JP2005241098A - Heat exchanger for high temperature - Google Patents

Heat exchanger for high temperature Download PDF

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JP2005241098A
JP2005241098A JP2004050039A JP2004050039A JP2005241098A JP 2005241098 A JP2005241098 A JP 2005241098A JP 2004050039 A JP2004050039 A JP 2004050039A JP 2004050039 A JP2004050039 A JP 2004050039A JP 2005241098 A JP2005241098 A JP 2005241098A
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tube
heat exchanger
folded portion
high temperature
tubes
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JP2004050039A
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Japanese (ja)
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Kimiaki Nakano
公昭 中野
Satoru Sakuma
哲 佐久間
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T Rad Co Ltd
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T Rad Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To reduce the inside resistance of a heat transfer pipe, to improve system efficiency, to simplify the shape of a holder of the heat transfer pipe, and to reduce the manufacturing cost. <P>SOLUTION: In this heat exchanger for high temperature 11 constituted to perform the heat exchange between the fluid circulated in a tube 12 and the other fluid circulated outside of the tube 12, the tube 12 is provided with fixed end parts 13, 14 at its both ends, and first fold-back parts 17 of large folding width and second fold-back parts of small folding width are alternately formed between the fixed end parts 13, 14. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、2つの流体間において熱交換を行う熱交換器に関し、特に、高温流体と低温流体との間で熱交換を行う高温度用熱交換器に関する。   The present invention relates to a heat exchanger that exchanges heat between two fluids, and more particularly, to a high-temperature heat exchanger that exchanges heat between a high-temperature fluid and a low-temperature fluid.

従来、ガスタービンから排出される高温ガスの排熱を回収する場合や、燃料電池において燃料となる水素を生成する場合等において、高温度用熱交換器が使用されている。   Conventionally, a high-temperature heat exchanger is used when recovering exhaust heat of a high-temperature gas discharged from a gas turbine or when generating hydrogen as fuel in a fuel cell.

図7は、この種の高温度用熱交換器を発電プラントにおいて使用した例を示すものである。この発電プラントには、ガスタービン1と、排気管2を介してこのガスタービン1に接続された排熱回収用の高温度用熱交換器3と、高温度用熱交換器3内に設けられた蒸発器4及びエコノマイザ5とが設けられている。そして、蒸発器4及びエコノマイザ5は蛇行して形成された伝熱管6,7により構成されており、これらの伝熱管6,7内にはそれぞれ蒸気及び水が流通するようになっている。また、各伝熱管6,7は、図示しないホルダーにより支持されており、このホルダーは平板に多数の支持孔を穿設したり、或いは、格子状に部材を結合したりして形成されている。   FIG. 7 shows an example in which this type of high temperature heat exchanger is used in a power plant. The power plant is provided in a gas turbine 1, a high temperature heat exchanger 3 for exhaust heat recovery connected to the gas turbine 1 via an exhaust pipe 2, and a high temperature heat exchanger 3. An evaporator 4 and an economizer 5 are provided. The evaporator 4 and the economizer 5 are composed of meandering heat transfer tubes 6, 7, and steam and water flow through the heat transfer tubes 6, 7, respectively. Each of the heat transfer tubes 6 and 7 is supported by a holder (not shown), and this holder is formed by drilling a large number of support holes in a flat plate or by joining members in a lattice shape. .

このような構成において、ガスタービン1から排出された高温の排気ガスは、排気管2を介して排熱回収用の高温度用熱交換器3に送られ、この高温度用熱交換器3において、各伝熱管6,7内をそれぞれ流通する蒸気及び水と熱交換され、排気ガスの排熱が回収される(例えば、特許文献1参照)。   In such a configuration, the high-temperature exhaust gas discharged from the gas turbine 1 is sent to the high-temperature heat exchanger 3 for exhaust heat recovery via the exhaust pipe 2, and in the high-temperature heat exchanger 3. Then, heat is exchanged with steam and water flowing through the heat transfer tubes 6 and 7, respectively, and exhaust heat of the exhaust gas is recovered (see, for example, Patent Document 1).

