CN201093702Y - Chain grate type single toroidal swirl pure smokeless hot water boiler - Google Patents

Chain grate type single toroidal swirl pure smokeless hot water boiler Download PDF

Info

Publication number
CN201093702Y
CN201093702Y CNU2007200239200U CN200720023920U CN201093702Y CN 201093702 Y CN201093702 Y CN 201093702Y CN U2007200239200 U CNU2007200239200 U CN U2007200239200U CN 200720023920 U CN200720023920 U CN 200720023920U CN 201093702 Y CN201093702 Y CN 201093702Y
Authority
CN
China
Prior art keywords
combustion
arch
boiler
coal
water boiler
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.)
Expired - Fee Related
Application number
CNU2007200239200U
Other languages
Chinese (zh)
Inventor
王树洲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CNU2007200239200U priority Critical patent/CN201093702Y/en
Application granted granted Critical
Publication of CN201093702Y publication Critical patent/CN201093702Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Solid-Fuel Combustion (AREA)

Abstract

The utility model relates to a chain grate type single rotational flow purely smokeless hot-water boiler, which belongs to heat engineering equipment. The utility model comprises a casing, a flag pattern tube row group at the upper part of the boiler, a water wall, a boiler cylinder and a coal-burning device at the lower part of the boiler, wherein, the coal-burning device comprises a coal feeding device, a chain grate, a boiler front arch and a boiler rear arch; a front hearth is formed between the boiler front arch and the chain grate; a rear hearth is formed between the boiler rear arch and the chain grate; a combustion heat gas outlet is arranged between the boiler front arch and the boiler rear arch; the top part of the cross-section of the front hearth of the combustion heat gas outlet is in the shape of arch which forms rational flow combustion; the side wall of the front hearth is matched with a combustion-supporting air hole which leads to the front hearth; the combustion-supporting air hole is tangential with the arch of the top part of the front hearth; and the rear part of the front hearth is connected with the combustion heat gas outlet. The chain grate type single rotational flow purely smokeless hot-water boiler has the advantages of simple and reasonable structure, low fabrication cost, fully coal combustion, high thermal efficiency and low energy consumption, and can solve the problems of black smoke and dust stratification of the coal to protect the environment.

