CN204987902U - Glass melting furnace exhaust -heat boiler's heat transfer structure - Google Patents
Glass melting furnace exhaust -heat boiler's heat transfer structure Download PDFInfo
- Publication number
- CN204987902U CN204987902U CN201520630880.0U CN201520630880U CN204987902U CN 204987902 U CN204987902 U CN 204987902U CN 201520630880 U CN201520630880 U CN 201520630880U CN 204987902 U CN204987902 U CN 204987902U
- Authority
- CN
- China
- Prior art keywords
- air
- intake duct
- escape pipe
- air intake
- group
- 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.)
- Active
Links
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model relates to a glass melting furnace exhaust -heat boiler low temperature flue gas (the flue -gas temperature is less than 180 DEG C ) utilizes field, concretely relates to glass melting furnace exhaust -heat boiler's heat transfer structure. Setting up the air intake duct group that is the longitudinal distribution in the casing and the air nest of tubes of giving vent to anger including casing and level, being equipped with air intake duct group air inlet, the air nest of tubes gas outlet of giving vent to anger on the casing lateral wall, the casing top is equipped with the flue gas entry, and the lower part is equipped with the exhanst gas outlet, air give vent to anger nest of tubes gas outlet and glass melting furnace intercommunication, and air intake duct group gives vent to anger end and air and gives vent to anger nest of tubes inlet end and feed through. Regard the air as the heat transferring medium, utilize the air heater of ordinary pressure to ban traditional high -pressure deoxidization evaporimeter, can not cause equipment to stop transport when the pipeline is corroded by the low temperature flue gas, eliminated exhaust -heat boiler's potential safety hazard.
Description
Technical field
The utility model relates to utilizing waste heat of glass furnace boiler low-temperature fume (flue-gas temperature is lower than 180 DEG C) and utilizes field, is specifically related to the heat exchange structure of utilizing waste heat of glass furnace boiler.
Background technology
In Improving Glass Manufacturing Processes, melting furnaces consume a large amount of fuel in melt raw material, produce a large amount of complicated component, be with mordant high-temperature flue gas, and heat energy adopts waste heat boiler to carry out UTILIZATION OF VESIDUAL HEAT IN usually.At the position that waste heat boiler low-temperature flue gas passes through, usual at present take water as heat transferring medium, adopts except oxygen evaporator is heat transmission equipment, utilizes the waste-heat boiler feedwater of flue gas, recycles fume afterheat.Except oxygen evaporator makes the part of pressure vessel, have a set of strict control system from the design of heat transmission equipment, Material selec-tion, manufacture, installation, require tight, the device fabrication cycle is long, cost is high.Due to glass production raw material and fuel complicated and changeable, the smoke components produced is complicated, high-temperature flue gas is after residual heat boiler for exchanging heat to low-temperature flue gas, in deoxygenation evaporator heat exchange region, flue-gas temperature may be upper and lower at the dew point of corrosive gas, very easily corrosion is caused to deoxygenation evaporator heat exchange equipment pipe, cause the leakage of heat transferring medium water, cause waste heat boiler to run continuously.Because of the continuity that glass furnace is produced, the problems such as waste heat boiler is stopped transport will cause that waste heat cannot reclaim, energy waste, recycling efficiency are low.In addition, after waste heat boiler is stopped transport, follow-up flue gas cannot carry out denitration, desulfurization, dust removal process, and flue gas can not qualified discharge, causes the pollution to air.Except oxygen evaporator is as a part for waste heat boiler, be all the part of pressure vessel, its corrosion is a great potential safety hazard, is a potential safety hazard source, and security risk is large, and equipment control difficulty is large.
Utility model content
For solving the problems of the technologies described above, the utility model provides a kind of heat exchange structure of safe, energy-conservation, free of contamination utilizing waste heat of glass furnace boiler.
