JPH0335563B2 - - Google Patents

Info

Publication number
JPH0335563B2
JPH0335563B2 JP8397485A JP8397485A JPH0335563B2 JP H0335563 B2 JPH0335563 B2 JP H0335563B2 JP 8397485 A JP8397485 A JP 8397485A JP 8397485 A JP8397485 A JP 8397485A JP H0335563 B2 JPH0335563 B2 JP H0335563B2
Authority
JP
Japan
Prior art keywords
evaporator tube
section
evaporator
heat transfer
evaporation
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
Application number
JP8397485A
Other languages
Japanese (ja)
Other versions
JPS61243203A (en
Inventor
Tei Misawa
Fuyuki Inoe
Yasuhide Oota
Yasushi Hoshino
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.)
SEKIYU SHIGEN KAIHATSU KK
Original Assignee
SEKIYU SHIGEN KAIHATSU KK
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 SEKIYU SHIGEN KAIHATSU KK filed Critical SEKIYU SHIGEN KAIHATSU KK
Priority to JP8397485A priority Critical patent/JPS61243203A/en
Publication of JPS61243203A publication Critical patent/JPS61243203A/en
Publication of JPH0335563B2 publication Critical patent/JPH0335563B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Detergent Compositions (AREA)

Description

【発明の詳細な説明】 この発明は、小径でコンパクトな構成の蒸気発
生装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam generator having a small diameter and compact configuration.

例えば坑底ボイラの場合、坑井のサイズに合せ
て小径とする必要があり、また坑井内への挿入設
置及び坑井までの搬送等を容易にするため長さも
できるだけ小さく、コンパクトな構成とすること
が要請されている。
For example, in the case of a bottom-hole boiler, the diameter needs to be small to match the size of the well, and the length should also be as small and compact as possible to facilitate insertion into the well and transportation to the well. This is requested.

上記要請に応えられるようにした蒸気発生装置
が、例えば特願昭59−61184により提案されてい
る。これは筒状缶囲の上端部に燃焼器を設け、環
状の給水管寄せから垂設された多数の蒸発管相互
を接続して円筒状水冷壁である放射伝熱部を形成
することにより外径寸法を小さくし、この放射伝
熱部に続いて蒸発管を内側にベンドした対流伝熱
部を設けることにより伝熱面積を減らすことなく
発生装置全体の長さを短かくしたコンパクトな構
成となつている。そして燃焼排ガスを缶囲内壁と
蒸発管部との間隙を通すことにより、給水を加熱
すると共に、排ガス出力温度を低下させるように
なつている。
A steam generator capable of meeting the above requirements has been proposed, for example, in Japanese Patent Application No. 59-61184. This is achieved by installing a combustor at the upper end of the cylindrical can, and connecting a large number of evaporator tubes hanging vertically from the annular water supply pipe header to form a radiant heat transfer section, which is a cylindrical water cooling wall. By reducing the diameter and providing a convection heat transfer section with the evaporation tube bent inward following the radiation heat transfer section, we have achieved a compact configuration that shortens the overall length of the generator without reducing the heat transfer area. It's summery. By passing the combustion exhaust gas through the gap between the inner wall of the can and the evaporator tube, the feed water is heated and the exhaust gas output temperature is lowered.

しかし、対流伝熱部でUベンドされた多数の蒸
発管を比較的短かい間隙で配設する場合、細長い
蒸発管は撓み易く、組立施工が面倒であること、
また使用状態で熱膨張により変形し、均一なガス
流路を形成する面で好ましくない等の問題があ
る。また缶囲と蒸発管部との熱膨張差を、缶囲下
端部と蒸気集合管との間に膨張接手を設けて吸収
するようにしているが、蒸気発生装置の固定を缶
囲上端部で行い懸吊する場合又は蒸気集合管部を
固定して装置荷重を受け持つようにした場合等に
膨張接手は相当の荷重に耐え得る構造としなけれ
ばならず、好ましい構造ではない。
However, when arranging a large number of U-bent evaporation tubes in a relatively short gap in a convection heat transfer section, the long and thin evaporation tubes are easily bent, making assembly and construction troublesome.
Further, there are problems such as deformation due to thermal expansion during use, making it difficult to form a uniform gas flow path. In addition, an expansion joint is provided between the lower end of the can enclosure and the steam collecting pipe to absorb the difference in thermal expansion between the can enclosure and the evaporator pipe, but the steam generator is fixed at the upper end of the can enclosure. When the equipment is suspended or the steam collecting pipe is fixed to take on the load of the equipment, the expansion joint must have a structure that can withstand a considerable load, which is not a preferable structure.

