CN201819239U - Composite tube air preheater - Google Patents
Composite tube air preheater Download PDFInfo
- Publication number
- CN201819239U CN201819239U CN2010205687652U CN201020568765U CN201819239U CN 201819239 U CN201819239 U CN 201819239U CN 2010205687652 U CN2010205687652 U CN 2010205687652U CN 201020568765 U CN201020568765 U CN 201020568765U CN 201819239 U CN201819239 U CN 201819239U
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- CN
- China
- Prior art keywords
- tube
- air
- silicon carbide
- preheating box
- pipe
- 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 - Lifetime
Links
- 239000002131 composite material Substances 0.000 title claims 9
- 229910010271 silicon carbide Inorganic materials 0.000 claims abstract description 66
- 238000002485 combustion reaction Methods 0.000 claims abstract description 50
- 229910052751 metal Inorganic materials 0.000 claims abstract description 38
- 239000002184 metal Substances 0.000 claims abstract description 38
- 239000000779 smoke Substances 0.000 claims abstract description 22
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims abstract 20
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 46
- 239000003546 flue gas Substances 0.000 claims description 46
- 229910000831 Steel Inorganic materials 0.000 claims description 11
- 239000010959 steel Substances 0.000 claims description 11
- 238000012423 maintenance Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 4
- 229910000680 Aluminized steel Inorganic materials 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 2
- 239000011819 refractory material Substances 0.000 claims description 2
- 239000000428 dust Substances 0.000 claims 2
- 238000005269 aluminizing Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000009825 accumulation Methods 0.000 abstract description 2
- 239000000446 fuel Substances 0.000 description 6
- 238000010276 construction Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000005338 heat storage Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 208000018875 hypoxemia Diseases 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Air Supply (AREA)
Abstract
The utility model relates to a heat exchange technology, in particular to a composited tube air preheater which is characterized in that a preheating box comprising silicon carbide pipes and containing air accumulation and dissipation serves as an air inlet end passageway for high temperature smoke; a metal pipe type preheating box body serves as an air outlet end passageway for the high temperature smoke; a high temperature smoke pipe and an adaptor connector are connected with a silicon carbide pipe preheated box body and a metal pipe type preheating box body in series so as to exhaust the cooled smoke out; the metal pipe type preheating box body serves as the air inlet end passageway of a burner combustion air, the preheat box body composed of the silicon carbide pipes serves as the air outlet end passageway of the combustion air, and the high temperature smoke pipe and the high temperature adaptor connector are connected with the silicon carbide pipe preheated box body and the metal pipe type preheating box body so as to exhaust the preheat combustion air out. The composited tube air preheater has the advantages that two independent preheat systems are adopted, namely, the high temperature passes through the silicon carbide pipe box body and then arrives at an aluminizing pipe box body, and the normal temperature combustion air firstly passes through the aluminizing pipe box body and then arrives at the silicon carbide pipe box body; in addition, the composited tube air preheater combines the advantages that the high preheat temperature of the combustion air for a heat accumulator preheater and the simple structure of a recuperative preheater.
Description
Technical field
The utility model relates to hot swapping, refers in particular to a kind of multiple tube air preheater.
Background technology
China's furnace type structure, technology and operational administrative are more backward, and the energy effective utilization degree is low, and the industrial furnace energy-saving potential is very huge.Reduce fuel consumption except that answer full production, improve the productivity of furnace as far as possible, also will reduce the accumulation of heat and the radiation loss of stove masonry, and the heat loss taken away of high-temperature flue gas etc.The industrial furnace that domestic enterprise generally uses accounts for the 30-60% that infeeds furnace heat because the flue-gas temperature of discharging in the stove reaches 600-1200 ℃, makes the interior reality of work thermal efficiency of stove low.Shortcomings such as part enterprise has utilized easy air preheater to reclaim this part heat in order to preheated air and coal gas, but pre-heat effect is poor, and service life is short are existing as follows with regard to the operating position of several frequently seen simple and easy air preheater:
The heat accumulating type preheater: be meant heat-transfer surface this as heat storage, the high-temperature flue gas preheating heat storage heat absorption of utilize discharging is afterwards again to the preheater of combustion air heat release; Advantage: regenerator temperature height.Shortcoming: production cost height, volume are big, complex structure; The coefficient of excess air instability; Need often to change heat storage, maintenance cost height; Recuperative airheater: be meant that flue gas continuously passes to heat the preheater of combustion air by solid walls; Advantage: simple in structure, easy to operate; Self-organizing system, irrelevant with other technical process; Shortcoming: be not suitable for large-scale burner hearth, service life is short; Gas-gas heat-transfer effect poor (preheated air temperature≤400 ℃).
