CN110068021B - Long jet tube shock wave soot blower with cooling and soot deposition preventing functions - Google Patents
Long jet tube shock wave soot blower with cooling and soot deposition preventing functions Download PDFInfo
- Publication number
- CN110068021B CN110068021B CN201910442922.0A CN201910442922A CN110068021B CN 110068021 B CN110068021 B CN 110068021B CN 201910442922 A CN201910442922 A CN 201910442922A CN 110068021 B CN110068021 B CN 110068021B
- Authority
- CN
- China
- Prior art keywords
- flue gas
- shock wave
- long
- pipeline
- flue
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 230000035939 shock Effects 0.000 title claims abstract description 53
- 239000004071 soot Substances 0.000 title claims abstract description 30
- 230000008021 deposition Effects 0.000 title claims abstract description 13
- 238000001816 cooling Methods 0.000 title claims abstract description 9
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 87
- 239000003546 flue gas Substances 0.000 claims abstract description 87
- 239000007921 spray Substances 0.000 claims abstract description 67
- 239000000428 dust Substances 0.000 claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 23
- 238000009826 distribution Methods 0.000 claims abstract description 11
- 238000000746 purification Methods 0.000 claims abstract description 10
- 238000009825 accumulation Methods 0.000 claims abstract description 8
- 238000004140 cleaning Methods 0.000 claims description 19
- 239000000779 smoke Substances 0.000 claims description 18
- 230000007797 corrosion Effects 0.000 claims description 4
- 238000005260 corrosion Methods 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 238000003466 welding Methods 0.000 claims description 4
- 238000007664 blowing Methods 0.000 abstract description 10
- 238000009827 uniform distribution Methods 0.000 abstract description 3
- 238000004939 coking Methods 0.000 abstract description 2
- 238000002485 combustion reaction Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J3/00—Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
- F23J3/02—Cleaning furnace tubes; Cleaning flues or chimneys
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2700/00—Ash removal, handling and treatment means; Ash and slag handling in pulverulent fuel furnaces; Ash removal means for incinerators
- F23J2700/001—Ash removal, handling and treatment means
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Chimneys And Flues (AREA)
Abstract
A long-jet pipe shock wave soot blower with cooling and soot deposition preventing functions in the technical field of boiler soot blowing comprises a gas distribution ignition device, an ignition pipeline, a shock wave generator, a long jet pipe, a furnace wall, a flue gas pipeline, a flue gas dust removal purification system, an induced draft fan, a flue pipe, a clean flue gas pipeline, a clean flue gas control valve and a clean flue gas one-way valve. In the invention, the long spray pipe penetrates through the furnace wall and is arranged in the flue, the bottom of the long spray pipe is symmetrically provided with a plurality of spray nozzles with gradually changed sizes, and the full-area coverage of soot blowing and the uniform distribution of shock wave energy can be realized; the clean flue gas pipeline can introduce clean flue gas after purification treatment into the shock wave generator, continuous air inflow is formed in the shock wave generator and the long spray pipe by utilizing negative pressure in the flue and micro positive pressure at the outlet of the induced draft fan, dust-containing flue gas is prevented from entering the long spray pipe and the shock wave generator, the problems of dust accumulation, coking, blockage and the like are prevented, and meanwhile, the clean flue gas with lower temperature plays a certain cooling role on the long spray pipe in the high-temperature flue.
Description
Technical Field
The invention relates to a soot blower in the technical field of boiler soot blowing, in particular to a long-nozzle shock wave soot blower which can prevent dust-containing smoke from entering a long-nozzle, a conveying pipeline and a shock wave generator and has the functions of cooling and preventing dust accumulation.
Background
Various industrial boilers are widely applied in the fields of energy and environmental protection, such as pulverized coal boilers, circulating fluidized bed boilers, waste heat furnaces, process furnaces, biomass boilers, garbage incinerators and the like. In the running process of the boilers, dust accumulation is generally easy to occur on the heated surfaces of convection tube bundles, so that the resistance of smoke is increased, the temperature of the smoke discharged is increased, the thermal efficiency of the boilers is reduced, and the normal running of the boilers is seriously influenced.
