JPH1123180A - Heat transfer accelerator for heat transfer tube - Google Patents

Heat transfer accelerator for heat transfer tube

Info

Publication number
JPH1123180A
JPH1123180A JP17448697A JP17448697A JPH1123180A JP H1123180 A JPH1123180 A JP H1123180A JP 17448697 A JP17448697 A JP 17448697A JP 17448697 A JP17448697 A JP 17448697A JP H1123180 A JPH1123180 A JP H1123180A
Authority
JP
Japan
Prior art keywords
heat transfer
transfer tube
heat
tube
plate
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.)
Pending
Application number
JP17448697A
Other languages
Japanese (ja)
Inventor
Hitoshi Miyamoto
仁志 宮本
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP17448697A priority Critical patent/JPH1123180A/en
Publication of JPH1123180A publication Critical patent/JPH1123180A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation

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)

Abstract

PROBLEM TO BE SOLVED: To provide a heat transfer accelerator of a heat transfer tube for effectively preventing bypassing of fluid by easily and effectively preventing a gap generated between an inner wall of the tube and a twisted plate. SOLUTION: In the heat transfer accelerator 3 for generating a swirl in fluid flowing in the heat transfer tube 1 by spirally inserting it into the tube 1 of a heat exchanger, a strip plate 2 extended in a lengthwise direction of the tube 1 is twisted to form a spirally twisted plate 2. And, U-shaped sectional springs 4 are integrally provided with both edges of the plate 2 to suppress a gap to the tube 1 by bringing into contact with an inner wall surface side of the tube 1 while urging.

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】本発明は、石油化学プラン
ト、貯蔵プラント等に備えられている熱交換器に係り、
特にその伝熱管の内部に挿入される伝熱促進体に関する
ものである。
The present invention relates to a heat exchanger provided in a petrochemical plant, a storage plant, and the like.
In particular, the present invention relates to a heat transfer enhancer inserted into the heat transfer tube.

【0002】[0002]

【従来の技術】図5に示すように、石油化学プラント、
貯蔵プラント等に備えられているエチレン蒸発器やLP
G蒸発器等の伝熱管1内には、螺旋状の捻り板2が収容
されており、伝熱管1内を流れる流体にスワールを発生
させることで、その流体の伝熱を促進するようになって
いる。
2. Description of the Related Art As shown in FIG.
Ethylene evaporator and LP provided in storage plants, etc.
A helical torsion plate 2 is accommodated in a heat transfer tube 1 such as a G evaporator. By generating a swirl in a fluid flowing in the heat transfer tube 1, heat transfer of the fluid is promoted. ing.

【0003】すなわち、エチレンやLPG等の低沸点流
体をそのまま伝熱管1内に流した場合、低沸点流体が膜
沸騰を起こし、伝熱管1の内壁面と低沸点流体の界面に
低沸点流体の蒸気(Vapor )が層状に集まった流れとな
ってしまい、液側への伝熱係数が著しく低下してしまう
ことがある。そのため、伝熱管1内に捻り板2を収容
し、流体を螺旋状に流して遠心力を発生させることで膜
沸騰の発生を未然に抑制して膜沸騰による伝熱係数の低
下を防止するようにしている。
That is, when a low-boiling fluid such as ethylene or LPG is allowed to flow into the heat transfer tube 1 as it is, the low-boiling fluid causes film boiling, and the low-boiling fluid flows to the interface between the inner wall surface of the heat transfer tube 1 and the low-boiling fluid. Vapor may flow in a layered manner, and the heat transfer coefficient to the liquid side may be significantly reduced. Therefore, the torsion plate 2 is accommodated in the heat transfer tube 1 and a fluid is spirally generated to generate a centrifugal force, thereby suppressing the occurrence of film boiling and preventing a decrease in the heat transfer coefficient due to the film boiling. I have to.

