CN206377651U - A kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine - Google Patents
A kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine Download PDFInfo
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- CN206377651U CN206377651U CN201621408574.3U CN201621408574U CN206377651U CN 206377651 U CN206377651 U CN 206377651U CN 201621408574 U CN201621408574 U CN 201621408574U CN 206377651 U CN206377651 U CN 206377651U
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- ring
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Abstract
The utility model is related to a kind of straw burning boiler smoke drop ash and denitrogenates cooling all-in-one machine.A face brick baffle IV is provided with straw boiler body burner hearth, the side of brick baffle IV connects with burner hearth right side wall, and opposite side is gas approach, the heavy grey room of rectangle steering is constituted between brick baffle IV and brick baffle I, ash room bottom is sunk provided with several heavy grey funnels II；Low temperature nitrogen removing device is fixed on straw boiler outer body, and heat energy exchange device is fixed in low temperature nitrogen removing device；Fuel feed device is mutually fixed through straw boiler bodies top with the external steelframe of boiler body；Straw burner is arranged on straw boiler body lower part, passes through burner sealing surface and straw boiler body burner hearth bottom steelframe sealing surface tight fit.Effect is to significantly improve the heat exchange of straw boiler, reduces the abrasion of straw boiler pipeline, flue gas is flowed in pipeline heat transfer process unobstructed.Material, manufacture can be reduced while air discharge and energy resource consumption is reduced, is installed and cost of floor space.
Description
Technical field
The utility model is related to a kind of straw burning boiler smoke drop ash and denitrogenates cooling all-in-one machine.Straw burning boiler is denitrogenated
Cooling all-in-one machine is the high density granular that a kind of use straw and weeds biolobic material are pressed into or is rolled into less than certain
Size particle is the thermal energy exchange equipment of fuel, belongs to biomass combustion boiler.
Background technology
Existing straw burning boiler only has boiler body, and inside turns to heavy grey room without flue gas, is not the combustion of boiler overhead
Expect feeding structure, low temperature nitrogen removing device and heat energy exchange device are then arranged in outside boiler body, burner and body of heater flange
And bolt connection.Said structure, many unfavorable factors can be produced for boiler furnace.
1. during straw burning boiler combustion stalk fuel, certain density flying dust can be formed, the more other fuel of these flying dusts
Flying dust amount it is big, this is just easier to form attachment on convection heating surface and accumulated, and influences heat exchange and the flue gas of heating surface
Flow velocity, the heat exchange property of boiler is poor, and abrasion of the flying dust to straw boiler pipeline is larger, add the maintenance of boiler tubing into
This.
All it is to apply flange and bolt connection, burner integrated suspension is in boiler sheet 2. conventional burner is connected with body
Body chassis bottom, whole weight is all attached on boiler pan, is posed a big pressure to boiler pan structure load-bearing.
4. the conveying of fuel is usually to enter burner in burner bottom pushing tow fuel, or enters combustion from side feed fuel
Burner, so all can produce fuel and block and dispense inequality.
3. low temperature nitrogen removing device and heat energy exchange device（Economizer）It is arranged in outside boiler body, is connected by flue,
I.e. floor space is larger and wastes the material of connection flue, also add installation cost.
So for problem above, it is necessary to be transformed and innovated in structure, it is necessary to which our technical staff are studied
Solve.
The content of the invention
In view of the situation and the deficiency of presence of prior art, the utility model drop there is provided a kind of straw burning boiler smoke
Ash denitrogenates cooling all-in-one machine, and a flue gas is set up inside boiler body and turns to heavy grey room, the concentration of flying dust is reduced, greatly
The heat exchange property of straw boiler is improved, the abrasion of straw boiler pipeline is reduced.
Low temperature denitrogenates easy coupling arrangement and afterbody heat energy exchange device（Economizer）Boiler body side is connected directly between, is saved
Floor space has been saved, the effect denitrogenated, cooled is improved.
Straw boiler overhead fuel feed mechanism, reduces floor space, fuel falls from the top down, and fuel will not be because of
Block and be unable to situation of the work feed to burner combustion disk and occur.
