JPH0534084A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH0534084A JPH0534084A JP21022591A JP21022591A JPH0534084A JP H0534084 A JPH0534084 A JP H0534084A JP 21022591 A JP21022591 A JP 21022591A JP 21022591 A JP21022591 A JP 21022591A JP H0534084 A JPH0534084 A JP H0534084A
- Authority
- JP
- Japan
- Prior art keywords
- heat transfer
- transfer tube
- temperature fluid
- fluid chamber
- high temperature
- 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
Links
- 239000012530 fluid Substances 0.000 claims abstract description 34
- 238000005192 partition Methods 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 abstract description 4
- 230000010485 coping Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008602 contraction Effects 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-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 arranged in parallel spaced relation
- F28D7/163—Heat-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 arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
- F28D7/1638—Heat-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 arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing with particular pattern of flow or the heat exchange medium flowing inside the conduits assemblies, e.g. change of flow direction from one conduit assembly to another one
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-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 having a single U-bend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0236—Header boxes; End plates floating elements
- F28F9/0239—Header boxes; End plates floating elements floating header boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/26—Safety or protection arrangements; Arrangements for preventing malfunction for allowing differential expansion between elements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は化学プラント等に広く
用いられている熱交換器に関する。更に詳しくは多管円
筒型の熱交換器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger widely used in chemical plants and the like. More specifically, it relates to a multi-tube cylindrical heat exchanger.
【0002】[0002]
【従来の技術】従来、多管円筒型熱交換器としては図3
〜図5に示すような各種のものが用いられている。図3
に示すものは固定管板式と言われるもので、同図におい
てaは円筒胴であり、その内部に伝熱管bが設けられ、
この伝熱管bは円筒胴aの両端に設けた高温流体室c及
び同dに連通させられている。一方の高温流体室cに設
けられたeは仕切板、fは高温流体入口、gは同出口、
hは低温流体の入口、iは同出口、jは邪魔板を示す。
又kは固定枠である。そして前記円筒胴aには伸縮継手
lが設けられている。高温流体はその入口fから入り、
円筒胴aの上部の伝熱管bを通り、ついで下部の伝熱管
bに至り、出口gから排出され、その間円筒胴a内の低
温流体を加熱するようになっている。そして、このよう
に形成された装置は作動中に伝熱管bと円筒胴aの熱膨
張の差が大きい場合、前記伸縮継手lが伸縮して自動的
にその差が調節される。次に、図4に示す装置はU字管
式熱交換器であり、伝熱管bが図示のようにU字状に形
成されており、伝熱管bは円筒胴aの両端部でなく、一
端部で固定されているため両者a、b間に熱膨張の差が
あても問題にならない。又図5に示す装置は遊動筒方式
と呼ばれ、伝熱管bの一方に設けられた、高温流体室に
該当する遊動頭mが円筒胴aに対して遊動し得るように
形成されており、これにより伝熱管bと円筒動aの熱膨
張の差に対応できるようになっている。2. Description of the Related Art Conventionally, as a multi-tubular cylindrical heat exchanger, FIG.
~ Various types as shown in Fig. 5 are used. Figure 3
The one shown in Fig. 6 is called a fixed tube plate type, and in the figure, a is a cylindrical body, inside which a heat transfer tube b is provided,
The heat transfer tube b is communicated with the high temperature fluid chambers c and d provided at both ends of the cylindrical body a. One of the high temperature fluid chambers c is provided with a partition plate, f is a high temperature fluid inlet, g is the same outlet,
h is the inlet of the cryogenic fluid, i is the outlet, and j is the baffle.
Further, k is a fixed frame. An expansion joint l is provided on the cylindrical body a. The hot fluid enters through its inlet f,
It passes through the heat transfer tube b in the upper part of the cylindrical body a, then reaches the heat transfer tube b in the lower part, is discharged from the outlet g, and heats the low temperature fluid in the cylindrical body a during that time. If the difference in thermal expansion between the heat transfer tube b and the cylindrical body a is large during operation of the device thus formed, the expansion joint 1 expands and contracts and the difference is automatically adjusted. Next, the device shown in FIG. 4 is a U-shaped tube heat exchanger, and the heat transfer tube b is formed in a U shape as shown in the drawing. Since it is fixed at the part, there is no problem even if there is a difference in thermal expansion between both a and b. The device shown in FIG. 5 is called a floating cylinder type, and is formed so that a floating head m corresponding to a high-temperature fluid chamber provided on one side of the heat transfer tube b can move freely with respect to the cylindrical barrel a. This makes it possible to cope with the difference in thermal expansion between the heat transfer tube b and the cylindrical movement a.
