CN201764698U - Spraying condensation type gas water heater - Google Patents
Spraying condensation type gas water heater Download PDFInfo
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- CN201764698U CN201764698U CN2010202785916U CN201020278591U CN201764698U CN 201764698 U CN201764698 U CN 201764698U CN 2010202785916 U CN2010202785916 U CN 2010202785916U CN 201020278591 U CN201020278591 U CN 201020278591U CN 201764698 U CN201764698 U CN 201764698U
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- flue gas
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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
- 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]
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Abstract
The utility model relates to a spraying condensation type gas water heater comprising a gas-water separator (1), a heat exchange barrel (2), two spray nozzle components (3), a flue gas swirler (5), a burning cylinder bent pipe (6) and a full pre-mixed metal fiber burner (9). Gas and air are accurately pre-mixed and then burnt with a micro-flame after passing through the metal fiber; high-temperature flue gas goes upwards along the burning cylinder bent pipe (6) and then is sprayed into the heat exchange barrel (2) in a rotary way; the flue gas and mist water sprayed out from the spray nozzle components (3) exchange heat energy completely and then are discharged into atmosphere by the gas-water separator (1); and the sprayed mist water is heated and then enters a water collecting tank (8). The spraying condensation type gas water heater has the advantages as follows: 1. for the full pre-mixed metal fiber burner, the burning is full, the efficiency is high, the environment-friendly property is good, and the burning intensity is high, and the volume of a boiler is greatly reduced; 2. the flue gas swirler improves the efficiency of heat exchange between the flue gas and the mist water; 3. the centrifugal gas-water separator lowers the water mist escaping loss to the minimum; and 4. the two layers of spray nozzle components maximumly reduce the heat energy loss of the flue gas.
Description
Technical field
Technical solutions according to the invention belong to the water heater field, concretely, are to belong to the water-storage heater field that has around the water mantle of or several combustion chambers, according to International Patent Classification, belong to F24H1/24.
Background technology
Existing water-storage heater, as China's patent No. is 200920108310.x, it is a kind of immersion water heater, it is by burner, the burning cylindrical shell, end cover interlayer, the awl cap, heat exchanger tube, jet head sets, the impeller current divider, exhaust opening, dewater unit, bolt, water inlet pipe, outlet pipe, relief valve, burner hearth, the spraying part flow arrangement, Heat Room and water jacket are formed, described spraying part flow arrangement is discoid cylindrical shell, the upper end, middle part of discoid cylindrical shell communicates with water inlet pipe, spacing distance is provided with 4-12 and crosses water pipe on the side perisporium of discoid cylindrical shell, each is crossed and is connected to fog-spray nozzle on the water pipe, described dewater unit bottom is a funnelform funnel dish, the upper end-face edge of funnel dish is provided with ring-shaped baffle, and spacing distance is provided with shredded tobacco for water pipes and enters the hole on the ring-shaped baffle.Its weak point is: one, atmosphere direct combustion formula burner, and flame is long, has increased the volume of combustion barrel and boiler; Flame divides three parts, and outer light is the high-temperature region, can reach more than 1500 ℃, easily produces nitrogen oxide, and the internal layer anoxycausis easily produces carbon monoxide, and is unfavorable to discharging; It is little to regulate the large and small fire scope in addition, and poor stability influences efficiency of combustion.Two, flue gas mixes undesirable with the water smoke of spray.Three, Pen Lin insufficient strength, exhaust gas temperature is higher.Four, exhaust opening fog is bigger, and water smoke escape loss is bigger.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, has adopted a kind of full premix metallic fiber combustor, has set up flue gas cyclone, moisture trap, one deck shower nozzle.
The purpose of this utility model is achieved in that this spray condensing gas water-heating furnace mainly is made up of moisture trap, heat exchange bucket, nozzle component, waterproof awl cap, flue gas cyclone, combustion barrel bend pipe, header tank and full premix metallic fiber combustor etc.Full premix metallic fiber combustor and combustion barrel bend pipe are separately fixed at the interior outside of the same sidewall of header tank.Waterproof awl cap and flue gas cyclone are fixed on the upper end of combustion barrel bend pipe.Nozzle component is fixed on the heat exchange bucket by angle steel, which is provided with water inlet.The heat exchange bucket is by being bolted on the header tank, and moisture trap is fixed on the exhaust outlet of heat exchange bucket, is respectively equipped with outlet pipe and blow-off pipe on the header tank.