Technical solutions of the utility model are: a kind of heat exchange structure of utilizing waste heat of glass furnace boiler, the air intake duct group comprising housing and be horizontally placed in genesis analysis in housing and air escape pipe group, described housing sidewall is provided with air intake duct group air inlet with air intake duct group correspondence position, air escape pipe group gas outlet is provided with air escape pipe group correspondence position, described case top is provided with smoke inlet, bottom is provided with exhanst gas outlet, described air escape pipe group gas outlet is communicated with glass melter, described air intake duct group outlet side is communicated with air escape pipe group inlet end.
Further, described air intake duct group and air escape pipe group include and to be vertically set in parallel in housing and the plate-shaped carrier that is fixedly connected with inner walls of periphery and lamination are fixed on Multi-row pipeline between plate-shaped carrier, every row pipeline comprises many tubules of horizontal homogeneous distribution, described plate-shaped carrier plate face is provided with the aperture be connected with tubule, gap is provided with between described tubule and tubule, described smoke inlet is communicated with by this gap with between exhanst gas outlet, forms flue gas heat exchange passage.
Further, the plate-shaped carrier of described air intake duct group outlet side and the plate-shaped carrier of air escape pipe group inlet end are positioned at housing homonymy, and and be provided with cavity between inner walls, this cavity forms the air channel that in air intake duct group and air escape pipe group, gas flows.
Further, blower fan is connected with between described air escape pipe group gas outlet and glass melter.
Further, described air intake duct group is positioned at below air escape pipe group.
The beneficial effects of the utility model: using air as heat transferring medium, the air preheater of normal pressure is utilized to ban traditional high pressure except oxygen evaporator, and by the pipeline of the only tubule of many merchandisers as transport heat transferring medium, even if some tubules are corroded by low-temperature flue gas, also the flowing of other thin inner air tube can not be affected, therefore equipment can not be caused to stop transport, eliminate the potential safety hazard of waste heat boiler.Air intake duct group and air escape pipe group are made up of many tubules, large with the contact area of low-temperature flue gas, good effect of heat exchange; It is combustion-supporting that air sends glass melter back to after the heat absorbing low-temperature flue gas, reduces the loss of fuel, economize energy.Adopt the waste heat boiler cycle of operation of this heat transmission equipment long, waste heat recovery efficiency is high, heat transmission equipment less investment, good in economic efficiency.Desulphurization and denitration, the cleaner of follow-up flue gas are stable, and flue gas qualified discharge, environmental benefit is obvious.
Accompanying drawing explanation
Fig. 1 is the utility model front view;
Fig. 2 is the utility model top view;
Fig. 3 is air intake duct group (air escape pipe group) front view;
Fig. 4 is air intake duct group (air escape pipe group) top view;
In figure: 1-housing, 2-tubule, 3-air intake duct group air inlet, 4-air escape pipe group gas outlet, 5-smoke inlet, 6-exhanst gas outlet, 7-flue gas heat exchange passage, 8-air channel, 9-plate-shaped carrier.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
As illustrated in fig. 1 and 2, the utility model comprises housing 1, housing 1 top is provided with smoke inlet 5, bottom is provided with exhanst gas outlet 6, side wall upper part is provided with air intake duct group air inlet 3 and air escape pipe group gas outlet 4, air escape pipe group gas outlet 4 is positioned at above sidewall, and air intake duct group air inlet 3 is positioned at below sidewall.Be provided with air intake duct group with air intake duct group air inlet 3 correspondence position in housing 1, be provided with air escape pipe group with air escape pipe group gas outlet 4 correspondence position, air intake duct group is identical with air escape pipe group structure.
Be air intake duct group (air escape pipe group) structural representation as shown in Figures 3 and 4, air intake duct group (air escape pipe group) includes and to be vertically set in parallel in housing 1 and three pieces of plate-shaped carrier 9 being fixedly connected with housing 1 inwall of periphery and lamination are fixed on Multi-row pipeline between plate-shaped carrier 9, every row pipeline comprises the many tubules 2 of horizontal homogeneous distribution, and tubule 2 is welded and fixed with the plate-shaped carrier 9 at two ends through middle plate-shaped carrier 9.The plate face of plate-shaped carrier 9 is provided with the aperture be connected with tubule 2, air escape pipe group is arranged at above air intake duct group, be provided with gap between their tubule and tubule, be communicated with by this gap between smoke inlet 5 with exhanst gas outlet 6, form flue gas heat exchange passage 7.
