbent media; 406. a second access opening;
5. an end cap; 6. an exhaust pipe; 7. an exhaust assembly.
Detailed Description
The technical solutions of the present invention will be described clearly and completely with reference to the following embodiments, and it should be understood that the described embodiments are some, but not all, embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1 to 4, the coal-fired power plant exhaust gas purification system of the present invention includes a housing, an air inlet pipe 2 and an exhaust pipe 6, wherein a liquid storage area, a spraying area 3 and an impurity removing area 4 are sequentially disposed inside the housing from bottom to top, the spraying area 3 is provided with a spiral air guide 304 and a plurality of nozzles 305, the air inlet pipe 2 is disposed at an air inlet end of the spiral air guide 304, the plurality of nozzles 305 are communicated with the liquid storage area through a liquid feeding pipe, the impurity removing area 4 is provided with an impurity removing component for removing impurities from exhaust gas, and the exhaust pipe 6 is disposed above the impurity removing area 4.
In the invention, the liquid storage area is used for storing a neutralizing agent (such as dilute sodium hydroxide solution and the like) which reacts with pollutants such as sulfide, nitrogen oxide and the like in the waste gas of the coal-fired power plant to remove; the spraying area 3 is used for contacting the neutralizing agent with the waste gas of the coal-fired power plant so as to remove the neutralizing agent and pollutants in the waste gas by reaction; the impurity removal is used for removing solid impurities such as smoke dust and the like in the waste gas of the coal-fired power plant, other pollutants and the like.
In the invention, the spiral air guide member 304 is used for guiding the coal-fired power plant waste gas to spirally rise and to contact and react with a neutralizing agent in the spraying area 3; the specific structure of the spiral air guide 304 is not limited as long as it is beneficial to maintain the exhaust gas flow rate and to make the exhaust gas sufficiently contact with the neutralizing agent, and for example, a spiral blade or the like that spirals up may be provided.
The spiral air guide member 304 increases the residence time of the waste gas in the spraying area 3, so that the waste gas can fully react with the neutralizing agent from the liquid storage area; meanwhile, the spiral air guide member 304 has small obstruction effect on the waste gas, the loss of the gas flow velocity is small, and the waste gas can be purified under the condition of rapid flow, so that the treatment efficiency and treatment effect of the waste gas are obviously improved.
In the invention, the specific structure of the shell is not strictly limited, and the interior of the shell only needs to be provided with a certain space for forming the liquid storage area, the spraying area 3 and the impurity removal area 4. In an embodiment, the shell may include a first shell 1 located in the liquid storage area, a second shell 301 located in the spraying area 3, and a third shell 401 located in the impurity removing area 4, wherein the bottom end and the top end of the second shell 301 are respectively connected with the first shell 1 and the third shell 401 in a sealing manner and in a detachable manner; more specifically, the first casing 1, the second casing 301, and the third casing 401 may be provided as cylinders having sizes matched with each other, which may be coupled by a conventional detachable coupling means such as bolts.
The waste gas purification system of the coal-fired power plant comprises a liquid storage component, a spraying component and an impurity removal component which are mutually independent, wherein each component consists of a corresponding shell and related parts inside the shell; this mode is integrated as an organic whole with stock solution subassembly, spray set, edulcoration subassembly, and area reduces greatly, and detachable connected mode is convenient for the transportation of whole system, installation, clearance and maintenance simultaneously.
The arrangement mode of the liquid storage area is not strictly limited, and the liquid storage area can be reasonably arranged according to actual requirements as long as a certain cavity is formed to accommodate a certain amount of neutralizing agent. For example, the first housing 1 may be a liquid storage region for storing a neutralizing agent; at this time, the air inlet pipe 2 may be fixedly disposed on the top side wall of the first housing 1, and it is understood that the position of the air inlet pipe 2 should be higher than the liquid level of the neutralizing agent.
Meanwhile, an opening can be arranged on the first shell 1 to be communicated with the liquid sending pipe; the position of the opening is not particularly limited as long as it is below the liquid level of the neutralizing agent, and may be specifically provided on the bottom side wall of the first casing 1. In addition, a liquid sending pump 309 can be arranged on the liquid sending pipe, and the liquid sending pump 309 can be electrically connected with an external power supply to pump the neutralizing agent in the liquid storage area to the spraying area 3; the liquid feed pump 309 is not strictly limited and is, for example, of the type QB 70. More specifically, the bottom side of the first casing 1 may be connected to the liquid-sending pump 309 through a hose, and the water outlet end of the liquid-sending pump 309 may be connected to one end of the liquid-sending pipe through a hose.
In the invention, the waste gas enters the spraying area 3 through the gas inlet pipe 2, spirally flows along the spiral air guide member 304 in the spraying area 3, simultaneously the neutralizing agent stored in the liquid storage area is sent to the spray head 305 through the liquid sending pipe and is sprayed out, the neutralizing agent is fully contacted with the waste gas in the spraying area 3, and the neutralizing agent reacts with the pollutants in the waste gas to be removed.