Summary of the invention
The purpose of this utility model is improved and is innovated at the shortcoming that exists in the background technology and problem, and a kind of preheat temperature height is provided, long service life, pollute few, simple to operate, the multiple tube air preheater that cost is low.
The technical solution of the utility model is a kind of multiple tube air preheater of structure, and its characteristics comprise:
Form by carborundum tube and to hold the inlet end passage that the collecting and distributing preheating casing of air is made high-temperature flue gas, by metal pipe type preheating casing as high-temperature flue gas the outlet side passage, the flue gas discharge after will lower the temperature by high temperature smoke pipe and joint polyphone carborundum tube preheating casing and metal pipe type preheating casing again;
By the inlet end passage of metal pipe type preheating casing as the burner combustion air, the preheating casing of being made up of carborundum tube is as the outlet side passage of combustion air, by high temperature airduct and high temperature joint polyphone metal pipe type preheating casing and carborundum tube preheating casing with preheating after combustion air discharge;
Described carborundum tube preheating casing is set to two up and down, constitute the vertical data feedback channel of high-temperature flue gas, metal pipe type preheating casing is arranged on the vertical down going channel of adjacent high-temperature flue gas, and high-temperature flue gas passes through outside preheating casing pipe, and combustion air passes through in preheating casing pipe;
Described carborundum tube is horizontally set under the carborundum tube on the preheating casing and carborundum tube in the preheating casing, preheating casing one side is provided with the combustion air blast pipe on the carborundum tube, opposite side is provided with the combustion air discharge pipe, preheating casing one side is provided with the combustion air blast pipe under the carborundum tube, and opposite side is provided with the combustion air discharge pipe and is connected to burner.
Advantage of the present utility model and beneficial effect:
1, improves the theoretical temperature combustion of combustion air preheat temperature, raising fuel: the theoretical temperature combustion that can improve fuel after the air preheat.The raising degree of temperature is relevant with the preheat temperature of gas, and the general every raising of air preheating temperature can improve about 50 ℃ of theoretical temperature combustions for 100 ℃.
2, improve combustion air preheat temperature fuel savings: air themperature can be preheating to 800 ℃.Theoretical calculating: 100 ℃ of every raising air preheating temperatures, capable of saving fuel about 5%, be effective energy-conservation means, the investment payback time is short, and very high business efficiency is arranged.
3, improve efficiency of combustion: because volumetric expansion is accelerated gas flow rates, impel combustible to mix and strengthen after the air preheat, mixture is active to be increased, thereby can realize hypoxemia completing combustion and improve efficiency of combustion.
4, reduce the favourable protection environment of smoke discharge amount: along with the raising of environmental protection requirement; not only require to reduce the concentration of emission of SO2 and NOx in the flue gas; require the total release of flue gas also will reduce simultaneously, this is because a large amount of dischargings of CO2 will influence global air quality in the flue gas.Reclaiming fume afterheat can reduce the quantity delivered of fuel under the constant situation of total heat capacity, that is has reduced the growing amount and the discharge capacity of flue gas.The heat that reclaims is many more, and then smoke discharge amount is few more, and is just bigger to the meaning of environmental protection.
5, improve service life: the preheater shell inner lining refractory, high-temperature flue gas is not contacted with common iron, improve the service life of shell steel; The preheated air pipe adopts carborundum tube to combine with aluminizing pipe, thereby has avoided the stop of high temperature combustion air in aluminizing pipe of preheating.
The utility model multiple tube highly effective air preheater combines carborundum tube and aluminizing pipe, adopt two independently preheating systems, high-temperature flue gas arrives the aluminizing pipe casing earlier behind the carborundum tube casing, the normal temperature combustion air arrives the carborundum tube casing earlier behind the aluminizing pipe casing, combine the combustion air preheat temperature height of heat storage preheater, the advantage of simple structure of dividing wall type preheater.And adopt multinomial innovation structure to reach the foregoing invention purpose.
The utility model has following characteristics:
1, the carborundum tube air preheater is adopted in the high-temperature region:
A: carborundum has the better physical chemical property, can anti-1000 ℃ of high-temperature flue gas, NOx and dioxin and the corrosion of other harmful smokes;
B, thermal conductivity are strong, reach 1000 ℃ owing to enter the high-temperature flue gas of carborundum tube, and combustion air is through carborundum tube the time, and air preheating temperature can reach 800-1000 ℃.