The shock wave ash blower, also called as gas pulse ash blower, uses common combustible gas such as acetylene (gas, natural gas, liquefied gas) and air, and after passing through respective flow measuring and controlling systems, they are uniformly mixed according to a certain proportion, and then fed into combustion chamber to burn. Unlike conventional combustion process and mode, the pulse combustion of fuel gas produces compression wave in high turbulence state with unstable combustion gas to form kinetic energy, sound energy and heat energy. The combustion speed is high, the gas pressure generated by combustion is limited within a certain range, and the impact wave energy emitted at the nozzle of the output pipe is adapted to the ash accumulation condition. The deposited dust on the heated surface is removed by the action of the shock wave, and dust particles, loose objects, adhesion objects and sediments on the polluted heated surface are removed.
The traditional shock wave soot blower jet pipe is a short jet pipe, generally, only a single jet pipe is arranged, the soot deposition area is covered by means of cutting and direction adjustment of the jet pipe, and because the high-speed jet flow generated by the shock wave soot blower is conical, the corresponding coverage area of the single jet pipe is limited, the energy of the area close to the jet pipe is high, the energy of the area far from the jet pipe is low, the soot blowing effect is reduced at the position far from the jet pipe, and a certain soot blowing dead angle exists.
In addition, because the shock wave soot blower is operated intermittently, when the shock wave soot blower stops working, the flue gas containing dust can enter the long spray pipe and the shock wave generator, a certain amount of plate accumulated dust can be generated in the long spray pipe, the external conveying pipeline of the furnace and the shock wave generator, and when the accumulated dust is serious, a gas mixing pipeline, a mixer and the like can be blocked, so that the shock wave soot blower cannot work normally; meanwhile, because the flue gas contains water vapor, the conveying pipeline outside the furnace and the shock wave generator are in the atmosphere, dust-containing water-containing flue gas in the flue gas is condensed on the inner wall and forms accumulated water after being cooled by the environment, and because the flue gas also generally contains SO2 and SO3 which are very soluble in water, the accumulated water generally has stronger acidity and can seriously corrode the inner wall of the soot blower.
Particularly, when the spray pipe in the flue is not cooled in a high-temperature environment with the temperature of more than 500 ℃ for a long time, the service life of the spray pipe can be reduced even if the high-temperature resistant stainless steel material is selected. Especially in the atmosphere that the flue gas dust such as garbage incinerator, process boiler and exhaust-heat boiler contains corrosive elements, the deposition in the spray pipe pipeline can not be removed, and the high temperature environment can accelerate the high temperature corrosion of the spray pipe, thereby greatly shortening the service life.
Aiming at the ash deposition phenomenon in the shock wave soot blower, air is introduced to clean, but because the oxygen content in the air is high and the long-nozzle soot blowing needs more air, if the carbon content in the ash deposition is higher, the ash deposition can be ignited in a high-temperature environment, secondary combustion of the ash deposition occurs in a flue, secondary damage can be generated to a heat exchange tube bundle, and on the other hand, the air temperature is lower, particularly in winter in northern areas, the heat exchange of the convection heat exchange tube bundle can be directly influenced by introducing more air.
Disclosure of Invention
Aiming at the defects of the prior art, the invention provides the long-jet pipe shock wave soot blower with the functions of cooling and preventing the dust deposition, which not only can solve the problem that dead angles and dead areas exist in the limited soot blowing coverage area of the short jet pipe, but also can solve the problems of dust deposition, coking and blockage in the long jet pipe, the conveying pipeline and the generator of the shock wave soot blower; meanwhile, the problems that the long spray pipe in the high-temperature flue cannot be cooled, the service life is shortened, the introduced air ignites accumulated ash, heat exchange is affected and the like can be solved.