Using the independent burning device of prior art, i.e. disk straw burner, connected mode is changed, boiler is alleviated
The supporting power of chassis structure.
To achieve the above object, the technical scheme used is the utility model：A kind of straw burning boiler smoke drop ash
Denitrogenate cooling all-in-one machine, including straw boiler body, low temperature nitrogen removing device, heat energy exchange device, straw burner, the stalk
Provided with one of brick baffle I in boiler body burner hearth, the side of brick baffle I connects with burner hearth left side wall, and opposite side is intake channel I,
Between rear wall in brick baffle I and burner hearth, the first convection bank, the second convection bank, the 3rd convection bank are sequentially provided with,
Provided with flue gas partition wall II together between first convection bank and the second convection bank, flue gas partition wall II is by intake channel I and passes in and out
Mouth passage I is separated, and provided with flue gas partition wall III together between the second convection bank and the 3rd convection bank, flue gas partition wall III will enter
Exit passageway II and exit passageway II are separated, and in intake channel I, import and export passage I, import and export passage II and the bottom of exit passageway II
Portion is respectively equipped with heavy grey funnel I；
It is characterized in that：Also include fuel feed device, the fuel feed device includes feed pipe, ring-type closure plate, two
Secondary wind channel tube, Secondary Air disk, refractory concrete；
The Secondary Air disk includes upper the ring disk, lower the ring disk, split-wind plate, and upper the ring disk internal diameter is more than lower the ring disk internal diameter, several points
Being arranged between the ring disk and lower the ring disk for aerofoil interval constitutes several points of air channels；
The feed pipe low side is straight tube, and upper end is inclined tube, and being externally provided with one in feed pipe is more than the two of feed pipe external diameter
Secondary wind channel tube, ring-type closure plate is provided with Secondary Air deferent upper end, and inner ring surface and the feed pipe outer tube wall of ring-type closure plate are welded, ring-type
The outer ring surface of closure plate is welded with the Secondary Air deferent mouth of pipe, and secondary air intake pipe is provided with the tube wall of Secondary Air deferent upper end,
Secondary Air deferent lower end is arranged in burner hearth sets refractory concrete on the tube wall of part,
The Secondary Air disk is arranged on the ring disk under the low side of feed pipe, Secondary Air deferent and refractory concrete, Secondary Air disk
Inner ring surface is welded with feed pipe outer tube wall, and the ring disk inner ring surface is welded with Secondary Air deferent outer tube wall on Secondary Air disk；
A face brick baffle IV is provided with the straw boiler body burner hearth, the side of brick baffle IV connects with burner hearth right side wall,
Opposite side is gas approach, and rectangle is constituted between brick baffle IV and brick baffle I and turns to heavy grey room, heavy ash room and the phase of intake channel I
It is logical, ash room bottom is sunk provided with several heavy grey funnels II, and boiler tube bank is provided with the indoor brick baffle IV of ash sinking, boiler tube bank,
First convection bank, the second convection bank, the boiler tube bank in the 3rd convection bank are communicated with upper lower drum respectively；
The low temperature nitrogen removing device is fixed on the boiler method on the outside of straw boiler rear body by nitrogen removing device flange frame
On blue disk, the heat energy exchange device is fixed in low temperature nitrogen removing device, the exit passageway II in straw boiler body burner hearth
Outlet is communicated with the gas approach I of low temperature nitrogen removing device, the exhanst gas outlet I of low temperature nitrogen removing device and the flue gas of heat energy exchange device
Import II is communicated, and exhanst gas outlet II is provided with the outside of heat energy exchange device；
The fuel feed device is through straw boiler bodies top with the fixation of straw boiler body every windband pipe, fuel
Feed device feed pipe inclined tube is mutually fixed with the external steelframe of boiler body, and the outlet of fuel feed device feed pipe straight tube is placed in stalk
Above burner, flexible fire resistant infilling is filled in fuel feed device Secondary Air deferent and in gap between windband pipe；
The burner sealing surface of the straw burner and straw boiler body burner hearth bottom steelframe sealing surface tight fit,
Provided with one layer of fire resistant seal filler between burner sealing surface and steelframe sealing surface, on the support of four columns of straw burner
It is respectively equipped with a burner resilient support.
