JP4132380B2 - Heat recovery amount increasing device in latent heat recovery boiler - Google Patents
Heat recovery amount increasing device in latent heat recovery boiler Download PDFInfo
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- JP4132380B2 JP4132380B2 JP09848599A JP9848599A JP4132380B2 JP 4132380 B2 JP4132380 B2 JP 4132380B2 JP 09848599 A JP09848599 A JP 09848599A JP 9848599 A JP9848599 A JP 9848599A JP 4132380 B2 JP4132380 B2 JP 4132380B2
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- JP
- Japan
- Prior art keywords
- exhaust gas
- heat recovery
- economizer
- heat
- gas passage
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- 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.)
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Description
【0001】
【産業上の利用分野】
本発明は、潜熱回収ボイラにおける熱回収量増加装置に関するものである。
【0002】
【従来の技術】
ボイラから排出される排ガスを通す排ガス通路にエコノマイザを設け、排ガスによって給水を予熱することにより、ボイラの効率を向上させることが広く行われている。エコノマイザは排ガス通路内の排ガスと、排ガス通路内に設けた伝熱管の間で熱交換を行うものであり、伝熱管の熱吸収量が多くなるほど伝熱管内を送られる給水の温度は上昇し、ボイラの効率は向上する。排ガスには燃焼によって発生した水分が気体の状態で含まれているため、排ガスの顕熱だけでなく潜熱の回収も行うことで、より多くの熱を回収することも行われている。しかし、潜熱回収部は熱交換の効率が悪いため、エコノマイザが非常に大きくなるという問題があった。
【0003】
また、ボイラは定期的に缶水の排出を行う必要があるが、排出されるブロー水には熱が含まれているため、そのまま排出したのでは効率が低下する。そこで高温のブロー水とエコノマイザに入る前の給水との間で熱交換することにより、ブロー水から熱を回収することが行われている。最初にブロー水の熱によって給水の温度を上昇させておき、温度の上昇した給水をエコノマイザへ入れることによりさらに給水温度を上昇させることができる。しかし、潜熱回収を行っているエコノマイザの場合、ブロー水によって給水温度を上昇させると、エコノマイザでの熱吸収効率が低下することとなり、ブロー水からの熱を回収しても排ガスからの熱回収量が低下するため、全体での熱回収量はあまり増加していなかった。
【0004】
【発明が解決しようとする課題】
本発明が解決しようとする課題は、潜熱回収部での熱回収効率を向上させ、潜熱回収量の増加と潜熱回収エコノマイザの小型化を可能とすることにある。
【0005】
【課題を解決するための手段】
燃焼装置で発生させた火炎によって得られる燃焼ガスを利用して蒸気を発生し、熱交換によって温度の低下した排ガスは排ガス通路を通して排出しており、排ガス通路内にはエコノマイザを設けて給水を予熱しているものであって、エコノマイザは排ガスの顕熱だけでなく潜熱の回収も行わせる潜熱回収ボイラにおいて、ボイラ内から排出した高圧のブロー水を排ガス通路内の伝熱管に直接噴射することなくフラッシュさせることにより、排ガス通路内に蒸気を発生させておき、エコノマイザ部分での排ガスに含まれる水分量を多くすることにより、エコノマイザの潜熱回収部での熱回収効率を向上させる。また、排ガス通路内に伝熱管設置部と分割する仕切板を設け、仕切板で分割した部分にブロー水配管を接続し、ボイラ内から排出した高圧のブロー水は仕切板で分割した部分でフラッシュさせることで、排ガス通路内の伝熱管にブロー水を直接噴射することなく排ガス通路内に蒸気を発生させる。
【0006】
【発明の実施の形態】
本発明の一実施例を図面を用いて説明する。図1は本発明に関する一実施例におけるボイラおよびエコノマイザの断面図である。ボイラ1は燃焼装置4によって火炎の燃焼を行い、火炎によって高温の燃焼ガスを発生させており、燃焼ガスによって缶水を加熱して蒸気を発生させる。発生した蒸気は気水分離器9へ送られて蒸気と缶水に分離し、分離した缶水はボイラ内に残して蒸気のみを取り出す。缶水を加熱することによって温度の低下した後の排ガスは、排ガス通路2を通して排気しており、排ガス通路2の途中にエコノマイザ7を設ける。エコノマイザ7内には水平方向に伸びる伝熱管3を多数設けており、伝熱管3には多数の熱吸収用フィン5を取り付けておく。エコノマイザ7内の各伝熱管は、ベンド管によって連結して一続きの給水流路を形成しており、エコノマイザ7に達した排ガスは、エコノマイザ7内の伝熱管3の間を下向きに流れる構成としている。
【0007】
エコノマイザ内への給水は、伝熱管群の最下段の伝熱管より入り、順次伝熱管を通って加熱されながら最上段の伝熱管まで達し、エコノマイザより取り出されて、ボイラ1内へ給水される。そのため伝熱管内を送られる給水の水温は下段ほど低く、上段ほど高くなっている。また、ボイラからエコノマイザ7へ送られた排ガスは、エコノマイザ内で伝熱管と熱交換を行いながら下向きに流れていくため、エコノマイザ内の下方へ行くほど排ガスの温度は低くなる。そのため排ガス流の下流側にあたる下方の伝熱管表面では、排ガス中に含まれていた水分の凝縮が発生し、水分の凝縮によって発生した熱は伝熱管に吸収される。
【0008】
図1の場合、一端は気水分離器9に接続し、他端は排ガス通路2に接続しており、ブロー水を排ガス通路2内へフラッシュするブロー水用配管10を設けている。ブロー水用配管10の途中にはフラッシュ制御弁11を設けておき、フラッシュ制御弁11を開くとブロー水が排ガス通路2内へ送られる。ボイラ内部は圧力が高いため、ボイラ内から取り出されるブロー水の圧力も高いものであり、高温高圧のブロー水を低圧の排ガス通路2へ噴射すると、ブロー水から蒸気が発生する。ブロー水を伝熱管3に直接噴射すると、ブロー水からの蒸気発生量が減少し、またブロー水の接触している部分では排ガスからの熱回収が行えない。そのため、ブロー水が伝熱管3に直接接触せず、ブロー水から発生した蒸気のみが伝熱管3と接触するように排ガス通路2内に仕切板12を設けている。ブロー水は仕切板12で分離されている部分へ噴射し、ブロー水から発生した蒸気を排ガスに供給するようにしている。