The invention is realized by the following technical scheme that the invention comprises a gas distribution ignition device, an ignition pipeline, shock wave generators, a long spray pipe, a furnace wall, a convection heat exchange tube bundle, a flue gas pipeline, a flue gas dust removal purification system, a draught fan, a chimney, a clean flue gas pipeline, a clean flue gas control valve and a clean flue gas one-way valve, wherein the gas distribution ignition device is connected with the shock wave generators through the ignition pipeline, and the two shock wave generators are symmetrically arranged; the gas outlet of the shock wave generator is connected with the gas inlet of the long spray pipe, the long spray pipe penetrates through the furnace wall and is arranged in the flue, the long spray pipe is formed by welding a left spray pipe, a right spray pipe and a rigid connecting column which are bilaterally symmetrical, and a plurality of spray nozzles are symmetrically arranged at the bottoms of the spray pipes at the left end and the right end of the long spray pipe; the convection heat exchange tube bundles are arranged in the flue between the furnace walls and positioned below the long spray pipes; the flue gas inlet of the flue gas pipeline is connected with the flue gas outlet at the bottom of the furnace wall, the flue gas outlet of the flue gas pipeline is connected with the flue gas inlet of the flue gas cylinder, and the flue gas dust removal and purification system and the induced draft fan are sequentially connected in series on the flue gas pipeline; the clean flue gas pipeline is of a three-way structure, the inlet end of the clean flue gas pipeline is connected with the flue gas pipeline between the induced draft fan and the chimney, the outlet end of the clean flue gas pipeline is respectively connected with the two ignition pipelines, and the air outlet pipeline of each clean flue gas pipeline is sequentially connected with the clean flue gas control valve and the clean flue gas check valve in series.
Further, in the invention, the diameter of the nozzle on the long nozzle is increased from the furnace wall to the middle in turn, and the nozzle is provided with a chamfer; the length and diameter of the spray pipe and the size of the spray nozzle are determined according to the flue size and the ash accumulation condition of the heat exchange tube bundle.
Further, in the invention, the cleaning smoke is connected with the ignition pipeline through the cleaning smoke pipeline, the cleaning smoke control valve and the cleaning smoke one-way valve, and continuous air flow is formed in the shock wave generator and the long spray pipe by utilizing negative pressure in the boiler flue and micro positive pressure of cleaning smoke at the outlet of the induced draft fan, so that no additional power equipment is needed.
Further, in the invention, two gas distribution ignition devices, two shock wave generators and two clean smoke control valves are connected into the same control system.
Still further, in the present invention, the cleaning fume control valve is a solenoid valve.
Furthermore, in the invention, the long spray pipe is made of high-temperature-resistant corrosion-resistant stainless steel.
Compared with the prior art, the invention has the following beneficial effects: the long-jet pipe multi-nozzle structure can realize the whole soot blowing area coverage of the heat exchange tube bundle without dead angles and dead zones; the multiple nozzles distributed on the spray pipe and with gradually changed sizes can realize the uniform distribution of laser energy, and the heat exchange tube bundles which are closer to the furnace wall are prevented from bearing larger energy; the left shock wave generator and the right shock wave generator work simultaneously, and the symmetrical design and the rigid connection of the long spray pipe can effectively resist the impact force during soot blowing; meanwhile, the problem of ash accumulation in the long spray pipe, the conveying pipeline and the shock wave generator can be effectively prevented, and particularly, the long spray pipe in a high-temperature environment is cooled to a certain extent, and the service life of the spray pipe is prolonged.
Drawings
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic view of the structure of the long nozzle of the present invention;
FIG. 3 is an enlarged cross-sectional view of FIG. 1 at A;
Wherein: 1. the gas distribution ignition device comprises a gas distribution ignition device body 2, an ignition pipeline body 3, a shock wave generator body 4, a long spray pipe body 41, a left spray pipe body 42, a right spray pipe body 43, a rigid connection column 5, a furnace wall 6, a convection heat exchange tube bundle 7, a flue gas pipeline body 8, a flue gas dust removal purification system 9, a draught fan 10, a flue pipe body 11, a clean flue gas pipeline body 12, a clean flue gas control valve 13 and a clean flue gas one-way valve.
Detailed Description
The following describes embodiments of the present invention in detail with reference to the accompanying drawings, and the embodiments and specific operation procedures of the present invention are given by this embodiment on the premise of the technical solution of the present invention, but the protection scope of the present invention is not limited to the following embodiments.
