CN105605607B - Multistage duct type coal burner - Google Patents

Multistage duct type coal burner Download PDF

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Publication number
CN105605607B
CN105605607B CN201610119821.6A CN201610119821A CN105605607B CN 105605607 B CN105605607 B CN 105605607B CN 201610119821 A CN201610119821 A CN 201610119821A CN 105605607 B CN105605607 B CN 105605607B
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Prior art keywords
combustion
pipe
fan
pipeline
primary
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CN201610119821.6A
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CN105605607A (en
Inventor
陈海军
陈晓航
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Inner Mongol Jin Tu Environmental Protection Technology Co Ltd
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Inner Mongol Jin Tu Environmental Protection Technology Co Ltd
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C7/00Combustion apparatus characterised by arrangements for air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel

Abstract

The invention discloses a kind of multistage duct type coal burners, it includes controller and several pipeline combustion mechanisms, controller is connect with the dosing pump of pipeline combustion mechanism, primary air fan, combustion fan, gas monitoring instrument respectively, and controller controls the feeding coal of dosing pump and the air output of primary air fan and combustion fan.Advantage:The tail gas of each pipeline combustion mechanism is monitored by gas monitoring instrument, and monitoring result is transferred to controller, and then realizes that the precision to each pipeline combustion mechanism controls by controller;Burner hearth is substituted with multiple pipeline combustion mechanisms, on the one hand, coal dust can be promoted to be sufficiently mixed burning with air, the utilization rate of coal dust is improved, the burn-off rate of coal dust is made to reach 98% or more;On the other hand, heat utilization efficiency can be improved, combustion conduit interior temperature is effectively reduced, and then fouling is inhibited to be formed, reduces the generation of oxynitrides, reduce environmental pollution.