The plate-shaped carrier of air intake duct group inlet end is corresponding with air intake duct group air inlet 3, and air intake duct group air inlet 3 is connected with air; The plate-shaped carrier of air escape pipe group outlet side is corresponding with air escape pipe group gas outlet 4, and air escape pipe group gas outlet 4 is communicated with glass melter by blower fan.The plate-shaped carrier of air intake duct group outlet side and the plate-shaped carrier of air escape pipe group inlet end are positioned at housing 1 homonymy, and and be provided with cavity between inner walls, this cavity forms the air channel 8 that in air intake duct group and air escape pipe group, gas flows, and the air in air intake duct group enters in air escape pipe group through this air channel.
It is inner that the low-temperature flue gas that glass melter produces enters housing 1 by smoke inlet 5, and the low-temperature flue gas after heat exchange is discharged through exhanst gas outlet 6 by flue gas heat exchange passage 7; And air enters in the tubule 2 of air intake duct group inside through air intake duct group air inlet 3, extract out from air escape pipe group gas outlet 4 through blower fan after absorbing the heat of flue gas, and deliver in glass melter combustion-supporting.The waste heat boiler that both can prevent from aqueous medium from leaking causing is stopped transport, economize energy again, and when tubule 2 and housing 1 inwall all can adopt enamel material as coating, can also play the effect preventing corrosion, and waste heat boiler can better be run.
The above; be only detailed description of the invention of the present utility model, it should be pointed out that any those of ordinary skill in the art are in the technical scope disclosed by the utility model; the change that can expect easily or replacement, all should be encompassed within protection domain of the present utility model.
Claims (5)
1. the heat exchange structure of a utilizing waste heat of glass furnace boiler, it is characterized in that: comprise housing (1) and the air intake duct group that is horizontally placed in genesis analysis in housing (1) and air escape pipe group, described housing (1) sidewall is provided with air intake duct group air inlet (3) with air intake duct group correspondence position, air escape pipe group gas outlet (4) is provided with air escape pipe group correspondence position, described housing (1) top is provided with smoke inlet (5), bottom is provided with exhanst gas outlet (6), described air escape pipe group gas outlet (4) is communicated with glass melter, described air intake duct group outlet side is communicated with air escape pipe group inlet end.
2. the heat exchange structure of utilizing waste heat of glass furnace boiler as claimed in claim 1, it is characterized in that: described air intake duct group and air escape pipe group include and to be vertically set in parallel in housing (1) and the plate-shaped carrier (9) that is fixedly connected with housing (1) inwall of periphery and lamination are fixed on Multi-row pipeline between plate-shaped carrier (9), every row pipeline comprises the many tubules (2) of horizontal homogeneous distribution, described plate-shaped carrier (9) plate face is provided with the aperture be connected with tubule (2), gap is provided with between described tubule (2) and tubule (2), be communicated with by this gap between described smoke inlet (5) with exhanst gas outlet (6), form flue gas heat exchange passage (7).
3. the heat exchange structure of utilizing waste heat of glass furnace boiler as claimed in claim 2, it is characterized in that: the plate-shaped carrier (9) of described air intake duct group outlet side and the plate-shaped carrier (9) of air escape pipe group inlet end are positioned at housing (1) homonymy, and and be provided with cavity between housing (1) inwall, this cavity forms the air channel (8) that in air intake duct group and air escape pipe group, gas flows.
4. the heat exchange structure of utilizing waste heat of glass furnace boiler as claimed in claim 1, is characterized in that: be connected with blower fan between described air escape pipe group gas outlet (4) and glass melter.