Nozzle component is two-layer by compositions such as nozzle, communicating pipe and spraying part flow arrangements.On the spraying part flow arrangement be housed 8~16 communicating pipe, nozzle is equipped with in the end of communicating pipe.The pressurization backwater that enters from water inlet through the spraying part flow arrangement, communicating pipe enter nozzle, be vaporific and spray in the heat exchange bucket, and become high-temperature-hot-water to fall into header tank after the high-temperature flue gas heat exchange.
Advantage of the present utility model: the one, adopted full premix metallic fiber combustor.This is present state-of-the-art gas burner system.Accurate metering and proportioning, mixing, the metallic fiber Cheng Weiyan burning of so closing permeation high temperature resistant are all passed through in whole air and combustion gas before the burning.Owing to be near ideal air-fuel ratio, so sufficient combustion, carbon monoxide is minimum and the flue gas loss is minimum.Owing to be little flame burning, there is not thermal extremes, so nitrogen oxide is few, environmental protection is good.The metallic fiber combustion can reach 2500kw/m around device combustion intensity height
2, can reduce to fire volume greatly around device, combustion barrel and boiler; The power output adjustable range is big, from 25%~100%, is particularly suitable for the automatic adjusting of heating according to need, saves the energy greatly.In addition, metal fiber burner also has heat shock resistance, lower resistance, safety no tempering, durable in use, and the life-span can reach 40 years.The 2nd, the burner exhanst gas outlet is provided with the flue gas cyclone, improves the efficient of flue gas and water smoke exchange heat.The 3rd, before exhaust opening, establish a centrifugal moisture trap, drop to the escape of water smoke loss minimum.The 4th, nozzle component is established two-layer, and flue gas is fully cooled off, and reduces the flue gas heat loss to greatest extent.The combination of above advantage can make boiler efficiency reach more than 98%.
Description of drawings
Fig. 1 is spray condensing gas water-heating furnace structural representation.
Fig. 2 is the nozzle component schematic diagram.
Fig. 3 is a flue gas cyclone schematic diagram.
Fig. 4 is the moisture trap schematic diagram.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further described.
Fig. 1 is spray condensing gas water-heating furnace structural representation.As can be seen from Figure 1, it is made up of moisture trap 1, heat exchange bucket 2, nozzle component 3, waterproof awl cap 4, flue gas cyclone 5, combustion barrel bend pipe 6, header tank 8 and full premix metallic fiber combustor 9 etc.Full premix metallic fiber combustor 9 and combustion barrel bend pipe 6 are separately fixed at the interior outside of header tank 8 same sidewalls.Waterproof awl cap 4 and flue gas cyclone 5 are fixed on the upper end of combustion barrel bend pipe 6.Two-layer nozzle component 3 links to each other by being communicated with main 19.Nozzle component 3 is fixed on the heat exchange bucket 2 by angle steel, which is provided with water inlet 12.Heat exchange bucket 2 is fixed on the header tank 8 by bolt 7, and moisture trap 1 is fixed on the exhaust outlet of heat exchange bucket 2, is respectively equipped with outlet pipe 11 and blow-off pipe 10 on the header tank 8.
The accurate metering of combustion gas ratio adjusting valve of combustion gas and the full premix metallic fiber combustor 9 of air process and proportioning, mixing, the metallic fiber Cheng Weiyan of permeation high temperature resistant burning then.High-temperature flue gas after the burning upwards sprays into heat exchange bucket 2 by 5 rotations of flue gas cyclone along combustion barrel bend pipe 6, and the abundant heat-shift of fog with nozzle component 3 ejections enters atmosphere through moisture trap 1.The fog of spray enters header tank 8 after the high-temperature flue gas heating, become high-temperature-hot-water, for bathing and heating.