Description

Multistage duct type coal burner
Technical field:
The present invention relates to a kind of coal burners, relate in particular to a kind of multistage duct type coal burner.
Background technology
Existing coal powder burner is mostly that coal dust is sprayed into burner hearth by nozzle, then lights burner hearth using igniter Interior breeze airflow.In coal dust firing, temperature reaches 900 DEG C or more in burner hearth, will produce a large amount of oxynitrides, pollutes ring Border;And since burner hearth inner space is larger, on the one hand, the coal dust in burner hearth can be caused to be unevenly distributed, burn insufficient, had Part coal dust is exhausted with flue gas, causes the waste of coal dust, pollutes air, on the other hand, hearth wall heat dissipation area and hearth body Product is smaller, causes radiation of burner hearth heat utilization efficiency low, causes the waste of the energy, and the hot environment in burner hearth can cause coal ash Melting, shows to form fouling in burner hearth, influences radiation of burner hearth heat and distributes outward.
Invention content:
Coal dust can be made fully to burn, improve the multistage duct type of efficiency of utilization the purpose of the present invention is to provide a kind of Coal burner.
The present invention is implemented by following technical solution:Multistage duct type coal burner comprising controller and several pipes Road combustion mechanism, controller dosing pump, primary air fan, combustion fan, the gas with the pipeline combustion mechanism respectively Body monitor connect, the controller control the dosing pump feeding coal and the primary air fan with the combustion air The air output of machine.
Further, the pipeline combustion mechanism include the dosing pump, primary combustion pipe, the primary air fan, Igniter, combustion-supporting chamber, the combustion fan, second-time burning pipe, overfire air fan, the gas monitoring instrument, the dosing pump, The primary combustion pipe, the combustion-supporting chamber, the second-time burning pipe are sequentially connected according to material conveying direction;In the primary combustion It burns pipe feed end and is equipped with the igniter, the air outlet of the primary air fan is connected to the primary combustion pipe feed end;It is described It is connected to inside the exhaust outlet of combustion fan and the combustion-supporting chamber;It is equipped with the gas monitoring instrument in second-time burning pipe tail portion, The air outlet of the overfire air fan is connected to the second-time burning pipe feed end.
Further, it is internally provided with conical nozzle in the primary combustion pipe discharge end, the combustion-supporting chamber.
Further, the pipeline combustion mechanism further include two heat-exchanger rigs and with each heat-exchanger rig water inlet It is connected to the water pump of setting, the heat-exchanger rig, institute are arranged in the outside of the primary combustion pipe and the second-time burning pipe The water inlet for stating heat-exchanger rig is connected to by pipeline with the water outlet of the corresponding water pump;The water pump connects with the controller It connects, the controller controls the working frequency of the water pump.
Advantages of the present invention:The tail gas of each pipeline combustion mechanism is monitored by gas monitoring instrument, and will monitoring As a result it is transferred to controller, and then realizes that the precision to each pipeline combustion mechanism controls by controller;With multiple pipelines Combustion mechanism substitutes burner hearth, on the one hand, coal dust can be promoted to be sufficiently mixed burning with air, the utilization rate of coal dust is improved, make coal The burn-off rate of powder reaches 98% or more;On the other hand, pipeline combustion mechanism heat dissipation area and pipeline combustion mechanism body can be increased Long-pending ratio, and then the radiant heat of pipeline combustion mechanism is made fully to distribute, heat utilization efficiency is improved, combustion conduit interior temperature is effectively reduced Degree;In addition, by controller control heat-exchanger rig coal dust low-temperature burning may be implemented, by ignition temperature control coal ash fusion temperature with Under, and then fouling is inhibited to be formed, ensure the heat-radiating properties of pipeline combustion mechanism, meanwhile, temperature control is being generated into nitrogen oxidation The critical-temperature of object is closed hereinafter, reducing the generation of oxynitrides, reduces environmental pollution.
Description of the drawings:
Fig. 1 is the overall structure diagram of embodiment 1.
Fig. 2 is 1 controller connection diagram of embodiment.
Fig. 3 is the overall structure diagram of embodiment 2.
Fig. 4 is 2 controller connection diagram of embodiment.
Controller 1, pipeline combustion mechanism 2, dosing pump 21, primary combustion pipe 22, primary air fan 23, igniter 24, Combustion-supporting chamber 25, combustion fan 26, second-time burning pipe 27, overfire air fan 28, gas monitoring instrument 29, heat-exchanger rig 210, water pump 211, Conical nozzle 212.
Specific implementation mode:
Embodiment 1:As depicted in figs. 1 and 2, multistage duct type coal burner comprising controller 1 and two pipelines The feed inlet of the dosing pump 21 of each pipeline combustion mechanism 2 is passed through pipeline when use and connected with pulverized coal bin by combustion mechanism 2 It is logical, 27 tail portion of second-time burning pipe of each pipeline combustion mechanism 2 is connect with heat-exchanger rig, tailing purification collection device successively; Dosing pump 21 can be pumped into the coal dust in pulverized coal bin is quantitative in primary combustion pipe 22;Pipeline combustion mechanism 2 includes Dosing pump 21, primary combustion pipe 22, primary air fan 23, igniter 24, combustion-supporting chamber 25, combustion fan 26, second-time burning pipe 27, overfire air fan 28, gas monitoring instrument 29, dosing pump 21, primary combustion pipe 22, combustion-supporting chamber 25, second-time burning pipe 27 are pressed It is sequentially connected according to material conveying direction;The air outlet of primary air fan 23 is connected to 22 feed end of primary combustion pipe, primary air fan 23 Air is sent into primary combustion pipe 22, and then air is made to be sufficiently mixed with the coal dust being discharged by dosing pump 21, forms coal dust Air-flow;It is equipped with igniter 24 in 22 feed end of primary combustion pipe, igniter 24 will be lighted with the breeze airflow in this combustion pipe; It is internally provided with conical nozzle 212 in 22 discharge end of primary combustion pipe, combustion-supporting chamber 25, conical nozzle 212 can make the coal dust gas of burning Spray into combustion-supporting chamber 25 in adfluxion, be connected to inside the exhaust outlet of combustion fan 26 and combustion-supporting chamber 25, combustion fan 26 can in time by Air fills into combustion-supporting chamber 25, and then coal dust is promoted fully to burn, and improves the utilization rate of coal dust, and the burn-off rate of coal dust is made to reach 98% More than;The air outlet of overfire air fan 28 is connected to 27 feed end of second-time burning pipe, and overfire air fan 28 can be by second-time burning pipe 27 Interior tail gas is sequentially sent in heat-exchanger rig and tailing purification collection device, and heat-exchanger rig can absorb the heat carried in tail gas, Heat utilization ratio is improved, tailing purification collection device can purify the dust particles collected and carried in tail gas, and cleaning of off-gas prevents ring It pollutes in border;It is equipped with gas monitoring instrument 29, the dosing pump of controller 1 and pipeline combustion mechanism 2 in 27 tail portion of second-time burning pipe 21, primary air fan 23, combustion fan 26, gas monitoring instrument 29 connect, and controller 1 controls the feeding coal and one of dosing pump 21 The air output of secondary wind turbine 23 and combustion fan 26;By gas monitoring instrument 29 to that can realize to each pipeline combustion mechanism 2 Tail gas is monitored in real time, and monitoring result is transferred to controller 1, and then is realized by controller 1 and burnt to each pipeline The precision control of the feed pump 21, primary air fan 23, combustion fan 26 of mechanism 2.
Embodiment 2:As shown in Figure 3 and Figure 4, difference lies in pipeline combustion mechanism 2 further includes two and changes with embodiment 1 Thermal 210 and the water pump 211 that setting is connected to 210 water inlet of each heat-exchanger rig, in primary combustion pipe 22 and second-time burning The outside of pipe 27 is arranged with heat-exchanger rig 210, the water outlet that the water inlet of heat-exchanger rig 210 passes through pipeline and corresponding water pump 211 Mouth connection;Water pump 211 is connect with controller 1, and controller 1 controls the working frequency of water pump 211;Heat-exchanger rig 210 can be abundant The radiant heat of primary combustion pipe 22 and second-time burning pipe 27 is absorbed, efficiency of utilization is improved;It will once be fired by heat-exchanger rig 210 The portion's temperature control burnt in pipe 22 and second-time burning pipe 27 is generating the critical-temperature of oxynitrides hereinafter, avoiding generating nitrogen oxygen Compound prevents environmental pollution;In addition, the low-temperature burning that coal dust may be implemented in heat-exchanger rig 210 is controlled by controller 1, it will Ignition temperature control in coal ash fusion temperature hereinafter, in turn inhibit fouling formed, ensure the heat-radiating properties of burner.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model Protection domain within.