The beneficial effects of the utility model are：
1. flue gas is set up inside boiler body turns to heavy grey room, it is enclosed by the boiler tube bank in design and building by laying bricks or stones
Into a rectangular enclosure, be provided with gas approach in boiler furnace side, pass through turn to and actual internal area expansion so that boiler
Grey particle in flue gas stall, such boiler smoke just loses most kinetic energy, makes dust natural subsidence by gravity, in addition
The larger dust particle of another part kinetic energy is bumped against on the furnace wall on smoke inlet opposite, and kinetic energy is lost, and makes dust natural subsidence.It
Easy arrangement simple in construction.By the depositing dust of heavy grey room, the heat exchange of straw boiler is significantly improved, straw boiler pipeline is reduced
Abrasion, reduces the work that boiler workman removes dust deposited in pipeline, flue gas is flowed in pipeline heat transfer process unobstructed.
2. low temperature denitrogenates easy coupling arrangement and afterbody heat energy exchange device（Economizer）All develop into flange form and connect knot soon
Structure, is linked together by flange with boiler body side.Using this structure, be conducive to connection quick and convenient, make equipment tight
Gather, good sealing effect saves connection flue, reduces floor space, so also just reducing raw material and labour cost hair
It is raw, user is so not only improved, the manufacturing enterprise of equipment and the installation enterprises of equipment is also beneficial to.Using this structure, setting
In the case of compact, the energy can be utilized efficiently can reduce the discharge of pollutant again.
It is a kind of new conveying fuel mode, it is installed by advance 3. fuel feed device is installed on straw boiler top
Steelframe set off every windband pipe, its fuel feed device, every windband pipe, is deep into straw boiler through this overhead
In thorax.Fuel feed device is mutually fixed or is connected with flange with the external steelframe of boiler body, but this should have rigidity after windband pipe
Support, fuel feed device can also be supported by rigid trestle, through every windband pipe, fuel feed device and every windband pipe
Between be filled and sealed with flexible fire resistant infilling, straw boiler top layout reduces floor space, meets burning
Device is fed demand, makes fuel conveying convenient, reduces floor space.Because the fuel feed device is from inclined tube feeding, by straight
Pipe is fallen on the tray for combustion of straw burner, and fuel falls from the top down, and such fuel will not can not be transported to because of blocking
On the tray for combustion of burner, such setting can also make the fuel dropped in dropping process, by the radiant heat of high-temperature burner hearth,
Make fuel by destructive distillation and ignite, fuel is when falling on tray for combustion, and fuel in burning or is ignited state, and this is also combustion
Combustion system needed for burner.
Secondary Air deferent and refractory concrete two layers of heat-resisting heat-barrier coating of formation, make feed pipe in the straw boiler of high temperature
The conveying task of fuel is favorably accomplished in burner hearth.
Secondary Air deferent gives straw burner uniform oxygen supply by Secondary Air disk, makes stalk fuel burning more abundant.
4. the disk straw burner of wall-attaching type seal style is connected with straw boiler.Straw burner is that collar plate shape is only
Vertical burner, is different from other combustion apparatus.Disk straw burner flange is patch with straw boiler base burning mouthful plane
Wall-shaped is sealed, the setting of four burner resilient support, and one is for straw burner sealing surface and straw boiler body burner hearth bottom
Portion's steelframe sealing surface provides top power and supported, another effect can be reduced causes screw rod and support force to become due to expanding with heat and contract with cold
Shape, reduces sealing surface cracking and causes flue gas to reveal.
Described on ancestor, straw boiler, which denitrogenates cooling all-in-one machine, effectively to minimize steam generator system, be a convenience, fast
Prompt, efficient heat transmission equipment.Material cost, manufacturing cost, installation can be reduced while air discharge and energy resource consumption is reduced
Cost, cost of floor space.