【0003】[0003]
【発明が解決しようとする課題】しかし、上記従来の各
装置はそれぞれ次のような難点を有している。即ち図3
に示す装置は前記伸縮継手lを設けなければならず製造
が面倒である。又この伸縮継手lの場所にスケールが溜
り、次第に伸縮が不可能になる。又そのスケールが腐蝕
の原因となる。又円筒胴の清掃は化学的な方法以外困難
である。又図4に示す装置は伝熱管bにU字状部が形成
されているため、しばしばこのU字状部に摩耗及び腐蝕
を起こす。又U字状伝熱管bの製作は面倒のため制作費
が割高となることが避けられない。However, each of the above-mentioned conventional devices has the following drawbacks. That is, FIG.
The device shown in (1) must be provided with the expansion joint (1), which is troublesome to manufacture. In addition, the scale accumulates at the location of this expansion joint l, and expansion and contraction becomes gradually impossible. In addition, the scale causes corrosion. Moreover, cleaning of the cylinder body is difficult except by a chemical method. Further, in the device shown in FIG. 4, the U-shaped portion is formed in the heat transfer tube b, so that the U-shaped portion is often worn and corroded. In addition, the manufacturing cost of the U-shaped heat transfer tube b is inevitable because the manufacturing cost is high.
【0004】又図5に示す装置は遊胴頭mの胴内部のフ
ランジnの部分から洩れの起こる恐れを有する。又構造
が複雑となるため製作費が高価となる。この発明はこの
ような種々の問題を解決するためになされたもので、そ
の目的は伸縮継手lを省略でき、従ってその部分にスケ
ールの溜るのを防止でき、かつ又円筒胴aの掃除が容易
にでき、又伝熱管bにU字状部を形成せずにすみ、従っ
て摩耗の恐れがない、又遊胴頭mを形成せずにすみ、掃
除の容易な、かつ製作費も割高となることのない熱交換
器を提供することである。Further, the apparatus shown in FIG. 5 has a risk of leakage from a portion of the flange n inside the barrel of the idler head m. In addition, the structure is complicated and the manufacturing cost is high. The present invention has been made in order to solve such various problems, and its purpose is to omit the expansion joint l, so that the scale can be prevented from accumulating in that portion, and the cylindrical body a can be easily cleaned. In addition, the heat transfer tube b need not be formed with a U-shaped portion, and therefore there is no fear of wear, and the idler head m need not be formed, which is easy to clean and the manufacturing cost is high. It is to provide a heat exchanger that does not exist.
【0005】[0005]
【課題を解決するための手段】上記の目的を達成するこ
の発明について述べるとそれは、仕切板により仕切ら
れ、高温流体の入口及び同出口を有する高温流体室に複
数の伝熱管の一端を連通させて設け、該伝熱管の他端
を、ガイドを有する伝熱管ヘッダに連通せしめ、又前記
伝熱管を収容しかつ低温流体の入口及び同出口を有する
円筒胴を設け、該円筒胴の前記高温流体室側端部を、同
流体室に接続し、他端部をOリングを介して前記ガイド
に気密にかつ移動自在に設けたことを特徴とする熱交換
器である。The present invention which achieves the above object will be described in which one end of a plurality of heat transfer tubes is connected to a high temperature fluid chamber which is partitioned by a partition plate and has an inlet and an outlet for the high temperature fluid. The heat transfer tube has a second end connected to a heat transfer tube header having a guide, and a cylindrical cylinder for accommodating the heat transfer tube and having a low temperature fluid inlet and a low temperature fluid outlet is provided. The heat exchanger is characterized in that the chamber side end is connected to the same fluid chamber, and the other end is provided in an airtight and movable manner on the guide via an O-ring.