特開昭58−203303号公報JP 58-203303 A

しかしながら、上記した従来の高温度用熱交換器では、伝熱管6,7が蛇行して形成されているため、管内抵抗が大きくなり、動力源が大型化し、システム効率を高めることが難しいといった問題があった。   However, in the above-described conventional high temperature heat exchanger, since the heat transfer tubes 6 and 7 are meandered, the resistance in the tubes is increased, the power source is enlarged, and it is difficult to increase the system efficiency. was there.

また、伝熱管のホルダーの形状が複雑なため、製造に手間が掛かり、製造コストの低減化が図り難いといった問題もあった。   In addition, since the shape of the heat transfer tube holder is complicated, there is a problem that it takes time to manufacture and it is difficult to reduce the manufacturing cost.

本発明は、上記した課題を解決すべくなされたものであり、伝熱管の管内抵抗を低く抑え、システム効率を高めることができ、さらに、伝熱管のホルダーの形状を簡素化し、製造コストの低減化が可能な高温度用熱交換器を提供しようとするものである。   The present invention has been made to solve the above-described problems, and can reduce the internal resistance of the heat transfer tube, increase the system efficiency, simplify the shape of the heat transfer tube holder, and reduce the manufacturing cost. An object of the present invention is to provide a high-temperature heat exchanger that can be made into a high temperature.

本発明は、チューブ12内を流通する一方の流体と、チューブ12の外側を流通する他方の流体との間で熱交換を行うように構成された高温度用熱交換器11であって、チューブ12には、両端に固定端部13,14が形成され、固定端部13,14間に折り返し幅の大きい第1折り返し部17と折り返し幅の小さい第2折り返し部18とが交互に形成されていることを特徴とする。   The present invention is a high-temperature heat exchanger 11 configured to perform heat exchange between one fluid flowing in the tube 12 and the other fluid flowing outside the tube 12, 12, fixed end portions 13 and 14 are formed at both ends, and a first folded portion 17 having a large folding width and a second folding portion 18 having a small folding width are alternately formed between the fixed end portions 13 and 14. It is characterized by being.

そして、好ましくは、チューブ12は2本1組で設けられ、一方のチューブ12の第1折り返し部17に他方のチューブ12’の第2折り返し部18’が配置されると共に、一方のチューブ12の第2折り返し部18に他方のチューブ12’の第1折り返し部17’が配置されるように構成されている。   Preferably, two tubes 12 are provided as a set, and the second folded portion 18 ′ of the other tube 12 ′ is disposed at the first folded portion 17 of the one tube 12, and the The second folded portion 18 is configured such that the first folded portion 17 ′ of the other tube 12 ′ is disposed.

また、チューブ12が複数列で設けられており、複数列のチューブ12を2列ずつ支持可能なホルダー21が設けられ、ホルダー21の両側には、チューブ12が嵌設可能な切欠部23がそれぞれ形成されている。   Further, the tubes 12 are provided in a plurality of rows, holders 21 capable of supporting the rows of the tubes 12 in two rows are provided, and notches 23 on which the tubes 12 can be fitted are respectively provided on both sides of the holder 21. Is formed.

本発明によれば、チューブに折り返し幅の大きい第1折り返し部が形成されているため、管内抵抗を低減することができ、動力源の小型化が可能となり、システム効率を高めることができる。また、チューブを2本1組で組み合わせた場合には、効率よくコンパクトにチューブを配置することができ、スペースの有効利用を図ることが可能となる。さらに、チューブを2列ずつ支持可能なホルダーの両側にチューブが嵌設可能な切欠部を設けた場合には、ホルダーの構造が簡素化され、製造コストの低減化を図ることができる等、種々の優れた効果を得ることができる。   According to the present invention, since the first folded portion having a large folded width is formed in the tube, the in-pipe resistance can be reduced, the size of the power source can be reduced, and the system efficiency can be increased. Moreover, when two tubes are combined in one set, the tubes can be efficiently and compactly arranged, and the space can be effectively used. Furthermore, when notches are provided on both sides of the holder that can support the tubes in two rows, the structure of the holder is simplified and the manufacturing cost can be reduced. The excellent effect can be obtained.

