JP2940489B2 - Double tube coil type steam generator - Google Patents

Double tube coil type steam generator

Info

Publication number
JP2940489B2
JP2940489B2 JP8263647A JP26364796A JP2940489B2 JP 2940489 B2 JP2940489 B2 JP 2940489B2 JP 8263647 A JP8263647 A JP 8263647A JP 26364796 A JP26364796 A JP 26364796A JP 2940489 B2 JP2940489 B2 JP 2940489B2
Authority
JP
Japan
Prior art keywords
tube
pipe
double
coil
fluid
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
Application number
JP8263647A
Other languages
Japanese (ja)
Other versions
JPH1089606A (en
Inventor
敏広 茅原
収 田中
裕一 高橋
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.)
Miura Co Ltd
Original Assignee
Miura Co 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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP8263647A priority Critical patent/JP2940489B2/en
Publication of JPH1089606A publication Critical patent/JPH1089606A/en
Application granted granted Critical
Publication of JP2940489B2 publication Critical patent/JP2940489B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/022Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of two or more media in heat-exchange relationship being helically coiled, the coils having a cylindrical configuration

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、蒸気発生装置に
関するものであり、リボイラ、多重効用缶、吸収式冷凍
機の再生器、アンモニア吸収式の濃縮器等に用いられ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam generator, and is used for a reboiler, a multiple effect can, a regenerator of an absorption refrigerator, an ammonia absorption type concentrator, and the like.

【0002】[0002]

【従来の技術】医療用などで、クリーンな蒸気を発生さ
せるためのリボイラは、加熱源として蒸気を用い、蒸気
で純水を加熱するようになっている。その構造として
は、シェルアンドチューブ型のものが広く用いられてい
る。
2. Description of the Related Art A reboiler for generating clean steam for medical use uses steam as a heating source and heats pure water with the steam. As its structure, a shell-and-tube type is widely used.

【0003】[0003]

【発明が解決しようとする課題】上述のシェルアンドチ
ューブ型のリボイラは、液相の停滞域があるため熱伝達
が充分でなく、また、加工工数がかかりコスト的にも高
価なものとなっている。この発明は、熱伝達の向上と装
置の小型化を図り、加工工数を大幅に低減した蒸気発生
装置を提供とすることを目的としている。
The above-mentioned shell and tube type reboiler has a problem that the heat transfer is not sufficient due to the stagnation area of the liquid phase, and the number of processing steps is high and the cost is high. I have. SUMMARY OF THE INVENTION An object of the present invention is to provide a steam generator in which heat transfer is improved and the size of the device is reduced, and the number of processing steps is significantly reduced.

【0004】[0004]

【課題を解決するための手段】この発明は、上述の課題
に鑑みてなされたもので、外管内に内管を同心円状に挿
入した二重管をコイル状に巻回して立設し、前記外管と
前記内管との間の流通路に加熱流体を上方から下方に向
かって流通させ、前記内管内に被加熱流体を下方から上
方に向かって流通させることを第1の特徴としている。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and has a structure in which a double pipe in which an inner pipe is inserted concentrically in an outer pipe is wound up in a coil shape and stands up. The first feature is that a heating fluid is caused to flow from above to below in a flow passage between the outer tube and the inner tube, and a fluid to be heated is caused to flow from below to above in the inner tube.

【0005】また、この発明は、外管内に内管を同心円
状に挿入した二重管をコイル状に巻回して立設し、前記
外管および前記内管のうちどちらか一方または両方の断
面を略楕円形状とし、その長径方向を鉛直方向に設定
し、前記外管と前記内管との間の流通路に加熱流体を、
前記内管内に被加熱流体をそれぞれ流通させることを第
2の特徴としている。
Further, according to the present invention, a double tube in which an inner tube is concentrically inserted into an outer tube is wound in a coil shape and erected, and a cross section of one or both of the outer tube and the inner tube is provided. A substantially elliptical shape, the major axis direction is set to the vertical direction, heating fluid in the flow passage between the outer tube and the inner tube,
A second feature is that the fluids to be heated are respectively circulated in the inner pipe.

