CN2758594Y - Heat exchange boiler of fuel oil gas phase converting to vacuum - Google Patents
Heat exchange boiler of fuel oil gas phase converting to vacuum Download PDFInfo
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- CN2758594Y CN2758594Y CN 200420114972 CN200420114972U CN2758594Y CN 2758594 Y CN2758594 Y CN 2758594Y CN 200420114972 CN200420114972 CN 200420114972 CN 200420114972 U CN200420114972 U CN 200420114972U CN 2758594 Y CN2758594 Y CN 2758594Y
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Abstract
The utility model relates to a heat exchange boiler capable of converting fuel oil gas phase into vacuum, which mainly comprises a boiler barrel, wherein the lower part of the boiler barrel is provided with a burning chamber one of which is provided with an opening and the wall is provided with a burner over against the burning chamber. The opening of the burning chamber is communicated with a return burning chamber which is communicated with a smoke vent opening by a group of convection smoke pipes. The burning chamber, the return burning chamber and the convection smoke pipes are made of heat transfer materials and are submerged in heating medium water. A vacuum chamber is arranged above the heat medium water, and a heat exchanger pipe which is arranged in the vacuum chamber is respectively communicated with a circulating hot water inlet and a circulating hot water outlet. The utility model has the advantages of complete burning and energy saving with the adoption of a return burning structure, and a machine group adopts a wet back type and a fire pipe structure; the inner part of the machine group is in a negative pressure state in the process of operation, the dangers of expansion, explosion and rupture do not exist, and the constant quantity of the heat medium water is kept so as to ensure the machine group not to have no danger of burning idly; the heating medium water in the boiler is pure water which is completely deoxidized, and the boiler is not corroded in an oxygen-free mode and is not scaled so that the service life of the boiler is extended by 2 to 3 times.
Description
Technical field
The utility model relates to a kind of vacuum hot water boiler, particularly a kind of fuel vapor phase transformation vacuum heat exchange boiler.
Background technology
Phase transformation vacuum heat exchange boiler is to utilize water under the different pressures state, and the principle that its evaporating temperature is also different comes water is heated; When being evacuated in the boiler, heat medium water (high-purity water adds corrosion inhibiter or certain density lithium bromide water solution) is heated to boiling under vacuum state, produce the saturated vapor under the relevant pressure, this steam is the flowing water in the heating tube in heat exchanger, the hot water of the uniform temperature that the generation user needs.The heat medium water of phase transformation vacuum heat exchange boiler is under vacuum state, and boiling, condensation in pot circulate at the pot inner sealing, and when normal operation, heat medium water does not have consume; Do not have level fluctuation yet, do not have the danger of dry combustion method; Heat medium water is a high-purity water, and non flouling behaviour in boiler does not pollute heating surface, thereby can not cause the heat decay that boiler produces; It is long that phase transformation vacuum heat exchange boiler has the efficient high life, pollutes characteristics such as few and safe in utilization.Present phase transformation vacuum heat exchange boiler unreasonable structure, fuel vapor be fully burning, and efficiency of combustion is low, causes energy waste.
Summary of the invention
The utility model will solve the shortcoming of above-mentioned prior art, and a kind of rational in infrastructure, fuel vapor phase transformation vacuum heat exchange boiler that energy utilization rate is high is provided.
The utility model solves the technical scheme that its technical problem adopts: this fuel vapor phase transformation vacuum heat exchange boiler, mainly comprise drum, and be equipped with the combustion chamber of an end opening in the bottom of drum, be provided with over against the burner at combustion chamber openings place at the drum wall; The opening of combustion chamber communicates with the chamber of strile-bacing, and this chamber of strile-bacing communicates with exhaust opening by one group of convection current smoke pipe; Combustion chamber, the chamber of strile-bacing, convection current smoke pipe are made by heat-transfer matcrial, and are dipped in the heat medium water; The heat medium water top is a vacuum chamber, and this vacuum chamber is built-in with Tube Sheet of Heat Exchanger, and Tube Sheet of Heat Exchanger is imported and exported with circulating hot water and communicated.
