CN208059292U - Biomass fuel hot air stove - Google Patents

Biomass fuel hot air stove Download PDF

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Publication number
CN208059292U
CN208059292U CN201820400752.0U CN201820400752U CN208059292U CN 208059292 U CN208059292 U CN 208059292U CN 201820400752 U CN201820400752 U CN 201820400752U CN 208059292 U CN208059292 U CN 208059292U
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CN
China
Prior art keywords
furnace chamber
biomass fuel
hot air
outlet
exhaust gases
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
CN201820400752.0U
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Chinese (zh)
Inventor
刘威
刘宏
刘小莉
王克伟
刘亚松
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.)
Henan Province Fung Boiler Co Ltd
Original Assignee
Henan Province Fung Boiler Co Ltd
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
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Priority to CN201820400752.0U priority Critical patent/CN208059292U/en
Application granted granted Critical
Publication of CN208059292U publication Critical patent/CN208059292U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a kind of biomass fuel hot air stoves, heat exchanger including furnace chamber and positioned at furnace chamber top, it is provided with fuel inlet and exhanst gas outlet on the furnace chamber, the cold air inlet and heat outlet with air communication are provided on the heat exchanger, isocon is installed at the exhanst gas outlet or heat outlet at least one, the isocon is connected to fuel inlet.Hot gas or flue gas are returned to burner hearth and re-use preheating therein by the application, improve the efficiency of combustion of fuel;Type dust arrester can stop most of ash content, reduce the adverse effect of the ash content exchange thermal efficiency.

