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JPH0631696B2 - Combined gas preheater - Google Patents

Combined gas preheater

Info

Publication number
JPH0631696B2
JPH0631696B2 JP5804185A JP5804185A JPH0631696B2 JP H0631696 B2 JPH0631696 B2 JP H0631696B2 JP 5804185 A JP5804185 A JP 5804185A JP 5804185 A JP5804185 A JP 5804185A JP H0631696 B2 JPH0631696 B2 JP H0631696B2
Authority
JP
Japan
Prior art keywords
heat
gas
heat transfer
exhaust gas
heat exchanger
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
Application number
JP5804185A
Other languages
Japanese (ja)
Other versions
JPS61217694A (en
Inventor
牧男 岩渕
光男 神坂
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5804185A priority Critical patent/JPH0631696B2/en
Publication of JPS61217694A publication Critical patent/JPS61217694A/en
Publication of JPH0631696B2 publication Critical patent/JPH0631696B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Supply (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は石炭焚きボイラ排ガス等含塵ガスから排熱回収
に用いるボイラ用エアヒータ、燃料ガス加熱装置等の複
合形気体予熱器に関する。
TECHNICAL FIELD The present invention relates to a composite gas preheater such as an air heater for a boiler and a fuel gas heating device used for recovering exhaust heat from dust-containing gas such as coal-fired boiler exhaust gas.

〔従来の技術〕[Conventional technology]

第4図は従来例を示す気体予熱装置の側面図である。 FIG. 4 is a side view of a gas preheating device showing a conventional example.

従来、隔壁を隔てて複数の熱交換器01,02を配置し、そ
れぞれの熱交換器01,02間に伝熱媒体03を循環させて熱
の授受を行う気体予熱器は、高温排ガス04等の加熱気体
と被加熱気体05の混合、あるいは一方のダクト06から他
方のダクト07への気体の漏洩を避ける場合に使用されて
いる。上記気体予熱器08において、水を伝熱媒体03とし
て使用し、かつ熱交換器01,02の一方を蒸発器09、他方
を凝縮器010として、蒸気と水の密度差を利用する自然
循環で伝熱媒体を循環させる方式が一般に採用されてい
る。しかしながら、上記方式では熱交換を行う温度領域
が高くなるに従つて、伝熱媒体03である水の飽和圧力も
高くなるため、水と蒸気の密度差が減少し、自然循環力
が低下する。したがつて水を伝熱媒体03として使用する
上記気体予熱器08では実用できる上限の温度レベルが存
在し、被加熱気体05の温度を350℃以上とすることは困
難である。
Conventionally, a gas preheater in which a plurality of heat exchangers 01 and 02 are arranged with a partition wall and heat is transferred by circulating a heat transfer medium 03 between the heat exchangers 01 and 02 is a high temperature exhaust gas 04, etc. It is used to avoid mixing of the heated gas and the heated gas 05, or leakage of gas from one duct 06 to the other duct 07. In the gas preheater 08, water is used as the heat transfer medium 03, one of the heat exchangers 01 and 02 is used as the evaporator 09, and the other is used as the condenser 010, which is a natural circulation utilizing the density difference between steam and water. A method of circulating a heat transfer medium is generally adopted. However, in the above method, the saturation pressure of water, which is the heat transfer medium 03, increases as the temperature range in which heat is exchanged increases, so the density difference between water and steam decreases, and the natural circulation force decreases. Therefore, in the gas preheater 08 that uses water as the heat transfer medium 03, there is a practical upper limit temperature level, and it is difficult to set the temperature of the heated gas 05 to 350 ° C. or higher.