【0009】
排ガス通路2内で蒸気を発生することにより、排ガス中の水分量が増加することとなる。排ガス中の水分量が増加すると排ガスの露点が上昇し、より早い段階で排ガス内水分の凝縮が始まるため、排ガスからの潜熱回収量を増加させることができる。また、排ガス中の水分量を増加させると凝縮する水量も増加することになるため、排ガスからの潜熱回収量が増加する。さらに、排ガス通路2内で発生させた蒸気自身も熱を持っているため、蒸気の熱による伝熱管の加熱も行われる。
【0010】
これらのことにより、エコノマイザの潜熱回収部での熱回収効率が向上し、熱回収量が増加するため、ボイラの効率は向上する。この場合の熱回収量は、ブロー水によってエコノマイザへ導入する前の給水を加熱し、その後にエコノマイザにて排ガスから熱を回収していた場合よりも多くなる。
【0011】
【発明の効果】
本発明を実施することによって、潜熱回収部での熱回収効率を向上させることができるため、潜熱回収量を増加することができる。また、熱回収効率が向上するため伝熱管を少なくすることができ、潜熱回収エコノマイザを小型化することも可能となる。
【図面の簡単な説明】
【図1】 本発明の請求項1に関する一実施例のボイラおよびエコノマイザの断面図
【符号の説明】
1 ボイラ
2 排ガス通路
3 伝熱管
4 燃焼装置
5 熱吸収用フィン
6 火炎
7 エコノマイザ
8 水噴霧装置
9 気水分離器
10 ブロー水用配管
11 フラッシュ制御弁
12 仕切板[0001]
[Industrial application fields]
The present invention relates to a heat recovery amount increasing device in a latent heat recovery boiler.
[0002]
[Prior art]
It is widely practiced to improve boiler efficiency by providing an economizer in an exhaust gas passage through which exhaust gas discharged from a boiler passes and preheating feed water with the exhaust gas. The economizer exchanges heat between the exhaust gas in the exhaust gas passage and the heat transfer tube provided in the exhaust gas passage, and as the heat absorption amount of the heat transfer tube increases, the temperature of the feed water sent through the heat transfer tube increases. The efficiency of the boiler is improved. Since the exhaust gas contains moisture generated by combustion in a gaseous state, more heat is also recovered by recovering not only the sensible heat of the exhaust gas but also the latent heat. However, the latent heat recovery unit has a problem that the economizer becomes very large because the efficiency of heat exchange is poor.
[0003]
In addition, the boiler needs to periodically discharge the can water, but since the blown water discharged contains heat, the efficiency is reduced if it is discharged as it is. Therefore, heat is recovered from the blow water by exchanging heat between the high temperature blow water and the water supply before entering the economizer. First, the temperature of the feed water is raised by the heat of the blow water, and the feed water temperature can be further raised by putting the feed water whose temperature has risen into the economizer. However, in the case of an economizer performing latent heat recovery, if the water supply temperature is increased by blow water, the heat absorption efficiency of the economizer will decrease, and the amount of heat recovered from exhaust gas even if heat from the blow water is recovered. Therefore, the overall heat recovery amount did not increase so much.
[0004]
[Problems to be solved by the invention]
The problem to be solved by the present invention is to improve the heat recovery efficiency in the latent heat recovery section, and to increase the amount of latent heat recovery and downsize the latent heat recovery economizer.