【0004】[0004]

【発明が解決しようとする課題】ところで、この捻り板
2は図6に示すように、断面略直線状をしているため、
伝熱管1及びその内部に収容される捻り板2の隙間が大
きすぎる(例えば、0.5mm以上)と、図7に示すよ
うに、捻り板2の縁部と伝熱管1内壁との間に大きなギ
ャップ(隙間)Gが生じ、このギャップGから流体がパ
イパスしてしまい、この結果、良好なスワールが生成さ
れなくなり、大幅な性能低下が起こることがあった。
Since the torsion plate 2 has a substantially straight cross section as shown in FIG.
If the gap between the heat transfer tube 1 and the torsion plate 2 accommodated therein is too large (for example, 0.5 mm or more), the gap between the edge of the torsion plate 2 and the inner wall of the heat transfer tube 1 as shown in FIG. A large gap (gap) G is generated, and the fluid bypasses the gap G. As a result, good swirl is not generated, and the performance may be greatly reduced.

【0005】そのため、このような隙間を可能な限りな
くすために、伝熱管1の内径dをその都度正確に計った
後、捻り板2の外径(幅)を決定し、これを数種類製作
した上で隙間が最小となるものを選定し施工する必要が
ある。
Therefore, in order to eliminate such a gap as much as possible, the inner diameter d of the heat transfer tube 1 is accurately measured each time, and then the outer diameter (width) of the torsion plate 2 is determined, and several kinds of these are manufactured. It is necessary to select the one with the minimum gap above and construct it.

【0006】従って、一つの捻り板入り伝熱管を製作す
るには、多大な費用と時間を浪費する結果となってい
た。
[0006] Therefore, producing a single heat transfer tube with a twisted plate results in wasting a great deal of cost and time.

【0007】そこで、本発明はこのような課題を有効に
解決するために案出されたものであり、その目的は、伝
熱管内壁と捻り板との間に発生するギャップを容易且つ
確実になくして、バイパス流を確実に防止することがで
きる新規な伝熱管の伝熱促進体を提供するものである。
The present invention has been devised in order to effectively solve such a problem, and an object of the present invention is to eliminate easily and reliably a gap generated between an inner wall of a heat transfer tube and a torsion plate. Accordingly, the present invention provides a novel heat transfer promoting body for a heat transfer tube that can surely prevent a bypass flow.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に本発明は、熱交換器の伝熱管内に螺旋状に挿入されて
その伝熱管内を流れる流体にスワールを発生すべく伝熱
促進体において、上記伝熱管の長さ方向に延びる帯板を
捻って螺旋状の捻り板を形成すると共に、その捻り板の
両縁部に、上記伝熱管の内壁面側に付勢しながら密着し
て上記伝熱管とのキャップを抑制すべく断面U字状のバ
ネ体を一体的に備えたものである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a heat exchanger which is spirally inserted into a heat transfer tube of a heat exchanger to generate a swirl in a fluid flowing through the heat transfer tube. In the body, a helical torsion plate is formed by twisting the strip extending in the length direction of the heat transfer tube, and is closely attached to both edges of the torsion plate while urging the inner wall surface side of the heat transfer tube. Thus, a spring body having a U-shaped cross section is integrally provided to suppress the cap with the heat transfer tube.

【0009】従って、この捻り板が伝熱管内を流れる流
体にスワールを発生させると同時に、この捻り板の両側
に設けられたバネ体がスプリングバック効果により、伝
熱管の内壁面側に密着することで伝熱管内壁と捻り板の
両縁部とのギャップがなくなり、流体のバイパス流を効
果的に防止することができる。さらに、バネ体のスプリ
ングバック効果により、伝熱管促進体の幅を自由に変化
させることができるため、両者の公差を効果的に許容す
ることができる。尚、捻り板自体を断面S字状に形成し
ても同様の効果を得ることができる。
Accordingly, the torsion plate generates a swirl in the fluid flowing in the heat transfer tube, and the spring bodies provided on both sides of the torsion plate are brought into close contact with the inner wall surface of the heat transfer tube due to a springback effect. Thus, the gap between the inner wall of the heat transfer tube and both edges of the torsion plate is eliminated, and the bypass flow of the fluid can be effectively prevented. Further, the width of the heat transfer tube promoting body can be freely changed by the spring back effect of the spring body, so that the tolerance between both can be effectively allowed. The same effect can be obtained even if the torsion plate itself is formed in an S-shaped cross section.