Brief description of the drawings
Fig. 1 is front view of the present utility model；
Fig. 2 is Fig. 1 A-A sectional views；
Fig. 3 is Fig. 1 C-C sectional views；
Fig. 4 is the utility model vertical view cutaway drawing；
Fig. 5 is the partial enlarged drawing that the utility model is connected with low temperature nitrogen removing device；
Fig. 6 is Fig. 5 A-A sectional views；
Fig. 7 is Fig. 5 B-B sectional views；
Fig. 8 is Fig. 5 C-C sectional views；
Fig. 9 is Fig. 8 D enlarged drawing；
Figure 10 is Fig. 9 E-E sectional views；
Figure 11 is the structural representation of the utility model fuel feed device；
Figure 12 is the front view of the utility model Secondary Air disk；
Figure 13 is the vertical view cutaway drawing of the utility model Secondary Air disk；
Figure 14 is the partial enlarged drawing that the utility model is connected with straw burner；
Figure 15 is Fig. 1 4B enlarged drawings；
Figure 16 is that the utility model flue gas denitrogenates flow chart.
Embodiment
As shown in Fig. 1 to Figure 15, a kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine, including straw boiler sheet
Body 1, low temperature nitrogen removing device 2, heat energy exchange device 3, straw burner 4, in addition to fuel feed device 5.
Fuel feed device 5 includes feed pipe 5-1, ring-type closure plate 5-2, Secondary Air deferent 5-3, Secondary Air disk 5-4, fire resisting
Concrete 5-5.
Secondary Air disk 5-4 includes upper the ring disk 5-41, lower the ring disk 5-42, split-wind plate 5-43, under upper the ring disk 5-41 internal diameters are more than
The ring disk 5-42 internal diameters, being arranged between the ring disk 5-41 and lower the ring disk 5-42 for several split-wind plates 5-43 intervals constitutes several points of wind
Road.
Feed pipe 5-1 low sides are straight tube, and upper end is inclined tube, and being externally provided with one in feed pipe 5-1 is more than feed pipe 5-1 external diameters
Secondary Air deferent 5-3, Secondary Air deferent 5-3 upper ends be provided with ring-type closure plate 5-2, ring-type closure plate 5-2 inner ring surface and feeding
Pipe 5-1 outer tube walls are welded, and ring-type closure plate 5-2 outer ring surface and the Secondary Air deferent 5-3 mouths of pipe are welded, on Secondary Air deferent 5-3
The tube wall at end is provided with secondary air intake pipe 5-31, is arranged in burner hearth on the tube wall of part and sets in Secondary Air deferent 5-3 lower ends
Refractory concrete 5-5.
Secondary Air disk 5-4 is arranged on feed pipe 5-1, Secondary Air deferent 5-3 and refractory concrete 5-5 low side, Secondary Air
The ring disk 5-42 inner ring surfaces and feed pipe 5-1 outer tube walls are welded under disk 5-4, on Secondary Air disk 5-4 the ring disk 5-41 inner ring surfaces with it is secondary
Wind channel tube 5-3 outer tube walls are welded.
Provided with one of 1-1 of brick baffle I in the burner hearth of straw boiler body 1, the 1-1 sides of brick baffle I connect with burner hearth left side wall,
Opposite side is between the 1-1-1 of intake channel I, the rear wall in the 1-1 of brick baffle I and burner hearth, to be sequentially provided with the first convection bank 1-
2nd, the second convection bank 1-3, the 3rd convection bank 1-4, are provided between the first convection bank 1-2 and the second convection bank 1-3
One flue gas partition wall II 1-5, the 1-5 of flue gas partition wall II separate the 1-1-1 of intake channel I and the import and export 1-6 of passage I, at second pair
Provided with the 1-7 of flue gas partition wall III together between flowing bundle 1-3 and the 3rd convection bank 1-4, the 1-7 of flue gas partition wall III will import and export passage
II 1-8 and the 1-9 of exit passageway II are separated, and in the 1-1-1 of intake channel I, imported and exported passage I 1-6, are imported and exported the 1-8 of passage II and go out
Mouth passage II 1-9 bottoms are respectively equipped with the heavy grey 1-10 of funnel I.