Description

Biomass fuel hot air stove
Technical field
The utility model is related to energy conversions, and in particular to biomass fuel hot air stove.
Background technology
Boiler is the equipment that the chemical energy of fuel is converted to thermal energy, usually requires to be passed through thereto in fuel combustion and help Combustion gas, the usually air containing oxygen.In order to make fuel fully burn as possible, it is usually passed through excessive air, but air After being largely passed through, the temperature of fuel can be caused to reduce, influence the burning of fuel on the other hand, influence the conversion of energy.But It will directly help to be passed into again in furnace chamber after gas heating and need a large amount of energy in this way, and improve cost, it is a kind of to solve the problems, such as this New biomass fuel hot air boiler is even more important.
Utility model content
The purpose of this utility model is to provide a kind of biomass fuel hot air stoves, solve fuel and low temperature in the prior art Help combustion gas mixing that fuel is made to be difficult to clean-burning problem.
In order to solve the above technical problems, the utility model uses following technical scheme:
A kind of biomass fuel hot air stove, including furnace chamber and the heat exchanger positioned at furnace chamber top are arranged on the furnace chamber There are fuel inlet and exhanst gas outlet, cold air inlet and heat outlet with air communication are provided on the heat exchanger, it is described Isocon is installed at exhanst gas outlet or heat outlet at least one, the isocon is connected to fuel inlet.
Biomass fuel hot air stove in the application is low to avoid combustion-supporting temperature from spending, and causes fuel that cannot fully burn, By heat extra in heat outlet and combustion gas mixing is helped, to improve the temperature of combustion-supporting gas, allows the fuel to fully burn.Tool Body is in use, pressure-regulating device can be installed at heat outlet, according to production needs, by the pressure adjusting at heat outlet To suitable value, remaining hot wind is passed through by isocon from fuel inlet, mixed with the new combustion-supporting gas of low temperature while being passed through It closes.
Pressure at heat outlet is just met for that production needs or the insufficient pressure of remaining hot gas is with by the temperature of combustion-supporting gas Degree is increased to designated value, can partial fume that smoke outlet leaves and low temperature be helped combustion gas mixing at this time, improved combustion-supporting The temperature of gas.
Since the combustion-supporting component contents such as oxygen in flue gas are less, so preferentially selecting the heat that will not be utilized at heat outlet Gas returns to furnace chamber and is continuing with, and when hot gas is it is impossible to meet needing, can just reuse flue gas.
Preferably, being enclosed with more than two gas circulation layers, the gas on the outside of the furnace chamber successively from inside to outside The layer that circulates includes exhaust gases passes and pre- hot gas path, and the exhaust gases passes are connected to exhanst gas outlet, and preheater channel enters with cold air Mouth connection.
As much as possible to improve the utilization rate of flue gas, using remaining flue gas after heat exchange to the gas in heat exchanger It is preheated.Exhaust gases passes and preheater channel are equivalent to cover and impinge upon on furnace chamber, and contact area is big, and heat exchange efficiency is high.
Preferably, the exhaust gases passes and pre- hot gas path at least one there are two more than, and exhaust gases passes and Pre- hot gas channel spacing setting, is interconnected between two neighboring exhaust gases passes or pre- hot gas path.
Theoretically, the time that flue gas and cold air flow in exhaust gases passes and preheater channel is longer, and heat exchange efficiency is got over Height, but the cost of equipment can also increase, it is possible to as needed, select the quantity of exhaust gases passes and pre- hot gas path.
Preferably, the pre- hot gas path there are two more than, leads between two gases circulation layer of furnace chamber Cross the heat exchanger connection.
Cold air preheating after enter heat exchanger in, carry out heat exchange after from most close to the gas of furnace chamber circulation layer in from It opens, can further heat at this time.
Preferably, being provided with type dust arrester in the furnace chamber, the type dust arrester includes that one end is fixed by elastic strip Dust-break net on furnace chamber inner wall.
Biomass fuel boiler and oil-burning gas-fired boiler are different, some ash contents are will produce in combustion process, to avoid these Ash content accumulates in the boiler, influences the heat exchange efficiency of boiler, needs to be fallen as possible in furnace cavity bottom, then from furnace cavity bottom Ash outlet leaves.
Dust-break Netcom crosses elastic strip and is connected on boiler inner wall, when dust-break falls the ash content of constant weight on the net, dust-break Side of the net far from elastic strip can tilt down, and grey branch thereon automatically falls off.
Preferably, the dust-break net and elastic strip radially tilt gradually downward from inside to outside along furnace chamber, the dust-break Percussion device is fixed on device, the percussion device includes impacting tube and can be hit along what furnace chamber radially slided in impacting tube Batting.
Due to the lighter in weight of ash content itself, and elastic strip deforms upon relatively soft, and ash content is slided on the net from dust-break The effect fallen may be bad, so impact bead is arranged on type dust arrester, impact bead is located at close to furnace chamber wall under normal circumstances Side, when ash content runs up to constant weight, dust-break net can move down, and impact bead can slide down under gravity Side far from furnace chamber wall, ash content slide under the action of shock, and the then online pressure reduction of dust-break can be moved up, be hit Batting can be slided into again close to the side of furnace chamber wall, self-return.
Elastic strip therein can make spring, can also be the sheet metal for having certain toughness, specifically also need to according in stove Temperature and the selection of boiler size.
Compared with prior art, the beneficial effects of the utility model are at least one of following:
Hot gas or flue gas are returned into burner hearth and re-use preheating therein, improves the efficiency of combustion of fuel.
Type dust arrester can stop most of ash content, reduce the adverse effect of the ash content exchange thermal efficiency.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model biomass fuel hot air stove.