Description

Single-spiral flow smokeless hot-water boiler of chain fire grated
Technical field
The utility model relates to a kind of single-spiral flow smokeless hot-water boiler of chain fire grated, belongs to Thermal Equipment.
Background technology
At present, traveling-grate stoker formula hot-water boiler, widelyd popularize at home and performance is advanced belongs to QXL type series of products, structure comprises shell, the flag style tube row group on top, water-cooling wall, the coal-burning installation of drum and bottom, coal-burning installation comprises coaling gear, traveling-grate stoker, trimmer arch and stove rear arch, constitute front furnace between trimmer arch and the traveling-grate stoker, constitute rear hearth between stove rear arch and the traveling-grate stoker, the outlet of combustion heat gas is arranged between trimmer arch and the stove rear arch, it is the advanced technology that China introduces from Italy, convection tube in " pot " adopts advanced corner tube type, convection heating surface all adopts " flag style tube row " structure, adopts the current forced circulation, and very high heat transfer coefficient is arranged, typing drawing and manufacturing inspection standard that thermal power 2.8MW-30MW, each cauldron factory have national Ministry of Labour to issue.
What boiler adopted on the structure of " stove " is traditional " traveling-grate stoker formula " structure, be called for short " chain-arranged type ", because the suitable coal of this structure must be " mixing foam bituminous coal ", add that again also will mix the 25-30% fineness according to national regulation in this foam coal is 100 purpose spoil powder (in order to make full use of spoil), this has created sufficient condition just for a large amount of flying dusts, add the problem of bad with regard to the burning that exists originally and the flying dust of original conventional chains fire grate again, the problem of smoldering in addition is also very outstanding, the two adds cigarette and dirt and is in the same place, effective heat-transfer surface of serious obstruction " pot ", although designed ash removing opening, but also can't resolve the dust stratification problem all the time, so although the heat exchanger effectiveness of the theoretical design of this boiler is very high, but, seriously restricted the thermal efficiency of its actual motion to a great extent, the energy waste that existence in service is very big because of the existence of the problems referred to above, the thermal efficiency is low, and contaminated environment is serious.
The utility model content
The purpose of this utility model is to provide a kind of single-spiral flow smokeless hot-water boiler of chain fire grated, and is simple and reasonable, cheap, and fired coal combustion is abundant, thermal efficiency height, and energy consumption is low, can solve coal-fired over-emitting black exhaust and dust stratification problem, the protection environment.
Single-spiral flow smokeless hot-water boiler of chain fire grated described in the utility model, comprise shell, the flag style tube row group on top, water-cooling wall, the coal-burning installation of drum and bottom, coal-burning installation comprises coaling gear, traveling-grate stoker, trimmer arch and stove rear arch, constitute front furnace between trimmer arch and the traveling-grate stoker, constitute rear hearth between stove rear arch and the traveling-grate stoker, the outlet of combustion heat gas is arranged between trimmer arch and the stove rear arch, the top of its front furnace cross section is the arch that forms swirl flow combustion, form single eddy flow chimney arch, the sidewall of front furnace is fitted with the combustion-supporting air port of leading to front furnace, the arch at combustion-supporting air port and front furnace top is tangent, and the rear portion of front furnace is communicated with the outlet of combustion heat gas.
Front furnace is divided into the two parts that communicate up and down, and cross section is R shape, and the front furnace sidewall is provided with the combustion-supporting air channel of leading to upper furnace along the pin of R shape, makes burning more abundant, preferably is equipped with the combustion-supporting air channel of leading to upper furnace along two pins.So-called R shape also can be anti-R shape, can form clockwise eddy flow burning and counterclockwise swirl flow combustion respectively.
Set up the combustion-supporting air channel of leading to lower hearth along the inclination pin of R shape, further promote burning preferably to be equipped with the combustion-supporting air channel of leading to lower hearth along two pins.
Cross section is the also just approximate pictograph of R shape structure to be described, can there be distortion to a certain degree to develop, two pins as R shape can be that symmetry tilts, can set up the combustion-supporting air channel of leading to lower hearth along two inclination pins, be that the side-blown air channel is all established in both sides, the cross section of upper furnace can be rounded or ellipse etc., burner hearth also can be positioned at the middle part of body of heater, especially during symmetrical structure, generally is positioned at the middle part, at this moment, R shape structure will develop into approximate Ω shape, or the like, when structure is asymmetric, two tiltedly take on a weak point, and one long.
Establish training wall upwards at the front end of stove rear arch, combustion heat gas is carried out water conservancy diversion, what preferably the water conservancy diversion coping is provided with tilts to combustion heat gas outlet side, further improves the water conservancy diversion effect.
The utility model only improves the coal-burning installation in the hot-water boiler, and the structure that other structure can still be continued to use existing QXL series chain-arranged type hot-water boiler gets final product, and improves simply, is beneficial to by market and accepts.Coal-burning installation part and other structure division can be divided into two supporting body structures, make equipped respectively.
In practice, according to the needs of different size the longitudinal length and the transverse width of body of heater are set, when the longitudinal length of body of heater was big, combustion-supporting air channel can distribute on longitudinal length and be provided with severally, guarantees fully to burn.
Coaling gear in the utility model comprises from manual coal that adds coal bunker and coaling machine automatic stoking device etc.
Operation principle:
Under the effect of the combustion air that enters from air compartment, at high temperature burn in coal seam on the fire grate, produce a large amount of dense flue gases, coal tar steam wherein, coal gas (carbon monoxide), the particle of the coal that hydrocarbon gas evaporates and subparticle or the like volatile combustible product can rise rapidly, air-flow is concentrated to the crown center quirk, compress and the flow velocity increase, this strand contains the high concentration flue gas of a large amount of flammable compositions and flame enters top with higher flow velocity swirl flow combustion zone, it is upper furnace, can claim " single swirl flow combustion district ", enter rotation status immediately, the eddy flow combustion air is through the combustion-supporting burning air channel of the right and left simultaneously, tangential direction with this circle, spray with certain pressure and flow velocity, the two makes a concerted effort to form stronger turning moment, flammable flue gas and combustion-supporting oxygen (air) are mixed consumingly, cause burning fiercely, produce high temperature (1200-1450 ℃), this temperature has been strengthened the burning condition in this combustion zone more, according to " high-speed rotational principle ", this strand air-flow of rotation at a high speed all will produce consumingly " entrainmenting " effect to overhead all volatile materials of the whole front furnace that covers, none is slipped through the net, because the airflow route in the swirl flow combustion district is " a spiral stroke ", the track route and the residence time of fuel have greatly so extended, in this burning system, volatile fuel and combustible dust (flue gas): 1. essential temperature; 2. enough oxygen; 3. good stirring; 4. sufficient burning time.Essential elemental burns, " flawless " of Ti Xianing here, so flue gas will be by slap-up after-flame, what obtain is clean, tasteless, colourless, dustless high-temperature gas enters the high temperature turbulent area that training wall 31 places form with certain flow rate, owing to lost " constraint " of combustion zone, air-flow begins to tear mutually to turn round, collision, pulverize, form many irregular disorderly air-flows, because the inertia of high speed swirling eddy, these air-flows still form " turbulence-like " in the rotation of establishing one's own system, and very high at this turbulent area degree of filling, here temperature reaches the highest simultaneously, and these high-temperature combustion gas are directly used in the heating of hot-water boiler.
Single-spiral flow smokeless hot-water boiler of chain fire grated of the present utility model; fugitive constituent burn-off rate 100%; the gas of discharging is clean, colourless, tasteless, dustless; lingemann blackness is 0; the ash content carbon of discharging only has 3-5% (conventional boiler is more than 28%); compare with conventional boiler; 20-30% can economize on coal; simple and reasonable, cheap, thermal efficiency height; energy consumption is low; can solve coal-fired over-emitting black exhaust problem, the protection environment, combination property can with advanced but expensive " CFBB " compare favourably.
Description of drawings
Fig. 1 is existing QXL type traveling-grate stoker formula hot-water boiler structural representation.
Fig. 2 is the utility model one example structure schematic diagram in conjunction with operation logic.
Fig. 3 is the coal-burning installation structural representation among Fig. 2.
Fig. 4 is the front furnace cross-sectional structure schematic diagram among Fig. 3.
Among the figure: 1, flame-observing hole 2, front furnace 3, manhole door 4, combustion heat gas outlet 5, stove rear arch 6, traveling-grate stoker 7, air compartment 8, sealing block (also claiming grey iron block) 9, back roller 10, rear hearth 11, ash-falling hole 12, back manhole 13, maintenance hand hole 14, next part case 15, flue gas goes out 16, back-water valve (BWV) 17, guardrail 18, flag style tube row group 19, water-cooling wall 20, safety anti-explosive valve 21, vent valve 22, Pressure gauge 23, drum 24, manhole 25, furnace wall 26, shell 27, trimmer arch 28, coal bunker 29, coal flashboard 30, blanket roller 31, single eddy flow chimney arch 32, upper furnace 33, burning gases go out 34, training wall 35, high temperature turbulent area 36, the combustion-supporting air port 37 of secondary, coal seam 38, grieshoch 39,41,43, the combustion-supporting air channel 40 of secondary, lower hearth 42, cloth wind box F1, F2, combustion air B1, B2, air blast.
The specific embodiment
The utility model is described in further detail below in conjunction with the embodiment accompanying drawing.
As Fig. 2, shown in 3, single-spiral flow smokeless hot-water boiler of chain fire grated described in the utility model, on existing QXL type traveling-grate stoker formula hot-water boiler basis shown in Figure 1, except that coal-burning installation, other continues to use original structure, comprise shell 26, the flag style tube row group 18 on top, water-cooling wall 19, the coal-burning installation of drum 23 and bottom, coal-burning installation comprises by coal bunker 28, the coaling gear that coal flashboard 29 is formed, traveling-grate stoker 6, chimney arch, constitute rear hearth 10 between stove rear arch 5 and the traveling-grate stoker 6, the top of front furnace cross section is the arch that forms swirl flow combustion, replace trimmer arch by single eddy flow chimney arch 31, constitute front furnace between trimmer arch and the traveling-grate stoker 6, the sidewall of front furnace is fitted with the combustion-supporting air port 36 of leading to front furnace, combustion-supporting air port 36 is tangent with the arch at front furnace top, makes front furnace form vortex furnace, and the front end of stove rear arch 5 is provided with training wall 34 upwards, the top of training wall 34 exports 33 lopsidedness to combustion heat gas, and the rear portion of front furnace is communicated with combustion heat gas outlet 33.
As shown in Figure 4, front furnace is divided into the two parts that communicate up and down, and cross section is R shape, or approximate Ω shape, the front furnace sidewall is provided with combustion-supporting air port 36 or the air channel 41 of leading to upper furnace 32 along two pins of R shape, and the front furnace sidewall also is provided with the combustion-supporting air channel 39,43 of leading to lower hearth 40 along the pin of R shape.
The course of work:
Under the effect of the combustion air that enters from air compartment 7, at high temperature burn in coal seam 37 on the traveling-grate stoker 6, produce a large amount of dense flue gases, coal tar steam wherein, coal gas (carbon monoxide), hydrocarbon gas, the particle of coal and subparticle or the like volatile combustible product can rise rapidly, and the guiding that tiltedly takeed on by front furnace top two, air-flow is concentrated to the crown center quirk, compress and the flow velocity increase, because two oblique shoulders are not isometric, the weak point on the left side, the length on the right, both sides corresponding downwards grate area also different, so the right flame flow is bigger than the flame flow density on the left side, flow velocity is also fast, the two past left side deflection occurred when concentrating at fire channel place, last top, this strand contains the high concentration flue gas of a large amount of flammable compositions and flame enters top with higher flow velocity swirl flow combustion zone, it is upper furnace 32, also can be described as " single swirl flow combustion district ", enter rotation status immediately, the eddy flow combustion air is through the combustion-supporting air port 36 or the air channel 39 of the right and left simultaneously, 41,43, tangential direction with this circle, spray with certain pressure and flow velocity, the two makes a concerted effort to form stronger turning moment, flammable flue gas and combustion-supporting oxygen (air) are mixed consumingly, cause burning fiercely, produce high temperature, reach 1200-1450 ℃, strengthened the burning condition in this combustion zone more, according to " high-speed rotational principle ", this strand air-flow of rotation at a high speed all will produce consumingly " entrainmenting " effect to overhead all volatile materials of the whole front furnace that covers, none is slipped through the net, because the airflow route in the swirl flow combustion district is " a spiral stroke ", the track route and the residence time of fuel have greatly extended, in this burning system, volatile fuel and combustible dust (flue gas) have: 1. essential temperature; 2. enough oxygen; 3. good stirring; 4. sufficient burning time, essential elemental burns, " flawless " of Ti Xianing here, so flue gas will be by slap-up after-flame, what obtain is clean, tasteless, colourless, dustless high-temperature gas enters the high temperature turbulent area that training wall 34 places form with certain flow rate, owing to lost " constraint " of combustion zone, air-flow begins to tear mutually to turn round, collision, pulverize, form many irregular disorderly air-flows, because the inertia of high speed swirling eddy, these air-flows still form " turbulence-like " in the rotation of establishing one's own system, and it is very high at this turbulent area degree of filling, here temperature reaches the highest simultaneously, and these high-temperature combustion gas are directly used in the heating of hot-water boiler.