この発明は、上記のような問題点を解消できる
ようにした蒸気発生装置を提供することを目的と
するものである。
The object of the present invention is to provide a steam generator capable of solving the above-mentioned problems.

この発明の蒸気発生装置の特徴は、対流伝熱部
の上下方向にUベンドされた蒸発管を、缶軸方向
の熱膨張移動を許容しつつ半径方向支持金物によ
り支持したことである。また缶囲と蒸発管部との
熱膨張差を吸収するために、蒸発管部の末端部に
ループを形成したことである。
A feature of the steam generator of the present invention is that the evaporator tube, which is U-bent in the vertical direction of the convection heat transfer section, is supported by radial supporting metal fittings while allowing thermal expansion movement in the can axis direction. Additionally, a loop is formed at the end of the evaporator tube in order to absorb the difference in thermal expansion between the can enclosure and the evaporator tube.

以下この発明の一実施例を図面により説明す
る。図中1は円筒状の缶囲で、上端部に設けられ
た固定金物1aに、頭部接続金物5がボルトで固
定されている。この接続金物の上側に燃料、給
水、空気等の供給配管6が接続され、また下側に
環状の給水管寄せ2及び燃焼器4が設けられてい
る。給水管寄せ2に、多数の蒸発管31を垂設し
て、筒状の蒸発管部3が構成されている。蒸発管
部3は缶囲内壁との間に燃焼排ガス通路11とな
る間隙を介して設けられており、排ガスは上記接
続金物5に接続された排ガス管路7を通つて排出
される。
An embodiment of the present invention will be described below with reference to the drawings. In the figure, reference numeral 1 denotes a cylindrical can enclosure, and a head connecting metal fitting 5 is fixed with a bolt to a fixed metal fitting 1a provided at the upper end. Supply piping 6 for fuel, water, air, etc. is connected to the upper side of this connecting hardware, and an annular water supply header 2 and a combustor 4 are provided to the lower side. A cylindrical evaporation pipe section 3 is constructed by vertically disposing a large number of evaporation pipes 31 on the water supply pipe header 2. The evaporator pipe section 3 is provided with a gap between it and the inner wall of the can housing to form a combustion exhaust gas passage 11, and the exhaust gas is discharged through an exhaust gas pipe 7 connected to the connecting metal fitting 5.