【0006】[0006]
【作用】高温流体室に高温の流体を流入させ、円筒胴の
低温流体の入口から低温流体を供給する。そうすると前
記伝熱管の管壁において熱交換が行われ、低温流体は加
熱される。そして前記伝熱管と円筒胴間に熱膨張の差が
生じると、前記円筒胴はその一端がOリングを介して前
記伝熱管ヘッダのガイドに気密にかつ移動自在に設けら
れていることにより、このOリング部分で相対的に、気
密の状態で移動し、このため伝熱管と円筒胴の両者は拘
束されないので膨張による問題が起きない、従って前記
従来例に述べたような伸縮継手l、U字状の伝熱管B、
及び遊動筒m等はすべてこれを省略することができる。
従って製作費は割高とならない。そして伝熱管全体を円
筒胴内から取り出して、伝熱管の外面を容易に清掃する
ことができ、又同内面もベンド部がないため清掃が容易
にできる。又円筒胴内面の清掃も容易にできる。The high temperature fluid is caused to flow into the high temperature fluid chamber, and the low temperature fluid is supplied from the low temperature fluid inlet of the cylindrical body. Then, heat exchange is performed on the tube wall of the heat transfer tube, and the cryogenic fluid is heated. When a difference in thermal expansion occurs between the heat transfer tube and the cylinder body, one end of the cylinder body is provided in the guide of the heat transfer tube header via an O-ring in an airtight and movable manner. The O-ring portion moves relatively in an airtight state, and therefore both the heat transfer tube and the cylindrical body are not restrained, so that problems due to expansion do not occur. Therefore, the expansion joints l and U-shaped as described in the above-mentioned conventional example are not generated. Shaped heat transfer tube B,
The floating cylinder m and the like can be omitted.
Therefore, the production cost is not expensive. Then, the entire heat transfer tube can be taken out from the inside of the cylindrical body, and the outer surface of the heat transfer tube can be easily cleaned. Also, since the inner surface has no bend portion, it can be easily cleaned. Also, the inner surface of the cylindrical body can be easily cleaned.
【0006】[0006]
【実施例】図1において1は高温流体室であり、仕切り
板2を有し、かつ高温流体の入口3及び同出口4が設け
られている。5は複数の伝熱管であり、その一端部6が
上記高温流体室1に開口7させられており、かつ他端部
8は伝熱管ヘッダ9に連通させられている。同ヘッダ9
は図示のように筒状のガイド10、流体室11を有し、
蓋体12により開閉可能に形成されている。次に13は
円筒胴であり、上記伝熱管5を内蔵して、一端部14を
前記高温流体室1に設け、かつ他端部15をOリング1
6を介して前記伝熱管ヘッダ9の筒状のガイド10に、
気密にかつ移動自在に設けられている。17は低温流体
の入口、18は同出口、19はフランジ、20は開閉蓋
を示す。21は基台である。又上記Oリング16を設け
てある部分については図2にその詳細を示す。同図にお
いて22は保持部材であり、円筒胴13の前記他端部1
5にボルト23により固定され、凹状の、Oリング16
の保持部24が形成され、この保持部24にOリング1
6が収容されている。25はストッパである。なお上記
Oリング16はゴム、耐熱性ゴム、ポリウレタン、その
他適宜の合成樹脂等の弾性体により形成される。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In FIG. 1, reference numeral 1 is a high temperature fluid chamber having a partition plate 2 and provided with an inlet 3 and an outlet 4 for the high temperature fluid. Reference numeral 5 denotes a plurality of heat transfer tubes, one end 6 of which is opened to the high temperature fluid chamber 1 and the other end 8 of which is connected to a heat transfer tube header 9. Same header 9
Has a cylindrical guide 10 and a fluid chamber 11 as shown,
The lid 12 is formed so as to be openable and closable. Next, 13 is a cylindrical body, which has the heat transfer tube 5 built-in, one end portion 14 is provided in the high temperature fluid chamber 1, and the other end portion 15 is an O ring
To the tubular guide 10 of the heat transfer tube header 9 via 6,
It is airtight and movable. Reference numeral 17 is an inlet of the low temperature fluid, 18 is an outlet thereof, 19 is a flange, and 20 is an opening / closing lid. 21 is a base. The details of the portion provided with the O-ring 16 are shown in FIG. In the figure, reference numeral 22 is a holding member, which is the other end portion 1 of the cylindrical body 13.
