CN202938283U - Heat exchange device for biomass boiler - Google Patents
Heat exchange device for biomass boiler Download PDFInfo
- Publication number
- CN202938283U CN202938283U CN 201220568855 CN201220568855U CN202938283U CN 202938283 U CN202938283 U CN 202938283U CN 201220568855 CN201220568855 CN 201220568855 CN 201220568855 U CN201220568855 U CN 201220568855U CN 202938283 U CN202938283 U CN 202938283U
- Authority
- CN
- China
- Prior art keywords
- heat
- boiler
- heat exchange
- heat exchanger
- exchanger tube
- 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
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 15
- 238000009413 insulation Methods 0.000 claims description 12
- 239000004744 fabric Substances 0.000 claims description 8
- 239000011521 glass Substances 0.000 claims description 8
- 239000000741 silica gel Substances 0.000 claims description 4
- 229910002027 silica gel Inorganic materials 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 24
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 230000005540 biological transmission Effects 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 description 10
- 238000004378 air conditioning Methods 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 101700022107 ROBO3 Proteins 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- PZZOEXPDTYIBPI-UHFFFAOYSA-N 2-[[2-(4-hydroxyphenyl)ethylamino]methyl]-3,4-dihydro-2H-naphthalen-1-one Chemical compound C1=CC(O)=CC=C1CCNCC1C(=O)C2=CC=CC=C2CC1 PZZOEXPDTYIBPI-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
Abstract
The utility model discloses a heat exchange device for a biomass boiler. The heat exchange device comprises an inlet pipe, an outlet pipe and heat exchange pipes, wherein at least two heat exchange pipes are arranged inside the boiler; the inlet pipe and the outlet pipe respectively penetrate through the left side wall and the right side wall of the boiler; the heat exchange pipes are not mutually contacted; and an insulating sleeve is further arranged on the outlet pipe in a sleeving way. According to the heat exchange device provided by the utility model, the heat exchange contact surface of water in the heat exchange pipes and steam in the boiler can reach the maximum, so that the heat energy conversion rate of the boiler is improved; and the insulating sleeve is further arranged on the outlet pipe of the heat exchange device, so that excessive heat energy loss is avoided during the transmission of hot water.
Description
Technical field
The utility model relates generally to heat-exchanger rig, is specially a kind of heat-exchanger rig for biomass boiler.
Background technology
at present, biomass boiler generally adopts two kinds of mode of heatings, and one is the direct-type mode of heating, and namely the direct heated portion of boiler adopts the many backhaul designs of high-temperature flue gas, makes the heating surface area of boiler internal pipeline can reach maximum, two is the indirect type mode of heating, namely be provided with heat-exchanger rig at the boiler top, and with heat-exchanger rig and air-conditioning system, hot-water heating system directly is connected, and available technology adopting indirect type mode of heating, usually can be because of each pipeline compactness in heat-exchanger rig together, heating surface area is narrow, and cause the poor problem of heat transfer effect, and also exist heat-exchanger rig through after heat convection, owing to adopting iron pipe slowly to transmit, can cause the loss of heat in its process, wasted resource, when the hot water in boiler is applied to life by air-conditioning system and hot-water heating system again, adopt external heat exchanger tube, make heat energy loss large, and also need to increase an external plate and change water circulating pump, also caused certain electric energy loss.The utility model is called on and is being solved the problems of the technologies described above.
The utility model content
The purpose of this utility model is the problem of mentioning in the above-mentioned background technology in order to solve, and a kind of reasonable in design is provided, the heat-exchanger rig that is used for biomass boiler of good effect of heat exchange.
To achieve these goals, the technical solution of the utility model is as follows:
A kind of heat-exchanger rig for biomass boiler, comprise inlet tube, outlet and heat exchanger tube, described heat exchanger tube is arranged on described boiler internal, described inlet tube, outlet run through respectively described boiler left side wall, right side wall, described heat exchanger tube is provided with at least two, be not in contact with one another between described every heat exchanger tube, also be arranged with muff on described outlet.