C: cabinet shell adopts steel construction to combine with inner lining refractory, and steel construction does not contact with high temperature, improves service life; Simultaneously, cleaning door is installed, is convenient to the deashing and the maintenance of carborundum tube at sidepiece.
2, low-temperature space adopts the metal pipe type air preheater:
A: high-temperature flue gas is behind the carborundum tube preheater, and temperature is reduced to about 600 ℃, enters the metal tube air preheater.
B: in order to reduce the oxidation of common steel tube in flue gas, metal tube adopts aluminized steel tube, in the surperficial attached layer of aluminum matter of common steel tube, the service life of improving its metal tube;
C, cabinet shell adopt steel construction to combine with inner lining refractory, and steel construction does not contact with high temperature, improve service life; Simultaneously, cleaning door is installed, is convenient to the deashing and the maintenance of carborundum tube at sidepiece.
3, reduce exhaust gas temperature: 1000 ℃ high-temperature flue gas is through the carborundum tube preheater time, and flue-gas temperature is reduced to 500-600 ℃, and after through the metal tube air preheater, flue gas is reduced to 150-200 ℃, discharges through the general pipeline of discharging fume again;
4, improve combustion air temperature: the combustion air under the normal temperature is sent to the metal tube air preheater through blower fan, after the preheating for the first time of metal tube preheater, entering the carborundum tube regenerative air heater, through after the preheating of carbonized tube, the combustion air preheat temperature reaches 800-1000 ℃.
Description of drawings
Fig. 1 is the utility model front view.
Fig. 2 is Fig. 1 cutaway view.
Fig. 3 is Fig. 1 vertical view.
Fig. 4 is Fig. 1 right view.
The specific embodiment
By Fig. 1 to 4 as can be known, the utility model is made up of carborundum tube 8 and is held the inlet end passage that the collecting and distributing preheating casing of air is made high-temperature flue gas, by metal pipe type preheating casing 17 as high-temperature flue gas the outlet side passage, the flue gas discharge after will lower the temperature by high temperature smoke pipe and joint polyphone carborundum tube preheating casing and metal pipe type preheating casing 17 again;
By the inlet end passage of metal pipe type preheating casing 17 as the burner combustion air, the preheating casing of being made up of carborundum tube 8 is as the outlet side passage of combustion air, by high temperature airduct and high temperature joint polyphone metal pipe type preheating casing 17 and carborundum tube preheating casing with preheating after combustion air discharge;
Described carborundum tube preheating casing is set to two up and down, constitute the vertical data feedback channel of high-temperature flue gas, metal pipe type preheating casing is arranged on the vertical down going channel of adjacent high-temperature flue gas, and high-temperature flue gas passes through outside preheating casing pipe, and combustion air passes through in preheating casing pipe;
Described carborundum tube 8 is horizontally set under the carborundum tube on the preheating casing 2 and carborundum tube in the preheating casing 7, preheating casing 7 one sides are provided with combustion air blast pipe 16 on the carborundum tube, opposite side is provided with combustion air discharge pipe 6, preheating casing 2 one sides are provided with combustion air blast pipe 4 under the carborundum tube, and opposite side is provided with the combustion air discharge pipe and is connected to burner 23.
Preheating casing 2 bottoms connect the horizontal cigarette valve 22 of a high temperature by old name for the Arabian countries in the Middle East's ground round splce 1 under the carborundum tube described in the utility model, and following preheating casing 2 one sides are provided with deashing fire door 3.Preheating casing 7 tops connect horizontal high temperature smoke pipe 11 and high-temperature four-way smoke pipe 12 by the poly-tobacco pipe 9 in top on the described carborundum tube, and last preheating casing 7 one sides are provided with deashing fire door 3.The combustion air blast pipe 16 of preheating casing 7 one sides connects high temperature elbow 15, high temperature airduct 14, high temperature old name for the Arabian countries in the Middle East ground round splce 13 successively to the vertical down going channel of adjacent high temperature air on the described carborundum tube.Described metal tube hot type preheating casing 17 belows connect high-temperature flue gas and discharge three-way pipe 19 and combustion air air intake pipeline 20, and casing 17 is provided with deashing fire door 3.The top of described poly-tobacco pipe 9 is provided with the suspension arm 10 of maintenance usefulness, connects a cooling duct 21 on the horizontal high temperature smoke pipe 11.The shell of described carborundum tube preheating casing and metal pipe type preheating casing adopts steel construction, and inwall is lined with refractory material.The metal tube of described metal pipe type preheater adopts aluminized steel tube, in the attached layer of aluminum matter of steel tube surface.