以下、図面を参照しつつ、本発明の実施の形態について説明する。ここで、図1は本発明の実施の形態に係る高温度用熱交換器を示す概略説明図、図2は本発明の実施の形態におけるチューブを示す平面図、図3は本発明の実施の形態におけるホルダーを示す側面図である。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Here, FIG. 1 is a schematic explanatory view showing a high-temperature heat exchanger according to an embodiment of the present invention, FIG. 2 is a plan view showing a tube in the embodiment of the present invention, and FIG. 3 is an embodiment of the present invention. It is a side view which shows the holder in a form.

この高温度用熱交換器11には、内部に低温流体が流通可能なチューブ12が複数列で設けられており、チューブ12内を流通する低温流体とチューブ12の外側を流通する高温流体との間で熱交換が行われるようになっている。そして、チューブ12はZ型に曲成され、両端にそれぞれ固定端部13,14が形成されており、各固定端部13,14を介してそれぞれヘッダプレート15,16に溶接接合されるようになっている。   The high temperature heat exchanger 11 is provided with a plurality of rows of tubes 12 through which a low temperature fluid can flow, and a low temperature fluid flowing through the tube 12 and a high temperature fluid flowing outside the tube 12 are connected to each other. Heat exchange is performed between them. The tube 12 is bent into a Z shape, and fixed ends 13 and 14 are formed at both ends, respectively, and are welded to the header plates 15 and 16 via the fixed ends 13 and 14, respectively. It has become.

また、チューブ12には、各固定端部13,14間に折り返し幅の大きい第1折り返し部17と折り返し幅の小さい第2折り返し部18とがそれぞれ1箇所ずつ形成されており、第1折り返し部17は2箇所の90度曲がり部19を有し、第2折り返し部18は1箇所の180度曲がり部20を有している。これにより、図2に示すように、チューブ12,12’は、2本1組で組み合わせ可能となり、一方のチューブ12の第1折り返し部17によって囲まれた領域に他方のチューブ12’の第2折り返し部18’が配置されると共に、他方のチューブ12’の第1折り返し部17’によって囲まれた領域に一方のチューブ12の第2折り返し部18が配置されるように構成されている。   Further, the tube 12 is formed with a first folded portion 17 having a large folded width and a second folded portion 18 having a small folded width between the fixed end portions 13 and 14, respectively. 17 has two 90-degree bent portions 19, and the second folded portion 18 has one 180-degree bent portion 20. As a result, as shown in FIG. 2, the tubes 12 and 12 ′ can be combined in pairs, and the second tube 12 ′ of the other tube 12 ′ can be combined with the region surrounded by the first folded portion 17 of the one tube 12. The folded portion 18 ′ is arranged, and the second folded portion 18 of one tube 12 is arranged in a region surrounded by the first folded portion 17 ′ of the other tube 12 ′.

このように、チューブ12には折り返し幅の大きい第1折り返し部17が形成されており、チューブを2本1組で組み合わせることができるため、圧力損失の高い180度曲がり部20の数を削減することができる。したがって、管内抵抗を低減することができ、動力源の小型化が可能となる。また、チューブ12をZ型に曲成することにより、図6に示すように、従来のストレートチューブ8の場合に6箇所必要であったヘッダプレート15,16との溶接箇所Pを2箇所に減少させることができるため、組立て作業の簡素化を図ることが可能となる。また、圧力損失の高い固定端部が2箇所に減少するため、圧力損失の低減化も可能となる。   As described above, the tube 12 is formed with the first folded portion 17 having a large folded width, and two tubes can be combined in one set, thereby reducing the number of 180-degree bent portions 20 with high pressure loss. be able to. Therefore, the in-pipe resistance can be reduced, and the power source can be downsized. Further, by bending the tube 12 into a Z shape, as shown in FIG. 6, the number of welded portions P with the header plates 15 and 16 that are required in the case of the conventional straight tube 8 is reduced to two as shown in FIG. Therefore, the assembling work can be simplified. Further, since the fixed end portion having a high pressure loss is reduced to two places, the pressure loss can be reduced.