[0005]
[Means for Solving the Problems]
Steam is generated using the combustion gas obtained by the flame generated by the combustion device, and the exhaust gas whose temperature has decreased due to heat exchange is discharged through the exhaust gas passage. An economizer is installed in the exhaust gas passage to preheat the water supply. The economizer is a latent heat recovery boiler that collects not only sensible heat of exhaust gas but also latent heat, without directly injecting high-pressure blow water discharged from the boiler into the heat transfer pipe in the exhaust gas passage. By flushing, steam is generated in the exhaust gas passage, and the amount of water contained in the exhaust gas in the economizer part is increased, thereby improving the heat recovery efficiency in the latent heat recovery part of the economizer. In addition, a partition plate that divides the heat transfer tube installation part is provided in the exhaust gas passage, blow water piping is connected to the part divided by the partition plate, and high-pressure blow water discharged from the boiler is flushed at the part divided by the partition plate By doing so, steam is generated in the exhaust gas passage without directly injecting blow water into the heat transfer tube in the exhaust gas passage.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
An embodiment of the present invention will be described with reference to the drawings. Figure 1 is a cross-sectional view of the boiler and an economizer in one embodiment related to the present onset bright. The boiler 1 burns a flame with the combustion device 4, generates a high-temperature combustion gas by the flame, and heats can water with the combustion gas to generate steam. The generated steam is sent to the steam separator 9 and separated into steam and can water, and the separated can water is left in the boiler and only the steam is taken out. The exhaust gas after the temperature is lowered by heating the can water is exhausted through the exhaust gas passage 2, and an economizer 7 is provided in the middle of the exhaust gas passage 2. A large number of heat transfer tubes 3 extending in the horizontal direction are provided in the economizer 7, and a number of heat absorbing fins 5 are attached to the heat transfer tubes 3. Each heat transfer pipe in the economizer 7 is connected by a bend pipe to form a continuous water supply flow path, and the exhaust gas that has reached the economizer 7 flows downward between the heat transfer pipes 3 in the economizer 7. Yes.
[0007]
Water supplied into the economizer enters from the lowermost heat transfer tube of the heat transfer tube group, reaches the uppermost heat transfer tube while being sequentially heated through the heat transfer tubes, is taken out from the economizer, and is supplied into the boiler 1. Therefore, the water temperature of the feed water sent through the heat transfer tube is lower at the lower stage and higher at the upper stage. Further, since the exhaust gas sent from the boiler to the economizer 7 flows downward while exchanging heat with the heat transfer tube in the economizer, the temperature of the exhaust gas becomes lower as it goes downward in the economizer. For this reason, condensation of moisture contained in the exhaust gas occurs on the lower heat transfer tube surface on the downstream side of the exhaust gas flow, and heat generated by the condensation of moisture is absorbed by the heat transfer tube.
[0008]
In the case of FIG. 1, one end is connected to the steam separator 9 and the other end is connected to the exhaust gas passage 2, and a
[0009]
By generating steam in the exhaust gas passage 2, the amount of moisture in the exhaust gas increases. When the amount of moisture in the exhaust gas increases, the dew point of the exhaust gas rises, and condensation of the moisture in the exhaust gas begins at an earlier stage, so that the amount of latent heat recovered from the exhaust gas can be increased. Further, when the amount of water in the exhaust gas is increased, the amount of condensed water also increases, so that the amount of latent heat recovered from the exhaust gas increases. Furthermore, since the steam itself generated in the exhaust gas passage 2 also has heat, the heat transfer tube is also heated by the heat of the steam.
[0010]
By these things, since the heat recovery efficiency in the latent heat recovery part of the economizer is improved and the amount of heat recovery is increased, the efficiency of the boiler is improved. In this case, the heat recovery amount is larger than that in the case where the feed water before being introduced into the economizer is heated by blow water, and then the heat is recovered from the exhaust gas by the economizer.
[00 11 ]
【The invention's effect】
By carrying out the present invention, the heat recovery efficiency in the latent heat recovery unit can be improved, so that the amount of latent heat recovery can be increased. Further, since the heat recovery efficiency is improved, the number of heat transfer tubes can be reduced, and the latent heat recovery economizer can be downsized.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view of a boiler and an economizer of an embodiment relating to claim 1 of the present invention.
DESCRIPTION OF SYMBOLS 1 Boiler 2 Exhaust gas passage 3 Heat transfer pipe 4 Combustion device 5
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09848599A JP4132380B2 (en) | 1999-04-06 | 1999-04-06 | Heat recovery amount increasing device in latent heat recovery boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09848599A JP4132380B2 (en) | 1999-04-06 | 1999-04-06 | Heat recovery amount increasing device in latent heat recovery boiler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000291905A JP2000291905A (en) | 2000-10-20 |
| JP4132380B2 true JP4132380B2 (en) | 2008-08-13 |
Family
ID=14220962
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP09848599A Expired - Fee Related JP4132380B2 (en) | 1999-04-06 | 1999-04-06 | Heat recovery amount increasing device in latent heat recovery boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4132380B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101527753B1 (en) * | 2014-06-18 | 2015-06-16 | 주식회사 태성이엔텍 | A pellet boiler |
| JP6798249B2 (en) * | 2016-10-25 | 2020-12-09 | 三浦工業株式会社 | Boiler efficiency calculation method for latent heat recovery boiler |
-
1999
- 1999-04-06 JP JP09848599A patent/JP4132380B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2000291905A (en) | 2000-10-20 |
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