JPS6335266Y2 - - Google Patents

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Publication number
JPS6335266Y2
JPS6335266Y2 JP1931983U JP1931983U JPS6335266Y2 JP S6335266 Y2 JPS6335266 Y2 JP S6335266Y2 JP 1931983 U JP1931983 U JP 1931983U JP 1931983 U JP1931983 U JP 1931983U JP S6335266 Y2 JPS6335266 Y2 JP S6335266Y2
Authority
JP
Japan
Prior art keywords
gasket
heat exchanger
spiral
flow path
hole
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
JP1931983U
Other languages
Japanese (ja)
Other versions
JPS59124873U (en
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 filed Critical
Priority to JP1931983U priority Critical patent/JPS59124873U/en
Publication of JPS59124873U publication Critical patent/JPS59124873U/en
Application granted granted Critical
Publication of JPS6335266Y2 publication Critical patent/JPS6335266Y2/ja
Granted legal-status Critical Current

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Description

【考案の詳細な説明】 本考案はスパイラル式熱交換器に係り、横据付
にて使用される場合の空気抜とドレン抜を簡易に
行えるようになしたことを目的とする。
[Detailed Description of the Invention] The present invention relates to a spiral heat exchanger, and an object of the present invention is to enable easy air and drain removal when used in horizontal installation.

従来二流体の熱交換を行う場合、一方の流体も
しくは双方の流体が流下するスパイラル流路間の
隔壁を介して所望の熱交換をする螺旋型(スパイ
ラル式)熱交換器が使用されている。この種の熱
交換器は二枚の金属板を流路となる間隔をあけて
渦巻状に巻収し、この各板の側端縁を交互に異に
して折り曲げ、その折曲先端を隣接板の側面に接
触水密的に溶接して二流路を完全に独立したもの
とし、さらにこの渦巻状に巻収した板の両側面に
ガスケツト、ライニング、カバーを順次当接して
一体としている。従つてこの熱交換器に互いに熱
交換すべき二流体を流下せしめて使用することに
よつて隔壁を通して所望の熱交換が行われる。然
しこのスパイラル式熱交換器を竪てて使用する場
合には、該熱交換器内に封入された空気は流体の
流通によつて即ち各流路内に流体が徐々に満され
ることにより最初から入つていた空気は流体にて
押し上げられ、上方に設けられた空気抜孔より自
然に排出され、又ドレンも下部に設けたドレン孔
より排出される。然し流体の種別や熱交換の方法
等によつては該熱交換器を横に据え付けた状態で
使用することがある。横据付方式では渦巻状の流
路に於て各渦巻部にて空気が貯留され、流体の
1.5m/sec以上の高速流下でないと空気が排出さ
れず、1.5m/sec以下の流速で使用する場合、粘
性の高い流体下では空気の完全排出が不可能であ
る。この各渦巻流路内に空気が残留することはそ
の面積のみ熱交換が行われないデツドスペースと
なり熱交換器の効率が低下すると共に完全に空気
を排出した状態でしか使用できない流体の熱交換
には不適である。また同様にドレンも完全に排出
されず、各渦巻流路に帯留した状態となる。
Conventionally, when performing heat exchange between two fluids, a spiral heat exchanger is used, which performs desired heat exchange through a partition wall between spiral channels through which one or both fluids flow. This type of heat exchanger consists of two metal plates wound together in a spiral shape with a space between them to form a flow path.The side edges of each plate are bent in alternating directions, and the bent ends are connected to the adjacent plate. The two channels are made completely independent by contact welding to the side surfaces of the plate, and the gasket, lining, and cover are sequentially abutted on both sides of the spirally wound plate to form an integral unit. Therefore, the desired heat exchange can be performed through the partition wall by allowing two fluids to exchange heat with each other to flow down into this heat exchanger. However, when this spiral heat exchanger is used vertically, the air sealed inside the heat exchanger is initially drained by the fluid circulation, that is, by gradually filling each flow path with fluid. The air that has entered the tank is pushed up by the fluid and is naturally exhausted from the air vent hole provided at the top, and the drain is also exhausted from the drain hole provided at the bottom. However, depending on the type of fluid, heat exchange method, etc., the heat exchanger may be used in a horizontally installed state. In the horizontal installation method, air is stored in each spiral part of the spiral flow path, and the fluid is
Air cannot be discharged unless the flow rate is at a high speed of 1.5 m/sec or more, and when used at a flow rate of 1.5 m/sec or less, it is impossible to completely discharge the air under highly viscous fluid. If air remains in each spiral flow path, that area becomes a dead space where heat exchange does not take place, reducing the efficiency of the heat exchanger. Not suitable. Similarly, the drain is not completely discharged, but remains trapped in each spiral flow path.