5. the heat exchange structure of utilizing waste heat of glass furnace boiler as claimed in claim 1, is characterized in that: described air intake duct group is positioned at below air escape pipe group.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520630880.0U CN204987902U (en) | 2015-08-20 | 2015-08-20 | Glass melting furnace exhaust -heat boiler's heat transfer structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520630880.0U CN204987902U (en) | 2015-08-20 | 2015-08-20 | Glass melting furnace exhaust -heat boiler's heat transfer structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204987902U true CN204987902U (en) | 2016-01-20 |
Family
ID=55122263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520630880.0U Active CN204987902U (en) | 2015-08-20 | 2015-08-20 | Glass melting furnace exhaust -heat boiler's heat transfer structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204987902U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108507363A (en) * | 2018-04-12 | 2018-09-07 | 深圳市凯盛科技工程有限公司 | A kind of glass furnace flue gas cool-down heat-exchanger rig |
-
2015
- 2015-08-20 CN CN201520630880.0U patent/CN204987902U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108507363A (en) * | 2018-04-12 | 2018-09-07 | 深圳市凯盛科技工程有限公司 | A kind of glass furnace flue gas cool-down heat-exchanger rig |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102407070B (en) | Composite equipment for flue gas waste heat recovery and dust cleaning | |
| CN106247371B (en) | A kind of coal steam-electric plant smoke comprehensive waste-heat utilizing device | |
| CN104006401A (en) | Power station boiler smoke waste heat deep recycling and emission reducing system | |
| CN104633647A (en) | Emission reduction and energy saving system capable of omitting GGH | |
| CN203011206U (en) | Device capable of preheating water by adopting tail gas of boiler | |
| CN202813337U (en) | Two-stage closed circulating boiler flue gas waste heat utilization system | |
| CN105020734A (en) | Method and device for recycling smoke waste heat | |
| CN204987902U (en) | Glass melting furnace exhaust -heat boiler's heat transfer structure | |
| CN203223926U (en) | Heat energy recycle and purification device of boiler flue | |
| CN210688301U (en) | Novel flue gas recirculation system | |
| CN202692019U (en) | Flue gas waste heat recycling system of steam boiler | |
| CN201819192U (en) | Two-stage serial-parallel boiler tail heat exchanger | |
| CN204665224U (en) | A kind of Water pipe heating pipe afterheat boiler system be built on sintering machine flue | |
| CN208632455U (en) | A kind of energy-saving type coke oven flue residual neat recovering system | |
| CN201973698U (en) | Flue gas waste heat recovery device | |
| CN205482504U (en) | But fluoroplastics tubular heat exchanger structure that level was placed | |
| CN201636832U (en) | Exhaust heat boiler of electric steelmaking furnace | |
| CN204345689U (en) | Shunting string sheet flue gas waste heat recoverer in efficient | |
| CN205656099U (en) | A experimental system for testing flue gas low temperature corrosion | |
| CN204901732U (en) | Modular waste heat of boiler flue gas recovery system | |
| CN104315872B (en) | Boiler flue gas waste heat recycling and energy-saving device with boiler flue gas dust removing effect | |
| CN104832899B (en) | A kind of Water pipe heating pipe afterheat boiler system being built on sintering machine flue | |
| CN208832496U (en) | A kind of ventilation air methane oxidation device low-temperature flue gas waste heat utilizes system | |
| CN203869074U (en) | Device for recovering waste heat of gas boiler | |
| CN208124918U (en) | A kind of spare heat-exchange system of waste heat boiler of glass furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160513 Address after: 430000 Hubei Province, Wuhan City Economic Development Zone Hannan glass deep processing glass processing center joint workshop of the 1-3 layer (1). Patentee after: Wuhan Changli New Material Technology Co., Ltd. Address before: 485 No. 430090 Hubei city of Wuhan province Wuhan Hannan Hannan Road Patentee before: Wuhan Changli Glass (Hannan) Co., Ltd. |