Fig. 2 is the structural schematic diagram of the utility model type dust arrester.
Specific implementation mode
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain The utility model is not used to limit the utility model.
Embodiment 1:
A kind of biomass fuel hot air stove is present embodiments provided, as shown in Figure 1, including furnace chamber 1 and being located at 1 top of furnace chamber Heat exchanger 2, be provided with fuel inlet 3 and exhanst gas outlet 4 on the furnace chamber 1, be provided on the heat exchanger 2 and air Isocon is installed at the cold air inlet and heat outlet 5 of connection, the exhanst gas outlet 4 or heat outlet 5 at least one, it is described Isocon is connected to fuel inlet 3.
Biomass fuel hot air stove in the application is low to avoid combustion-supporting temperature from spending, and causes fuel that cannot fully burn, By heat extra in heat outlet 5 and combustion gas mixing is helped, to improve the temperature of combustion-supporting gas, allows the fuel to fully burn. When specifically used, pressure-regulating device can be installed at heat outlet 5, according to production needs, by the pressure at heat outlet 5 Adjust suitable value, remaining hot wind is passed through by isocon from fuel inlet 3, while being passed through with low temperature newly combustion-supporting Gas mixes.
Pressure at heat outlet 5 is just met for that production needs or the insufficient pressure of remaining hot gas is with by the temperature of combustion-supporting gas Degree is increased to designated value, at this time can improve the combustion gas mixing that helps of the partial fume left at exhanst gas outlet 4 and low temperature combustion-supporting The temperature of gas.
Since the combustion-supporting component contents such as oxygen in flue gas are less, so preferential selection will not utilize at heat outlet 5 Hot gas returns to furnace chamber 1 and is continuing with, and when hot gas is it is impossible to meet needing, can just reuse flue gas.
Embodiment 2:
The present embodiment further defines on the basis of embodiment 1:It wraps up successively from inside to outside in 1 outside of the furnace chamber There are two above gas circulation layer, the gas circulation layer includes exhaust gases passes 12 and pre- hot gas path 11, the exhaust gases passes 12 are connected to exhanst gas outlet 4, and preheater channel is connected to cold air inlet.
As much as possible to improve the utilization rate of flue gas, using remaining flue gas after heat exchange to the gas in heat exchanger 2 Body is preheated.Exhaust gases passes 12 and preheater channel are equivalent to cover and impinge upon on furnace chamber 1, and contact area is big, and heat exchange efficiency is high.
Embodiment 3:
The present embodiment further defines on the basis of embodiment 2:The exhaust gases passes 12 and pre- hot gas path 11 to There are one few there are two more than, and exhaust gases passes 12 and the setting of the interval of pre- hot gas path 11, two neighboring exhaust gases passes 12 or pre- It is interconnected between hot gas path 11.
Theoretically, the time that flue gas and cold air flow in exhaust gases passes 12 and preheater channel is longer, heat exchange efficiency It is higher, but the cost of equipment can also increase, it is possible to as needed, select the number of exhaust gases passes 12 and pre- hot gas path 11 Amount.
Embodiment 4:
The present embodiment further defines on the basis of embodiment 3:The pre- hot gas path 11 is there are two more than, most It is connected to by the heat exchanger 2 between two gases circulation layer of furnace chamber 1.
Cold air preheating after enter heat exchanger 2 in, carry out heat exchange after from most close to the gas of furnace chamber 1 circulation layer in from It opens, can further heat at this time.
Embodiment 5:
The present embodiment further defines on the basis of embodiment 1:Type dust arrester 7, institute are provided in the furnace chamber 1 It includes the dust-break net 72 that one end is fixed on by elastic strip 71 on 1 inner wall of furnace chamber to state type dust arrester 7, as shown in Figure 2.
Biomass fuel boiler and oil-burning gas-fired boiler are different, some ash contents are will produce in combustion process, to avoid these Ash content accumulates in the boiler, influences the heat exchange efficiency of boiler, needs to be fallen as possible in 1 bottom of furnace chamber, then from 1 bottom of furnace chamber Ash outlet leave.
Dust-break net 72 is connected to by elastic strip 71 on boiler inner wall, when the ash content for falling constant weight on dust-break net 72 When, side of the dust-break net 72 far from elastic strip 71 can tilt down, and grey branch thereon automatically falls off.
Embodiment 6:
The present embodiment further defines on the basis of embodiment 5:The dust-break net 72 and elastic strip 71 are along furnace chamber 1 It is radial to tilt gradually downward from inside to outside, percussion device 73 is fixed on the type dust arrester 7, the percussion device 73 includes hitting The impact bead 731 that hits cylinder and can be radially slided along furnace chamber 1 in impacting tube.
Due to the lighter in weight of ash content itself, and elastic strip 71 deforms upon relatively soft, and ash content is from dust-break net 72 The effect of upper landing may be bad, so impact bead 731 is arranged on type dust arrester 7, impact bead 731 is located at and leans under normal circumstances The side of 1 wall of nearly furnace chamber, when ash content runs up to constant weight, dust-break net 72 can move down, and impact bead 731 can be in the work of gravity Under, the side far from 1 wall of furnace chamber is slid down to, ash content slides under the action of shock, then the pressure on dust-break net 72 It reduces, can move up, impact bead 731 can be slided into again close to the side of 1 wall of furnace chamber, self-return.
Elastic strip 71 therein can make spring, can also be the sheet metal for having certain toughness, specifically also need to according to stove Interior temperature and the selection of boiler size.
Although reference be made herein to the utility model is described in multiple explanatory embodiments of the utility model, still, It should be understood that those skilled in the art can be designed that a lot of other modification and implementations, these modifications and implementations It will fall within scope and spirit disclosed in the present application.More specifically, it discloses in the application, drawings and claims In range, a variety of variations and modifications can be carried out to the building block and/or layout of theme combination layout.In addition to building block And/or outside the modification and improvement of layout progress, to those skilled in the art, other purposes also will be apparent.