また、従来の上記気体予熱器は、自然循環の上で有利な
伝熱管垂直配置を採用している。伝熱管は通常、円形フ
イン付管で構成されているが、排ガス中に灰などの塵埃
を含む場合、フインの表面に塵埃が堆積しやすく、また
水洗などよる洗浄も充分に効果を発揮しにくい伝熱管配
置である。
Further, the conventional gas preheater employs a vertical arrangement of heat transfer tubes which is advantageous in natural circulation. The heat transfer tube is usually composed of a circular finned tube, but if dust such as ash is contained in the exhaust gas, it is easy for dust to accumulate on the fin surface and it is difficult to sufficiently wash it with water. It is a heat transfer tube arrangement.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

石炭火力の燃料の炭種によつては、空気予熱温度が約35
0℃以上を必要としても、水だけを伝熱媒体として使用
する場合には、自然循環が成立せず、約400℃の排ガス
温度を有効に熱交換させることができなかつた。また、
排ガス中に含まれる塵が、熱交換器を構成する伝熱管の
フイン等の伝熱面に付着して伝熱面を閉塞し、伝熱効率
が低下する等の不具合があつた。
Depending on the coal type of the coal-fired fuel, the air preheating temperature is about 35
Even when 0 ° C or higher was required, when only water was used as the heat transfer medium, natural circulation was not established, and the exhaust gas temperature of about 400 ° C could not be effectively exchanged. Also,
The dust contained in the exhaust gas adheres to the heat transfer surfaces such as fins of the heat transfer tubes forming the heat exchanger to block the heat transfer surfaces, resulting in a decrease in heat transfer efficiency.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、区画壁をはさんで相隣る2本の竪向きのダク
トの一方を高温排ガスが上部から下向きに流れ、被加熱
気体は上記ダクトの他方を下部から上向きに流れ、上記
ダクト間にまたがつて上記区画壁を貫通し設けられた熱
交換器内を循環する伝熱媒体によつて熱輸送を行い上記
高温排ガスと上記被加熱気体間に熱交換を行なうカス竪
流れ方式の複合形気体予熱器において、高温部には有機
熱媒を伝熱媒体として使用した単管形ヒートパイプ式熱
交換器、中低温部には水が自然循環する分離形ヒートパ
イプ式熱交換器をそれぞれその伝熱管を実質的に水平に
配して取付けてなることを特徴とする複合形気体予熱器
を供するものである。
According to the present invention, the hot exhaust gas flows downward from one side of one of the two vertical ducts that are adjacent to each other across the partition wall, and the heated gas flows from the lower side of the duct to the upper side, and the heated gas flows between the ducts. A composite of a vertical flow system in which heat is transferred by a heat transfer medium circulating in a heat exchanger provided penetrating the partition wall to perform heat exchange between the high-temperature exhaust gas and the heated gas. In the gas preheater, a single pipe heat pipe heat exchanger using an organic heat medium as a heat transfer medium is used in the high temperature part, and a separate heat pipe heat exchanger in which water naturally circulates in the middle and low temperature parts. The composite gas preheater is characterized in that the heat transfer tubes are arranged substantially horizontally and attached.

〔実施例〕〔Example〕

以下、第1,2図に本発明に係わるガス竪流れ方式のハ
イブリツド形ヒートパイプ式空気予熱器の1実施例を概
念的に示しその構成作用を説明する。本実施例の空気予
熱器1において、高温部は有機熱媒を使用した単管形ヒ
ートパイプ式熱交換器2で構成され、中低温部は水が自
然循環する分離形ヒートパイプ式熱交換器3で構成され
ている。従つて、高温のボイラ排ガス4は上部から下向
きに流れ、熱交換によつて低温の排ガス5となり、図示
省略の脱硫装置あるいはそのまゝ図示省略の排煙装置へ
排出される。一方、図示省略の強制通風機より送られる
空気6は下部から上向きに流れ、熱交換によつて高温の
予熱空気7となり、図示省略のボイラ燃焼室へ送られ
る。また各ヒートパイプ伝熱管は熱媒循環を妨げない程
度に実質的に水平に配置されている。
An embodiment of a gas vertical flow type hybrid heat pipe type air preheater according to the present invention will be conceptually shown in FIGS. In the air preheater 1 of the present embodiment, the high temperature part is composed of a single tube heat pipe type heat exchanger 2 using an organic heat medium, and the middle and low temperature part is a separate heat pipe type heat exchanger in which water naturally circulates. It is composed of three. Therefore, the high-temperature boiler exhaust gas 4 flows downward from the upper part, and becomes a low-temperature exhaust gas 5 by heat exchange, and is discharged to a desulfurization device (not shown) or a smoke exhaust device (not shown). On the other hand, the air 6 sent from the forced draft fan (not shown) flows upward from the lower part and becomes high temperature preheated air 7 by heat exchange and is sent to the boiler combustion chamber (not shown). Each heat pipe heat transfer tube is arranged substantially horizontally so as not to hinder the circulation of the heat medium.

