CN201072138Y - Novel boiler air preheater - Google Patents
Novel boiler air preheater Download PDFInfo
- Publication number
- CN201072138Y CN201072138Y CNU2007201286444U CN200720128644U CN201072138Y CN 201072138 Y CN201072138 Y CN 201072138Y CN U2007201286444 U CNU2007201286444 U CN U2007201286444U CN 200720128644 U CN200720128644 U CN 200720128644U CN 201072138 Y CN201072138 Y CN 201072138Y
- Authority
- CN
- China
- Prior art keywords
- air
- valve
- heat exchanger
- pipelines
- smoke exhaust
- 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 - Fee Related
Links
- 239000000779 smoke Substances 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000003546 flue gas Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 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
- 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
Landscapes
- Air Supply (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及锅炉的附属设备,确切地说是锅炉的空气预热器。The utility model relates to auxiliary equipment of a boiler, in particular to an air preheater of the boiler.
背景技术 Background technique
目前的锅炉空气预热器主要有管式空气预热器与回转式空气预热器两种,对于提高锅炉效率有着重要作用,其中管式空气预热器面临的主要问题是低温腐蚀,而回转式空气预热器的漏风较为严重,能够做到6%的漏风率已是相当不易。The current boiler air preheaters mainly include tubular air preheaters and rotary air preheaters, which play an important role in improving boiler efficiency. The main problem faced by tubular air preheaters is low-temperature corrosion, while rotary The air leakage of the conventional air preheater is relatively serious, and it is not easy to achieve an air leakage rate of 6%.
实用新型内容Utility model content
针对现有回转式空气预热器漏风的问题,本实用新型的目的在于提供一种漏风率低的锅炉空气预热器。Aiming at the air leakage problem of the existing rotary air preheater, the purpose of the utility model is to provide a boiler air preheater with a low air leakage rate.
为实现上述目的,本实用新型采用的技术方案为:In order to achieve the above object, the technical solution adopted by the utility model is:
一种锅炉空气预热器,包括两个换热器,各换热器上均设有排烟管道和进气管道,两换热器的排烟管道通过两根连接管道交叉连通,两换热器的进气管道也通过两根连接管道交叉连通,排烟管道和进气管道分别在其两根连接管道之间的部分设有阀门,连接管道上也分别设有阀门。A boiler air preheater, including two heat exchangers, each heat exchanger is provided with a smoke exhaust pipe and an air intake pipe, the smoke exhaust pipes of the two heat exchangers are cross-connected through two connecting pipes, and the two heat exchangers The air intake pipe of the device is also cross-connected through two connecting pipes, the smoke exhaust pipe and the air inlet pipe are respectively provided with valves in the part between the two connecting pipes, and the connecting pipes are also respectively provided with valves.
本实用新型独特的线路设计可使空气和烟气交替流经两个换热器,通过开启或关系阀门即可进行切换。当空气流经第一个换热器时,由第一换热器对其进行加热,此时烟气正在对第二换热器进行加热,当空气流经第二个换热器时,由第二换热器对其进行加热,此时烟气正在对第一换热器进行加热。该预热器不仅能有效解决漏风的问题,还具有加热速度快、性能稳定、易于维护等有益效果。The unique circuit design of the utility model can make the air and flue gas alternately flow through the two heat exchangers, which can be switched by opening or closing the valve. When the air flows through the first heat exchanger, it is heated by the first heat exchanger. At this time, the flue gas is heating the second heat exchanger. When the air flows through the second heat exchanger, it is heated by the The second heat exchanger heats it while the flue gas is heating the first heat exchanger. The preheater can not only effectively solve the problem of air leakage, but also has beneficial effects such as fast heating speed, stable performance, and easy maintenance.
附图说明 Description of drawings
图1是本实用新型的整体结构示意图。Fig. 1 is a schematic diagram of the overall structure of the utility model.
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步详细的描述。Below in conjunction with accompanying drawing, the utility model is described in further detail.