さらに、高温度用熱交換器11には、図3に示すように、複数列のチューブ12を2列ずつ支持するためのホルダー21が設けられている。ホルダー21は、両端部においてそれぞれホルダープレート22に溶接接合され、ホルダー21の両側にはそれぞれ、チューブ12が嵌設可能な半長円形状の切欠部23が複数個(図3では6個)ずつ形成されている。切欠部23は、図3に示すように、千鳥掛け状に形成させるのが好ましく、そうすることにより、チューブ12の両固定端部13,14をコンパクトに集中させることができるため、チューブの両固定端部13,14側に設けられるタンク(図示せず)の小型化が可能となる。   Further, as shown in FIG. 3, the high-temperature heat exchanger 11 is provided with holders 21 for supporting a plurality of rows of tubes 12 by two rows. The holder 21 is welded to the holder plate 22 at both ends, and a plurality of semi-oval cutouts 23 (six in FIG. 3) on which the tube 12 can be fitted are provided on both sides of the holder 21, respectively. Is formed. As shown in FIG. 3, the notch 23 is preferably formed in a staggered manner, and by doing so, both the fixed end portions 13 and 14 of the tube 12 can be concentrated in a compact manner. A tank (not shown) provided on the fixed end portions 13 and 14 side can be downsized.

次に、上記した高温度用熱交換器11の作用について説明する。   Next, the operation of the above-described high temperature heat exchanger 11 will be described.

図1に示すように、低温流体は、一方(図1では右側上部)の固定端部13からチューブ12内に流入し、第1折り返し部17、第2折り返し部18を通って、他方(図1では左側下部)の固定端部14からチューブ12外に流出する。この時、低温流体の熱によりチューブ12は伸長するが、第1折り返し部17の2箇所の90度曲がり部19及び第2折り返し部18の180度曲がり部20によりチューブ12の伸びを吸収し、熱応力を緩和することができるため、両側の固定端部13,14とヘッダプレート15,16との溶接接合箇所に負荷が掛かることはない。また、チューブ12はホルダー21により保持されているため、伸びによる熱変形を防止することができる。   As shown in FIG. 1, the cryogenic fluid flows into the tube 12 from one fixed end 13 (upper right side in FIG. 1), passes through the first folded portion 17 and the second folded portion 18, and the other (shown in FIG. 1). 1 flows out of the tube 12 from the fixed end 14 at the lower left side. At this time, the tube 12 is expanded by the heat of the low-temperature fluid, but the extension of the tube 12 is absorbed by the two 90-degree bent portions 19 of the first folded portion 17 and the 180-degree bent portions 20 of the second folded portion 18. Since the thermal stress can be relaxed, no load is applied to the welded joints between the fixed ends 13 and 14 and the header plates 15 and 16 on both sides. Further, since the tube 12 is held by the holder 21, thermal deformation due to elongation can be prevented.

一方、高温流体は、全体的に低温流体の流れの方向と直交対向流となるような向き(図1では下から上方の向き)で、チューブ12の外側を流通し、その高温流体とチューブ12内を流通する低温流体との間で熱交換が行われる。この時、低温流体と高温流体とは直交対向流となるため、熱交換効率を高めることができる。   On the other hand, the high-temperature fluid circulates outside the tube 12 in a direction that is generally opposite to the flow direction of the low-temperature fluid (in FIG. 1, from the bottom to the top). Heat exchange is performed with a low-temperature fluid circulating in the interior. At this time, since the low-temperature fluid and the high-temperature fluid are orthogonally opposed, the heat exchange efficiency can be increased.