【0010】[0010]

【発明の実施の形態】次に、本発明を実施する好適一形
態を添付図面を参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a preferred embodiment of the present invention will be described with reference to the accompanying drawings.

【0011】図1は本発明に係る伝熱促進体3の実施の
一形態を示したものである。図示するように、この伝熱
促進体3は、伝熱管1内に螺旋状に挿入されるようにな
っており、その内部を流れる流体を伝熱管1の長さ方向
に二分割すると共に、螺旋状に旋回(スワール)させな
がら流すようになっている。
FIG. 1 shows an embodiment of a heat transfer enhancer 3 according to the present invention. As shown in the figure, the heat transfer promoting body 3 is helically inserted into the heat transfer tube 1, and divides a fluid flowing inside the heat transfer tube 1 into two parts in the longitudinal direction of the heat transfer tube 1. It is made to flow while swirling in a shape.

【0012】また、この伝熱促進体3は、ステンレスス
チール等の耐食性金属薄板からなる帯体を螺旋状に捻っ
て加工される捻り板2の両縁部に、それぞれ反対方向に
断面U字状に折り曲げたバネ体4,4を備えたものであ
り、この捻り板2によって伝熱管1内を流れる流体を伝
熱管1の長さ方向に二分割すると共に、バネ体4,4に
よって捻り板2を中心部に支持するようになっている。
また、このバネ体4は、それぞれ捻り板2の幅方向外方
に広がるように付勢されている。そのため、伝熱管1に
挿入される前の伝熱促進体3の外径は、図3に示すよう
に伝熱管1の内径dよりも+αだけ大きく広がるように
なっている。例えば、伝熱管1の内径が20mmとする
と、挿入前の外径が+0.5〜1.0mm程度大きくな
っている。
The heat transfer promoting body 3 has a U-shaped cross section in opposite directions on both edges of the twisted plate 2 formed by spirally twisting a strip made of a corrosion-resistant metal thin plate such as stainless steel. The fluid flowing in the heat transfer tube 1 is divided into two in the longitudinal direction of the heat transfer tube 1 by the torsion plate 2, and the torsion plate 2 is Is supported in the center.
The spring bodies 4 are urged so as to spread outward in the width direction of the torsion plate 2. Therefore, the outer diameter of the heat transfer promoting body 3 before being inserted into the heat transfer tube 1 is larger than the inner diameter d of the heat transfer tube 1 by + α as shown in FIG. For example, when the inner diameter of the heat transfer tube 1 is 20 mm, the outer diameter before insertion is increased by about +0.5 to 1.0 mm.

【0013】そして、このような伝熱促進体3を上述し
たように、例えば、3〜5D(伝熱管の外径)/180
゜のピッチで螺旋状に伝熱管1内に挿入すると、バネ体
4,4のスプリングバック効果によって捻り板2が伝熱
管1内の中央部に支持されて伝熱管1内を均等に二分割
すると同時に、バネ体4,4が伝熱管1内壁に沿って密
着することとなり、これによって図4に示すように伝熱
促進体3の両縁部と伝熱管1内壁とのギャップが解消さ
れて流体のバイパス流が効果的に防止されることにな
る。
Then, as described above, such a heat transfer promoting body 3 is, for example, 3 to 5D (outer diameter of the heat transfer tube) / 180.
When spirally inserted into the heat transfer tube 1 at a pitch of ゜, the torsion plate 2 is supported at the center of the heat transfer tube 1 by the springback effect of the spring bodies 4 and 4, and the inside of the heat transfer tube 1 is equally divided into two. At the same time, the spring bodies 4 and 4 come into close contact with the inner wall of the heat transfer tube 1, thereby eliminating the gap between both edges of the heat transfer promoting body 3 and the inner wall of the heat transfer tube 1 as shown in FIG. Is effectively prevented.