蒸発管部3の上部は、蒸発管31を相互に直接
接続するか、又は第4図に示す如く接続部材31
aを介してガスタイトにシール溶接して、円筒状
水冷壁である放射伝熱部Rを形成している。そし
て下端部で、第2図に示す如く、2本の蒸発管3
1,31を1本の蒸発管32にまとめることによ
り、蒸発管32,32間に燃焼排ガスの通路を形
成している。蒸発管32は内側上方にUベンドさ
れてから、更に内側下方にUベンドされて、その
断面を第4図に示す対流伝熱部Cを形成してい
る。この場合蒸発管32のUベンドは、断面にお
ける蒸発管相互間の半径方向間隔が離れている
3A型と、間隔が狭い3B型との2種類とし、3A型
と3B型を周方向に交互に配列して、狭い断面積
内に多数の蒸発管32a,32b及び33a,3
3bを配列できるようにしてある。この場合3A
型について第3図及び第5図に示す如く、2本の
蒸発管31,31と、1本にまとめられた上向き
蒸発管32a及び下向き蒸発管33aとは、半径
方向の支持金物20Aにより支持されている。こ
の支持金物20Aは、長手方向に適宜の間隔で設
けられている。支持金物20Aは、蒸発管31,
31に溶着されたL型金物21a,21aと、上
向き蒸発管32aに溶着されたT型金物22aと
の組合せ及び蒸発管32aに溶着されたL型金物
23a,23aと、下向き蒸発管33aに溶着さ
れたT型金物24aとの組合せの両者により構成
され、各蒸発管の熱膨張による缶軸方向の移動を
許容しつつ半径方向では蒸発管相互を所定の間隔
を保持して支持するようになつている。また3B
型についても第6図に示す如く、2本の蒸発管3
1,31と1本にまとめられた上向も蒸発管32
b及び下向き蒸発管33bとは半径方向支持金物
20Bにより支持されている。支持金物20B
は、第3図に示す如く、管長方向で支持金物20
Aとは異る位置に取付けて、支持金物による通気
抵抗の増大をさけるようにしてある。支持金物2
0Bは、蒸発管31,31に溶着されたL型金物
21b,21bと、上向き蒸発管32bに溶着さ
れた平板22bとの組合せ及び蒸発管32bに溶
着されたコ字状金物23b,23bと下向き蒸発
管33bに溶着された平板24bとの組合せの両
者により構成されている。そして、3A型及び3B
型の下向き蒸発管33aと33bとは逆T型金物
25を介して相互に連結されている。
The upper part of the evaporation tube section 3 can connect the evaporation tubes 31 directly to each other, or can be connected to a connecting member 31 as shown in FIG.
The radiant heat transfer portion R, which is a cylindrical water-cooled wall, is formed by gas-tight seal welding through the a. Then, at the lower end, two evaporation tubes 3 are installed as shown in FIG.
1 and 31 into one evaporator tube 32, a combustion exhaust gas passage is formed between the evaporator tubes 32 and 32. The evaporator tube 32 is U-bended inwardly upward and then further inwardly downwardly to form a convection heat transfer section C whose cross section is shown in FIG. In this case, the U-bend of the evaporator tubes 32 is such that the radial distance between the evaporator tubes in the cross section is large.
There are two types: 3A type and 3B type with narrow intervals, and the 3A type and 3B type are arranged alternately in the circumferential direction, so that a large number of evaporation tubes 32a, 32b and 33a, 3 are arranged within a narrow cross-sectional area.
3b can be arranged. In this case 3A
About the mold As shown in FIGS. 3 and 5, the two evaporation tubes 31, 31, and the upward evaporation tube 32a and the downward evaporation tube 33a, which are combined into one, are supported by a radial support metal fitting 20A. ing. The supporting hardware 20A is provided at appropriate intervals in the longitudinal direction. The supporting hardware 20A includes the evaporation tube 31,
A combination of L-shaped metal fittings 21a, 21a welded to 31 and T-shaped metal fittings 22a welded to upward evaporation tube 32a, and L-shaped metal fittings 23a, 23a welded to evaporation tube 32a and welded to downward evaporation tube 33a. The evaporator tubes are configured in combination with the T-shaped hardware 24a, which allows each evaporator tube to move in the can axis direction due to thermal expansion, while supporting the evaporator tubes while maintaining a predetermined distance from each other in the radial direction. ing. Also 3B
Regarding the mold, as shown in Fig. 6, two evaporation tubes 3 are used.
1, 31 and the upper evaporation tube 32 combined into one
b and the downward evaporation tube 33b are supported by a radial support metal fitting 20B. Support hardware 20B
As shown in FIG. 3, the supporting hardware 20 is
It is installed in a different position from A to avoid an increase in ventilation resistance due to supporting hardware. Support hardware 2
0B is a combination of the L-shaped metal fittings 21b, 21b welded to the evaporation tubes 31, 31 and the flat plate 22b welded to the upward evaporation tube 32b, and the combination of the U-shaped metal fittings 23b, 23b welded to the evaporation tube 32b and the downward facing evaporation tube 32b. The evaporation tube 33b and the flat plate 24b are welded together. And type 3A and 3B
The downward evaporation tubes 33a and 33b of the mold are interconnected via an inverted T-shaped metal fitting 25.

蒸発管33a,33bの末端部に缶囲2と蒸発
管部3との熱膨張差を吸収するループ13が形成
されている。これら蒸発管の末端は、缶囲2の下
端部に固着される管板8に接続され、蒸気は蒸気
集合管9に流れるようになつている。ところで、
蒸発管部3の上端は管寄せ2に接続され、この管
寄せは頭部金物5及び固定金物1aを介して缶囲
2に固定され、一方下端は管板8を介して缶囲2
に固定されているので、本装置の据付け、取外し
に際し缶囲2に外力が作用しても、蒸発管部3に
無理な力が作用することはない。一方缶囲2と蒸
発管部3との温度差により、蒸発管部3が膨張し
た場合、対流伝熱部での蒸発管のUベンド部は小
さな曲率で曲げられており、膨張差を余り吸収で
きないが、蒸発着末端に形成された大きな曲率の
ループ13によつて充分に吸収することができ
る。
A loop 13 is formed at the end of the evaporation tubes 33a, 33b to absorb the difference in thermal expansion between the can enclosure 2 and the evaporation tube section 3. The ends of these evaporation tubes are connected to a tube plate 8 fixed to the lower end of the can enclosure 2, so that steam flows into a steam collecting tube 9. by the way,
The upper end of the evaporator tube section 3 is connected to the header 2, and the header is fixed to the can enclosure 2 via the head fitting 5 and the fixed fitting 1a, while the lower end is connected to the can enclosure 2 via the tube plate 8.
Therefore, even if an external force is applied to the can enclosure 2 during installation or removal of the device, no unreasonable force will be applied to the evaporator tube section 3. On the other hand, when the evaporator tube section 3 expands due to a temperature difference between the can enclosure 2 and the evaporator tube section 3, the U-bend section of the evaporator tube in the convection heat transfer section is bent with a small curvature, and absorbs the difference in expansion. However, it can be sufficiently absorbed by the loop 13 of large curvature formed at the end of the vapor deposition.