5 is fixed by bolts 23 to the concave O-ring 16
The holding portion 24 of the O-ring 1 is formed on the holding portion 24.
6 are accommodated. 25 is a stopper. The O-ring 16 is formed of an elastic body such as rubber, heat resistant rubber, polyurethane, or other appropriate synthetic resin.
【0007】この実施例の熱交換器の作用は、前記のこ
の発明の作用とほぼ同様であるため省略する。ただ、こ
の熱交換器の清掃の場合、開閉蓋20、蓋体12等を外
して行う。又前記Oリング16は溝状に形成された保持
部24に収容されていることにより、安定して作動す
る。The operation of the heat exchanger of this embodiment is substantially the same as the operation of the present invention described above, and therefore will be omitted. However, when cleaning this heat exchanger, the opening / closing lid 20, the lid body 12 and the like are removed. Further, since the O-ring 16 is housed in the groove-shaped holding portion 24, it operates stably.
【0008】[0008]
【発明の効果】この発明の熱交換器は前記のように構成
され、円筒胴の一端部は高温流体室に設けられ、他端部
は、Oリングを介して、伝熱管ヘッダのガイドに気密に
かつ移動自在に設けられたことにより、前記従来例に示
されたような伸縮継手、U字状伝熱管、遊動頭等をすべ
て省略することができ、伸縮継手に起こるスケール堆
積、それによる伸縮機能の停止、スケール堆積の結果起
こる腐蝕、又はU字状伝熱管に起こる摩耗及び腐蝕、遊
動頭のフランジ部の部分から洩れの恐れ等の問題をすべ
て解決することができる。かつ又各種従来例のような製
造の面倒な構造ではなく、簡単な構造であるため製作費
を比較的安価にすることができる。又清掃の際は伝熱管
全体を前記Oリングの部分において円筒胴から抜き取る
ことができ、従って伝熱管の外側及び円筒胴の内側の清
掃を容易に行うことができる。又伝熱管の内側も前記従
来例のU字状部等を無くしたことにより容易に清掃する
ことができる。更に他の効果として、前記伝熱管ヘッダ
の、前記Oリングの外側に出ている長さを見れば、円筒
胴と伝熱管の熱膨張の差を正確に知ることもできる。The heat exchanger of the present invention is constructed as described above, one end of the cylindrical body is provided in the high temperature fluid chamber, and the other end is hermetically sealed to the guide of the heat transfer tube header via the O-ring. Since it is provided movably and freely, it is possible to omit all the expansion joints, U-shaped heat transfer tubes, floating heads, etc. as shown in the above-mentioned conventional example, and the scale accumulation that occurs in the expansion joints It is possible to solve all the problems such as malfunction, corrosion caused by scale accumulation, wear and corrosion of the U-shaped heat transfer tube, and leakage from the flange portion of the floating head. Moreover, the manufacturing cost can be made relatively low because the structure is simple and not a complicated structure as in various conventional examples. Further, at the time of cleaning, the entire heat transfer tube can be pulled out from the cylindrical body at the portion of the O-ring, so that the outside of the heat transfer tube and the inside of the cylindrical body can be easily cleaned. Also, the inside of the heat transfer tube can be easily cleaned by eliminating the U-shaped portion and the like of the conventional example. As yet another effect, the difference in thermal expansion between the cylindrical barrel and the heat transfer tube can be accurately known by looking at the length of the heat transfer tube header that extends outside the O-ring.
【図1】この発明の実施例を示し、熱交換器の断面図で
ある。FIG. 1 is a sectional view of a heat exchanger showing an embodiment of the present invention.
【図2】この発明の実施例を示し、図1に示す部分の拡
大詳細図である。FIG. 2 is an enlarged detailed view of the portion shown in FIG. 1, showing an embodiment of the present invention.
【図3】従来の熱交換器の断面図である。FIG. 3 is a sectional view of a conventional heat exchanger.
【図4】図3に示すものと異なる従来の熱交換器の断面
図である。FIG. 4 is a cross-sectional view of a conventional heat exchanger different from that shown in FIG.