【0014】従って、伝熱促進体3の両面に良好な旋回
流がそれぞれ形成されるため、流体に効果的に遠心力が
加わることとなり、膜沸騰が抑制されて良好な熱交換が
達成される。また、捻り板2の両縁部にバネ体4,4を
備えることにより、伝熱促進体3の幅の大きさをある程
度自由に変えることができるため、従来のように一つの
伝熱管1に対して捻り板2を複数用意する必要が無く、
製作に要する多大な費用と時間を節約することができ
る。
Therefore, since good swirling flows are formed on both surfaces of the heat transfer promoting body 3, respectively, a centrifugal force is effectively applied to the fluid, and film boiling is suppressed and good heat exchange is achieved. . Further, by providing the spring bodies 4 and 4 on both edges of the torsion plate 2, the width of the heat transfer promoting body 3 can be freely changed to some extent. On the other hand, there is no need to prepare a plurality of twisted plates 2,
Significant costs and time required for fabrication can be saved.

【0015】尚、このバネ体4,4は、捻り板2とは別
部材で別個に形成した後、捻り板2の両縁部に溶接など
により接合して形成したり、あるいは、予め幅の大きい
捻り板を用意し、この捻り板の両縁部を熱間加工して屈
曲させて形成するようにしても良い。また、捻り板2を
断面S字形に形成して捻り板2自体にスプリングパック
機能を付加させるようにしても良い。さらに、このバネ
体4,4の屈曲方向をそれぞれ同じ方向になるように形
成しても良い。
The spring members 4 and 4 are formed separately from the torsion plate 2 and then joined to both edges of the torsion plate 2 by welding or the like. A large torsion plate may be prepared, and both edges of the torsion plate may be formed by bending by hot working. Alternatively, the torsion plate 2 may be formed to have an S-shaped cross section so that the torsion plate 2 itself has a spring pack function. Further, the spring members 4 and 4 may be formed so that the bending directions thereof are the same.

【0016】[0016]

【発明の効果】以上要するに本発明によれば、伝熱促進
体と伝熱管内壁とのギャップが簡単且つ確実に解消され
るため、流体のバイパス流が効果的に防止されて良好な
熱交換を行うことができる上に、捻り板の幅方向の大き
さを自由に変えることができるため、従来のように一つ
の伝熱管に対して捻り板を複数用意する必要が無く、製
作に要する多大な費用と時間を節約することができる等
といった優れた効果を発揮することができる。
In summary, according to the present invention, since the gap between the heat transfer promoting body and the inner wall of the heat transfer tube is easily and reliably eliminated, the bypass flow of the fluid is effectively prevented, and good heat exchange is achieved. In addition to being able to perform, the size of the torsion plate in the width direction can be freely changed, so there is no need to prepare a plurality of torsion plates for one heat transfer tube as in the conventional case, which is a great deal of Excellent effects such as saving of cost and time can be exhibited.

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

【図1】本発明に係る伝熱促進体の実施の一形態を示す
側面図である。
FIG. 1 is a side view showing one embodiment of a heat transfer enhancer according to the present invention.

【図2】(A)は図1中X−X断面図である。(B)は
図1中Y−Y断面図である。
FIG. 2A is a sectional view taken along line XX in FIG. FIG. 2B is a sectional view taken along line YY in FIG.

【図3】伝熱管径と伝熱促進体径の関係を示す断面図で
ある。
FIG. 3 is a sectional view showing a relationship between a heat transfer tube diameter and a heat transfer promoting body diameter.

【図4】図2(B)中A部を示す部分拡大図である。FIG. 4 is a partially enlarged view showing a portion A in FIG. 2 (B).

【図5】従来の捻り板を示す側面図である。FIG. 5 is a side view showing a conventional twisted plate.

【図6】(A)は図5中X−X断面図である。(B)は
図5中Y−Y断面図である。
FIG. 6A is a sectional view taken along line XX in FIG. (B) is a sectional view taken along the line YY in FIG. 5.