The effect that the utility model is useful is: 1) rational in infrastructure, adopt the structure of strile-bacing, and sufficient combustion is saved the energy; Unit adopts wetting back-type, the fire tube structure, and combustion heat energy is fully utilized.Unit inside is in negative pressure state, the danger of do not have expansion, explode, breaking when 2) moving; The heat medium water that keeps constant in the machine guarantees that unit does not have empty danger of burning; Machine is assembled with the maltilevel security protective device, guarantees that unit operation is safe and reliable.3) heat medium water in the stove, in the overall process of boiler operatiopn, do not advance, do not go out, do not increase, do not subtract, be enclosed in the vacuum chamber of unit, transmit heat between the heat-transfer pipe of unit and heat exchanger, the heat medium water in the stove is the pure water of complete deoxidation, oxygenless corrosion, scaling does not make boiler life prolong 2-3 doubly.4) heating of vacuum hot water unit, heat supply water all adopt its built-in heat exchanger, heat exchanger internal pressure and boiler body steel construction are isolated fully, body is not subjected to the influence of hydrostatic pressing, and skyscraper heating and water supply need not be considered decompressor, the directly heating of 20-30 layer building, heat supply water.5) unit can provide hot water respectively for purposes such as heating or health hot waters; Bathing pool, the warm water swimming pool can be established closed circuit.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: burner 1, combustion chamber 2, the chamber 3 of strile-bacing, convection current smoke pipe 4, Tube Sheet of Heat Exchanger 5, circulating hot water imports and exports 6, exhaust opening 7, drum 8, heat medium water 9.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
This fuel vapor phase transformation vacuum heat exchange boiler mainly comprises drum 8, is equipped with the combustion chamber 2 of an end opening in the bottom of drum 8, is provided with the burner 1 of 2 opening parts over against the combustion chamber at drum 8 walls; The opening of combustion chamber 2 communicates with the chamber 3 of strile-bacing, and this chamber 3 of strile-bacing communicates with exhaust opening 7 by one group of convection current smoke pipe 4; Convection current smoke pipe 4 is built-in with spoiler.Make by heat-transfer matcrial combustion chamber 2, the chamber 3 of strile-bacing, convection current smoke pipe 4, and be dipped in the heat medium water 9; Heat medium water 9 tops are vacuum chambers 10, and this vacuum chamber 10 is built-in with Tube Sheet of Heat Exchanger 5, and Tube Sheet of Heat Exchanger 5 is imported and exported 6 with circulating hot water and communicated.
When operation, will be evacuated in the drum 8.Fuel sprays into combustion chamber 2 burnings through burner 1, the high-temperature flue gas that produces carries out strong radiation heat release to combustion chamber 2 walls, 2 walls refluxed along the combustion chamber after high-temperature flue gas ran into combustion chamber 2 rear walls, flue gas further carries out radiation and heat convection to the combustion chamber in the reflux course, this is after opening enters the chamber 3 of strile-bacing by convection current smoke pipe 4 convection heat transfers, after exhaust opening 7 discharge out of the furnace.Through the backhaul burning, fuel can fully burn, and makes full use of heat energy.Heat medium water 9 in the drum 8 seethes with excitement under vacuum state after absorbing heat, produces the saturated vapor under the corresponding pressure, and this steam is to condense in Tube Sheet of Heat Exchanger 5, and heat is passed to the interior flowing water of pipe, thereby produces the hot water under the uniform temperature; After the steam after Tube Sheet of Heat Exchanger 5 heat exchange is condensed into liquid, fall, burned again device 1 is heated into steam.Whole boiling, condensation process all are to circulate at drum 8 inner sealings.