【0006】また、この発明は、外管内に内管を同心円
状に挿入した二重管を複数本備え、この複数本の二重管
を上下方向に多段に配置してコイル状に巻回し、前記外
管と前記内管との間の流通路に加熱流体を、前記内管内
に被加熱流体をそれぞれ流通させることを第3の特徴と
している。
The present invention also provides a plurality of double tubes in which an inner tube is concentrically inserted into an outer tube, and the plurality of double tubes are arranged in multiple stages in a vertical direction and wound in a coil shape. A third feature is that a heating fluid flows through a flow passage between the outer pipe and the inner pipe, and a fluid to be heated flows through the inner pipe.

【0007】また、この発明は、外管内に内管を同心円
状に挿入した二重管をコイル状に巻回して立設し、この
コイル形状のコイル径を、一端から他端に向かって漸次
増大させて形成し、前記外管と前記内管との間の流通路
に加熱流体を、前記内管内に被加熱流体をそれぞれ流通
させることを第4の特徴としている。
Further, according to the present invention, a double tube in which an inner tube is concentrically inserted into an outer tube is wound in a coil shape and erected, and the coil diameter of the coil shape is gradually increased from one end to the other end. The fourth feature is that the heating fluid is flowed through the flow passage between the outer pipe and the inner pipe, and the fluid to be heated is flowed through the inner pipe.

【0008】また、この発明は、外管内に内管を同心円
状に挿入した二重管をコイル状に巻回して立設し、この
コイル形状の中央空間部にセパレータを設置し、前記内
管の下流側端部を前記セパレータに連通させ、前記外管
と前記内管との間の流通路に加熱流体を、前記内管内に
被加熱流体をそれぞれ流通させることを第5の特徴とし
ている。
The present invention also provides a double tube in which an inner tube is concentrically inserted into an outer tube and wound up in a coil shape to stand up, and a separator is installed in a center space of the coil shape. A fifth feature is that a downstream end of the fluid is communicated with the separator, and a heating fluid flows through a flow passage between the outer pipe and the inner pipe, and a fluid to be heated flows through the inner pipe.

【0009】[0009]

【発明の実施の形態】外管内に内管を同心円状に挿入し
て二重管を構成し、この二重管をコイル状に巻回して立
設する。外管と内管との間の流通路に加熱流体を上方か
ら下方に向かって流通させ、内管内に被加熱流体を下方
から上方に向かって流通させて、両者の間で熱交換を行
う。加熱流体としては蒸気を、被加熱流体としては純水
を用いる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A double pipe is constructed by concentrically inserting an inner pipe into an outer pipe, and the double pipe is wound up in a coil shape and erected. Heating fluid is caused to flow from the upper part to the lower part in the flow passage between the outer pipe and the inner pipe, and the fluid to be heated is made to flow from the lower part to the upper part in the inner pipe, thereby performing heat exchange between the two. Steam is used as the heating fluid, and pure water is used as the fluid to be heated.

【0010】前記コイル形状の中央空間部にセパレータ
を設置し、前記内管の下流側端部をセパレータに連通さ
せる。純水は加熱されて蒸気になり、セパレータに流入
する。セパレータで液滴を分離された蒸気は、外部の蒸
気使用機器に送られ、分離された液滴は、セパレータの
底部より前記内管の上流側端部に還流される。
A separator is provided in the central space of the coil shape, and a downstream end of the inner pipe communicates with the separator. The pure water is heated to become steam and flows into the separator. The vapor from which the droplets are separated by the separator is sent to an external steam-using device, and the separated droplets are returned from the bottom of the separator to the upstream end of the inner tube.

【0011】前記外管および前記内管のうちどちらか一
方または両方の断面を略楕円形状とし、その長径方向を
鉛直方向に設定する。すなわち、縦長の楕円形状とす
る。そうすることにより、加熱流体としての蒸気が凝縮
したとき、その凝縮水が下方へ分離されやすくなる。し
たがって、内管の外壁面に形成される水膜を薄くするこ
とができ、水膜により熱伝達が阻害されるのを防止する
ことができる。
One or both of the outer tube and the inner tube have a substantially elliptical cross section, and the major axis direction is set in the vertical direction. That is, it is a vertically long elliptical shape. By doing so, when the steam as the heating fluid condenses, the condensed water is easily separated downward. Therefore, the water film formed on the outer wall surface of the inner tube can be made thinner, and it is possible to prevent heat transfer from being hindered by the water film.