The 1-11 of a face brick baffle IV, the 1-11 sides of brick baffle IV and burner hearth right side wall are provided with the burner hearth of straw boiler body 1
Connect, opposite side is gas approach 1-11-1, rectangle is constituted between the 1-11 of brick baffle IV and the 1-1 of brick baffle I and turns to heavy ash room 1-
12, heavy ash room 1-12 is communicated with the 1-1-1 of intake channel I, ash room 1-12 bottoms is sunk provided with several heavy grey 1-12-1 of funnel II, heavy
The 1-11 of brick baffle IV in grey room 1-12 is provided with boiler tube bank 1-11-2, boiler tube bank 1-11-2, the first convection bank 1-2,
Boiler tube bank on second convection bank 1-3, the 3rd convection bank 1-4 is communicated with upper lower drum respectively.
Low temperature nitrogen removing device 2 is fixed on the boiler ring flange in the outside of straw boiler body 1 by nitrogen removing device flange frame 2-8
On 1-13, heat energy exchange device 3 is fixed in low temperature nitrogen removing device 2, the 1-9 of exit passageway II in the burner hearth of straw boiler body 1
Outlet 1-91 communicated with the 2-2-1 of gas approach I of low temperature nitrogen removing device 2, the 2-3-1 of exhanst gas outlet I of low temperature nitrogen removing device 2 with
The 3-1 of gas approach II of heat energy exchange device 3 is communicated, and the outside of heat energy exchange device 3 is provided with the 3-2 of exhanst gas outlet II.
Fuel feed device 5 is through the top of straw boiler body 1 with the fixation of straw boiler body 1 every windband pipe 6, combustion
The feed pipe 5-1 inclined tubes of feed device 5 are mutually fixed with the external steelframe of boiler body, and the feed pipe 5-1 straight tubes of fuel feed device 5 go out
Mouth is placed in the top of straw burner 4, is filled with the Secondary Air deferent 5-3 of fuel feed device 5 and between windband pipe 6 in gap
Flexible fire resistant infilling.
The burner sealing surface 4-1 of straw burner 4 and the burner hearth bottom steelframe sealing surface 1-14 close-fittings of straw boiler body 1
Close, provided with one layer of fire resistant seal filler between burner sealing surface 4-1 and steelframe sealing surface 1-14, in straw burner 4 four
A burner resilient support 4-3 is respectively equipped with individual column 4-2 support.
Burner resilient support 4-3 includes screw rod 4-3-1, spiral rod set 4-3-2, spring housing 4-3-3, spring 4-3-4,
It is respectively welded on four column 4-2 of burner arm in spiral rod set a 4-3-2, each spiral rod set 4-3-2 and is spirally connected one
Root screw rod 4-3-1, screw rod 4-3-1 upper ends are rectangular surfaces 4-3-11, and screw rod 4-3-1 lower ends are separately positioned on spring housing 4-
On spring 4-3-4 in 3-3.
Low temperature nitrogen removing device 2 includes center 2-1, front shroud 2-2, back shroud 2-3, plate washer 2-4, metallic catalyst filter layer
Framework is provided with flange frame 2-8 before and after 2-5, the center 2-1, and the first filtering area 2- is constituted provided with plate washer 2-4 in center 2-1
6th, the second filtering area 2-7, turns to passage, in the first filtering area 2-6 and the second filtering area 2-7 in plate washer 2-4 lower ends provided with flue gas
Inside it is respectively equipped with several layers of metallic catalyst filter layer 2-5, several layers of metallic catalyst filter layer 2-5 interval settings, the front shroud
2-2 and back shroud 2-3 are separately fixed on center 2-1 front and rear framework, and the 2-2-1 of gas approach I is provided with front shroud 2-2,
The 2-3-1 of exhanst gas outlet I is set on back shroud 2-3.
Metallic catalyst filter layer 2-5 is rectangle tabular, is spaced on metallic catalyst filter layer 2-5 plates several
Rectangular opening 2-5-1.
Metallic catalyst filter layer 2-5 is fired by MnOx/TiO2, V2O5 and sintering binder and constituted.