次に本発明の組立は、まず環状管寄せ2と蒸発
管部3を2分割した半割り状態で内外面の容接及
び対流伝熱部の組立を行ない、ついで両半割り部
を重ね合せ接続部を外面溶接して1体に組立て
る。この場合、逆T字型金物25(第6図)は対
流伝熱部の中心部にあるので、分割面に位置する
逆T字型金物25の片側を蒸発管33aに溶接す
ることはできないが、この蒸発管33aの他側は
次の逆T字型金物に溶接されているので特に支障
はない。
Next, in the assembly of the present invention, first, the annular header 2 and the evaporator tube part 3 are divided into two halves, and the inner and outer surfaces are joined and the convection heat transfer part is assembled, and then the two halves are overlapped and connected. The parts are welded on the outside and assembled into one body. In this case, since the inverted T-shaped hardware 25 (Fig. 6) is located at the center of the convection heat transfer section, one side of the inverted T-shaped hardware 25 located at the dividing surface cannot be welded to the evaporation tube 33a. Since the other side of this evaporation tube 33a is welded to the next inverted T-shaped metal fitting, there is no particular problem.

この発明の蒸気発生装置は上記のようなもの
で、対流伝熱部の蒸発管を半径方向支持金物で支
持する構成により組立、施工を容易にすることが
でき、またガス流を均一にすることができる。ま
た、蒸発管部の末端部に缶囲と蒸発管部との熱膨
張差吸収用のループを形成したので、本装置の据
付取外しを何らの制約を受けることなく行うこと
ができる。
The steam generator of the present invention is as described above, and has a structure in which the evaporation tube of the convection heat transfer section is supported by radial support hardware, which facilitates assembly and construction, and also makes the gas flow uniform. Can be done. Furthermore, since a loop for absorbing the difference in thermal expansion between the can enclosure and the evaporator tube is formed at the end of the evaporator tube, the device can be installed and removed without any restrictions.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明装置の一実施例を示す縦断面
図、第2図は第1図の−矢視の蒸発管の接合
状体を示す説明図、第3図は対流伝熱部の蒸発管
のUベンド状態及び支持状態を示す説明図、第4
図は第1図−矢視の拡大断面図、第5図、第
6図はそれぞれ3A型及び3B型の蒸発管を支持金
物で支持した状態の拡大説明図である。 1……缶囲、2……環状給水管寄せ、3……蒸
発管部、4……燃焼器、8……管板、9……蒸気
集合管、11……燃焼排ガス通路、13……ルー
プ、31……蒸発管、32a,32b,33a,
33b……蒸発管、20A,20B……支持金
物、R……放射伝熱部、C……対流伝熱部。
Fig. 1 is a longitudinal sectional view showing an embodiment of the device of the present invention, Fig. 2 is an explanatory view showing a joined body of evaporation tubes in the - arrow direction of Fig. 1, and Fig. 3 is an evaporation of the convection heat transfer section. Explanatory diagram showing the U-bend state and support state of the pipe, No. 4
The figure is an enlarged sectional view taken in the direction of the arrows in FIG. 1, and FIGS. 5 and 6 are enlarged explanatory views of 3A type and 3B type evaporation tubes supported by supporting metal fittings, respectively. DESCRIPTION OF SYMBOLS 1... Can enclosure, 2... Annular water supply pipe header, 3... Evaporator pipe section, 4... Combustor, 8... Tube plate, 9... Steam collecting pipe, 11... Combustion exhaust gas passage, 13... Loop, 31... Evaporation tube, 32a, 32b, 33a,
33b... Evaporation tube, 20A, 20B... Support hardware, R... Radiation heat transfer section, C... Convection heat transfer section.