Further, can adopt spiral plate-like or bending-like between described heat exchanger tube, in the utility model, heat exchanger tube is set to spiral plate-like or bending-like, makes water and the energy of the hydro-thermal in boiler convective exchange time lengthening in heat exchanger tube, has improved the boiler hot exchange efficiency.
Preferably, described heat exchanger tube diameter is the 16mm left and right, and the distance of 6mm left and right at least of being separated by between described every heat exchanger tube, this arranges the water not only improved in copper tube and the thermal energy exchange speed of boiler hot gas, has guaranteed that also the temperature of water in the heat-exchanger rig outlet satisfies air-conditioning system and the requirement of the domestic water number of degrees.
Further, described muff inner face is glass fabric, is insulation surface outside described muff.
Further, described insulation surface is the glass fabric that scribbles layer of silica gel.
Compared with prior art, the beneficial effects of the utility model are as follows:
1, the utility model heat-exchanger rig reasonable in design can make the heating surface area of heat exchanger tube reach maximum, has improved boiler steam thermal energy conversion efficiency.In the utility model by heat exchanger tube is arranged on boiler internal, and each heat exchange is not in contact with one another between changing, the steam in boiler can permeate in whole heat exchanger tube surrounding, make the interior water of heat exchanger tube and the steam in boiler that larger heat exchange contact area be arranged, improve widely the boiler hot exchange efficiency, thereby reduced the flue-gas temperature at boiler smoke outlet place.
2, in the utility model, the thermal losses of heat-exchanger rig outlet is lower, makes in transmitting procedure, avoids heat energy loss too much.In prior art, heat-exchanger rig outlet pipe end all adopts iron pipe to transmit slowly, without any Insulation, caused very large energy loss, be provided with muff in the utility model on the heat-exchanger rig outlet, this muff inner face adopts glass fabric, insulation surface is adopted in the outside, and insulation surface is the glass fabric that scribbles layer of silica gel, thereby the hot water in outlet has been taked Insulation effectively, has reduced the thermal losses in the outlet.
Description of drawings
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, during the below will describe embodiment, the accompanying drawing of required use is done to introduce simply, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is the structural representation of the present embodiment;
Reference numeral: 1-heat-exchanger rig, 2-heat exchanger tube, 3-inlet tube, 4-outlet, 5-boiler, 6-muff.
The specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, rather than whole embodiment.Based on the embodiment in the utility model, those of ordinary skills are not making the every other embodiment that obtains under the creative work prerequisite, all belong to the scope of the utility model protection.
In conjunction with Fig. 1, a kind of heat-exchanger rig for biomass boiler, comprise inlet tube 3, outlet 4 and heat exchanger tube 2, this heat exchanger tube 2 is arranged on boiler 5 inside, this inlet tube 3, outlet 4 run through respectively boiler 5 left side walls, right side wall, and in addition, heat exchanger tube 2 is provided with at least two, and be not in contact with one another between every heat exchanger tube 2, also be arranged with muff 6 on outlet 4.
In the present embodiment, the heat exchanger tube 2 in heat-exchanger rig 1 is arranged on boiler 5 inside, this heat exchanger tube 2 is provided with two at least, in actual the setting, can select according to the boiler drum space size radical of heat exchanger tube.In the present embodiment, be not in contact with one another between each heat exchanger tube 2, make water and the steam in boiler 5 in heat exchanger tube 2 that the heat exchange contact area of maximum be arranged, greatly improved boiler 5 rates of heat exchange, thereby reduced the flue-gas temperature at boiler 5 exhaust opening places.
In the present embodiment, be arranged with muff 6 on heat-exchanger rig 1 outlet 4, the hot water in 6 pairs of outlets of this muff 4 has been taked Insulation effectively, has reduced the loss in outlet 4.
In the present embodiment, can adopt spiral plate-like or bending-like between heat exchanger tube 2, the heat exchanger tube 2 of these two kinds of set-up modes, heat exchanger tube 2 is increased at the interior total length of boiler 5, thereby make water and the interior steam thermal convection current of boiler 5 in heat exchanger tube 2 extend swap time, the water of heat exchanger tube 2 can be heated more abundant.