Claims (3)

1. multistage duct type coal burner, which is characterized in that it includes controller and several pipeline combustion mechanisms, the control Device processed is connect with dosing pump, primary air fan, combustion fan, the gas monitoring instrument of the pipeline combustion mechanism respectively, described Controller controls the feeding coal of the dosing pump and the air output of the primary air fan and the combustion fan;The pipeline Combustion mechanism includes the dosing pump, primary combustion pipe, the primary air fan, igniter, combustion-supporting chamber, the combustion air Machine, second-time burning pipe, overfire air fan, the gas monitoring instrument, it is the dosing pump, the primary combustion pipe, described combustion-supporting Room, the second-time burning pipe are sequentially connected according to material conveying direction;It is equipped with the igniting in the primary combustion pipe feed end Device, the air outlet of the primary air fan are connected to the primary combustion pipe feed end;The exhaust outlet of the combustion fan with it is described Connection inside combustion-supporting chamber;Second-time burning pipe tail portion be equipped with the gas monitoring instrument, the air outlet of the overfire air fan with The second-time burning pipe feed end connection.
2. multistage duct type coal burner according to claim 1, which is characterized in that discharge in the primary combustion pipe End, the combustion-supporting chamber are internally provided with conical nozzle.
3. according to any multistage duct type coal burner of claims 1 or 2, which is characterized in that the pipeline burning Mechanism further includes two heat-exchanger rigs and is connected to the water pump of setting with each heat-exchanger rig water inlet, in the primary combustion The outside of pipe and the second-time burning pipe is arranged with the heat-exchanger rig, the water inlet of the heat-exchanger rig by pipeline with it is right The water outlet of the water pump is answered to be connected to;The water pump is connect with the controller, and the controller controls the water pumping of the water pump Amount.
CN201610119821.6A 2016-03-02 2016-03-02 Multistage duct type coal burner Active CN105605607B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610119821.6A CN105605607B (en) 2016-03-02 2016-03-02 Multistage duct type coal burner

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Application Number Priority Date Filing Date Title
CN201610119821.6A CN105605607B (en) 2016-03-02 2016-03-02 Multistage duct type coal burner

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CN105605607B true CN105605607B (en) 2018-09-21

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101749700A (en) * 2010-03-04 2010-06-23 郑平安 Pulverized coal furnace tiny-oil ignition combustion method
CN203024179U (en) * 2012-11-23 2013-06-26 施正 Intelligent control system of pulverized coal burner
CN204474622U (en) * 2015-01-22 2015-07-15 福建兴源新能源科技有限公司 A kind of novel biomass gas cleaning device

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Publication number Priority date Publication date Assignee Title
JP3873458B2 (en) * 1998-05-26 2007-01-24 株式会社ノーリツ Combustor with CO sensor
CN100572917C (en) * 2007-07-27 2009-12-23 福建省丰泉环保设备有限公司 The double-loop double-pyrogenation incinerator and the using method thereof that are used for rubbish processing to be harmless
CN202501457U (en) * 2012-01-04 2012-10-24 泰安市利达热工设备有限公司 Efficient clean-combustion multi-powder cyclone burner
JP5746646B2 (en) * 2012-02-09 2015-07-08 リンナイ株式会社 Combined combustion device
WO2014149368A1 (en) * 2013-03-15 2014-09-25 Research Triangle Institute Biomass combustion device with a thermoelectric-powered control
CN203364126U (en) * 2013-06-03 2013-12-25 诸暨天立环保节能技术有限公司 Efficient multivariant industrial boiler powder combustor
CN103672884A (en) * 2013-12-27 2014-03-26 安其云 Novel efficient low-nitrogen full-automatic pulverized coal burner
JP5920410B2 (en) * 2014-07-08 2016-05-18 株式会社ノーリツ Water heater
CN204574049U (en) * 2015-02-17 2015-08-19 河南省豫园锅炉机电有限公司 The burner of gas fired-boiler
CN205560829U (en) * 2016-03-02 2016-09-07 内蒙古金土环保科技有限公司 Multistage pipeline formula coal burner

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101749700A (en) * 2010-03-04 2010-06-23 郑平安 Pulverized coal furnace tiny-oil ignition combustion method
CN203024179U (en) * 2012-11-23 2013-06-26 施正 Intelligent control system of pulverized coal burner
CN204474622U (en) * 2015-01-22 2015-07-15 福建兴源新能源科技有限公司 A kind of novel biomass gas cleaning device

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Denomination of invention: Multi-section pipeline type pulverized coal combustor

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Denomination of invention: Multi stage pipe type pulverized coal burner

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