A kind of straw burning boiler smoke drop ash denitrogenates the implementation method of cooling all-in-one machine, and step is as follows：
Straw burner 4 is arranged on the boiler furnace lower end of straw boiler body 1, four burner elasticity are caught in instrument
The rectangular surfaces 4-3-11 of 4-3 screw rod 4-3-1 upper ends is supported, turn clockwise screw rod 4-3-1, makes straw burner sealing surface
4-1 and the burner hearth bottom steelframe sealing surface 1-14 tight fits of straw boiler body 1, in burner sealing surface 4-1 and steelframe sealing surface
Provided with one layer of fire resistant seal filler between 1-14, four burners flexibly support 4-3 setting, and one is sealed for straw burner
The face 4-1 and burner hearth bottom steelframe sealing surface 1-14 of straw boiler body 1 provides top power and supports that another effect can be reduced due to heat
Swollen shrinkage causes screw rod 4-3-1 and burner arm stress deformation, reduces by two sealing surface crackings and causes flue gas to reveal.
Stalk fuel enters on feed pipe 5-1 inclined tubes, the tray for combustion that straw burner 4 is fallen into by straight tube, and fuel will not
It can not be transported on the tray for combustion of burner because of blocking, such setting can also make the fuel dropped in dropping process,
By the radiant heat of high-temperature burner hearth, make fuel by destructive distillation and ignite, fuel is when falling on tray for combustion, and fuel is in burning
Or it is ignited state, feed pipe 5-1, Secondary Air deferent 5-3, refractory concrete 5-5 structure, Secondary Air deferent 5-3 and fire resisting
Concrete 5-5 two layers of heat-resisting heat-barrier coating of formation, makes feed pipe 5-1 favorably accomplish combustion in the straw boiler burner hearth of high temperature
The conveying task of material.
Straw burning boiler external fan, enters Secondary Air deferent 5-3, then lead to by air by secondary air intake pipe 5-31
Secondary Air disk 5-4 several points of air channels are crossed, give straw burner 4 uniform oxygen supply, make stalk fuel burning abundant.
Heat smoke when stalk fuel burns, can form certain density flying dust, heat smoke passes through gas approach 1-11-1
Heavy ash room 1-12 rectangular enclosure is redirected into, passes through steering and the expansion of actual internal area so that heat smoke stall, such pot
Grey particle in kiln gas just loses most kinetic energy, makes a part of flying dust dirt natural subsidence, another part by gravity
The larger dust particle of kinetic energy is bumped against on the 1-1 of brick baffle I on gas approach 1-11-1 opposites, and kinetic energy is lost, and dust is sunk naturally
Drop, the dust of sedimentation is dropped in several heavy grey 1-12-1 of funnel II.
Heat smoke after sedimentation pass sequentially through the 1-1-1 of intake channel I, the first convection bank 1-2, import and export passage I 1-6,
Second convection bank 1-3, import and export passage II 1-8, the 3rd convection bank 1-4, the 1-9 of exit passageway II lose again heat smoke
Speed, settles dust, and the dust of sedimentation is dropped in several heavy grey 1-10 of funnel I.
Heat smoke after sedimentation is directly entered low temperature nitrogen removing device 2 by the 2-2-1 of gas approach I, and heat smoke is passed sequentially through
The several layers of metallic catalyst filter layer 2-5 of the first filter layer 2-4 in low temperature nitrogen removing device 2, the flue gas of plate washer 2-4 lower ends are turned to
Passage, the second filter layer 2-5 number layer metallic catalyst filter layers 2-5, remove after nitrogen content in flue gas from the 2-3- of exhanst gas outlet I
1 discharge, is directly entered heat energy exchange device 3, heat energy exchange device 3 will pass through after flue gas cool-down again by the 3-1 of gas approach II
The 3-2 of exhanst gas outlet II enters following apparatus.
Low temperature catalyst conversion zone main component is fired by MnOx/TiO2 and V2O5 etc. and constituted, in modularization honeycomb inverted
Answer in device, under catalyst action, ammonia chemically reacts with NOx, realize further denitrogenation, as shown in figure 16.