附图标记说明如下:The reference signs are explained as follows:
11、22——换热器11, 22 - heat exchanger
13、23——排烟管道13, 23 - smoke exhaust pipe
14、24——进气管道14, 24 - intake pipe
15、25、15′、25′——连接管道15, 25, 15', 25' - connection pipe
16、17、26、27、18、28、18′、28′——阀门16, 17, 26, 27, 18, 28, 18', 28' - valve
如图1所示,该空气预热器主要由换热器11和换热器22组成,换热器11上设有排烟管道13和进气管道14,换热器22上设有排烟管道23和进气管道24,排烟管道13与排烟管道23通过连接管道15和连接管道25交叉连通,进气管道14和进气管道24通过连接管道15′和连接管道25′交叉连通,排烟管道13和进气管道14分别在其两根连接管道之间的部分设有阀门16和阀门17,排烟管道23和进气管道24分别在其两根连接管道之间的部分设有阀门26和阀门27,连接管道15和连接管道25上分别设有阀门18和阀门28,连接管道15′和连接管道25′上分别设有阀门18′和阀门28′。使用时,首先热烟气通过阀门16、阀门17流经换热器11,加热换热器11,与此同时空气通过阀门26、阀门27流经换热器22,换热器22加热流过的空气,在这个过程中,阀门18、阀门28、阀门18′、阀门28′均关闭,以防止烟气与空气混合,在换热器吸热、放热较为充分后,阀门18、阀门28、阀门18′、阀门28′打开而阀门16、阀门17、阀门26、阀门27关闭,此时热烟气加热换热器22而换热器11加热空气。As shown in Figure 1, the air preheater is mainly composed of a heat exchanger 11 and a heat exchanger 22. The heat exchanger 11 is provided with a smoke exhaust pipe 13 and an intake pipe 14, and the heat exchanger 22 is provided with a smoke exhaust pipe. The pipe 23 and the air inlet pipe 24, the exhaust pipe 13 and the smoke exhaust pipe 23 are cross-communicated through the connecting pipe 15 and the connecting pipe 25, and the air inlet pipe 14 and the air inlet pipe 24 are cross-communicated through the connecting pipe 15' and the connecting pipe 25', The smoke exhaust pipe 13 and the air intake pipe 14 are respectively provided with a valve 16 and a valve 17 at the part between its two connecting pipes, and the smoke exhaust pipe 23 and the air inlet pipe 24 are respectively provided with a valve 16 at the part between its two connecting pipes. The valve 26 and the valve 27 are respectively provided with the valve 18 and the valve 28 on the connecting pipe 15 and the connecting pipe 25, and are respectively provided with a valve 18' and a valve 28' on the connecting pipe 15' and the connecting pipe 25'. When in use, first the hot flue gas flows through the heat exchanger 11 through the valve 16 and the valve 17, and heats the heat exchanger 11. At the same time, the air flows through the heat exchanger 22 through the valve 26 and the valve 27, and the heat exchanger 22 heats and flows During this process, valve 18, valve 28, valve 18', and valve 28' are all closed to prevent the flue gas from mixing with air. After the heat exchanger absorbs and releases heat sufficiently, valve 18, valve 28 , valve 18', valve 28' are open and valve 16, valve 17, valve 26, valve 27 are closed, at this time the hot flue gas heats the heat exchanger 22 and the heat exchanger 11 heats the air.
下面对这种改造后的空气预热器的漏风率进行计算:假定换热器的主体长度为L,总横截面积为S,其中通流面积为S1,非通流面积为S2,很显然:S=S1+S2。The air leakage rate of this modified air preheater is calculated as follows: Assume that the main body length of the heat exchanger is L, the total cross-sectional area is S, and the flow area is S 1 , and the non-flow area is S 2 , obviously: S=S 1 +S 2 .