【0012】前記二重管は1本でもよいが、複数本にす
ることもできる。この複数本の二重管は、上下方向に多
段に配置してコイル状に巻回する。この構造にすると、
各二重管の傾斜角をより大きくすることができ、自然循
環のみで高い循環比を得ることができる(2以上)。
The number of the double tubes may be one, but may be plural. The plurality of double tubes are arranged in multiple stages in the vertical direction and wound in a coil shape. With this structure,
The inclination angle of each double pipe can be made larger, and a high circulation ratio can be obtained only by natural circulation (2 or more).

【0013】前記二重管のコイル形状は、コイル径を一
端から他端まで同一にした平行状のコイル形状としても
よいが、コイル径を一端から他端に向かって漸次増大さ
せて形成し、テーパ形状とすることもできる。二重管は
円筒状の型に巻き付けてコイル形状に成形するが、テー
パ状の型を用いることにより、型と二重管との離脱が容
易になる。
[0013] The coil shape of the double tube may be a parallel coil shape having the same coil diameter from one end to the other end, but is formed by gradually increasing the coil diameter from one end to the other end. It can also be tapered. Although the double pipe is wound around a cylindrical mold and formed into a coil shape, the use of a tapered mold facilitates separation between the mold and the double pipe.

【0014】この発明の二重管コイル式蒸気発生装置
は、リボイラ、多重効用缶、吸収式冷凍機の再生器、ア
ンモニア吸収式の濃縮器等に適用することができる。
The double-tube coil type steam generator of the present invention can be applied to a reboiler, a multiple effect can, a regenerator of an absorption refrigerator, an ammonia absorption type concentrator, and the like.

【0015】[0015]

【実施例】以下、この発明の好ましい実施例を図面に基
づいて説明する。図1は、この発明の一実施例を示す正
面図、図2はその平面図(ライン構成省略)である。外
管2内に内管3を同心円状に挿入して二重管1を構成
し、この二重管1をコイル状に巻回して立設している。
図示した実施例では、2本の二重管1を設け、上下方向
に多段に配置してコイル状に巻回している。すなわち、
2本の二重管1が上下方向に交互に配列された構成にな
っている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a front view showing an embodiment of the present invention, and FIG. 2 is a plan view thereof (line configuration omitted). The inner tube 3 is concentrically inserted into the outer tube 2 to form the double tube 1, and the double tube 1 is wound up in a coil shape and stands upright.
In the illustrated embodiment, two double tubes 1 are provided, arranged in multiple stages in the vertical direction, and wound in a coil shape. That is,
It has a configuration in which two double tubes 1 are alternately arranged in the vertical direction.

【0016】外管2と内管3との間の流通路4に加熱流
体を上方から下方に向かって流通させ、内管3内に被加
熱流体を下方から上方に向かって流通させて、両者の間
で熱交換を行うようにしている。加熱流体としては蒸気
を、被加熱流体としては純水を用いる。給水としての純
水の水質を維持するために、内管3の材質としては耐腐
食性の高いステンレス鋼を用いる。外管2の材質として
は、STPG等の通常の鉄鋼材料を用いる。
The heating fluid is caused to flow from above to below in the flow passage 4 between the outer pipe 2 and the inner pipe 3, and the fluid to be heated is caused to flow from below to upper in the inner pipe 3. Heat exchange between the two. Steam is used as the heating fluid, and pure water is used as the fluid to be heated. In order to maintain the quality of pure water as feed water, stainless steel having high corrosion resistance is used as the material of the inner pipe 3. As a material of the outer tube 2, a normal steel material such as STPG is used.