Claims (3)
1. a kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine, including straw boiler body（1）, low temperature nitrogen removing device
（2）, heat energy exchange device（3）, straw burner（4）, the straw boiler body（1）Provided with one of brick baffle I in burner hearth（1-
1）, brick baffle I（1-1）Side connects with burner hearth left side wall, and opposite side is intake channel I（1-1-1）, in brick baffle I（1-1）With
Between rear wall in burner hearth, the first convection bank is sequentially provided with（1-2）, the second convection bank（1-3）, the 3rd convection bank（1-
4）, in the first convection bank（1-2）With the second convection bank（1-3）Between provided with one flue gas partition wall II（1-5）, flue gas partition wall
Ⅱ（1-5）By intake channel I（1-1-1）With import and export passage I（1-6）Separate, in the second convection bank（1-3）With the 3rd convection current
Tube bank（1-4）Between provided with one flue gas partition wall III（1-7）, flue gas partition wall III（1-7）Passage II will be imported and exported（1-8）And outlet
Passage II（1-9）Separate, in intake channel I（1-1-1）, import and export passage I（1-6）, import and export passage II（1-8）It is logical with outlet
Road II（1-9）Bottom is respectively equipped with heavy grey funnel I（1-10）；
It is characterized in that：Also include fuel feed device（5）, the fuel feed device（5）Including feed pipe（5-1）, ring-type
Closure plate（5-2）, Secondary Air deferent（5-3）, Secondary Air disk（5-4）, refractory concrete（5-5）；
The Secondary Air disk（5-4）Including upper the ring disk（5-41）, lower the ring disk（5-42）, split-wind plate（5-43）, upper the ring disk（5-41）
Internal diameter is more than lower the ring disk（5-42）Internal diameter, several split-wind plates（5-43）What is be spaced is arranged on the ring disk（5-41）With lower the ring disk（5-
42）Between constitute several points of air channels；
The feed pipe（5-1）Low side is straight tube, and upper end is inclined tube, in feed pipe（5-1）It is externally provided with one and is more than feed pipe（5-
1）The Secondary Air deferent of external diameter（5-3）, in Secondary Air deferent（5-3）Upper end is provided with ring-type closure plate（5-2）, ring-type closure plate（5-2）
Inner ring surface and feed pipe（5-1）Outer tube wall is welded, ring-type closure plate（5-2）Outer ring surface and Secondary Air deferent（5-3）The mouth of pipe is welded
Connect, in Secondary Air deferent（5-3）The tube wall of upper end is provided with secondary air intake pipe（5-31）, in Secondary Air deferent（5-3）Lower end
It is arranged in burner hearth and sets refractory concrete on the tube wall of part（5-5）,
The Secondary Air disk（5-4）It is arranged on feed pipe（5-1）, Secondary Air deferent（5-3）And refractory concrete（5-5）It is low
End, Secondary Air disk（5-4）Lower the ring disk（5-42）Inner ring surface and feed pipe（5-1）Outer tube wall is welded, Secondary Air disk（5-4）Upper the ring disk
（5-41）Inner ring surface and Secondary Air deferent（5-3）Outer tube wall is welded；
The straw boiler body（1）A face brick baffle IV is provided with burner hearth（1-11）, brick baffle IV（1-11）Side and burner hearth
Right side wall connects, and opposite side is gas approach（1-11-1）, brick baffle IV（1-11）With brick baffle I（1-1）Between constitute rectangle
Turn to heavy grey room（1-12）, heavy ash room（1-12）With intake channel I（1-1-1）Communicate, heavy ash room（1-12）Bottom is provided with several
Heavy ash funnel II（1-12-1）, in heavy grey room（1-12）Interior brick baffle IV（1-11）It is provided with boiler tube bank（1-11-2）, pot
Boiler tube is arranged（1-11-2）, the first convection bank（1-2）, the second convection bank（1-3）, the 3rd convection bank（1-4）On boiler
Pipe row communicates with upper lower drum respectively；
The low temperature nitrogen removing device（2）Pass through nitrogen removing device flange frame（2-8）It is fixed on straw boiler body（1）Rear outside
Boiler ring flange（1-13）On, the heat energy exchange device（3）It is fixed on low temperature nitrogen removing device（2）On, straw boiler body（1）
Exit passageway II in burner hearth（1-9）Outlet（1-91）With low temperature nitrogen removing device（2）Gas approach I（2-2-1）Communicate, it is low
Warm nitrogen removing device（2）Exhanst gas outlet I（2-3-1）With heat energy exchange device（3）Gas approach II（3-1）Communicate, heat energy is handed over
Changing device（3）Outside is provided with exhanst gas outlet II（3-2）；
The fuel feed device（5）Through straw boiler body（1）Top and straw boiler body（1）It is fixed every windband pipe
（6）, fuel feed device（5）Feed pipe（5-1）Inclined tube is mutually fixed with the external steelframe of boiler body, fuel feed device（5）Send
Expects pipe（5-1）Straight tube outlet is placed in straw burner（4）Top, in fuel feed device（5）Secondary Air deferent（5-3）With every wind
Sleeve pipe（6）Between fill flexible fire resistant infilling in gap；
The straw burner（4）Burner sealing surface（4-1）With straw boiler body（1）Burner hearth bottom steelframe sealing surface
（1-14）Tight fit, in burner sealing surface（4-1）With steelframe sealing surface（1-14）Between provided with one layer of fire resistant seal filler,
Straw burner（4）Four columns（4-2）Support on be respectively equipped with burner resilient support（4-3）.