The course of work of the present utility model and principle:
1, high-temperature flue gas is in that horizontal cigarette valve 22, the carborundum tube that enters in 2 pairs of casings of carborundum lower box after through old name for the Arabian countries in the Middle East's ground circle 1 carry out the preheating first time from high temperature, make flue-gas temperature drop to 800 ℃ from initial 1100 ℃, enter carborundum tube upper box 7 then, carborundum in the carborundum upper box 7 is carried out the preheating second time, flue-gas temperature is dropped to about 500-600 ℃ from 800 ℃.
2,500-600 ℃ middle temperature flue gas is behind process carborundum tube casing, by the poly-tobacco pipe 9 in top, horizontal high temperature smoke pipe 11 and high-temperature four-way smoke pipe 12 enter metal pipe type preheater 17, at this moment, because the decline of flue-gas temperature, dustiness reduces in the flue gas, thereby reduce the damage of metal tube preheater 17 is also corresponding, flue gas is behind process metal pipe type preheater 17, and flue-gas temperature is reduced to 200 ℃, discharge through smoke evacuation threeway 19 again, reduced the pollution of flue gas environment.
3, combustion air is by blower fan elder generation process metal pipe type air preheater 17, after air themperature brought up to 300 ℃ by normal temperature, by high temperature old name for the Arabian countries in the Middle East ground circle 13, high temperature airduct 14, high temperature elbow 15 and high temperature airduct 16 enter the carborundum tube upper box, conduct heat to combustion air by casing carbonized tube 8, combustion air temperature is brought up to about 600 ℃, arrive the carborundum lower box through high temperature opposite sex reducing head 5 with high temperature elbow 6 again, combustion air is after through the carborundum in the lower box, air themperature is brought up to 800-1000 ℃ rapidly, after the high temperature airduct is delivered in the burner combustion-supporting.
4, the preheated air pipe of cleaning for convenience and maintenance preheater inside has all been installed deashing fire door 3 on each casing, under normal circumstances is in sealing state, simple and easy suspension arm 10 has been installed simultaneously, the high temperature smoke pipe on top for convenience detach.
Embodiment described in the utility model only is the description that preferred implementation of the present utility model is carried out; be not that the utility model design and scope are limited; under the prerequisite that does not break away from the utility model design philosophy; engineers and technicians make the technical solution of the utility model in this area various modification and improvement; all should fall into protection domain of the present utility model; the technology contents that the utility model is asked for protection all is documented in claims.
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205687652U CN201819239U (en) | 2010-10-20 | 2010-10-20 | Composite tube air preheater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205687652U CN201819239U (en) | 2010-10-20 | 2010-10-20 | Composite tube air preheater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201819239U true CN201819239U (en) | 2011-05-04 |
Family
ID=43917191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205687652U Expired - Lifetime CN201819239U (en) | 2010-10-20 | 2010-10-20 | Composite tube air preheater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201819239U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101956995A (en) * | 2010-10-20 | 2011-01-26 | 岳阳市巴陵节能炉窑工程有限公司 | Composite tube air preheater |
| CN103267302A (en) * | 2013-06-17 | 2013-08-28 | 广西志远节能环保设备有限公司 | Air preheater for boiler |
| CN110822951A (en) * | 2019-11-26 | 2020-02-21 | 哈尔滨锅炉厂有限责任公司 | Novel tubular preheater of biomass boiler and preheating method |
-
2010
- 2010-10-20 CN CN2010205687652U patent/CN201819239U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101956995A (en) * | 2010-10-20 | 2011-01-26 | 岳阳市巴陵节能炉窑工程有限公司 | Composite tube air preheater |
| CN101956995B (en) * | 2010-10-20 | 2011-12-21 | 岳阳市巴陵节能炉窑工程有限公司 | Composite tube air preheater |
| CN103267302A (en) * | 2013-06-17 | 2013-08-28 | 广西志远节能环保设备有限公司 | Air preheater for boiler |
| CN103267302B (en) * | 2013-06-17 | 2016-03-23 | 广西志远节能环保设备有限公司 | Boiler air preheater |
| CN110822951A (en) * | 2019-11-26 | 2020-02-21 | 哈尔滨锅炉厂有限责任公司 | Novel tubular preheater of biomass boiler and preheating method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110504 Effective date of abandoning: 20111221 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20110504 Effective date of abandoning: 20111221 |