【0017】外管2の上流側端部に外管用上部ヘッダ6
を、外管2の下流側端部に外管用下部ヘッダ7をそれぞ
れ接続している。前記外管用上部ヘッダ6には加熱流体
供給ライン8を接続し、この加熱流体供給ライン8に加
熱流体の供給量を制御する電動弁9を挿入している。前
記外管用上部ヘッダ6には、加熱流体の圧力(外管2内
の圧力)を検出する圧力センサ10を設けている。前記
外管用下部ヘッダ7には、凝縮水を排出するために、ス
チームトラップ11を挿入した排出ライン12を接続し
ている。
At the upstream end of the outer tube 2, an upper header 6 for the outer tube is provided.
Are connected to the downstream end of the outer tube 2 with the lower header 7 for the outer tube. A heating fluid supply line 8 is connected to the upper header 6 for the outer pipe, and an electric valve 9 for controlling the supply amount of the heating fluid is inserted into the heating fluid supply line 8. The upper header 6 for the outer pipe is provided with a pressure sensor 10 for detecting the pressure of the heating fluid (the pressure in the outer pipe 2). A discharge line 12 in which a steam trap 11 is inserted is connected to the outer pipe lower header 7 for discharging condensed water.

【0018】内管3の上流側端部は、前記外管用下部ヘ
ッダ7を貫通して突出させ、内管用下部ヘッダ13を接
続し、内管3の下流側端部は、前記外管用上部ヘッダ6
を貫通して突出させ、内管用上部ヘッダ14を接続して
いる。前記内管用下部ヘッダ13には、被加熱流体を供
給する給水ライン15を接続し、この給水ライン15に
は、給水ポンプ16と、前記排出ライン12と熱交換を
行い凝縮水から熱回収する給水加熱器17とが設けられ
ている。一方、前記内管用上部ヘッダ14には、蒸気中
の液滴を分離するセパレータ5を連絡管18を介して接
続している。このセパレータ5の頂部には、蒸気弁19
を挿入した蒸気ライン20を接続している。また、セパ
レータ5には、内部の圧力を検出する圧力センサ21を
設けている。セパレータ5の底部には戻り管22を接続
し、この戻り管22の一端を前記内管用下部ヘッダ13
に連結し、セパレータ5で分離した分離水を内管3の上
流側端部に戻し、循環させるようにしている。前記セパ
レータ5は、二重管1で形成したコイル形状の中央空間
部に設置してあり、省スペース化を図っている。
The upstream end of the inner pipe 3 is projected through the lower header 7 for the outer pipe to connect to the lower header 13 for the inner pipe. The downstream end of the inner pipe 3 is connected to the upper header 7 for the outer pipe. 6
And projecting therethrough to connect the upper header 14 for the inner tube. A water supply line 15 for supplying a fluid to be heated is connected to the lower header 13 for the inner pipe. The water supply line 15 exchanges heat with a water supply pump 16 and the discharge line 12 to recover heat from condensed water. A heater 17 is provided. On the other hand, the separator 5 for separating the droplets in the vapor is connected to the upper header 14 for the inner pipe via a communication pipe 18. The top of the separator 5 has a steam valve 19
Is connected to the steam line 20. Further, the separator 5 is provided with a pressure sensor 21 for detecting an internal pressure. A return pipe 22 is connected to the bottom of the separator 5, and one end of the return pipe 22 is connected to the lower header 13 for the inner pipe.
The separated water separated by the separator 5 is returned to the upstream end of the inner pipe 3 and circulated. The separator 5 is provided in a coil-shaped central space formed by the double pipe 1 to save space.

【0019】外管2および内管3の断面形状は略円形状
としてもよいが、図3に示すように、外管2および内管
3のうちどちらか一方または両方の断面を略楕円形状と
することもできる。この楕円形状は、縦長の楕円形状と
し、その長径方向を鉛直方向に設定している。そうする
ことにより、加熱流体としての蒸気が凝縮したとき、そ
の凝縮水が下方へ分離されやすくなり、内管3の外壁面
に形成される水膜を薄くすることができる。したがっ
て、水膜により熱伝達が阻害されるのを防止することが
できる。
The cross section of the outer pipe 2 and the inner pipe 3 may be substantially circular, but as shown in FIG. 3, one or both of the cross sections of the outer pipe 2 and the inner pipe 3 are substantially elliptical. You can also. The elliptical shape is a vertically long elliptical shape, and its major axis direction is set to the vertical direction. By doing so, when the steam as the heating fluid is condensed, the condensed water is easily separated downward, and the water film formed on the outer wall surface of the inner pipe 3 can be thinned. Therefore, it is possible to prevent the heat transfer from being hindered by the water film.