Examples
1-3, The invention comprises a gas distribution ignition device 1, an ignition pipeline 2, a shock wave generator 3, a long spray pipe 4, a furnace wall 5, a convection heat exchange tube bundle 6, a flue gas pipeline 7, a flue gas dust removal purification system 8, a draught fan 9, a flue pipe 10, a clean flue gas pipeline 11, a clean flue gas control valve 12 and a clean flue gas one-way valve 13, wherein the gas distribution ignition device 1 is connected with the shock wave generator 3 through the ignition pipeline 2, and the two shock wave generators 3 are symmetrically arranged; the gas outlet of the shock wave generator 3 is connected with the gas inlet of the long spray pipe 4, the long spray pipe 4 penetrates through the furnace wall 5 and is arranged in the flue, the long spray pipe 4 is formed by welding a left spray pipe 41, a right spray pipe 42 and a rigid connecting column 43 which are bilaterally symmetrical, and a plurality of spray nozzles are symmetrically arranged at the bottoms of the left end and the right end of the long spray pipe 4; the convection heat exchange tube bundle 6 is arranged in the flue between the furnace walls 5 and below the long spray tube 4; the flue gas inlet of the flue gas pipeline 7 is connected with the flue gas outlet at the bottom of the furnace wall 5, the flue gas outlet of the flue gas pipeline 7 is connected with the flue gas inlet of the flue gas cylinder 10, and the flue gas dust removal and purification system 8 and the induced draft fan 9 are sequentially connected on the flue gas pipeline 7 in series; the clean flue gas pipeline 11 is of a three-way structure, the inlet end of the clean flue gas pipeline 11 is connected with the flue gas pipeline 7 between the induced draft fan 9 and the chimney 10, the outlet end of the clean flue gas pipeline 11 is respectively connected with the two ignition pipelines 2, and the air outlet pipeline of each clean flue gas pipeline 11 is sequentially connected with the clean flue gas control valve 12 and the clean flue gas one-way valve 13 in series.
In the invention, the long spray pipe 4 is formed by welding a left spray pipe 41, a right spray pipe 42 and a rigid connecting column 43 which are bilaterally symmetrical, the bottoms of the left end and the right end of the long spray pipe 4 are symmetrically provided with a plurality of spray nozzles, the diameters of the spray nozzles are sequentially increased from the furnace wall to the middle, the sizes of the long spray pipes and the diameters of the spray nozzles are selected according to the sizes of the flues, the soot blowing whole-area coverage of the heat exchange tube bundle can be realized, dead angles and dead areas are not remained, the distributed multiple spray nozzles with gradually changed sizes on the spray pipes can realize the uniform distribution of laser energy, and the heat exchange tube bundle which is nearer to the furnace wall is prevented from bearing larger energy. Further, the nozzle is provided with a chamfer, which is helpful for enlarging the coverage area of the jet air flow.
When the shock wave generator 3 stops working, the cleaning smoke control valve 12 is opened, the cleaned smoke after purification treatment is led to the ignition pipeline in front of the shock wave generator 3 through a pipeline, a circulation loop is formed by utilizing the negative pressure of the flue in the furnace wall 5 and the micro positive pressure of the smoke at the rear end of the induced draft fan 9, and the cleaning smoke with a certain temperature can form a continuous air inlet flow in the shock wave generator 3 and the long spray pipe 4 without additional power equipment, so that dust-containing smoke is prevented from entering the long spray pipe 4 and the shock wave generator 3, and dust accumulation is prevented. Further, when the shock wave generator 3 works, the cleaning smoke check valve 13 can prevent shock waves from reversely entering the cleaning flue 11, and the cleaning smoke check valve is protected.
The left shock wave generator 3 and the right shock wave generator 3 are connected into the same control system and are simultaneously opened and closed, and impact forces acting on two sides of the rigid connecting shaft 43 in the middle of the long spray pipe 4 can be counteracted.
The introduced clean flue gas also has a certain temperature, generally between 120 and 160 ℃, plays a role in heat preservation of the conveying pipeline outside the furnace and the shock wave generator 3, and can reduce the influence on heat exchange of the convection heat exchange tube bundles at the lower part of the long spray pipe 4.
The long spray pipe 4 is made of high-temperature-resistant corrosion-resistant stainless steel, such as 310S or TP347H, and can work for a long time under the environment below 670 ℃ to prolong the service life of the spray pipe.
