CN201463276U - Finned diaphragm wall condensation type vacuum boiler - Google Patents
Finned diaphragm wall condensation type vacuum boiler Download PDFInfo
- Publication number
- CN201463276U CN201463276U CN2009200927271U CN200920092727U CN201463276U CN 201463276 U CN201463276 U CN 201463276U CN 2009200927271 U CN2009200927271 U CN 2009200927271U CN 200920092727 U CN200920092727 U CN 200920092727U CN 201463276 U CN201463276 U CN 201463276U
- Authority
- CN
- China
- Prior art keywords
- boiler
- condenser
- heat exchanger
- finned
- water inlet
- Prior art date
Links
- 238000009833 condensation Methods 0.000 title abstract description 5
- 230000005494 condensation Effects 0.000 title abstract description 5
- 239000000779 smoke Substances 0.000 claims abstract description 13
- 239000011901 water Substances 0.000 claims description 23
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000005755 formation reactions Methods 0.000 claims 1
- 239000011257 shell materials Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 7
- 238000011084 recovery Methods 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 238000007254 oxidation reactions Methods 0.000 description 1
- YZCKVEUIGOORGS-IGMARMGPSA-N protium Chemical compound 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[1H] YZCKVEUIGOORGS-IGMARMGPSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substances Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
Abstract
A finned diaphragm wall condensation type vacuum boiler belongs to a boiler product. The technical scheme of the utility model is as follows: the utility model comprises a boiler body, a heat exchanger and a condenser, wherein the boiler body comprises a hearth formed by fins and pipes, a front smoke box rotary combustor and a vacuum hearth, hot medium water is arranged in the boiler body, the upper half of the vacuum hearth is provided with a heat exchange tube, the heat exchanger comprises a heat exchange tube, a container, a water inlet and a water outlet, the right part of the hearth is provided with the condenser, a finned tube group of which finned tubes are connected together in series are arranged in the condenser, the water inlet of the finned tube group is connected with a return pipe of the boiler, and the water outlet of the finned tube group is connected with the water inlet of the heat exchanger through pipes. The utility model has the advantages that the hearth formed by fins and pipes has large heating surface, the water capacity is small, the boiler can be started fast; the temperature of the front smoke box is low, the service life is long; and the temperature of the condenser is reduced, and the heat recovery efficiency is higher, thus reaching the aim of energy-saving and environmental protection.
Description
One, technical field: the utility model belongs to boiler product.
Two, technical background
Owing to contain protium in the natural gas, can produce about 1.55kg/m during burning
3Steam, its latent heat of vaporization is about 3600KJ/kg, accounts for about 10% of natural gas low heat valve.When exhaust gas temperature was higher, steam can not be condensed, and fell with fume emission, formed flue gas loss.The vacuum boiler that has the condensation function of recovering waste heat at present is provided with the smoke evacuation chamber at boiler tail usually, and the heat medium water in the pipeline of smoke evacuation chamber communicates with heat medium water in the body of heater vacuum chamber.Because boiler when work heat medium water temperature is more than 85 ℃, and the condensation temperature of flue gas causes most of flue gas that condensation can not take place between 55-65 ℃, energy-saving effect is bad.
Three, summary of the invention
The purpose of this utility model is that a kind of finned tube that adopts of design is main heated element and the vacuum boiler that significantly improves condenser efficiency.
The technical solution of the utility model is: this utility model is made up of body of heater, heat exchanger and condenser, wherein strile-back chamber, vacuum furnace chamber of the burner hearth, the front smoke box that are surrounded by fin and pipeline of oven body part formed, there is heat medium water its inside, dress heat exchanger tube in the vacuum furnace chamber first half, heat exchanger is made up of heat exchanger tube, collection case, water inlet and delivery port, the burner hearth right part is provided with condenser, be equipped with finned tube group connected in series in the condenser, finned tube group water inlet is linked the return pipe of boiler, and the delivery port of finned tube group is linked the water inlet of heat exchanger by pipeline.
The beneficial effects of the utility model: the furnace heating surface that fin and pipeline surround is big, and water capacity is little, and boiler startup is fast.The front smoke box temperature is low, long service life.Condenser temperature reduces, and energy recovery efficient is higher, reaches the purpose of energy-conserving and environment-protective.
Four, description of drawings
Accompanying drawing 1 is the utility model overall structure schematic diagram.
Accompanying drawing 2 is that A-A is to cross-sectional view.
