JPS5883193A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS5883193A JPS5883193A JP18117781A JP18117781A JPS5883193A JP S5883193 A JPS5883193 A JP S5883193A JP 18117781 A JP18117781 A JP 18117781A JP 18117781 A JP18117781 A JP 18117781A JP S5883193 A JPS5883193 A JP S5883193A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- tube
- heat exchanger
- dummy
- flow
- 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 abstract description 4
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
- 238000007796 conventional method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- F28F9/24—Arrangements for promoting turbulent flow of heat-exchange media, e.g. by plates
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、多管式熱交換器の熱交率の向」二を計るため
に、ダミーチューブを設けた多管式熱交換器である。DETAILED DESCRIPTION OF THE INVENTION The present invention is a shell-and-tube heat exchanger provided with dummy tubes in order to measure the heat exchange coefficient of the shell-and-tube heat exchanger.
従来の多管式熱交換器においては、胴体内の流動が、欠
円形バッフルを使用しているため、バックル板前後によ
どみ部ができ効率的な熱交換ができない。又、胴体ノズ
ル取付上よシできる管板面近くの部分が、有効な伝熱面
積として使用できないデッドスペースが生ずる。In conventional multi-tube heat exchangers, the flow inside the body uses a circular baffle, which creates stagnation before and after the buckle plate, making efficient heat exchange impossible. In addition, a dead space is created in which the area near the tube plate surface, which can be moved when mounting the nozzle on the body, cannot be used as an effective heat transfer area.
本発明の目的は、多管式熱交換器内にダミーチューブを
使用し流れを均一化し、熱交換効率を向上させることに
ある。An object of the present invention is to use dummy tubes in a shell-and-tube heat exchanger to equalize the flow and improve heat exchange efficiency.
本発明は、胴体内の流動において、流れがよどんで、伝
熱面積が有効に生かされていない箇所に胴体バッフルを
バイパスする流路を設け、よどみ領域における熱交換を
向上させるものである。The present invention improves heat exchange in the stagnation region by providing a flow path that bypasses the fuselage baffle at a location where the flow in the fuselage is stagnant and the heat transfer area is not effectively utilized.
第1図、第2図、第3図において、入口ノズル11より
入った流体が、バックル板2によって、伝熱管内の流路
を形式する。この時に、バッフル板2前後によどみ領域
が発生する。このよどみの最も著しい箇所に、ダミーチ
ューブ3を設け、ダミーチューブ内の圧損を考慮して、
ダミ一つ一ユープ下流に行くに従い大きい穴を、よどみ
部に設けよどみ部にダミーチューブによる流路を形成し
て噴流をおこすことにより乱流状態とし熱交換率を向上
するようにする。In FIGS. 1, 2, and 3, the fluid entering from the inlet nozzle 11 forms a flow path within the heat transfer tube by the buckle plate 2. At this time, a stagnation area occurs before and after the baffle plate 2. A dummy tube 3 is installed at the point where this stagnation is most significant, and taking into consideration the pressure loss inside the dummy tube,
A hole that becomes larger as it goes downstream of each dummy is provided in the stagnation part to form a flow path using a dummy tube in the stagnation part to create a jet flow, thereby creating a turbulent flow state and improving the heat exchange rate.
最も効果が期待される箇所は、デッドスペース7部とな
るので、この位置までダミーチューブを伝わって、入口
ノズルより入った高温流体が流れることにより、従来方
式と比較し、大きな温度差及び、流速が得られる。従っ
て、デッドスペース7の熱交換量の増加が期待される。The point where the most effective effect is expected is the dead space 7, so the high temperature fluid that entered from the inlet nozzle flows through the dummy tube to this point, resulting in a large temperature difference and flow rate compared to the conventional method. is obtained. Therefore, an increase in the amount of heat exchange in the dead space 7 is expected.
本発明によれば、熱交換器の熱交換量が増加する。According to the present invention, the amount of heat exchanged by the heat exchanger increases.
第1図は熱交換器全体と流動状態を表わした図第2図は
管板近くのデッドスペース部の詳細図、第3図はダミー
チューブ途中の開口部の状態図である。
1・・・伝熱管、2・・・バッフル板、3・・・ダミー
チューブ、4・・・胴、5・・・管板、6・・・水室、
7・・・デッドスペース、8・・・伝熱管、11・・・
入口ノズル、12・・・第1 図
第 3 目Fig. 1 shows the entire heat exchanger and its flow state, Fig. 2 shows a detailed view of the dead space near the tube plate, and Fig. 3 shows the state of the opening in the middle of the dummy tube. DESCRIPTION OF SYMBOLS 1... Heat exchanger tube, 2... Baffle plate, 3... Dummy tube, 4... Body, 5... Tube plate, 6... Water chamber,
7... Dead space, 8... Heat exchanger tube, 11...
Inlet nozzle, 12...Figure 1, item 3
Claims (1)
る胴体内の流路において、伝熱管群中にダミーチューブ
を設け、このダミーチューブに流路のバイパスルートを
設けたことにより、熱交換器内バッフル部のよどみ防止
を行ない熱交率を高める、及び、管板面近くのデッドス
ペースを有効に利用することを特徴とした熱交換器。1. In the flow path in the body formed by the heat exchanger tube baffle plate of a multi-tube heat exchanger, a dummy tube is provided in the heat exchanger tube group, and a bypass route for the flow path is provided in this dummy tube. A heat exchanger characterized by preventing stagnation in the baffle part within the exchanger, increasing the heat exchange rate, and effectively utilizing dead space near the tube plate surface.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18117781A JPS5883193A (en) | 1981-11-13 | 1981-11-13 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18117781A JPS5883193A (en) | 1981-11-13 | 1981-11-13 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5883193A true JPS5883193A (en) | 1983-05-18 |
Family
ID=16096224
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18117781A Pending JPS5883193A (en) | 1981-11-13 | 1981-11-13 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5883193A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006035951A1 (en) * | 2004-09-27 | 2006-04-06 | Sumitomo Chemical Company, Limited | Multitubular reaction apparatus for contact gas-phase reaction |
JP2020532073A (en) * | 2017-08-28 | 2020-11-05 | ワットロー・エレクトリック・マニュファクチャリング・カンパニー | Continuous spiral baffle heat exchanger |
US11913736B2 (en) | 2017-08-28 | 2024-02-27 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
US11920878B2 (en) | 2017-08-28 | 2024-03-05 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
-
1981
- 1981-11-13 JP JP18117781A patent/JPS5883193A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006035951A1 (en) * | 2004-09-27 | 2006-04-06 | Sumitomo Chemical Company, Limited | Multitubular reaction apparatus for contact gas-phase reaction |
US7771674B2 (en) | 2004-09-27 | 2010-08-10 | Sumitomo Chemical Company, Limited | Multitubular reaction apparatus for contact gas-phase reaction |
JP2020532073A (en) * | 2017-08-28 | 2020-11-05 | ワットロー・エレクトリック・マニュファクチャリング・カンパニー | Continuous spiral baffle heat exchanger |
US11808534B2 (en) | 2017-08-28 | 2023-11-07 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
US11913736B2 (en) | 2017-08-28 | 2024-02-27 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
US11920878B2 (en) | 2017-08-28 | 2024-03-05 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
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