本考案はこれに鑑みてなしたもので、金属板を
所要間隔をおいてスパイラル状に巻収して二流路
を独立してスパイラル状に形成したる熱交換器に
於て、該流路の端部に熱交換器を横置とした場合
ノズルを接続される孔の上部と下部に長孔状をし
た空気抜とドレン用の溝孔を一直線状に設けたガ
スケツトを当接し、このガスケツト外側にカバー
を設けてなることを要旨とする。
The present invention was developed in view of this, and is a heat exchanger in which metal plates are wound up in a spiral shape at a required interval to form two independent flow paths in a spiral shape. When the heat exchanger is placed horizontally at the end, a gasket with elongated air vent and drain slots arranged in a straight line is placed at the top and bottom of the hole to which the nozzle is connected, and this gasket is placed on the outside. The gist is that a cover is provided for the

以下本考案を図示の実施例に基づいて説明す
る。
The present invention will be explained below based on the illustrated embodiments.

図に於て1,2は渦巻状の流路を形成するため
の帯状金属板で、この材質は用途や流体の性状等
によりステンレス鋼、チタニウム、ハステロイ、
ニツケル、モネル、軟鋼等を適宜選択して使用す
ると共に該板1又は2の一方もしくは双方に所定
間隔でデイスタンスピースを突設するか、その他
の方法で両板間を所定の流路となるよう間隔をあ
けてそしてこの金属板1,2を重ねて渦巻状に巻
収するが、この金属板1,2の両側端縁は屈曲し
て流路側端を閉塞するか、又は図示の如く螺旋型
即ち渦巻状に巻収した二金属板の両側端面に各流
路を水密的に分離するためカバー3,4を当接す
るが、このカバー3,4の内面にはガスケツト5
を重ね、この対向するカバー3,4間を圧締する
ことによりガスケツト5に金属板1,2の側端縁
を強圧接せしめるようになし、一方のカバーには
一方の流体を流入もしくは流出せしめるノズル6
を他方のカバーには他方の流体を流入もしくは流
出せしめるノズル7を夫々突設し、このノズル
6,7は各流路A,Bのその中心側と導通せし
め、また流路A,Bの外周側にはノズル8,9を
設け、流路AとBを夫々流通する流体が一方のノ
ズルより流入し、他方より流出するようになす。
In the figure, 1 and 2 are band-shaped metal plates for forming a spiral flow path, and the material may be stainless steel, titanium, Hastelloy, etc. depending on the application and the properties of the fluid.
Nickel, Monel, mild steel, etc. are appropriately selected and used, and distance pieces are protruded from one or both of the plates 1 or 2 at predetermined intervals, or by other methods, a predetermined flow path is formed between the two plates. The metal plates 1 and 2 are stacked at a certain interval and wound up in a spiral shape.The edges on both sides of the metal plates 1 and 2 are either bent to close the channel side ends, or they are spirally wound as shown in the figure. Covers 3 and 4 are brought into contact with both end surfaces of the mold, that is, two metal plates wound in a spiral shape, in order to separate each flow passage in a watertight manner.
By stacking the covers 3 and 4 and pressing the opposite covers 3 and 4, the side edges of the metal plates 1 and 2 are brought into strong pressure contact with the gasket 5, and one fluid is allowed to flow into or out of one cover. Nozzle 6
A nozzle 7 is provided on the other cover to allow the other fluid to flow in or out, respectively, and these nozzles 6 and 7 are brought into communication with the center side of each flow path A and B, and are connected to the outer periphery of each flow path A and B. Nozzles 8 and 9 are provided on the sides so that fluids flowing through channels A and B, respectively, flow in from one nozzle and flow out from the other.