なお分離形ヒートパイプ式熱交換器3は排ガス5および
空気6の温度レベルに応じて複数のモジユールに分割す
る必要がある。また自然循環力を確保する上から、排ガ
ス5側の蒸発器部分3aを空気側の凝縮部分3bよりも低い
位置におく必要がある。これに対して、単管形ヒートパ
イプ式熱交換器2では排ガスGおよび空気6の温度レベ
ルに応じてヒートパイプの作動点(熱媒圧力および温
度)が自動的に決まる。第3図は、ハイブリツド形ヒー
トパイプ式空気予熱器全体の作動状態を示す温度線図の
例である。この例では、排ガス温度400℃から350℃まで
を単管形ヒートパイプ2の使用範囲とし、また、350℃
から140℃までを分離形ヒートパイプ3の使用範囲とし
て、分離形の範囲についてはさらに温度レベルによつて
6個のモジユールに分割している。
The separated heat pipe heat exchanger 3 needs to be divided into a plurality of modules according to the temperature levels of the exhaust gas 5 and the air 6. Further, in order to secure the natural circulation force, it is necessary to place the evaporator portion 3a on the exhaust gas 5 side at a position lower than the condensation portion 3b on the air side. On the other hand, in the single-tube heat pipe type heat exchanger 2, the operating point (heat medium pressure and temperature) of the heat pipe is automatically determined according to the temperature levels of the exhaust gas G and the air 6. FIG. 3 is an example of a temperature diagram showing the operating state of the entire hybrid heat pipe type air preheater. In this example, the exhaust gas temperature from 400 ° C to 350 ° C is set as the usage range of the single-pipe heat pipe 2, and 350 ° C.
To 140 ° C. is the range of use of the separate type heat pipe 3, and the range of the separate type is further divided into 6 modules according to the temperature level.

〔発明の効果〕〔The invention's effect〕

気体予熱器は有機熱媒を伝熱媒体として使用した単管形
ヒートパイプ式熱交換器を高温部に、水が自然循環する
分離形ヒートパイプ式熱交換器を中低部に配設した竪形
の複合形気体予熱器で、上記各熱交換器が複数段積層し
たダクト内は、高温排ガスと被加熱気体とは隔壁で完全
に区画されているので、効率よく被加熱気体の予熱温度
が必要に応じて350℃ないしそれ以上にできる。
The gas preheater consists of a single-pipe heat pipe heat exchanger using an organic heat medium as the heat transfer medium in the high temperature section, and a separate heat pipe heat exchanger in which water circulates naturally in the middle and lower sections. In the complex-type gas preheater of the type, in the duct in which each of the heat exchangers is laminated in multiple stages, the high-temperature exhaust gas and the heated gas are completely partitioned by the partition wall, so the preheating temperature of the heated gas is efficiently It can be 350 ℃ or higher if necessary.