【0020】以下、上述の実施例について、その作用を
説明する。被加熱流体としての純水(圧力約2kg/cm2
が、給水ライン15より内管用下部ヘッダ13を介して
内管3内に供給され、加熱流体としての蒸気(圧力約5
kg/cm2)が、加熱流体供給ライン8より外管用上部ヘッ
ダ6を介して外管2内、すなわち流通路4に供給され
る。被加熱流体は、内管3に沿って螺旋状に流動しなが
ら上昇し、加熱流体は、流通路4に沿って螺旋状に流動
しながら下降する。そして、両者の間で、内管3の壁面
を通して熱交換が行われ、被加熱流体としての純水は加
熱されて蒸気(クリーン蒸気)になる。蒸気は、内管用
上部ヘッダ14、連絡管18を通ってセパレータ5に接
線方向に流入し、旋回運動の遠心力により液滴を分離さ
れて、蒸気ライン20より流出する。分離された液滴
は、戻り管22を通って内管用下部ヘッダ13に戻る。
一方、加熱流体としての蒸気は熱を奪われて凝縮水とな
り、外管用下部ヘッダ7を介して排出ライン12より排
出される。このとき、排出される高温の凝縮水は、給水
加熱器17通過時に給水と熱交換を行い、給水を予熱す
るようになっている(なおかつ、凝縮水の大気開放時の
フラッシングを防止している)。
The operation of the above embodiment will be described below. Pure water as the fluid to be heated (pressure about 2kg / cm 2 )
Is supplied from the water supply line 15 into the inner pipe 3 through the lower header 13 for the inner pipe, and steam (pressure of about 5
kg / cm 2 ) is supplied from the heating fluid supply line 8 to the inside of the outer tube 2, that is, to the flow passage 4 through the upper header 6 for the outer tube. The fluid to be heated rises while flowing spirally along the inner pipe 3, and the heated fluid descends while flowing spirally along the flow passage 4. Then, heat exchange is performed between the two through the wall surface of the inner pipe 3, and the pure water as the fluid to be heated is heated to become steam (clean steam). The steam flows tangentially into the separator 5 through the upper header 14 for the inner pipe and the connecting pipe 18, the droplets are separated by the centrifugal force of the swirling motion, and flows out from the steam line 20. The separated droplets return to the inner tube lower header 13 through the return tube 22.
On the other hand, the steam as the heating fluid is deprived of heat and becomes condensed water, and is discharged from the discharge line 12 via the outer pipe lower header 7. At this time, the discharged high-temperature condensed water exchanges heat with the feed water when passing through the feed water heater 17 so as to preheat the feed water (in addition, the flushing of the condensed water at the time of opening to the atmosphere is prevented. ).

【0021】加熱流体としての蒸気を、内管3の外壁面
に沿って内管3の軸方向に流動させているので、その速
度を速くすることができ、蒸気流動時の剪断力によって
凝縮水膜が薄くなり、熱抵抗を低減することができる。
また、外管2および内管3の断面形状を縦長の楕円形状
とすることにより、凝縮した蒸気が下方に分離されやす
くなり、特に内管3の外壁面の凝縮水膜を薄くすること
ができ、水膜により熱伝達が阻害されるのを防止するこ
とができる。
Since the steam as the heating fluid is caused to flow in the axial direction of the inner tube 3 along the outer wall surface of the inner tube 3, the speed can be increased, and the condensed water is generated by the shearing force when the steam flows. The film becomes thin, and the thermal resistance can be reduced.
In addition, when the cross-sectional shapes of the outer pipe 2 and the inner pipe 3 are vertically long elliptical shapes, the condensed steam is easily separated downward, and the condensed water film on the outer wall surface of the inner pipe 3 can be particularly thinned. In addition, it is possible to prevent heat transfer from being hindered by the water film.