上記ガスケツト5は第2図に示す如く円盤形で
中央にノズル6又は7を突設せしめるための孔5
aが穿孔されると共に渦巻状の流路A,Bの端部
に於て導通されるよう空気抜用の溝孔5bとドレ
ン用の溝孔5cとを設ける。そしてこの溝孔5
b,5cはスパイラル式熱交換器を横置とした場
合ガスケツトの中心を通る鉛直方向に夫々上下に
設けるもので、そして溝孔5bの上端にはカバー
3,4の上部に設けた空気抜と導通せしめ、溝孔
5cは同カバー下部に設けたドレンに導通するよ
うになすものである。
The gasket 5 is disc-shaped as shown in FIG. 2, and has a hole 5 in the center for protruding the nozzle 6 or 7.
A is bored and an air vent slot 5b and a drain slot 5c are provided at the ends of the spiral channels A and B so as to be electrically conductive. And this slot 5
b and 5c are provided above and below in the vertical direction passing through the center of the gasket when the spiral heat exchanger is placed horizontally, and air vents provided at the top of the covers 3 and 4 are provided at the upper end of the slot 5b. The slot 5c is designed to be electrically conductive to a drain provided at the bottom of the cover.

またガスケツト5が第2図に示す如く溝孔5
b,5cが一直線状のものでは流路A,Bを流下
する流体の一部(若干)が互いに混合されること
があり、二流体の混合を避けねばならい場合は異
流体の混合を避けて空気抜ドレン抜を行えるよう
に第3図に示す如き構造のガスケツトが用いられ
る。即ち該図に於てはガスケツト5は少くとも2
枚を重ねて用いられ、一枚のガスケツト5Xは各
流路A,Bの各回巻毎に一つの孔を穿孔した孔穿
板とし、他方のガスケツト5Yは溝孔を有する溝
孔穿板とする。ガスケツト5Xは中心のノズル取
付部の孔5aと外周縁とを結ぶ直線上に、且熱交
換器を横置とした時略鉛直方向に孔5aより上部
と下部に夫々空気抜孔とドレン孔とを穿孔する。
これは一方の流路Aの一回巻毎に一つ又は二つの
孔5l,5mを有するようにして一直線上の孔列
aとbに夫々穿孔し、又この孔列と異なる一直線
の孔列cとa上に同様にして他方の流路Bの一回
巻毎に一又は二つの孔5n,5oを夫々穿孔し、
両流路AとBとはこの千鳥状になした空気抜孔と
ドレン孔とによつて互いに導通しないよう独立し
て形成し、またガスケツトYは前記ガスケツト5
Xと重ねた時各孔列5l,5m,5n,5oと互
いに導通するようにしかも第2図と同様に設けた
一直線長孔状の溝孔5p,5q,5r,5sを
夫々設けて成るものである。従つてこの二枚のガ
スケツトを重ねて使用すると各流路のドレンと空
気抜は独立して行なわれ、両流路内の流体が互い
に混合されることを防ぐことができるものであ
る。
Also, the gasket 5 is connected to the slot 5 as shown in FIG.
If b and 5c are straight, some of the fluids flowing down channels A and B may mix with each other, so if mixing of two fluids must be avoided, avoid mixing different fluids. A gasket having a structure as shown in FIG. 3 is used to allow air and drain to be removed. That is, in the figure, the gasket 5 is at least 2
The gaskets 5X are used in a stacked manner, and one gasket 5X is a perforated plate with one hole per turn for each turn of each channel A and B, and the other gasket 5Y is a perforated plate with slots. . The gasket 5X has an air vent hole and a drain hole above and below the hole 5a, respectively, on a straight line connecting the hole 5a of the center nozzle attachment part and the outer periphery, and in a substantially vertical direction when the heat exchanger is placed horizontally. perforate.
This is done by drilling hole rows a and b in a straight line so that each turn of channel A has one or two holes 5l and 5m, respectively, and a hole row in a straight line different from this hole row. Similarly, one or two holes 5n and 5o are drilled on each turn of the other channel B on c and a, respectively.
The flow paths A and B are formed independently by the staggered air vent holes and drain holes so as not to be electrically connected to each other, and the gasket Y is connected to the gasket 5.
The slot holes 5p, 5q, 5r, and 5s are provided in the same manner as shown in FIG. It is. Therefore, when these two gaskets are used in a stacked manner, each flow path is drained and air vented independently, and it is possible to prevent the fluids in both flow paths from being mixed with each other.