なお、上記実施の形態では、チューブ12に第1折り返し部17と第2折り返し部18がそれぞれ1箇所ずつ形成されているが、第1折り返し部17と第2折り返し部18は、それらが交互に形成されていれば、何箇所設けられていてもよく、例えば、図4に示すように、第1折り返し部17と第2折り返し部18をそれぞれ2箇所ずつ設けたり、或いは、図5に示すように、第1折り返し部17を2箇所設けると共に第2折り返し部18を1箇所設けたりしてもよい。   In the above embodiment, the tube 12 is provided with the first folded portion 17 and the second folded portion 18 one by one. However, the first folded portion 17 and the second folded portion 18 are alternately arranged. As long as it is formed, any number of locations may be provided. For example, as shown in FIG. 4, two first folded portions 17 and two second folded portions 18 may be provided, or alternatively, as shown in FIG. In addition, two first folded portions 17 may be provided and one second folded portion 18 may be provided.

本発明の実施の形態に係る高温度用熱交換器を示す概略説明図である。It is a schematic explanatory drawing which shows the high temperature heat exchanger which concerns on embodiment of this invention. 本発明の実施の形態におけるチューブを示す平面図である。It is a top view which shows the tube in embodiment of this invention. 本発明の実施の形態におけるホルダーを示す側面図である。It is a side view which shows the holder in embodiment of this invention. 本発明の実施の形態におけるチューブの別の例を示す平面図である。It is a top view which shows another example of the tube in embodiment of this invention. 本発明の実施の形態におけるチューブのさらに別の例を示す平面図である。It is a top view which shows another example of the tube in embodiment of this invention. 従来におけるチューブの配列を示す概略説明図である。It is a schematic explanatory drawing which shows the arrangement | sequence of the tube in the past. 従来例を示す系統図である。It is a systematic diagram which shows a prior art example.

符号の説明Explanation of symbols

11 高温度用熱交換器
12 チューブ
13 固定端部
14 固定端部
17 第1折り返し部
18 第2折り返し部
21 ホルダー
23 切欠部
DESCRIPTION OF SYMBOLS 11 High temperature heat exchanger 12 Tube 13 Fixed end part 14 Fixed end part 17 1st return part 18 2nd return part 21 Holder 23 Notch part

Claims (3)

チューブ内を流通する一方の流体と、該チューブの外側を流通する他方の流体との間で熱交換を行うように構成された高温度用熱交換器であって、
前記チューブには、両端に固定端部が形成され、該固定端部間に折り返し幅の大きい第1折り返し部と折り返し幅の小さい第2折り返し部とが交互に形成されていることを特徴とする高温度用熱交換器。
A high-temperature heat exchanger configured to exchange heat between one fluid flowing in the tube and the other fluid flowing outside the tube,
The tube has fixed end portions at both ends, and a first folded portion having a large folded width and a second folded portion having a small folded width are alternately formed between the fixed ends. High temperature heat exchanger.
前記チューブは2本1組で設けられ、一方のチューブの第1折り返し部に他方のチューブの第2折り返し部が配置されると共に、前記一方のチューブの第2折り返し部に前記他方のチューブの第1折り返し部が配置されるように構成されている請求項1に記載の高温度用熱交換器。 The tubes are provided as a set of two tubes, the second folded portion of the other tube is disposed at the first folded portion of one tube, and the second folded portion of the other tube is disposed at the second folded portion of the one tube. The high temperature heat exchanger according to claim 1, wherein the one folded portion is arranged. 前記チューブが複数列で設けられており、該複数列のチューブを2列ずつ支持可能なホルダーが設けられ、該ホルダーの両側には、前記チューブが嵌設可能な切欠部がそれぞれ形成されている請求項1又は2に記載の高温度用熱交換器。 The tube is provided in a plurality of rows, a holder capable of supporting the plurality of rows of tubes in two rows is provided, and a notch portion in which the tube can be fitted is formed on both sides of the holder. The high temperature heat exchanger according to claim 1 or 2.
JP2004050039A 2004-02-25 2004-02-25 Heat exchanger for high temperature Pending JP2005241098A (en)

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