【0022】内管3内においては、被加熱流体としての
純水が沸騰しながら二相流となって増速するため、伝熱
性がよい。また、内管3内においては、図3に矢印で示
すように、遠心力による二次流れが生じ、被加熱流体が
上下方向へ分離した流れとなり、二相伝熱がより促進さ
れる。
In the inner pipe 3, since pure water as a fluid to be heated boils and forms a two-phase flow while increasing the speed, the heat conductivity is good. Further, in the inner pipe 3, as shown by an arrow in FIG. 3, a secondary flow is generated due to the centrifugal force, and the fluid to be heated is a vertically separated flow, and the two-phase heat transfer is further promoted.

【0023】実験によれば、この発明の蒸気発生装置に
おける熱貫流率は約2800kcal/m2h℃となり、従来のシェ
ルアンドチューブ型のものと比較して約40%も向上し
ている。また、加熱流体と被加熱流体との温度差が低く
ても、高い熱貫流率を維持する傾向があり、非常に優れ
た伝熱性能を得ることができる。
According to experiments, the heat transmission coefficient of the steam generator of the present invention is about 2800 kcal / m 2 h ° C., which is about 40% higher than that of the conventional shell and tube type. Further, even if the temperature difference between the heating fluid and the fluid to be heated is low, there is a tendency to maintain a high heat transmission coefficient, and extremely excellent heat transfer performance can be obtained.

【0024】また、複数本の二重管1を、上下方向に多
段に配置してコイル状に巻回した構成にすることによ
り、各二重管1の傾斜角をより大きくすることができ、
自然循環のみで高い循環比を得ることができる(2以
上)。したがって、管内温度が均一化され、急激な負荷
変動に対して自己蒸発量が増加する。また、防食、スケ
ール付着等の管内の水処理についても、局部腐食、局部
濃縮が抑制される。
Further, by arranging a plurality of double tubes 1 in multiple stages in the vertical direction and winding them in a coil shape, the inclination angle of each double tube 1 can be further increased.
A high circulation ratio can be obtained only by natural circulation (2 or more). Therefore, the temperature in the pipe is made uniform, and the amount of self-evaporation increases with rapid load fluctuation. In addition, local corrosion and local concentration are also suppressed in water treatment in a pipe such as anticorrosion and scale adhesion.

【0025】この発明の二重管1は、外管2内に内管3
を挿入固定した後、円筒状の型に巻き付けてコイル状に
成形するため、従来のシェルアンドチューブ型のものと
比較して、加工工数を大幅に低減することができる。ま
た、重さの上でも軽量化が可能である。さらに、この発
明の蒸気発生装置は、保有水量が少なく安全性が高いと
ともに、高温・高圧の蒸気発生装置にも適用が可能であ
る。
The double pipe 1 of the present invention comprises an inner pipe 3 inside an outer pipe 2.
After being inserted and fixed, it is wound around a cylindrical mold to form a coil, so that the number of processing steps can be greatly reduced as compared with the conventional shell and tube type. Further, the weight can be reduced even in terms of weight. Further, the steam generator of the present invention has a small amount of water and a high safety, and is applicable to a high-temperature and high-pressure steam generator.

【0026】図4は、この発明における二重管1の他の
実施例を示すもので、コイル径を一端から他端に向かっ
て漸次増大させて形成し、テーパ形状としている。この
形状は、二重管1を巻き付ける型をテーパ状にすること
により成形することができるが、型と二重管1との離脱
が容易になるというメリットがある。図示した実施例で
は、コイル径を上から下に向かって漸次増大させて形成
しているが、その逆に、コイル径を下から上に向かって
漸次増大させて形成することもできる。テーパ角θは約
5〜60°に設定する。
FIG. 4 shows another embodiment of the double tube 1 according to the present invention, in which the coil diameter is gradually increased from one end to the other end, and is formed in a tapered shape. This shape can be formed by making the mold around which the double pipe 1 is wound into a tapered shape, but has an advantage that the mold and the double pipe 1 can be easily separated. In the illustrated embodiment, the coil diameter is formed so as to gradually increase from the top to the bottom. Conversely, the coil diameter may be formed to gradually increase from the bottom to the top. The taper angle θ is set to about 5 to 60 °.