また、各熱交換器を構成する複数本の伝熱管が水平に配
設されているので、含塵ガスによる伝熱部伝熱面の閉塞
防止ないし、ダクト付着対策としてスーツブローおよび
水洗が容易な伝熱面配置の採用が可能となる。
Further, since the plurality of heat transfer tubes constituting each heat exchanger are horizontally arranged, it is easy to blow suit and wash with water as a measure to prevent clogging of the heat transfer surface of the heat transfer section due to dust-containing gas and as a measure against duct adhesion. It is possible to adopt the heat transfer surface arrangement.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明に係わるガス竪流れ方式の複合形空気予
熱器の1実施例を概念的に示した側面図、第2図は、第
1図のA−A矢視側面図、第3図はハイブリツド形ヒー
トパイプ式空気予熱器全体の作動状態を示す温度線図の
例、第4図は従来例を示す装置の側面図である。 1…複合形気体予熱器、2…単管形ヒートパイプ式熱交
換器、3…分離形ヒートパイプ式熱交換器、4…高温の
ボイラ排ガス、5…低温の排ガス、6…被加熱用の空
気、3a…排ガス側の蒸発器部分、3b…空気側の凝縮部
分。
FIG. 1 is a side view conceptually showing one embodiment of a gas vertical flow type composite air preheater according to the present invention, and FIG. 2 is a side view taken along the line AA in FIG. FIG. 4 is an example of a temperature diagram showing an operating state of the entire hybrid type heat pipe type air preheater, and FIG. 4 is a side view of an apparatus showing a conventional example. DESCRIPTION OF SYMBOLS 1 ... Composite type gas preheater, 2 ... Single tube heat pipe type heat exchanger, 3 ... Separation type heat pipe type heat exchanger, 4 ... High temperature boiler exhaust gas, 5 ... Low temperature exhaust gas, 6 ... For heating Air, 3a ... Evaporator part on exhaust gas side, 3b ... Condensing part on air side.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】区画壁をはさんで相隣る2本の竪向きのダ
クトの一方を高温排ガスが上部から下向きに流れ、被加
熱気体は上記ダクトの他方を下部から上向きに流れ、上
記ダクト間にまたがつて上記区画壁を貫通し設けられた
熱交換器内を循環する伝熱媒体によつて熱輸送を行い上
記高温排ガスと上記被加熱気体間に熱交換を行なうガス
竪流れ方式の複合形気体予熱器において、高温部には有
機熱媒を伝熱媒体として使用した単管形ヒートパイプ式
熱交換器、中低温部には水が自然循環する分離形ヒート
パイプ式熱交換器をそれぞれの伝熱管を実質的に水平に
配して取付けてなることを特徴とする複合形気体予熱
器。
1. A hot exhaust gas flows downward from one side of one of two vertical ducts adjacent to each other across a partition wall, and a gas to be heated flows from the lower side of the other duct to an upward direction. In a vertical gas flow system in which heat is transferred by a heat transfer medium circulating in a heat exchanger that is provided penetrating the partition wall in between to perform heat exchange between the high-temperature exhaust gas and the heated gas. In the combined gas preheater, a single pipe heat pipe heat exchanger using an organic heat medium as a heat transfer medium is used in the high temperature part, and a separate heat pipe type heat exchanger in which water naturally circulates in the middle and low temperature parts. A composite gas preheater, characterized in that the respective heat transfer tubes are arranged substantially horizontally and mounted.
JP5804185A 1985-03-22 1985-03-22 Combined gas preheater Expired - Lifetime JPH0631696B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5804185A JPH0631696B2 (en) 1985-03-22 1985-03-22 Combined gas preheater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5804185A JPH0631696B2 (en) 1985-03-22 1985-03-22 Combined gas preheater

Publications (2)

Publication Number Publication Date
JPS61217694A JPS61217694A (en) 1986-09-27
JPH0631696B2 true JPH0631696B2 (en) 1994-04-27

Family

ID=13072847

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5804185A Expired - Lifetime JPH0631696B2 (en) 1985-03-22 1985-03-22 Combined gas preheater

Country Status (1)

Country Link
JP (1) JPH0631696B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2642154A1 (en) * 1989-01-25 1990-07-27 Const Aero Navales Method for cooling a hot fluid using a cold fluid, without a common exchange surface in contact with these fluids, and exchanger for implementation thereof
US5607011A (en) * 1991-01-25 1997-03-04 Abdelmalek; Fawzy T. Reverse heat exchanging system for boiler flue gas condensing and combustion air preheating
CN102012039B (en) * 2010-12-22 2014-01-22 深圳中兴节能环保股份有限公司 Forced circulation air preheat system
CN106152169A (en) * 2016-07-08 2016-11-23 彭东林 A kind of horizontal heat-pipe air preheater

Also Published As

Publication number Publication date
JPS61217694A (en) 1986-09-27

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