The thickness in coal seam can be determined according to the height that the boiler heat load adjustment is positioned at the coal flashboard of trimmer arch front, this stage from the coal flashboard to manhole door, it is the zone that " fugitive constituent " of bituminous coal separated out in a large number, " yet single swirl flow combustion district " is in the top of going up in this zone just, all flue gases all will be involved in this high temperature flue that rotates at a high speed, by thorough after-flame, clean flame flow enters the high temperature turbulent area that the training wall place forms with certain flow rate.
The bituminous coal of front is quilt " destructive distillation " while walking, fugitive constituent volatilizees basically and burns totally, after the process manhole door is sentenced, become " coke ", " burning-point " of this coke is very high, there is not sufficiently high temperature to burn endless, " high temperature turbulent area " yet here just just, so " burnt nuclear " in the lime-ash that in conventional boiler, is difficult to burn, in this zone also by thorough after-flame, the lime-ash of after-flame is " noncombustibles " all, and the motion backward along with fire grate falls into ash hole and discharges out of the furnace.
In addition, in order to make the coke after-flame, " coke forms the district " corresponding air compartment has certain ventilation (can regulate by corresponding air-valve), again because this regional gas permeability is fine, there be a small amount of " overheated remaining oxygen " to pass coke layer always and add to this " high temperature turbulent area ", this just more makes the condition of burning reach best, suppose to leak and serve flue gas from the front, also can be by this " high-intensity zoneofoxidation " slap-up oxidizing away, certain superfluous oxygen is too many, because temperature is too high, be easy to generate harmful nitrogen oxide (NOx) again.Can reasonably regulate this regional air capacity under the prerequisite that does not have cigarette fully, suitably be in " reasonably anaerobic condition ", because of the chemical property of nitrogen (N) active not as the chemical property of the carbon (C) under the red-hot state, so following reduction reaction occurs:
NOx+HC→CO 2+H 2O+N
NOx+CO→CO 2+N
NOx+C→CO 2+N
Nitrogen oxide is seized oxygen atom by carbon and hydrogen as a result, is reduced into nitrogen again.
Therefore, " high temperature turbulent area " is equivalent to the tight pernicious gas of one deck " screen pack ", and all none is processed into non-toxic gas with slipping through the net and emits through this zone the time for three kinds of toxic gases.
In the chemical examination of coal, the material of incombustibility is called " ash ", difference according to the constitutional chemistry composition, the temperature of pairing " ash fusion point " is also different, but the overwhelming majority can melt to burn about 1350 ℃ to form slag, fraction in burning in these ash rises up slowly with air-flow, contained flammable composition is suspended the afterburnt, not flammable composition will form tiny " slag dirt ", because very light weight, shape is disorderly and unsystematic, better aerodynamic effect is arranged, taken away by air-flow easily or with the form of dust stratification be deposited on the boiler tube and the boiler random in or float in the atmosphere through chimney and to go, this is a matter of course feelings in traditional combustion apparatus, is not so just in the utility model.
In combustion mode of the present utility model, combustible dust and incombustibility dust are under suspended state and high temperature, rotary collision intensely, because temperature is very high, generally be between 1350 ℃-1450 ℃, this temperature almost is all ash " ash fusion points ", because fine dust is fused into small " bead " easily fast, add again at swirl flow combustion section motion collision intensely, wherein some also can be agglomerated into bigger " bead " shape, no matter be big and tiny all having become " sphere ", the aerodynamic quality of this geometry is bad, be difficult to floating with air-flow, go so can settle out to stick together to be discharged to outside the stove at " high temperature turbulent area " with following big lime-ash, has only few part along with the high velocity air that upwards sprays enters into very big boiler cup the inside, space, here the speed of air-flow is slack-off rapidly, add the cooling effect of water-cooling wall again, temperature also reduces rapidly, these " microballoons " have lost high velocity air " supporting effect ", settle out immediately, be deposited on the bottom of " cup ", pass through ash removing opening, periodic cleaning is come out, can not be bonded on the heat-exchange surface of boiler, so perfect combination of the present utility model makes " pot " and " stove " all can reach best running status, realizes high efficiency truly, low energy consumption.
Cloth wind box can be passed through in the combustion-supporting air channel of in the utility model each, realizes that as required cloth wind distributes, and provides cloth pneumatic power by same power source, simplifies auxiliary equipment.
Air feed system can be equipped with the automation frequency-changing control system, realizes automation mechanized operation.Mode as the available frequency control of adjusting of wind supply quantity solves, that is changes the method control wind supply quantity of the rotating speed of blower fan by the frequency that changes fan power.Utilize flue gas sensor (the industrial electronic retail department all has commercially available), as zirconium dioxide flue gas sensor, it presents " gas sensitive effect " to carbon monoxide, as long as it is exactly anoxic that flue gas is arranged, as long as anoxic just certainly leads to carbon monoxide, so the content of detection CO gas how much, also just directly reflected " air distribution coefficient " and the combustion conditions of combustion apparatus inside.The content of CO gas is become on the voltage signal input terminal that voltage signal is input to frequency converter, can utilize the voltage signal controlled frequency to change, the frequency conversion out-put supply is exactly the power supply of air blast, like this, rational air distribution coefficient can be arranged, fundamentally control the excessive generation of nitrogen oxide.