Because the temperature of the boiler flue gas is higher, generally between 500 and 900 ℃, the long spray pipe 4 is positioned in a high-temperature flue for a long time, the temperature is correspondingly increased, and the clean flue gas has a certain temperature, but can still play a certain cooling role relative to the long spray pipe 4 in a high-temperature environment, so that the service life of the long spray pipe is prolonged.
The clean flue gas has the same composition as the dust-containing flue gas, has lower oxygen content, and does not cause ash deposit secondary combustion or other unpredictable reactions.
The foregoing describes specific embodiments of the present invention. It is to be understood that the invention is not limited to the particular embodiments described above, and that various changes and modifications may be made by one skilled in the art within the scope of the claims without affecting the spirit of the invention.
Claims (2)
1. The long-jet pipe shock wave soot blower with the functions of cooling and preventing dust deposition is characterized by comprising a gas distribution ignition device (1), an ignition pipeline (2), a shock wave generator (3), a long jet pipe (4), a furnace wall (5), a convection heat exchange tube bundle (6), a flue gas pipeline (7), a flue gas dust removal purification system (8), a draught fan (9), a flue pipe (10), a clean flue gas pipeline (11), a clean flue gas control valve (12) and a clean flue gas one-way valve (13), wherein the gas distribution ignition device (1) is connected with a gas inlet of the shock wave generator (3) through the ignition pipeline (2), a gas outlet of the shock wave generator (3) is connected with a gas inlet of the long jet pipe (4), the two shock wave generators (3) are symmetrically arranged, the long jet pipe (4) penetrates through the furnace wall (5) and is arranged in a flue, the long jet pipe (4) is formed by welding a left jet pipe (41), a right jet pipe (42) and a rigid connecting column (43), and a plurality of nozzles are symmetrically arranged at the bottoms of the jet pipes at the left end and the right end of the long jet pipe (4); the convection heat exchange tube bundles (6) are arranged in the flue between the furnace walls (5) and are positioned below the long spray tubes (4), a flue gas inlet of the flue gas pipeline (7) is connected with a flue gas outlet at the bottom of the furnace walls (5), a flue gas outlet of the flue gas pipeline (7) is connected with a flue gas inlet of the flue pipe (10), and the flue gas dust removal and purification system (8) and the induced draft fan (9) are sequentially connected on the flue gas pipeline (7) in series; the cleaning flue gas pipeline (11) is of a three-way structure, the inlet end of the cleaning flue gas pipeline (11) is connected with the flue gas pipeline (7) between the induced draft fan (9) and the chimney (10), the outlet end of the cleaning flue gas pipeline (11) is respectively connected with the two ignition pipelines (2), and the air outlet pipeline of each cleaning flue gas pipeline (11) is sequentially connected with the cleaning flue gas control valve (12) and the cleaning flue gas one-way valve (13) in series;
the diameter of a nozzle on the long spray pipe (4) is sequentially increased from the furnace wall to the middle, and a chamfer is formed at the nozzle; the length and the diameter of the long spray pipe (4) and the size of the spray nozzle are determined according to the flue size and the ash accumulation condition of the convection heat exchange tube bundle (6);
The two gas distribution ignition devices (1), the two shock wave generators (3) and the two cleaning smoke control valves (12) are connected into the same control system;
The cleaning smoke control valve (12) is an electromagnetic valve.