The specific arrangement of the spiral air guide 304 and the nozzle 305 in the present invention is not limited, as long as the exhaust gas spirally rises and the neutralizing agent sufficiently contacts. In one embodiment, a liquid storage cylinder 303 may be axially disposed in the spraying region 3, a spiral air guide 304 may be annularly disposed outside the liquid storage cylinder 303, a plurality of spray heads 305 may be distributed on an outer wall of the liquid storage cylinder 303, and the liquid storage cylinder 303 is communicated with the liquid sending pipe through a connecting pipe 306.
The mode sets up axial and deposits a liquid section of thick bamboo 303 in the middle part of spraying district 3, and a plurality of shower nozzles 305 of distributing on depositing a liquid section of thick bamboo 303 lateral wall can make the neutralizer distribute fully in spraying district 3, and then realize the abundant contact of waste gas with the neutralizer, and this mode is showing and has improved the exhaust-gas treatment effect, makes waste gas discharge up to standard.
More specifically, the second casing 301 of the spray zone 3 can be connected with the top end of the first casing 1 through bolts, the supporting plate 302 can be fixedly arranged at the bottom end inside the second casing 301 in a welding mode and the like, the liquid storage cylinder 303 can be fixedly arranged at the top end of the supporting plate 302 through bolts, the spiral air guide piece 304 can be welded at the outer side of the liquid storage cylinder 303, a plurality of spray heads 305 can be uniformly arranged on the outer wall of the liquid storage cylinder 303 through threaded connection, the top side wall of the liquid storage cylinder 303 can be connected with the connecting pipe 306 through threads in a penetrating manner, the connecting hole can be formed in the position, corresponding to the connecting pipe, of the liquid storage cylinder 303 at.
Further, a first access opening 307 may be provided on the second housing 301, and a sealing door 308 may be hinged and sealed at the first access opening 307 to allow access to the components of the shower area 3. More specifically, the first access opening 307 may be opened in the middle of the front surface of the second housing 301, the sealing door 308 may be hinged to one side of the first access opening 307, and a sealing ring may be bonded to an edge of the sealing door 308, so as to improve the sealing property between the sealing door 308 and the first access opening 307.
The structure of the impurity removing component is not strictly limited, and the impurity removing component can be reasonably arranged according to actual impurity removing requirements. In one embodiment, the impurity removing component comprises an adsorption component for performing adsorption impurity removal on the waste gas, the adsorption component comprises a net cage 403 for filling an adsorption medium 405, and the net cage 403 is detachably arranged in the impurity removing area 4.
The coal power plant waste gas purification system with the adsorption component can fill the adsorption medium 405 through the net cage 403, so that harmful substances in waste gas are adsorbed, and the purification effect of the waste gas is improved; in addition, set up the cylinder mould 403 to detachable, be convenient for change the adsorption medium 405 who fills in the cylinder mould 403, be favorable to guaranteeing the exhaust-gas treatment effect.
In addition, the edulcoration subassembly can also include the filter assembly that is used for carrying out the filtration edulcoration to waste gas, and filter assembly can include the filter bag 404 of installing at edulcoration district 4 detachablely, and the open end of filter bag 404 faces the inlet end of edulcoration district 4. The specific arrangement of the filter bag 404 is not critical, for example, the open end and the closed end of the filter bag 404 can be detachably mounted on the bottom end and the top end of the net cage 403, respectively, and the adsorption medium 405 can be filled between the filter bag 404 and the net cage 403.
More specifically, the third housing 401 may be connected to the second housing 301 by bolts, the top end of the third housing 401 may be connected to the end cap 5 by bolts, and the exhaust pipe 6 may be fixedly disposed at the top end of the end cap 5 by welding or the like. The support ring 402 can be welded at the inside bottom end of the third shell 401, the net cage 403 can be arranged at the top end of the support ring 402, the bottom end of the net cage 403 can be connected with the filter bag 404 through a string, a hook can be installed at the top end of the filter bag 404, a hanging ring is welded at the position, corresponding to the hook, of the inside top end of the net cage 403, so that the filter bag 404 can be installed, and adsorption media such as an activated carbon block can be filled in gaps between the two sides of the filter bag 404 and the net cage 403.
According to the waste gas purification system of the coal power plant, the filter bag 404 is arranged to remove solid impurities in the waste gas, so that the waste gas purification effect is further improved; in addition, by arranging the filter bag 404 to be detachable, the filter bag 404 can be cleaned conveniently, so that the waste gas treatment effect is improved.
Further, a second access opening 406 may be provided on the third housing 401, and a tempered glass door may be hinged and hermetically provided at the second access opening 406. More specifically, the second access opening 406 may be opened in the middle of the front surface of the third housing 401, and the tempered glass door is hinged to one side of the second access opening 406, so that the condition inside the impurity removing area 4 can be observed conveniently while the second access opening 406 is closed.
According to the invention, the second access hole 406 is formed in the third shell 401, so that the parts in the impurity removing area 4 can be conveniently overhauled; simultaneously, set up the toughened glass door, be convenient for observe the inside situation in edulcoration district 4 to in time change the adsorption media 405 in the cylinder mould 403 and clear up filter bag 404.
Further, an exhaust unit 7, such as an exhaust fan of JT-1380 type for example, for increasing the flow rate of exhaust gas may be provided at the outlet end of the exhaust pipe 6. More specifically, the exhaust fan can be installed inside the output end of the exhaust pipe 6 through screws, and the input end of the exhaust fan is electrically connected with the output end of the external power supply, so that the exhaust of gas is accelerated, and the exhaust gas purification efficiency is improved.
The exhaust assembly 7 is arranged to improve the gas flow rate reduced by the blockage of the impurity removal assembly, so that the gas flow rate of the whole coal-fired power plant waste gas purification system is ensured.
The working process of the waste gas purification system of the coal-fired power plant is as follows: adding a neutralizing agent dilute sodium hydroxide solution into the liquid storage area, feeding waste gas to be treated into the spraying area 3 through the air inlet pipe 2, wherein the waste gas flows in the spraying area 3 in a spiral lifting manner along the spiral air guide piece 304, and the flowing distance of the gas and the detention time in the spraying area 3 are greatly increased; meanwhile, the liquid feeding pump 309 is started to pump the dilute sodium hydroxide solution in the liquid storage area, the dilute sodium hydroxide solution is fed into the liquid storage cylinder 303 of the spraying area 3 through the liquid feeding pipe, and then the dilute sodium hydroxide solution is sprayed out from the plurality of spray nozzles 305 to react with pollutants such as sulfide and nitrogen oxide in the waste gas; waste gas after the reaction gets into edulcoration district 4, is blockked in order to get rid of solid impurity by the inside filter bag 404 of crossing of cylinder mould 403, and adsorption media 405 such as active carbon piece adsorbs the harmful substance in the waste gas simultaneously, starts the air discharge fan when gas flow to improve because of receiving the gas flow rate that the blocking of filter assembly reduced, guarantee the gas flow rate. After the operation is carried out for a period of time, the sealing door 308 of the first access hole 307 can be opened, and all parts of the spraying area 3 can be overhauled; meanwhile, the net cage 403 on the top surface of the support ring 402 can be taken out through the second access hole 406, the filter bag 404 is cleaned, the activated carbon block is replaced, and the efficiency and the effect of waste gas treatment are guaranteed.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the invention has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.
Claims (10)
1. The utility model provides a coal fired power plant exhaust gas purification system, its characterized in that, includes casing, intake pipe and blast pipe the inside of casing is by supreme storage liquid district, the district that sprays and the edulcoration district of being equipped with in proper order the district that sprays is equipped with heliciform air guide and a plurality of shower nozzle, the intake pipe sets up the inlet end of heliciform air guide, it is a plurality of the shower nozzle through send liquid pipe with storage liquid district intercommunication the edulcoration district is equipped with and is used for carrying out the edulcoration subassembly of edulcoration to waste gas, the blast pipe sets up the top in edulcoration district.
2. The system of claim 1, wherein a liquid storage cylinder is axially disposed in the spray area, the spiral air guide member is annularly disposed outside the liquid storage cylinder, the plurality of nozzles are distributed on an outer wall of the liquid storage cylinder, and the liquid storage cylinder is communicated with the liquid delivery pipe through a connecting pipe.
3. The coal-fired power plant exhaust gas purification system of claim 1, wherein the edulcoration subassembly includes an adsorption subassembly for adsorbing the edulcoration to the exhaust gas, the adsorption subassembly includes a cylinder mould for filling adsorption media, the cylinder mould is detachably installed in the edulcoration district.
4. The coal fired power plant exhaust gas purification system of claim 3, the edulcoration subassembly still includes the filter assembly who is used for filtering the edulcoration to waste gas, filter assembly is including installing the filter bag in the edulcoration district detachablely, the open end of filter bag is towards the inlet end in edulcoration district.
5. The coal fired power plant exhaust gas purification system of claim 4, wherein the open end and the closed end of the filter bag are detachably mounted at the bottom end and the top end of the mesh cage, respectively, and the adsorption medium is filled between the filter bag and the mesh cage.
6. The coal fired power plant exhaust gas purification system according to claim 1, wherein an exhaust assembly for increasing the flow rate of exhaust gas is provided at the gas outlet end of the exhaust pipe.
7. The coal-fired power plant waste gas purification system of claim 1, wherein the casing includes a first casing located in the liquid storage area, a second casing located in the spraying area, and a third casing located in the impurity removal area, and the bottom end and the top end of the second casing are respectively connected with the first casing and the third casing in a sealing and detachable manner.
8. The coal fired power plant exhaust gas purification system of claim 7, wherein a first access opening is provided on the second housing, and a sealing door is hinged and sealed at the first access opening.
9. The coal fired power plant exhaust gas purification system of claim 7, wherein a second access opening is provided on the third housing, and a tempered glass door is hinged and sealed at the second access opening.
10. The coal fired power plant exhaust gas purification system of claim 1, wherein a liquid delivery pump is provided on the liquid delivery pipe, the liquid delivery pump being electrically connected to an external power source.
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