Claims (7)

1. single-spiral flow smokeless hot-water boiler of chain fire grated, comprise shell, the flag style tube row group on top, water-cooling wall, the coal-burning installation of drum and bottom, coal-burning installation comprises coaling gear, traveling-grate stoker, trimmer arch and stove rear arch, constitute front furnace between trimmer arch and the traveling-grate stoker, constitute rear hearth between stove rear arch and the traveling-grate stoker, the outlet of combustion heat gas is arranged between trimmer arch and the stove rear arch, the top that it is characterized in that the front furnace cross section is the arch that forms swirl flow combustion, the sidewall of front furnace is fitted with the combustion-supporting air port of leading to front furnace, the arch at combustion-supporting air port and front furnace top is tangent, and the rear portion of front furnace is communicated with the outlet of combustion heat gas.
2. single-spiral flow smokeless hot-water boiler of chain fire grated according to claim 1 is characterized in that front furnace is divided into the two parts that communicate up and down, and cross section is R shape, and the front furnace sidewall is provided with the combustion-supporting air channel of leading to upper furnace along the pin of R shape.
3. single-spiral flow smokeless hot-water boiler of chain fire grated according to claim 2 is characterized in that the front furnace sidewall is equipped with the combustion-supporting air channel of leading to upper furnace along two pins of R shape.
4. single-spiral flow smokeless hot-water boiler of chain fire grated according to claim 2 is characterized in that the front furnace sidewall is provided with the combustion-supporting air channel of leading to lower hearth along the pin of R shape.
5. single-spiral flow smokeless hot-water boiler of chain fire grated according to claim 2 is characterized in that the front furnace sidewall is equipped with the combustion-supporting air channel of leading to lower hearth along two pins of R shape.
6. according to claim 2,3,4 or 5 described single-spiral flow smokeless hot-water boiler of chain fire grated, it is characterized in that the front end of stove rear arch is provided with training wall upwards.
7. single-spiral flow smokeless hot-water boiler of chain fire grated according to claim 6 is characterized in that the water conservancy diversion coping tilts to combustion heat gas outlet side.
CNU2007200239200U 2007-06-16 2007-06-16 Chain grate type single toroidal swirl pure smokeless hot water boiler Expired - Fee Related CN201093702Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007200239200U CN201093702Y (en) 2007-06-16 2007-06-16 Chain grate type single toroidal swirl pure smokeless hot water boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007200239200U CN201093702Y (en) 2007-06-16 2007-06-16 Chain grate type single toroidal swirl pure smokeless hot water boiler