2. The long jet tube shock wave soot blower with the functions of cooling and preventing dust deposition according to claim 1, wherein the long jet tube (4) is made of high-temperature-resistant corrosion-resistant stainless steel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910442922.0A CN110068021B (en) | 2019-05-26 | 2019-05-26 | Long jet tube shock wave soot blower with cooling and soot deposition preventing functions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910442922.0A CN110068021B (en) | 2019-05-26 | 2019-05-26 | Long jet tube shock wave soot blower with cooling and soot deposition preventing functions |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110068021A CN110068021A (en) | 2019-07-30 |
CN110068021B true CN110068021B (en) | 2024-04-30 |
Family
ID=67371690
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910442922.0A Active CN110068021B (en) | 2019-05-26 | 2019-05-26 | Long jet tube shock wave soot blower with cooling and soot deposition preventing functions |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110068021B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113623671B (en) * | 2021-09-23 | 2024-08-20 | 苏州行知环保科技有限公司 | Acoustic shock wave coupling soot blowing system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202938321U (en) * | 2012-12-03 | 2013-05-15 | 唐山市金沙工贸有限公司 | Soot blower system of pulverized coal fired boiler |
CN204717706U (en) * | 2015-06-23 | 2015-10-21 | 安徽皖苏电力运检科技有限公司 | A kind of large-sized boiler sonic shock mixed soot blower system |
CN206695155U (en) * | 2017-03-02 | 2017-12-01 | 北京楚能科技发展有限公司 | Shock wave soot blower |
CN108317530A (en) * | 2018-03-27 | 2018-07-24 | 中山市天乙能源有限公司 | A kind of waste incineration and generating electricity boiler pulse shockwave dust-blower |
CN209960522U (en) * | 2019-05-26 | 2020-01-17 | 中船重工(上海)新能源有限公司 | Long-nozzle shock wave soot blower with cooling and soot deposition preventing functions |
-
2019
- 2019-05-26 CN CN201910442922.0A patent/CN110068021B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202938321U (en) * | 2012-12-03 | 2013-05-15 | 唐山市金沙工贸有限公司 | Soot blower system of pulverized coal fired boiler |
CN204717706U (en) * | 2015-06-23 | 2015-10-21 | 安徽皖苏电力运检科技有限公司 | A kind of large-sized boiler sonic shock mixed soot blower system |
CN206695155U (en) * | 2017-03-02 | 2017-12-01 | 北京楚能科技发展有限公司 | Shock wave soot blower |
CN108317530A (en) * | 2018-03-27 | 2018-07-24 | 中山市天乙能源有限公司 | A kind of waste incineration and generating electricity boiler pulse shockwave dust-blower |
CN209960522U (en) * | 2019-05-26 | 2020-01-17 | 中船重工(上海)新能源有限公司 | Long-nozzle shock wave soot blower with cooling and soot deposition preventing functions |
Also Published As
Publication number | Publication date |
---|---|
CN110068021A (en) | 2019-07-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102537975A (en) | Circulating fluidized bed garbage incineration boiler and pollution control system with same | |
US8234985B2 (en) | Boiler producing steam from flue gases under optimized conditions | |
US9476582B2 (en) | System and method for removing slag inside a utility furnace | |
CN101037193A (en) | Technology and device for producing yellow Phosphorus by electric oven process | |
CN209960522U (en) | Long-nozzle shock wave soot blower with cooling and soot deposition preventing functions | |
CN216131907U (en) | Biomass fuel burning corner tube type steam boiler | |
CN110068021B (en) | Long jet tube shock wave soot blower with cooling and soot deposition preventing functions | |
CN202938321U (en) | Soot blower system of pulverized coal fired boiler | |
CN111981473A (en) | Slag burnout system and method of biomass boiler | |
CN202581356U (en) | Dust cleaning device for waste incineration boiler and biomass boiler | |
CN211040972U (en) | Waste incineration equipment | |
CN102644930A (en) | Deashing device and method for waste incineration boiler and biomass boiler | |
CN113483596A (en) | Dry ice cleaning method and dry ice cleaning machine for furnace tube | |
CN112664953A (en) | Circulating fluidized bed incineration boiler for burning solid waste | |
CN110657439A (en) | Flue gas recirculation device for separating primary air and secondary air | |
CN219120566U (en) | Circulating fluidized bed boiler capable of burning sludge purely | |
CN217131290U (en) | High-temperature high-pressure boiler structure for incinerating solid waste | |
CN214664476U (en) | Waste heat type solid waste treatment device | |
CN215637210U (en) | Pulverized coal fired boiler and grate furnace combined waste incineration power generation system | |
CN217816771U (en) | Tail flue system of pure-combustion sludge circulating fluidized bed boiler | |
RU120750U1 (en) | WATER BOILER | |
KR101496298B1 (en) | Vertical type thermal oil boiler for refuse derived fuel | |
CN102183153A (en) | Tail gas heat exchanger for salt-melting furnace | |
CN212644652U (en) | Pulse soot blowing mechanism for garbage incinerator | |
CN213089779U (en) | Active coke carbonization high-temperature high-dust flue gas sectional type evaporation device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |