JP2714904B2 - Spiral heat exchanger - Google Patents

Spiral heat exchanger

Info

Publication number
JP2714904B2
JP2714904B2 JP3337836A JP33783691A JP2714904B2 JP 2714904 B2 JP2714904 B2 JP 2714904B2 JP 3337836 A JP3337836 A JP 3337836A JP 33783691 A JP33783691 A JP 33783691A JP 2714904 B2 JP2714904 B2 JP 2714904B2
Authority
JP
Japan
Prior art keywords
spiral
flow path
heat exchanger
cylinder
main body
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
JP3337836A
Other languages
Japanese (ja)
Other versions
JPH05149686A (en
Inventor
繁 荒古
Original Assignee
株式会社クロセ
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 株式会社クロセ filed Critical 株式会社クロセ
Priority to JP3337836A priority Critical patent/JP2714904B2/en
Publication of JPH05149686A publication Critical patent/JPH05149686A/en
Application granted granted Critical
Publication of JP2714904B2 publication Critical patent/JP2714904B2/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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/04Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being formed by spirally-wound plates or laminae

Description

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

【0001】[0001]

【産業上の利用分野】本発明は渦巻状流路の出入口部の
構成を容易に形成するようになしたスパイラル式熱交換
器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a spiral heat exchanger in which the structure of an inlet / outlet of a spiral flow path is easily formed.

【0002】[0002]

【従来の技術】渦巻状伝熱部の上下に仕切室をもつスパ
イラル式熱交換器は一般に図5、図6に示すように蒸留
塔の頂部に取り付けられる塔頂型コンデンサーとして用
いられている。このスパイラル式熱交換器は上下の仕切
室を、単一円筒にて連結し、渦巻状流路のヘッダーはそ
の円筒内部に半割円筒を溶接にて行い構成している。
2. Description of the Related Art A spiral heat exchanger having partitions above and below a spiral heat transfer section is generally used as a top condenser mounted on the top of a distillation column as shown in FIGS. In this spiral heat exchanger, the upper and lower partitioning chambers are connected by a single cylinder, and the header of the spiral channel is formed by welding a half-cylinder inside the cylinder.

【0003】[0003]

【発明が解決しようとする課題】従って従来のスパイラ
ル式熱交換器においては連結円筒の内部に半割円筒を溶
接にて取り付けるため、連結円筒内に作業者が入って溶
接作業を行わねばならず、このため連結円筒径を小さく
するにも限度がある。またこの溶接作業は狭い空間で行
うため困難が伴うとともにこの連結円筒は上下の仕切室
をつなぐため不可欠であるが、この連結円筒内部の形状
は複雑となり、かつ連結円筒内部で流路断面積が変化し
ているため、この流路内を流れる流体の圧力損失が増大
する。さらに連結円筒内を上昇し、上部仕切室より流下
する流体は渦巻状伝熱部に均一に分散することが望まし
いが、連結円筒内部の渦巻状流路のヘッダー部が流体の
流れを邪魔するので分散が悪くなり、伝熱性能が低下す
る等の欠点がある。
Accordingly, in the conventional spiral heat exchanger, since the half cylinder is attached to the inside of the connecting cylinder by welding, an operator must enter the connecting cylinder to perform the welding operation. Therefore, there is a limit in reducing the diameter of the connecting cylinder. In addition, this welding work is difficult because it is performed in a narrow space, and this connecting cylinder is indispensable because it connects the upper and lower partitioning chambers, but the shape inside this connecting cylinder becomes complicated, and the cross-sectional area of the flow path inside the connecting cylinder is Due to the change, the pressure loss of the fluid flowing in the flow path increases. Further, it is desirable that the fluid that rises in the connecting cylinder and flows down from the upper partition chamber is uniformly dispersed in the spiral heat transfer portion, but the header portion of the spiral flow path inside the connecting cylinder obstructs the flow of the fluid. There are disadvantages such as poor dispersion and poor heat transfer performance.

【0004】本発明は設計上の制約及び工作上の問題点
を解決し、連結管内部の形状を単純化し、流体の圧力損
失を減少し、かつ伝熱部への分散を均一化することを目
的とする。
[0004] The present invention solves design constraints and machining problems, simplifies the shape of the inside of a connecting pipe, reduces pressure loss of fluid, and makes uniform distribution to a heat transfer section. Aim.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、複数枚の板を渦巻状に巻き付
け渦巻状流路と渦巻形の軸方向流路とを交互に配設して
熱交換器本体を形成し、かつこの熱交換器本体内に外円
筒を嵌挿し、この外円筒内に嵌挿した内円筒と外円筒と
の間に環状流路を形成するとともにこの環状流路と渦巻
状流路の中央部とを導通せしめ、かつ内円筒の両端を熱
交換器本体の上下両端部に形成する仕切室に開口せしめ
たことを要旨とする。
SUMMARY OF THE INVENTION The present invention has been made to achieve the above-mentioned object, and a plurality of plates are spirally wound to form a spiral flow path and a spiral axial flow path alternately. To form a heat exchanger main body, and an outer cylinder is inserted into the heat exchanger main body, and an annular flow path is formed between the inner cylinder and the outer cylinder inserted into the outer cylinder. The gist of the invention is that the annular flow path and the center of the spiral flow path are electrically connected, and both ends of the inner cylinder are opened to partition chambers formed at the upper and lower ends of the heat exchanger body.

【0006】[0006]

【作用】渦巻状伝熱部中央に配設される渦巻状流路のヘ
ッダーを、所要径の外円筒内に内円筒を嵌挿し、この内
外両円筒の上下端を上板と下板を溶接して製作するた
め、従来のように狭い円筒内での溶接作業が無くなり、
作業性が良く、かつ連結部の径を自由に制定できる。さ
らに連結管は円筒と単純形状となり、かつ流路断面積の
変化がなくなるので、流体の圧力損失が少なくなり、連
結管内を上昇した流体の仕切室内での分散も良くなり、
渦巻状伝熱部へ均一に流入し、伝熱性能が向上するもの
となる。
[Function] Insert the inner cylinder into the outer cylinder of the required diameter, and insert the upper and lower ends of the inner and outer cylinders into the upper plate and the lower plate by inserting the header of the spiral flow passage arranged in the center of the spiral heat transfer section. Since it is manufactured, welding work in a narrow cylinder as in the past is eliminated,
Workability is good, and the diameter of the connecting portion can be freely set. Furthermore, since the connecting pipe has a simple shape with a cylinder, and there is no change in the cross-sectional area of the flow path, the pressure loss of the fluid is reduced, and the dispersion of the fluid that has risen in the connecting pipe in the partition chamber is improved,
The heat uniformly flows into the spiral heat transfer portion, and the heat transfer performance is improved.

【0007】[0007]

【実施例】以下本発明スパイラル式熱交換器を図示の実
施例にもとづいて説明する。図において1はスパイラル
式熱交換器の本体外管で、所要の径と全長とを有し、こ
の本体外管1内にスパイラル式熱交換器となる熱交換器
本体2を嵌挿して一体とし、この熱交換器本体2に渦巻
状流路a内を流下させる流体の供給口3と吐出口4を本
体外管1を貫通して突設するとともに本体外管1の一端
開口部より供給され、渦巻の軸方向流路b内を流下する
流体の凝縮水吐出口5を本体外管1に突設する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view of a spiral heat exchanger according to the present invention. In the drawing, reference numeral 1 denotes a main body outer tube of a spiral heat exchanger having a required diameter and a total length. A heat exchanger main body 2 serving as a spiral heat exchanger is inserted into the main body outer tube 1 to be integrated therewith. A supply port 3 and a discharge port 4 for a fluid flowing down the spiral flow path a into the heat exchanger main body 2 are provided so as to protrude through the main body outer pipe 1 and supplied from one end opening of the main body outer pipe 1. A condensed water discharge port 5 for the fluid flowing down in the spiral axial flow path b is provided on the outer tube 1 of the main body.

【0008】前記熱交換器本体2は2枚(または4枚)
の金属板21,22を板間に所要流路を形成するための
隙間をあけて対設し、これを渦巻状に巻くとともに、こ
の2枚の金属板21,22の両端縁は図示のように閉鎖
し、金属板21,22に閉鎖され渦巻状に渦巻状流路a
を形成し、この渦巻状流路a,a間に渦巻の軸方向流路
bを配設し、この軸方向流路bは渦巻状となっているけ
れども金属板21,22の端縁部では開放されており、
本体外管1内に供給される流体が自由に流下するように
なし、渦巻状流路aには供給口3より供給される流体が
渦巻状流路にそって流下し、吐出口4より外部へ導き出
される。
The heat exchanger body 2 has two (or four) heat exchangers.
The metal plates 21 and 22 are opposed to each other with a gap for forming a required flow path between the plates, and are spirally wound. Both end edges of the two metal plates 21 and 22 are as shown in the figure. And is closed by the metal plates 21 and 22 and is spirally swirled.
And a spiral axial flow path b is disposed between the spiral flow paths a. The axial flow path b has a spiral shape, but at the edges of the metal plates 21 and 22. It is open,
The fluid supplied into the main body outer tube 1 is made to flow freely. The fluid supplied from the supply port 3 flows down the spiral flow path a along the spiral flow path, and the fluid is supplied from the discharge port 4 to the outside. It is led to.

【0009】この熱交換器本体2の中央にはすなわち2
枚の金属板21,22を渦巻状に巻いた中央部にはこれ
を貫通するようにして外円筒23を配設固定し、この外
円筒23内に所要の流路を形成するよう隙間をあけて小
径の内円筒24を嵌挿し、この内外両円筒23,24の
上下両端を座金状の上板25と下板26を当接し、この
内外両円筒23,24の端縁と上下両板25,26間を
溶着して一体とし、外円筒23、しかも渦巻状流路aと
接する位置に複数の孔を穿孔し、渦巻状流路aの終端部
より外円筒内へすなわち内外両円筒間の環状流路Cへ流
体が流入するようになす。
In the center of the heat exchanger body 2,
An outer cylinder 23 is disposed and fixed at the center where the metal plates 21 and 22 are spirally wound so as to penetrate the center, and a gap is formed in the outer cylinder 23 to form a required flow path. The inner and outer cylinders 23, 24 are fitted with upper and lower plates 25 and 26 at the upper and lower ends of the inner and outer cylinders 23, 24. , 26 are welded together to form an integral body, and a plurality of holes are drilled at a position in contact with the outer cylinder 23 and the spiral flow path a, and from the end of the spiral flow path a into the outer cylinder, that is, between the inner and outer cylinders. Fluid flows into the annular flow path C.

【0010】なお図1、図2の実施例では一方の流体を
渦巻状の熱交換器本体2の渦巻状流路aの外周部より供
給し、順次熱交換しつつ内周側へ流下させて中央部の環
状流路Cを経て吐出口4より器外へ導き出すようにした
が、この流体を環状流路Cより渦巻状流路aの中央部よ
り外周方向へ流下させるように供給することも可能であ
る。
In the embodiment shown in FIGS. 1 and 2, one fluid is supplied from the outer peripheral portion of the spiral flow path a of the spiral heat exchanger body 2 and is caused to flow down to the inner peripheral side while sequentially performing heat exchange. Although the fluid is led out of the discharge port 4 through the central annular flow path C, the fluid may be supplied from the annular flow path C so as to flow downward from the center of the spiral flow path a in the outer peripheral direction. It is possible.

【0011】従って上述の如く構成されるスパイラル式
熱交換器の本体外管1内に供給される他方の流体は内円
筒24内を流通するように下板26と本体外管1間にテ
ーパ状の仕切板27を設けている。このため流体は内円
筒内を下方より上方へ流通し、密閉された上仕切室Rよ
り熱交換器本体2の軸方向流路b内を流下するとき、渦
巻状流路a内を流下される流体のもつ熱エネルギーによ
り金属板21,22を介して熱交換され、所望の冷却ま
たは加熱された後、吐出口5より器外へ排出されるもの
である。なおこの吐出口5は図1に示すように仕切板2
7と熱交換器本体下部との間に設けられ、流体の凝縮液
が仕切板27にて形成される室を経て吐出口5より排出
されるようになす。
Therefore, the other fluid supplied into the main body outer tube 1 of the spiral heat exchanger constructed as described above is tapered between the lower plate 26 and the main body outer tube 1 so as to flow through the inner cylinder 24. Is provided. Therefore, the fluid flows upward from below in the inner cylinder, and flows down in the spiral flow path a when flowing down in the axial flow path b of the heat exchanger body 2 from the sealed upper partition R. The heat is exchanged through the metal plates 21 and 22 by the thermal energy of the fluid, and after being cooled or heated as desired, the fluid is discharged from the discharge port 5 to the outside. The discharge port 5 is provided on the partition plate 2 as shown in FIG.
The condensed liquid of the fluid is provided between the heat exchanger 7 and the lower part of the heat exchanger main body, and is discharged from the discharge port 5 through a chamber formed by the partition plate 27.

【0012】図3、図4に示すものはサーモサイホン式
リボイラーとして用いる実施例を示す。この場合は本体
外管1内に上述の如く構成した熱交換器本体2を配設
し、本体外管1の上下両端を蓋板6,6にて閉鎖し、下
方の仕切室Rに流体の供給口7を、上方の仕切室Rに吐
出口8を夫々突設し、渦巻状流路aにスチームまたは熱
媒を流通させ、軸方向流路b内で流体を熱交換(加熱)
して気化ガスを吐出口8より外部へ導き出すようにする
ものである。
FIGS. 3 and 4 show an embodiment used as a thermosiphon reboiler. In this case, the heat exchanger main body 2 configured as described above is disposed in the main body outer pipe 1, the upper and lower ends of the main body outer pipe 1 are closed by the cover plates 6, 6, and the fluid is supplied to the lower partition chamber R. A supply port 7 is provided with a discharge port 8 protruding from an upper partition R, and steam or a heat medium is circulated through a spiral flow path a to exchange heat (heat) fluid in an axial flow path b.
Thus, the vaporized gas is led out from the discharge port 8 to the outside.

【0013】なお上記実施例では2枚の金属板21,2
2を重ねて渦巻状に巻いて形成したものであるが、この
金属板を4枚重ねて渦巻状に巻き、2つの渦巻状流路
と、2つの軸方向流路の計4つの流路を一体に形成する
スパイラル式熱交換器においても同様に構成することが
できる。
In the above embodiment, the two metal plates 21 and
2 and are spirally formed. The four metal plates are stacked and spirally wound, and two spiral channels and two axial channels, a total of four channels, are formed. A spiral heat exchanger integrally formed can be similarly configured.

【0014】[0014]

【発明の効果】本発明スパイラル式熱交換器は渦巻状伝
熱部中央に配設される渦巻状流路ヘッダーを、所要径の
外円筒内に内円筒を嵌挿し、この内外両円筒の上下端を
上板と下板を溶接して製作するため、連結管は円筒と単
純形状となり、かつ流路断面積の変化がなくなるので、
流体の圧力損失が少なくなり、連結管内を流下した流体
の仕切室内での分散も良くなり、渦巻状伝熱部へ均一に
流入し、伝熱性能が向上するとともに製作が簡易になる
等の利点を有する。
According to the spiral heat exchanger of the present invention, a spiral flow path header provided at the center of the spiral heat transfer portion is provided by inserting an inner cylinder into an outer cylinder having a required diameter, and vertically moving the inner and outer cylinders. Since the end is manufactured by welding the upper plate and the lower plate, the connecting pipe has a simple shape with a cylinder and the cross-sectional area of the flow path does not change, so
Advantages such as reduced pressure loss of fluid, better dispersion of fluid flowing down the connecting pipe in the partitioning chamber, uniform flow into the spiral heat transfer section, improved heat transfer performance and simplified manufacturing Having.

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

【図1】本発明スパイラル式熱交換器の縦断面図であ
る。
FIG. 1 is a longitudinal sectional view of a spiral heat exchanger of the present invention.

【図2】同横断面図である。FIG. 2 is a cross-sectional view of the same.

【図3】サーモサイホン式リボイラーの実施例の縦断面
図である。
FIG. 3 is a longitudinal sectional view of an embodiment of a thermosiphon reboiler.

【図4】同横断面図である。FIG. 4 is a cross-sectional view of the same.

【図5】公知例のスパイラル式熱交換器の縦断面図であ
る。
FIG. 5 is a longitudinal sectional view of a known spiral heat exchanger.

【図6】同横断面図である。FIG. 6 is a transverse sectional view of the same.

【符号の説明】[Explanation of symbols]

1 本体外管 2 熱交換器本体 21 金属板 23 外円筒 24 内円筒 25 上板 26 下板 a 渦巻状流路 b 渦巻形の軸方向流路 c 環状流路 R 仕切室 DESCRIPTION OF SYMBOLS 1 Main body outer tube 2 Heat exchanger main body 21 Metal plate 23 Outer cylinder 24 Inner cylinder 25 Upper plate 26 Lower plate a Spiral flow path b Spiral axial flow path c Annular flow path R Partition chamber

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 複数枚の板を渦巻状に巻き付け渦巻状流
路と渦巻形の軸方向流路とを交互に配設して熱交換器本
体を形成し、かつこの熱交換器本体内に外円筒を嵌挿
し、この外円筒内に嵌挿した内円筒と外円筒との間に環
状流路を形成するとともにこの環状流路と渦巻状流路の
中央部とを導通せしめ、かつ内円筒の両端を熱交換器本
体の上下両端部に形成する仕切室に開口せしめたことを
特徴とするスパイラル式熱交換器。
1. A heat exchanger main body is formed by spirally winding a plurality of plates and alternately providing a spiral flow path and a spiral axial flow path to form a heat exchanger main body. An outer cylinder is inserted, an annular flow path is formed between the inner cylinder and the outer cylinder inserted into the outer cylinder, and the annular flow path and the center of the spiral flow path are electrically connected to each other. A spiral type heat exchanger characterized in that both ends of the spiral heat exchanger are opened to partition chambers formed at upper and lower ends of a heat exchanger body.
JP3337836A 1991-11-26 1991-11-26 Spiral heat exchanger Expired - Fee Related JP2714904B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3337836A JP2714904B2 (en) 1991-11-26 1991-11-26 Spiral heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3337836A JP2714904B2 (en) 1991-11-26 1991-11-26 Spiral heat exchanger

Publications (2)

Publication Number Publication Date
JPH05149686A JPH05149686A (en) 1993-06-15
JP2714904B2 true JP2714904B2 (en) 1998-02-16

Family

ID=18312431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3337836A Expired - Fee Related JP2714904B2 (en) 1991-11-26 1991-11-26 Spiral heat exchanger

Country Status (1)

Country Link
JP (1) JP2714904B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5938243B2 (en) * 2012-03-16 2016-06-22 住友精密工業株式会社 Tower condenser
CN103743277A (en) * 2013-12-24 2014-04-23 苏州欢颜电气有限公司 Heat exchange pipe outer cooling ring

Also Published As

Publication number Publication date
JPH05149686A (en) 1993-06-15

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