Publications (1)

Publication Number Publication Date
CN201093702Y true CN201093702Y (en) 2008-07-30

Family

ID=39901670

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2007200239200U Expired - Fee Related CN201093702Y (en) 2007-06-16 2007-06-16 Chain grate type single toroidal swirl pure smokeless hot water boiler

Country Status (1)

Country Link
CN (1) CN201093702Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106196616A (en) * 2016-06-29 2016-12-07 无锡锡能锅炉有限公司 A kind of boiler plant automatically controlled

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106196616A (en) * 2016-06-29 2016-12-07 无锡锡能锅炉有限公司 A kind of boiler plant automatically controlled

Similar Documents

Publication Publication Date Title
CN100538172C (en) Industrial Boiler, kiln double swirl-flow combustion apparatus
CN101074774A (en) Bi-spiral flow smokeless steam boiler with chain grates
CN201396743Y (en) Angle pipe type circulating fluidized bed boiler
CN207019075U (en) A kind of circulating fluid bed garbage furnace
CN101074801A (en) Double-spiral flow smokeless hot-water boiler of chain fire grated
CN201093702Y (en) Chain grate type single toroidal swirl pure smokeless hot water boiler
CN202074686U (en) Biomass cyclone hot air furnace
CN201059547Y (en) Chain-grate stoker type single rotational flow pure smokeless steam boilers
CN206037022U (en) Biomass circulating fluid bed boiler arranges sediment device
CN201059747Y (en) Chain-grate stoker type double rotational flow pure smokeless water heater boiler
CN101074800A (en) Single-spiral flow smokeless hot-water boiler of chain fire grated
CN201059548Y (en) Chain-grate stoker type double rotational flow pure smokeless steam boilers
CN210441220U (en) CFB boiler coal-fired coupling processing line to combustible solid waste
CN107178785A (en) A kind of circulating fluid bed garbage furnace
CN101074773A (en) Single-spiral flow smokeless steam boiler with chain grates
CN209431381U (en) A kind of biomass steam producer
CN100520216C (en) Flow guiding tapering shape pure smokeless vertical type water heater boiler
CN201497188U (en) Organic heat carrier boiler
CN106287686A (en) Biomass recirculating fluidized bed boiler slag-draining device
CN201443753U (en) Boiler system for burning coal powder
CN205710615U (en) The pulverized coal gasification furnace that a kind of preheated air enters with eddy flow
CN201059614Y (en) Venturi tube effect type pure smokeless vertical type water heater boiler
CN100494776C (en) Adequate and clean combustion equipment
CN100520169C (en) Conical guide smokeless vertical steam boiler
CN2919051Y (en) Single vortex coal-burning installation

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080730