Five, the specific embodiment
This utility model is by body of heater 1, heat exchanger 8 and condenser 6 are formed, body of heater 1 adopts seamless steel pipe 3 and fin 4 to surround the convection heating surface of center strile-back type burner hearth 1-1, seamless steel pipe 3 is inner to communicate with strile-back chamber 2 and vacuum furnace chamber 7 inside of front smoke box, it is inner for vacuum state and be marked with heat medium water 5. heat medium waters 5 and be high purity water, to the boiler No oxidation corrosion, contain small amounts of inorganic salt, make the boiler non-scaling. during burner 11 work, strile-back chamber 2 of front smoke box is water-cooled structure, forming passage by inside and outside two coaming plates is communicated with the upper and lower cavity of vacuum boiler, constitute the passage of heat medium water, front smoke box is cooled off, lower than plain cylindrical furnace temperature, thereby longer service life. the heat exchanger tube 8-1 of heat exchanger 8 is housed in vacuum furnace chamber 7 first halves, heat exchanger 8 is by heat exchanger tube 8-1, collection case 8-2, water inlet 8-3, delivery port 8-4 and cleaning cover plate 8-5 form. and wherein heat exchanger 8-1 is a straight tube, after the boiler heating, the heat of steam is by heat exchanger tube 8-1 output heat energy. and heat exchanger 8 two ends are provided with collection case 8-2, can open during maintenance, clear up with utensil heat exchanging device 8 surperficial dirts such as hairbrush. be equipped with finned tube group 6-1 connected in series in the condenser 6, its material adopts steel-aluminum composite fin tube or stainless steel finned tube, the water inlet 6-2 of finned tube group 6-1 links the return pipe 9-1 of boiler, the delivery port 6-3 of finned tube group 6-1 links the water inlet 8-3 of heat exchanger 8 by pipeline 9-2, make condenser 6 communicate with the recirculated water of heat exchanger 8 inside. can significantly reduce exhaust gas temperature during boiler work, and utilize smoke discharging residual heat heating recirculated water by heat exchanger 8. between the finned tube water inlet 6-2 of condenser 6 and the delivery port 6-3 valve 10 is arranged, its effect is identical with plain cylindrical furnace, no longer describe in detail herein. the utility model has the advantages that: the flue gas condensing waste heat recovery heating surface of forming by spiral fin coil, can increase 5-10 doubly with respect to the light pipe heat transfer area. increase the fin surface fluid turbulent, heat transfer coefficient improves 1-3 doubly. and vacuum furnace chamber system water capacity is little, boiler startup is fast. and the front smoke box temperature is low, long service life. condenser temperature reduces, energy recovery efficient is higher, reduce emission of harmful substances simultaneously, reached the purpose of energy-conserving and environment-protective.
Claims (3)
1. fin membranous wall condensing vacuum boiler, it is characterized in that: this utility model is by body of heater (1), heat exchanger (8) and condenser (6) are formed, the burner hearth (1-1) that surrounds by fin (4) and pipeline (3) of body of heater (1) wherein, the front smoke box chamber (2) of strile-bacing, vacuum furnace chamber (7) is formed, there is heat medium water (5) its inside, dress heat exchanger tube (8-1) in the vacuum furnace chamber first half, heat exchanger (8) is by heat exchanger tube (8-1), collection case (8-2), water inlet (8-3) and delivery port (8-4) are formed, burner hearth (1-1) right part is provided with condenser (6), be equipped with finned tube group (6-1) connected in series in the condenser (6), finned tube water inlet (6-2) is linked the return pipe (9-1) of boiler, and the delivery port of finned tube (6-3) is linked the water inlet (8-3) of heat exchanger by pipeline (9-2).
2. a kind of fin membranous wall condensing vacuum boiler according to claim 1 is characterized in that: between the finned tube water inlet (6-2) of condenser (6) and the delivery port (6-3) valve (10) is arranged.
3. a kind of fin membranous wall condensing vacuum boiler according to claim 1 is characterized in that: front smoke box strile-backs, and the formation passage is communicated with the upper and lower cavity of vacuum boiler between the inner and outer shell of chamber (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200927271U CN201463276U (en) | 2009-08-20 | 2009-08-20 | Finned diaphragm wall condensation type vacuum boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200927271U CN201463276U (en) | 2009-08-20 | 2009-08-20 | Finned diaphragm wall condensation type vacuum boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201463276U true CN201463276U (en) | 2010-05-12 |
Family
ID=42390627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200927271U CN201463276U (en) | 2009-08-20 | 2009-08-20 | Finned diaphragm wall condensation type vacuum boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201463276U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102419005A (en) * | 2011-12-23 | 2012-04-18 | 广州贝龙环保热力设备股份有限公司 | Vacuum hot-water boiler |
| CN102692077A (en) * | 2011-03-23 | 2012-09-26 | 庆东纳碧安株式会社 | Vacuum boiler |
| CN103245232A (en) * | 2012-02-07 | 2013-08-14 | 朱杰 | High-temperature flue gas waste heat thermal tube recovery system |
| CN104633636A (en) * | 2013-11-15 | 2015-05-20 | 安阳市方快锅炉有限公司 | Saturated steam combined boiler and quick steam manufacturing method |
| CN105004052A (en) * | 2015-08-22 | 2015-10-28 | 郑州大学 | Water tube type vacuum boiler with central reverse flames |
| CN106052113A (en) * | 2015-04-15 | 2016-10-26 | 博瑞特热能设备股份有限公司 | Symmetrical film wall type vacuum hot water boiler and heating method thereof |
-
2009
- 2009-08-20 CN CN2009200927271U patent/CN201463276U/en not_active IP Right Cessation
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102692077A (en) * | 2011-03-23 | 2012-09-26 | 庆东纳碧安株式会社 | Vacuum boiler |
| CN102419005A (en) * | 2011-12-23 | 2012-04-18 | 广州贝龙环保热力设备股份有限公司 | Vacuum hot-water boiler |
| CN103245232A (en) * | 2012-02-07 | 2013-08-14 | 朱杰 | High-temperature flue gas waste heat thermal tube recovery system |
| CN104633636A (en) * | 2013-11-15 | 2015-05-20 | 安阳市方快锅炉有限公司 | Saturated steam combined boiler and quick steam manufacturing method |
| CN106052113A (en) * | 2015-04-15 | 2016-10-26 | 博瑞特热能设备股份有限公司 | Symmetrical film wall type vacuum hot water boiler and heating method thereof |
| CN106052113B (en) * | 2015-04-15 | 2020-01-14 | 博瑞特热能设备股份有限公司 | Symmetric film wall type vacuum hot water boiler and heating method thereof |
| CN105004052A (en) * | 2015-08-22 | 2015-10-28 | 郑州大学 | Water tube type vacuum boiler with central reverse flames |
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