In the present embodiment; heat exchanger tube 2 diameters are the 16mm left and right; and 6mm left and right at least is separated by between every heat exchanger tube 2; this arranges the water not only improved in heat exchanger tube 2 and the exchange heat speed in boiler 5 steam, can guarantee that also the temperature of water in heat-exchanger rig 1 outlet 4 can satisfy air-conditioning system and the requirement of domestic water water temperature in practical application.
In the present embodiment, outer sheathed muff 6 inner faces of outlet 4 are glass fabric, muff 6 outsides are insulation surface, further, insulation surface is the glass fabric that scribbles layer of silica gel, this muff 6 has solved hot water in transmitting procedure, because there is no Insulation, and causes the problem of energy loss.
Heat-exchanger rig of the present utility model, be used in biomass boiler, it can directly be connected with air-conditioning system, hot-water heating system, forms a closed system, reduced heat-exchanger rig and be arranged on the outside and thermal losses that causes of boiler, and saved that external plate changes water circulating pump and the electric energy loss that brings.
The heat-exchanger rig that the utility model provides, have advantages of that reasonable in design, pipeline heating surface area are large, it is by being arranged on boiler internal with heat exchanger tube, and each heat exchange is not in contact with one another between changing, and the steam in boiler can be permeated in whole heat exchanger tube surrounding, make the interior water of heat exchanger tube and the steam in boiler that larger heat exchange contact area be arranged, improved widely the boiler hot exchange efficiency, thereby reduced the flue-gas temperature at boiler smoke outlet place.
In addition, in the utility model the thermal losses of heat-exchanger rig outlet lower, make in transmitting procedure, avoid wasting too much heat energy.Solved the deficiency that prior art exists.
The above is only preferred embodiment of the present utility model, not in order to limiting the utility model, all any modifications of doing, is equal to replacement etc., within all should being included in protection domain of the present utility model in protection domain of the present utility model.
Claims (6)
1. heat-exchanger rig that is used for biomass boiler, comprise inlet tube, outlet and heat exchanger tube, it is characterized in that: described heat exchanger tube is arranged on described boiler internal, described inlet tube, outlet run through respectively described boiler left side wall, right side wall, described heat exchanger tube is provided with at least two, be not in contact with one another between described every heat exchanger tube, also be arranged with muff on described outlet.
2. a kind of heat-exchanger rig for biomass boiler according to claim 1, is characterized in that: can adopt spiral plate-like or bending-like between described heat exchanger tube.
3. a kind of heat-exchanger rig for biomass boiler according to claim 1 is characterized in that: described heat exchanger tube diameter is the 16mm left and right.
4. a kind of heat-exchanger rig for biomass boiler according to claim 3, is characterized in that: the distance of 6mm left and right at least of being separated by between described every heat exchanger tube.
5. a kind of heat-exchanger rig for biomass boiler according to claim 1, it is characterized in that: described muff inner face is glass fabric, described muff outside is insulation surface.
6. a kind of heat-exchanger rig for biomass boiler according to claim 5, it is characterized in that: described insulation surface is the glass fabric that scribbles layer of silica gel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220568855 CN202938283U (en) | 2012-10-31 | 2012-10-31 | Heat exchange device for biomass boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220568855 CN202938283U (en) | 2012-10-31 | 2012-10-31 | Heat exchange device for biomass boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202938283U true CN202938283U (en) | 2013-05-15 |
Family
ID=48322520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220568855 Expired - Fee Related CN202938283U (en) | 2012-10-31 | 2012-10-31 | Heat exchange device for biomass boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202938283U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104728955A (en) * | 2015-03-16 | 2015-06-24 | 王忠信 | Normal-pressure biomass gasified combustion horizontal water pipe steam boiler central air conditioner |
-
2012
- 2012-10-31 CN CN 201220568855 patent/CN202938283U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104728955A (en) * | 2015-03-16 | 2015-06-24 | 王忠信 | Normal-pressure biomass gasified combustion horizontal water pipe steam boiler central air conditioner |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130515 Termination date: 20211031 |