Claims (3)
1, a kind of fuel vapor phase transformation vacuum heat exchange boiler mainly comprises drum (8), it is characterized in that: be equipped with the combustion chamber (2) of an end opening in the bottom of drum (8), be provided with the burner (1) of (2) opening part over against the combustion chamber at drum (8) wall; The opening of combustion chamber (2) communicates with the chamber of strile-bacing (3), and this chamber of strile-bacing (3) communicates with exhaust opening (7) by one group of convection current smoke pipe (4); Combustion chamber (2), the chamber of strile-bacing (3), convection current smoke pipe (4) are made by heat-transfer matcrial, and are dipped in the heat medium water (9); Heat medium water (9) top is vacuum chamber (10), and this vacuum chamber (10) is built-in with Tube Sheet of Heat Exchanger (5), and Tube Sheet of Heat Exchanger (5) is imported and exported (6) with circulating hot water and communicated.
2, fuel vapor phase transformation vacuum heat exchange boiler according to claim 1, it is characterized in that: described convection current smoke pipe (4) is built-in with spoiler.
3, fuel vapor phase transformation vacuum heat exchange boiler according to claim 1, it is characterized in that: described convection current smoke pipe (4) is built-in with threaded steel pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420114972 CN2758594Y (en) | 2004-12-29 | 2004-12-29 | Heat exchange boiler of fuel oil gas phase converting to vacuum |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420114972 CN2758594Y (en) | 2004-12-29 | 2004-12-29 | Heat exchange boiler of fuel oil gas phase converting to vacuum |
Publications (1)
Publication Number | Publication Date |
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CN2758594Y true CN2758594Y (en) | 2006-02-15 |
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CN 200420114972 Expired - Fee Related CN2758594Y (en) | 2004-12-29 | 2004-12-29 | Heat exchange boiler of fuel oil gas phase converting to vacuum |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101832645A (en) * | 2010-05-20 | 2010-09-15 | 浙江上能锅炉有限公司 | Evaporation chamber of vacuum hot water boiler |
CN101126545B (en) * | 2006-08-18 | 2010-11-17 | 山西通能锅炉有限责任公司 | Vacuum boiler without exhauster |
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 |
CN102439375A (en) * | 2009-05-20 | 2012-05-02 | S.Tra.Te.G.I.E.有限公司 | Heat recovery apparatus |
CN102444980A (en) * | 2010-10-14 | 2012-05-09 | 陈铁刚 | Novel vacuum phase-change boiler |
CN105889887A (en) * | 2014-12-16 | 2016-08-24 | 赵联众 | Positive-pressure heat energy device |
-
2004
- 2004-12-29 CN CN 200420114972 patent/CN2758594Y/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101126545B (en) * | 2006-08-18 | 2010-11-17 | 山西通能锅炉有限责任公司 | Vacuum boiler without exhauster |
CN102439375A (en) * | 2009-05-20 | 2012-05-02 | S.Tra.Te.G.I.E.有限公司 | Heat recovery apparatus |
CN101832645A (en) * | 2010-05-20 | 2010-09-15 | 浙江上能锅炉有限公司 | Evaporation chamber of vacuum hot water boiler |
CN101832645B (en) * | 2010-05-20 | 2012-02-29 | 浙江上能锅炉有限公司 | Evaporation chamber of vacuum hot water boiler |
CN102444980A (en) * | 2010-10-14 | 2012-05-09 | 陈铁刚 | Novel vacuum phase-change 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 |
CN105889887A (en) * | 2014-12-16 | 2016-08-24 | 赵联众 | Positive-pressure heat energy device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee |
Owner name: ZHEJIANG TEFFU BOILER CO., LTD. Free format text: FORMER NAME: HANGZHOU SPECIAL BOILER FACTORY |
|
CP03 | Change of name, title or address |
Address after: 314423 No. 16 hang Hai Road, Haining hang Development Zone, Zhejiang, China Patentee after: Zhejiang Teffu Boiler Co., Ltd. Address before: 310020 No. 48, Xintang Road, Hangzhou, Zhejiang Patentee before: Hangzhou Special Boiler Factory |
|
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060215 Termination date: 20121229 |