Fig. 2 is the nozzle component schematic diagram.As can be seen from Figure 2, two-layer nozzle component 3 is formed by nozzle 13, communicating pipe 15 and spraying part flow arrangement 14.On the spraying part flow arrangement 14 be housed 8~16 communicating pipe 15, nozzle 13 is equipped with in the end of communicating pipe 15.The pressurization backwater that enters from water inlet 12 passes through spraying part flow arrangement 14, communicating pipe 15 enters nozzle 13, is vaporific and sprays in the heat exchange bucket 2, falls into header tank 8 with becoming high-temperature-hot-water after the high-temperature flue gas heat exchange.
Fig. 3 is a flue gas cyclone schematic diagram.Flue gas cyclone 5 is made up of annular bottom plate 16, upper cover plate 18 and swirl vane 17 etc.Annular bottom plate 16 joins with combustion barrel bend pipe 6, and high-temperature flue gas sprays along swirl vane 17 rotations through flue gas cyclone 5, enters the spray fog heat exchange of heat exchange bucket 2 and nozzle component 3.
Fig. 4 is the moisture trap schematic diagram.Moisture trap 1 is made up of rectifying ribs 20, retainer plate 21, centrifugal blower 22.Four rectifying ribs 20 are fixed on the retainer plate 21, and centrifugal blower 22 is fixed on the rectifying ribs 20.Flue gas quickens rotation through centrifugal blower 22, and the mist integument of carrying secretly is thrown to retainer plate 21 sidewalls and rectifying ribs 20, gathers into current and drops down, thereby realize gas-water separation, has reduced fog escape loss.
Claims (4)
1. one kind sprays the condensing gas water-heating furnace, it is characterized in that: it comprises moisture trap (1), heat exchange bucket (2), nozzle component (3), waterproof awl cap (4), flue gas cyclone (5), combustion barrel bend pipe (6), header tank (8) and full premix metallic fiber combustor (9), and full premix metallic fiber combustor (9) and combustion barrel bend pipe (6) are separately fixed at the interior outside of the same sidewall of header tank (8); Waterproof awl cap (4) and flue gas cyclone (5) are fixed on the upper end of combustion barrel bend pipe (6); Two-layer nozzle component (3) links to each other by being communicated with main (19); Nozzle component (3) is fixed on the heat exchange bucket (2) by angle steel, which is provided with water inlet (12); Heat exchange bucket (2) is fixed on the header tank (8) by bolt (7), and moisture trap (1) is fixed on the exhaust outlet of heat exchange bucket (2), is respectively equipped with outlet pipe (11) and blow-off pipe (10) on the header tank (8).
2. a kind of spray condensing gas water-heating furnace according to claim 1, it is characterized in that: described nozzle component (3) comprises two-layer nozzle component, every layer by nozzle (13), communicating pipe (15) and spraying part flow arrangement (14) composition; On the spraying part flow arrangement (14) be housed 8~16 communicating pipe (15), nozzle (13) is equipped with in the end of communicating pipe (15); The pressurization backwater that enters from water inlet (12) passes through spraying part flow arrangement (14), communicating pipe (15) enters nozzle (13), is vaporific and sprays in the heat exchange bucket (2), falls into header tank (8) with becoming high-temperature-hot-water after the high-temperature flue gas heat exchange.
3. a kind of spray condensing gas water-heating furnace according to claim 1 is characterized in that: described flue gas cyclone (5) comprises annular base plate (16), swirl vane (17) and upper cover plate (18); Annular base plate (16) is joined with combustion barrel bend pipe (6), and high-temperature flue gas sprays along swirl vane (17) rotation through flue gas cyclone (5), enters the spray fog heat exchange of heat exchange bucket (2) and nozzle component (3).