如果阀门能够瞬时关严,这种对吹的预热器漏风主要是因为空气或烟气在通过换热器后,在换热器本身的空隙中有所残留,那么换热器的漏风率ε计为残留空气/烟气量与一个周期内通流的空气/烟气量之比,即:If the valve can be closed instantly, the air leakage of the counter blowing preheater is mainly due to the air or flue gas remaining in the gap of the heat exchanger itself after passing through the heat exchanger, then the air leakage rate of the heat exchanger ε Calculated as the ratio of the residual air/flue gas volume to the air/flue gas volume that passes through in one cycle, namely:
其中v为气流速度,t为一个工作周期内气流的通流时间。Among them, v is the air velocity, and t is the passage time of the air in a working cycle.
因为气流放热全部被换热器所吸收,根据能量平衡:Because all the heat released by the airflow is absorbed by the heat exchanger, according to the energy balance:
cp·S1·v·t·ρg(T1-T2)=c·S2·L·ρ(T1-T2)c p ·S 1 ·v·t·ρ g (T 1 -T 2 )=c·S 2 ·L·ρ(T 1 -T 2 )
整理得:cp·S1·v·t·ρg=c·S2·L·ρArranged: c p · S 1 · v · t · ρ g = c · S 2 · L · ρ
结合上式可得:Combining the above formula can get:
其中cp为空气定压比热容,ρg为空气密度,c为换热器材料比热容,ρ为换热器材料密度。Where c p is the specific heat capacity of air at constant pressure, ρ g is the air density, c is the specific heat capacity of the heat exchanger material, and ρ is the density of the heat exchanger material.
根据该公式可以很容易估算出这种对吹空气预热器的漏风率:空气比热容为1.0045,密度取1.25(常压下500℃热烟气密度约0.5),材料比热容取1(一般大于1),而密度取1000(实际密度应大于1000),如通流面积与非通流面积相等,即S1=S2,那么ε≈0.125%,由此可见,这种预热器的漏风率是非常小的。According to this formula, the air leakage rate of this kind of blowing air preheater can be easily estimated: the air specific heat capacity is 1.0045, the density is 1.25 (the density of hot flue gas at 500°C under normal pressure is about 0.5), and the material specific heat capacity is 1 (generally greater than 1 ), and the density is 1000 (the actual density should be greater than 1000), if the flow area is equal to the non-flow area, that is, S 1 = S 2 , then ε≈0.125%, it can be seen that the air leakage rate of this preheater is very small.
以上用两个换热器的实施例进行了说明,在实际使用过程中,可以采用至少两个换热器或多组并联的方式使用,这里就不再赘述。The above is described with the embodiment of two heat exchangers. In actual use, at least two heat exchangers or multiple sets of parallel connection can be used, so no more details will be given here.
本实用新型不局限于上述最佳实施方式,任何人在本发明的启示下都可得出其它各种形式的产品。但不论在其形状或结构上作任何变化,凡是与本实用新型相同或相近似的技术方案,均在其保护范围之内。The utility model is not limited to the above-mentioned best implementation mode, and anyone can draw other various forms of products under the enlightenment of the present invention. But no matter any changes are made in its shape or structure, all technical solutions identical or similar to the utility model are all within its protection scope.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2007201286444U CN201072138Y (en) | 2007-09-10 | 2007-09-10 | Novel boiler air preheater |
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CNU2007201286444U CN201072138Y (en) | 2007-09-10 | 2007-09-10 | Novel boiler air preheater |
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CN201072138Y true CN201072138Y (en) | 2008-06-11 |
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CNU2007201286444U Expired - Fee Related CN201072138Y (en) | 2007-09-10 | 2007-09-10 | Novel boiler air preheater |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110062868A (en) * | 2016-12-21 | 2019-07-26 | 乔治洛德方法研究和开发液化空气有限公司 | Heat exchanger and the heat change method for using the heat exchanger |
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2007
- 2007-09-10 CN CNU2007201286444U patent/CN201072138Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110062868A (en) * | 2016-12-21 | 2019-07-26 | 乔治洛德方法研究和开发液化空气有限公司 | Heat exchanger and the heat change method for using the heat exchanger |
CN110062868B (en) * | 2016-12-21 | 2021-03-26 | 乔治洛德方法研究和开发液化空气有限公司 | Heat exchanger and heat exchange method using the same |
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Legal Events
Date | Code | Title | Description |
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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: 20080611 |