Claims (1)

【特許請求の範囲】 1 上端部に燃焼器を設けた円筒状缶囲と、この
缶囲内に該缶囲内壁との間に燃焼排ガスの通路と
なる間隙を存して設けられた筒状の蒸発管部と、
この蒸発管部の末端に接続された蒸気集合管とか
らなり、上記蒸発管部は環状給水管寄せに垂設さ
れた多数の蒸発管から構成され、これら蒸発管の
上部は相互に接続され円筒状水冷壁である放射伝
熱部を形成すると共に、下端部で蒸発管は複数本
が1本にまとめられて内側上方にUベンドされて
から更に内側下方にUベンドされて対流伝熱を形
成し、その末端が上記蒸気集合管に接続されてい
るものにおいて、上記対流伝熱部の上下方向にU
ベンドされた蒸発管は半径方向支持金物により缶
軸方向の熱膨張移動を許容しつつ支持されている
ことを特徴とする蒸気発生装置。 2 蒸発管部の末端部に、缶囲と蒸発管部との熱
膨張差吸収用のループが形成されている特許請求
の範囲第1項に記載の蒸気発生装置。
[Scope of Claims] 1. A cylindrical can housing provided with a combustor at its upper end, and a cylindrical can housing provided with a gap between the can housing and the inner wall of the can housing to serve as a passage for combustion exhaust gas. an evaporation pipe section;
The evaporator tube section is composed of a steam collecting pipe connected to the end of the evaporator tube section, and the evaporator tube section is composed of a large number of evaporator tubes vertically installed on the annular water supply pipe header. In addition to forming a radiant heat transfer section that is a water-cooled wall, multiple evaporation tubes are combined into one at the lower end and are U-bended inward and upward, and then further inward and downward in a U-bend to form convective heat transfer. In the case where the end is connected to the steam collecting pipe, there is a U in the vertical direction of the convection heat transfer section.
1. A steam generator characterized in that the bent evaporator tube is supported by radial supporting metal fittings while allowing thermal expansion movement in the axial direction of the can. 2. The steam generator according to claim 1, wherein a loop for absorbing a difference in thermal expansion between the can enclosure and the evaporator tube is formed at the end of the evaporator tube.
JP8397485A 1985-04-19 1985-04-19 steam generator Granted JPS61243203A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8397485A JPS61243203A (en) 1985-04-19 1985-04-19 steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8397485A JPS61243203A (en) 1985-04-19 1985-04-19 steam generator

Publications (2)

Publication Number Publication Date
JPS61243203A JPS61243203A (en) 1986-10-29
JPH0335563B2 true JPH0335563B2 (en) 1991-05-28

Family

ID=13817510

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8397485A Granted JPS61243203A (en) 1985-04-19 1985-04-19 steam generator

Country Status (1)

Country Link
JP (1) JPS61243203A (en)

Also Published As

Publication number Publication date
JPS61243203A (en) 1986-10-29

Similar Documents

Publication Publication Date Title
JPS62185192A (en) Nuclear reactor pressure vessel
JPS6334395B2 (en)
CN112361866B (en) Intermediate heat exchanger for high-temperature gas cooled reactor
JPH0131118B2 (en)
JPH0335563B2 (en)
US5299535A (en) Furnace buckstay stirrup
US3176761A (en) Heat exchanger
US3446279A (en) Air-cooled radiation recuperator
JPS636596Y2 (en)
JP2989425B2 (en) Heat transfer tube support device
JPS5812045Y2 (en) heat exchanger tube equipment
JPS5915702A (en) Vertical type high-pressure feedwater preheater
JPS60213796A (en) Heat exchanger
JPH0313481B2 (en)
US2681640A (en) Boiler construction
JPH0216084Y2 (en)
JPS5844318B2 (en) Heat exchanger with spiral heat exchanger tubes
JPS6210625Y2 (en)
JPS5912956B2 (en) 2.
JPH0655056U (en) Helical coil heat exchanger
JP2601164Y2 (en) Heat exchanger
JPS6339576Y2 (en)
JPS5816104A (en) Waste heat recovering heat exchanger
JPS636595Y2 (en)
JPH09318042A (en) Boiler device