2. a kind of straw burning boiler smoke drop ash according to claim 1 denitrogenates cooling all-in-one machine, it is characterised in that：Institute
The low temperature nitrogen removing device stated（2）Including center（2-1）, front shroud（2-2）, back shroud（2-3）, plate washer（2-4）, metallic catalyst
Filter layer（2-5）, the center（2-1）Front and rear framework is provided with flange frame（2-8）, in center（2-1）It is interior to be provided with plate washer（2-4）
Constitute the first filtering area（2-6）, the second filtering area（2-7）, in plate washer（2-4）Lower end turns to passage provided with flue gas, in the first mistake
Filter area（2-6）With the second filtering area（2-7）Inside it is respectively equipped with several layers of metallic catalyst filter layer（2-5）, several layers of metallic catalyst
Filter layer（2-5）It is arranged at intervals, the front shroud（2-2）And back shroud（2-3）It is separately fixed at center（2-1）Front and rear framework
On, in front shroud（2-2）It is provided with gas approach I（2-2-1）, in back shroud（2-3）On set exhanst gas outlet I（2-3-1）；
Metallic catalyst filter layer（2-5）For rectangle tabular, in metallic catalyst filter layer（2-5）It is spaced on plate several
Rectangular opening（2-5-1）；
Metallic catalyst filter layer（2-5）Fired and constituted by MnOx/TiO2, V2O5 and sintering binder.
3. a kind of straw burning boiler smoke drop ash according to claim 1 denitrogenates cooling all-in-one machine, it is characterised in that：Institute
The burner resilient support stated（4-3）Including screw rod（4-3-1）, spiral rod set（4-3-2）, spring housing（4-3-3）, spring
（4-3-4）, four columns of burner arm（4-2）On a spiral rod set is respectively welded（4-3-2）, each spiral rod set
（4-3-2）Inside be spirally connected a screw rod（4-3-1）, screw rod（4-3-1）Upper end is rectangular surfaces（4-3-11）, screw rod（4-3-
1）Lower end is separately positioned on spring housing（4-3-3）Interior spring（4-3-4）On.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621408574.3U CN206377651U (en) | 2016-12-21 | 2016-12-21 | A kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621408574.3U CN206377651U (en) | 2016-12-21 | 2016-12-21 | A kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine |
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| Publication Number | Publication Date |
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| CN206377651U true CN206377651U (en) | 2017-08-04 |
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ID=59408952
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621408574.3U Withdrawn - After Issue CN206377651U (en) | 2016-12-21 | 2016-12-21 | A kind of straw burning boiler smoke drop ash denitrogenates cooling all-in-one machine |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106642075A (en) * | 2016-12-21 | 2017-05-10 | 天津市星拓科技发展有限公司 | Ash settling, denitrifying and cooling all-in-one machine for flue gas of straw combustion boiler and implementation method |
-
2016
- 2016-12-21 CN CN201621408574.3U patent/CN206377651U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106642075A (en) * | 2016-12-21 | 2017-05-10 | 天津市星拓科技发展有限公司 | Ash settling, denitrifying and cooling all-in-one machine for flue gas of straw combustion boiler and implementation method |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170804 Effective date of abandoning: 20180706 |