4. a kind of spray condensing gas water-heating furnace according to claim 1, it is characterized in that: described moisture trap (1) comprises rectifying ribs (20), retainer plate (21), centrifugal blower (22), four rectifying ribs (20) are fixed on the retainer plate (21), centrifugal blower (22) is fixed on the rectifying ribs (20), flue gas quickens rotation through centrifugal blower (22), and the mist integument of carrying secretly is thrown to retainer plate (21) sidewall and rectifying ribs (20).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202785916U CN201764698U (en) | 2010-08-02 | 2010-08-02 | Spraying condensation type gas water heater |
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CN2010202785916U CN201764698U (en) | 2010-08-02 | 2010-08-02 | Spraying condensation type gas water heater |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102788420A (en) * | 2011-05-18 | 2012-11-21 | 朱杰 | Condensing type gas and fuel oil hot water furnace capable of preheating air |
CN102913909A (en) * | 2012-11-07 | 2013-02-06 | 青海聚合热力有限责任公司 | Metal fiber post-mixing type burner and boiler employing same |
CN103697592A (en) * | 2013-11-29 | 2014-04-02 | 山西新聚星锅炉有限公司 | Condensing gas-fired boiler |
CN103776161A (en) * | 2012-10-22 | 2014-05-07 | 朱杰 | Spraying condensing and high temperature water source heat pump combined smoke waste heat recycling device |
CN104296380A (en) * | 2013-07-15 | 2015-01-21 | 北京恒盛春环保科技有限公司 | Combustion type heat supply system |
CN105588323A (en) * | 2016-02-24 | 2016-05-18 | 北京东方德泰科技有限公司 | Gas water heater |
CN107352609A (en) * | 2017-09-12 | 2017-11-17 | 哈尔滨锅炉厂环保工程技术有限公司 | A kind of evaporator for waste water evaporation |
CN108489083A (en) * | 2018-04-25 | 2018-09-04 | 大连恒通和科技有限公司 | Complete hot swirl penetrates formula water heater |
CN109915844A (en) * | 2018-12-21 | 2019-06-21 | 新疆博纳格材料科技有限公司 | A kind of atmosphere pollution energy conservation improvement utilization system |
-
2010
- 2010-08-02 CN CN2010202785916U patent/CN201764698U/en not_active Expired - Fee Related
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102788420A (en) * | 2011-05-18 | 2012-11-21 | 朱杰 | Condensing type gas and fuel oil hot water furnace capable of preheating air |
CN103776161B (en) * | 2012-10-22 | 2016-04-13 | 朱杰 | Spray condensation, heat pump of high-temp water source associating flue gas waste heat recovery apparatus |
CN103776161A (en) * | 2012-10-22 | 2014-05-07 | 朱杰 | Spraying condensing and high temperature water source heat pump combined smoke waste heat recycling device |
CN102913909B (en) * | 2012-11-07 | 2015-08-26 | 青海聚合热力有限责任公司 | Mixed burner and apply the boiler of this burner after a kind of metallic fiber |
CN102913909A (en) * | 2012-11-07 | 2013-02-06 | 青海聚合热力有限责任公司 | Metal fiber post-mixing type burner and boiler employing same |
CN104296380B (en) * | 2013-07-15 | 2017-05-17 | 北京恒盛春环保科技有限公司 | Combustion type heat supply system |
CN104296380A (en) * | 2013-07-15 | 2015-01-21 | 北京恒盛春环保科技有限公司 | Combustion type heat supply system |
CN103697592A (en) * | 2013-11-29 | 2014-04-02 | 山西新聚星锅炉有限公司 | Condensing gas-fired boiler |
CN105588323A (en) * | 2016-02-24 | 2016-05-18 | 北京东方德泰科技有限公司 | Gas water heater |
CN105588323B (en) * | 2016-02-24 | 2019-03-01 | 北京东方德泰科技有限公司 | Gas heater |
CN107352609A (en) * | 2017-09-12 | 2017-11-17 | 哈尔滨锅炉厂环保工程技术有限公司 | A kind of evaporator for waste water evaporation |
CN108489083A (en) * | 2018-04-25 | 2018-09-04 | 大连恒通和科技有限公司 | Complete hot swirl penetrates formula water heater |
CN108489083B (en) * | 2018-04-25 | 2023-10-13 | 李宏生 | Total heat jet type water heater |
CN109915844A (en) * | 2018-12-21 | 2019-06-21 | 新疆博纳格材料科技有限公司 | A kind of atmosphere pollution energy conservation improvement utilization system |
CN109915844B (en) * | 2018-12-21 | 2024-03-15 | 新疆博纳格材料科技有限公司 | Energy-conserving comprehensive utilization system that administers of atmosphere pollution |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110316 Termination date: 20130802 |