【図5】図3及び図4に示すものと異なる従来の熱交換
器の断面図である。5 is a cross-sectional view of a conventional heat exchanger different from that shown in FIGS. 3 and 4. FIG.
1 高温流体室 2 仕切板 3 高温流体の入口 4 高温流体の出口 5 伝熱管 6 一端部 7 開口部 8 他端部 9 伝熱管ヘッダ 10 ガイド 13 円筒胴 14 一端部 15 他端部 1 High Temperature Fluid Chamber 2 Partition Plate 3 High Temperature Fluid Inlet 4 High Temperature Fluid Outlet 5 Heat Transfer Tube 6 One End 7 Opening 8 Other End 9 Heat Transfer Tube Header 10 Guide 13 Cylindrical Body 14 One End 15 Other End
Claims (1)
及び同出口を有する高温流体室に複数の伝熱管の一端を
連通させて設け、該伝熱管の他端を、ガイドを有する伝
熱管ヘッダに連通せしめ、又前記伝熱管を収容しかつ低
温流体の入口及び同出口を有する円筒胴を設け、該円筒
胴の前記高温流体室側端部を、同流体室に接続し、他端
部をOリングを介して前記ガイドに気密にかつ移動自在
に設けたことを特徴とする熱交換器。Claim: What is claimed is: 1. A high temperature fluid chamber, which is partitioned by a partition plate and has an inlet and an outlet for the high temperature fluid, is provided with one end of a plurality of heat transfer tubes in communication with the other end of the heat transfer tube. A heat transfer tube header having a guide is connected to the heat transfer tube, and a cylindrical cylinder having the heat transfer tube and having an inlet and an outlet for the low temperature fluid is provided, and the end of the cylindrical cylinder on the high temperature fluid chamber side is connected to the fluid chamber. The heat exchanger is characterized in that the other end is airtightly and movably provided on the guide through an O-ring.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21022591A JPH0534084A (en) | 1991-07-27 | 1991-07-27 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21022591A JPH0534084A (en) | 1991-07-27 | 1991-07-27 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0534084A true JPH0534084A (en) | 1993-02-09 |
Family
ID=16585863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21022591A Pending JPH0534084A (en) | 1991-07-27 | 1991-07-27 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0534084A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009513921A (en) * | 2005-10-26 | 2009-04-02 | ベール ゲーエムベーハー ウント コー カーゲー | Heat exchanger and method for manufacturing the heat exchanger |
EP2241848A2 (en) | 2009-04-15 | 2010-10-20 | TLV Co., Ltd. | Heat exchanger |
KR101283733B1 (en) * | 2009-09-02 | 2013-07-08 | 아틀라스 코프코 에네르가스 게엠베하 | Pressurized-gas cooler for a compressor |
US9863723B2 (en) | 2011-08-25 | 2018-01-09 | Silvio Giachetti | Integrated pressure compensating heat exchanger and method |
US11428473B2 (en) * | 2019-02-01 | 2022-08-30 | Modine Manufacturing Company | Heat exchanger |
-
1991
- 1991-07-27 JP JP21022591A patent/JPH0534084A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009513921A (en) * | 2005-10-26 | 2009-04-02 | ベール ゲーエムベーハー ウント コー カーゲー | Heat exchanger and method for manufacturing the heat exchanger |
US8967235B2 (en) | 2005-10-26 | 2015-03-03 | Behr Gmbh & Co. Kg | Heat exchanger, method for the production of a heat exchanger |
EP2241848A2 (en) | 2009-04-15 | 2010-10-20 | TLV Co., Ltd. | Heat exchanger |
EP2241848A3 (en) * | 2009-04-15 | 2011-05-25 | TLV Co., Ltd. | Heat exchanger |
KR101283733B1 (en) * | 2009-09-02 | 2013-07-08 | 아틀라스 코프코 에네르가스 게엠베하 | Pressurized-gas cooler for a compressor |
US9863723B2 (en) | 2011-08-25 | 2018-01-09 | Silvio Giachetti | Integrated pressure compensating heat exchanger and method |
US11428473B2 (en) * | 2019-02-01 | 2022-08-30 | Modine Manufacturing Company | Heat exchanger |
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