而して本考案による時は隔壁を介してスパイラ
ル状に形成された二つの流路の片端又は両端に熱
交換器を横置とした場合、上下方向になるよう長
孔状の空気抜とドレン用の溝孔を設けたガスケツ
トを当接しているため従来流路内に残留した空気
やドレンも確実に排出することができる利点を有
する。
According to the present invention, when a heat exchanger is placed horizontally at one or both ends of two spiral channels formed through a partition wall, long hole-shaped air vents and drains are installed in the vertical direction. Since the gasket is in contact with the gasket provided with the groove, it has the advantage that the air and drain remaining in the conventional flow path can be reliably discharged.

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

第1図は一部破断した外観図、第2図、第3図
はガスケツトの正面図である。 1,2……金属板、3,4……カバー、5……
ガスケツト、6,7,8,9……ノズル、A,B
……流路。
FIG. 1 is a partially cutaway external view, and FIGS. 2 and 3 are front views of the gasket. 1, 2...metal plate, 3, 4...cover, 5...
Gasket, 6, 7, 8, 9... Nozzle, A, B
...Flow path.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 金属板を所要間隔をおいてスパイラル状に巻収
して二流路を独立してスパイラル状に形成したる
熱交換器に於て、該流路の端部に熱交換器を横置
とした場合ノズルを接続される孔の上部と下部に
長孔状をした空気抜とドレン用の溝孔を一直線状
に設けたガスケツトを当接し、このガスケツト外
側にカバーを設けてなるスパイラル式熱交換器。
In a heat exchanger in which metal plates are wound in a spiral shape at required intervals to form two independent flow paths in a spiral shape, when the heat exchanger is placed horizontally at the end of the flow path. A spiral heat exchanger in which a gasket with elongated air vent and drain slots arranged in a straight line is in contact with the upper and lower parts of the hole to which the nozzle is connected, and a cover is provided on the outside of the gasket.
JP1931983U 1983-02-12 1983-02-12 spiral heat exchanger Granted JPS59124873U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1931983U JPS59124873U (en) 1983-02-12 1983-02-12 spiral heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1931983U JPS59124873U (en) 1983-02-12 1983-02-12 spiral heat exchanger

Publications (2)

Publication Number Publication Date
JPS59124873U JPS59124873U (en) 1984-08-22
JPS6335266Y2 true JPS6335266Y2 (en) 1988-09-19

Family

ID=30150474

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1931983U Granted JPS59124873U (en) 1983-02-12 1983-02-12 spiral heat exchanger

Country Status (1)

Country Link
JP (1) JPS59124873U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016063399A1 (en) * 2014-10-23 2016-04-28 中国電力株式会社 Gasifier using supercritical fluid and gasification method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016063399A1 (en) * 2014-10-23 2016-04-28 中国電力株式会社 Gasifier using supercritical fluid and gasification method
JPWO2016063399A1 (en) * 2014-10-23 2017-04-27 中国電力株式会社 Gasification apparatus and gasification method using supercritical fluid

Also Published As

Publication number Publication date
JPS59124873U (en) 1984-08-22

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