【図7】図6(B)中A部を示す部分拡大図である。FIG. 7 is a partially enlarged view showing a portion A in FIG. 6 (B).

【符号の説明】[Explanation of symbols]

1 伝熱管 2 捻り板 3 伝熱促進体 4 バネ部 G ギャップ DESCRIPTION OF SYMBOLS 1 Heat transfer tube 2 Twisted plate 3 Heat transfer promoting body 4 Spring part G gap

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱交換器の伝熱管内に螺旋状に挿入され
てその伝熱管内を流れる流体にスワールを発生すべく伝
熱促進体において、上記伝熱管の長さ方向に延びる帯板
を捻って螺旋状の捻り板を形成すると共に、その捻り板
の両縁部に、上記伝熱管の内壁面側に付勢しながら当接
して上記伝熱管とのキャップを抑制すべく断面U字状の
バネ部を一体的に備えたことを特徴とする伝熱管の伝熱
促進体。
1. A heat-transfer accelerating body which is spirally inserted into a heat-transfer tube of a heat exchanger and generates a swirl in a fluid flowing through the heat-transfer tube, a strip extending in the longitudinal direction of the heat-transfer tube. A twisted helical torsion plate is formed, and both sides of the torsion plate are pressed against the inner wall surface side of the heat transfer tube while being in contact with the heat transfer tube to suppress a cap with the heat transfer tube. A heat transfer enhancer for a heat transfer tube, wherein the heat transfer tube is integrally provided with a spring portion.
【請求項2】 熱交換器の伝熱管内に螺旋状に挿入され
てその伝熱管内を流れる流体を螺旋状に流すべく伝熱促
進体において、上記伝熱管の長さ方向に延びる帯板を捻
って螺旋状の捻り板を形成すると共に、その捻り板の断
面形状をS字状に形成して伝熱管に挿入した後にその両
縁部がそれぞれ伝熱管内壁側に密着するようにしたこと
を特徴とする伝熱管の伝熱促進体。
2. A heat-transfer accelerating body which is spirally inserted into a heat-transfer tube of a heat exchanger so as to spirally flow a fluid flowing through the heat-transfer tube, a strip extending in the longitudinal direction of the heat-transfer tube. The twisted helical twisted plate was formed, and the torsion plate was formed in an S-shaped cross-section and inserted into the heat transfer tube so that both edges thereof were brought into close contact with the heat transfer tube inner wall side, respectively. A heat transfer enhancer for heat transfer tubes.
JP17448697A 1997-06-30 1997-06-30 Heat transfer accelerator for heat transfer tube Pending JPH1123180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17448697A JPH1123180A (en) 1997-06-30 1997-06-30 Heat transfer accelerator for heat transfer tube

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17448697A JPH1123180A (en) 1997-06-30 1997-06-30 Heat transfer accelerator for heat transfer tube

Publications (1)

Publication Number Publication Date
JPH1123180A true JPH1123180A (en) 1999-01-26

Family

ID=15979332

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17448697A Pending JPH1123180A (en) 1997-06-30 1997-06-30 Heat transfer accelerator for heat transfer tube

Country Status (1)

Country Link
JP (1) JPH1123180A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104806511A (en) * 2015-05-12 2015-07-29 西南石油大学 Spring type spoiler of long-stroke fracturing pump
JP2019086180A (en) * 2017-11-02 2019-06-06 カルソニックカンセイ株式会社 Double pipe and manufacturing method thereof
CN111065880A (en) * 2017-09-13 2020-04-24 开利公司 Screw insert for shell and tube heat exchanger background

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104806511A (en) * 2015-05-12 2015-07-29 西南石油大学 Spring type spoiler of long-stroke fracturing pump
CN111065880A (en) * 2017-09-13 2020-04-24 开利公司 Screw insert for shell and tube heat exchanger background
JP2019086180A (en) * 2017-11-02 2019-06-06 カルソニックカンセイ株式会社 Double pipe and manufacturing method thereof

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