【0027】[0027]

【発明の効果】この発明は、以上のように、外管内に内
管を同心円状に挿入した二重管をコイル状に巻回して立
設し、外管と内管との間の流通路に加熱流体を上方から
下方に向かって流通させ、内管内に被加熱流体を下方か
ら上方に向かって流通させる構成とし、また、外管およ
び前記内管のうちどちらか一方または両方の断面を略楕
円形状とすることにより、伝熱性能を大幅に向上させる
ことができる。製造時においても、従来のものと比較し
て、加工工数を大幅に低減することができる。
As described above, according to the present invention, a double pipe having an inner pipe inserted concentrically inside an outer pipe is wound up in a coil shape and erected to form a flow passage between the outer pipe and the inner pipe. The heating fluid is allowed to flow downward from above, and the fluid to be heated is allowed to flow upward from below in the inner tube.The cross section of one or both of the outer tube and the inner tube is approximately By making the shape elliptical, the heat transfer performance can be significantly improved. Also at the time of manufacturing, the number of processing steps can be significantly reduced as compared with the conventional one.

【0028】複数本の二重管を上下方向に多段に配置し
てコイル状に巻回した構成にすることにより、各二重管
の傾斜角をより大きくすることができ、自然循環のみで
高い循環比を得ることができる。コイル形状のコイル径
を一端から他端に向かって漸次増大させて形成し、テー
パ形状とすることにより、成形時における型と二重管の
離脱が容易になる。コイル形状の中央空間部にセパレー
タを設置することにより、全体の構成をコンパクトにす
ることができ、省スペース化を図ることができる。
By arranging a plurality of double pipes in multiple stages in the vertical direction and winding them in a coil shape, the inclination angle of each double pipe can be made larger, and high with only natural circulation. A circulation ratio can be obtained. By forming the coil shape such that the coil diameter is gradually increased from one end to the other end and is formed in a tapered shape, the mold and the double tube can be easily separated at the time of molding. By installing the separator in the central space of the coil shape, the overall configuration can be made compact and space can be saved.

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

【図1】この発明の一実施例を示す正面図である。FIG. 1 is a front view showing an embodiment of the present invention.

【図2】図2の平面図(ライン構成省略)である。FIG. 2 is a plan view of FIG. 2 (line configuration omitted);

【図3】この発明における二重管の拡大断面図である。FIG. 3 is an enlarged sectional view of a double pipe according to the present invention.

【図4】この発明における二重管の他の実施例を示す正
面図である。
FIG. 4 is a front view showing another embodiment of the double pipe according to the present invention.

【符号の説明】[Explanation of symbols]

1 二重管 2 外管 3 内管 4 流通路 5 セパレータ DESCRIPTION OF SYMBOLS 1 Double pipe 2 Outer pipe 3 Inner pipe 4 Flow passage 5 Separator

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平5−44901(JP,A) (58)調査した分野(Int.Cl.6,DB名) F22B 21/28 F22B 1/08 F22B 1/16 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-5-44901 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) F22B 21/28 F22B 1/08 F22B 1 / 16