Claims (6)

1. a kind of biomass fuel hot air stove, including furnace chamber(1)With positioned at furnace chamber(1)The heat exchanger on top(2), the furnace chamber (1)On be provided with fuel inlet(3)And exhanst gas outlet(4), the heat exchanger(2)On be provided with to enter with the cold air of air communication Mouthful(6)And heat outlet(5), it is characterised in that:The exhanst gas outlet(4)Or heat outlet(5)It is equipped at least one point Flow tube, the isocon and fuel inlet(3)Connection.
2. biomass fuel hot air stove according to claim 1, which is characterized in that the furnace chamber(1)Outside is from inside to outside It is enclosed with more than two gas circulation layers successively, the gas circulation layer includes exhaust gases passes(12)With pre- hot gas path(11), The exhaust gases passes(12)With exhanst gas outlet(4)Connection, preheater channel and cold air inlet(6)Connection.
3. biomass fuel hot air stove according to claim 2, which is characterized in that the exhaust gases passes(12)With pre- hot gas Channel(11)At least one is there are two more than, and exhaust gases passes(12)With pre- hot gas path(11)Interval setting, it is two neighboring Exhaust gases passes(12)Or pre- hot gas path(11)Between be interconnected.
4. biomass fuel hot air stove according to claim 3, which is characterized in that the pre- hot gas path(11)There are two More than, near furnace chamber(1)Two gases circulation layer between pass through the heat exchanger(2)Connection.
5. biomass fuel hot air stove according to claim 1, which is characterized in that the furnace chamber(1)Inside it is provided with dust-break Device(7), the type dust arrester(7)Including one end by elastic strip(71)It is fixed on furnace chamber(1)Dust-break net on inner wall(72).
6. biomass fuel hot air stove according to claim 5, which is characterized in that the dust-break net(72)And elastic strip (71)Along furnace chamber(1)It is radial to tilt gradually downward from inside to outside, the type dust arrester(7)On be fixed with percussion device(73), institute State percussion device(73)Including impacting tube and can be in impacting tube along furnace chamber(1)The impact bead radially slided(731).
CN201820400752.0U 2018-03-23 2018-03-23 Biomass fuel hot air stove Expired - Fee Related CN208059292U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820400752.0U CN208059292U (en) 2018-03-23 2018-03-23 Biomass fuel hot air stove

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820400752.0U CN208059292U (en) 2018-03-23 2018-03-23 Biomass fuel hot air stove

Publications (1)

Publication Number Publication Date
CN208059292U true CN208059292U (en) 2018-11-06

Family

ID=63988332

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820400752.0U Expired - Fee Related CN208059292U (en) 2018-03-23 2018-03-23 Biomass fuel hot air stove

Country Status (1)

Country Link
CN (1) CN208059292U (en)

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CF01 Termination of patent right due to non-payment of annual fee
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Granted publication date: 20181106

Termination date: 20200323