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 外管2内に内管3を同心円状に挿入した
二重管1をコイル状に巻回して立設し、前記外管2と前
記内管3との間の流通路4に加熱流体を上方から下方に
向かって流通させ、前記内管3内に被加熱流体を下方か
ら上方に向かって流通させることを特徴とする二重管コ
イル式蒸気発生装置。
1. A double tube 1 in which an inner tube 3 is concentrically inserted into an outer tube 2 is wound up in a coil shape and erected, and a flow passage 4 between the outer tube 2 and the inner tube 3 is provided. A double-tube coil-type steam generator characterized in that a heating fluid is caused to flow downward from above and a fluid to be heated is caused to flow inside the inner pipe 3 from below to above.
【請求項2】 外管2内に内管3を同心円状に挿入した
二重管1をコイル状に巻回して立設し、前記外管2およ
び前記内管3のうちどちらか一方または両方の断面を略
楕円形状とし、その長径方向を鉛直方向に設定し、前記
外管2と前記内管3との間の流通路4に加熱流体を、前
記内管3内に被加熱流体をそれぞれ流通させることを特
徴とする二重管コイル式蒸気発生装置。
2. A double tube 1 in which an inner tube 3 is inserted concentrically inside an outer tube 2 is wound up in a coil shape and erected, and one or both of the outer tube 2 and the inner tube 3 are provided. Has a substantially elliptical cross section, and its major axis direction is set in a vertical direction. A heating fluid is supplied to the flow passage 4 between the outer pipe 2 and the inner pipe 3, and a heated fluid is supplied to the inner pipe 3. A double-tube coil-type steam generator characterized by being distributed.
【請求項3】 外管2内に内管3を同心円状に挿入した
二重管1を複数本備え、この複数本の二重管1を上下方
向に多段に配置してコイル状に巻回し、前記外管2と前
記内管3との間の流通路4に加熱流体を、前記内管3内
に被加熱流体をそれぞれ流通させることを特徴とする二
重管コイル式蒸気発生装置。
3. A plurality of double pipes 1 in which an inner pipe 3 is concentrically inserted into an outer pipe 2, and the plurality of double pipes 1 are arranged in multiple stages in a vertical direction and wound in a coil shape. A double-tube coil-type steam generator, wherein a heating fluid flows through a flow passage 4 between the outer pipe 2 and the inner pipe 3, and a fluid to be heated flows through the inner pipe 3.
【請求項4】 外管2内に内管3を同心円状に挿入した
二重管1をコイル状に巻回して立設し、このコイル形状
のコイル径を、一端から他端に向かって漸次増大させて
形成し、前記外管2と前記内管3との間の流通路4に加
熱流体を、前記内管3内に被加熱流体をそれぞれ流通さ
せることを特徴とする二重管コイル式蒸気発生装置。
4. A double tube 1 in which an inner tube 3 is concentrically inserted into an outer tube 2 is wound in a coil shape and erected, and the coil diameter of the coil shape is gradually increased from one end to the other end. A double-tube coil type wherein the heating fluid flows through the flow passage 4 between the outer tube 2 and the inner tube 3 and the fluid to be heated flows through the inner tube 3. Steam generator.
【請求項5】 外管2内に内管3を同心円状に挿入した
二重管1をコイル状に巻回して立設し、このコイル形状
の中央空間部にセパレータ5を設置し、前記内管3の下
流側端部を前記セパレータ5に連通させ、前記外管2と
前記内管3との間の流通路4に加熱流体を、前記内管3
内に被加熱流体をそれぞれ流通させることを特徴とする
二重管コイル式蒸気発生装置。
5. A double tube 1 in which an inner tube 3 is concentrically inserted into an outer tube 2 is wound in a coil shape and erected, and a separator 5 is installed in a center space of the coil shape. The downstream end of the pipe 3 is communicated with the separator 5, and the heating fluid is supplied to the flow passage 4 between the outer pipe 2 and the inner pipe 3 by the inner pipe 3.
A double-tube coil-type steam generator characterized in that a fluid to be heated is circulated inside the steam generator.
JP8263647A 1996-09-11 1996-09-11 Double tube coil type steam generator Expired - Fee Related JP2940489B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8263647A JP2940489B2 (en) 1996-09-11 1996-09-11 Double tube coil type steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8263647A JP2940489B2 (en) 1996-09-11 1996-09-11 Double tube coil type steam generator

Publications (2)

Publication Number Publication Date
JPH1089606A JPH1089606A (en) 1998-04-10
JP2940489B2 true JP2940489B2 (en) 1999-08-25

Family

ID=17392390

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8263647A Expired - Fee Related JP2940489B2 (en) 1996-09-11 1996-09-11 Double tube coil type steam generator

Country Status (1)

Country Link
JP (1) JP2940489B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105757632A (en) * 2016-04-19 2016-07-13 山东豪迈机械制造有限公司 Low-pressure steam generating device
JP7192471B2 (en) * 2018-12-17 2022-12-20 富士電機株式会社 steam generator

Also Published As

Publication number Publication date
JPH1089606A (en) 1998-04-10

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