CN101929811A - A shell-and-tube heat exchanger with multi-shell-side countercurrent speed-up - Google Patents
A shell-and-tube heat exchanger with multi-shell-side countercurrent speed-up Download PDFInfo
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- 239000012530 fluid Substances 0.000 claims abstract description 33
- 230000001360 synchronised effect Effects 0.000 claims abstract description 4
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- 238000003466 welding Methods 0.000 claims description 2
- 230000002411 adverse Effects 0.000 claims 4
- 230000015572 biosynthetic process Effects 0.000 claims 2
- 239000011148 porous material Substances 0.000 claims 1
- 239000002131 composite material Substances 0.000 abstract description 2
- 239000003507 refrigerant Substances 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 10
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- 230000009977 dual effect Effects 0.000 description 2
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Abstract
Description
技术领域technical field
本发明涉及换热器加工制造领域,尤其是一种箱壳式多壳程逆流增速型管壳式换热器。The invention relates to the field of processing and manufacturing of heat exchangers, in particular to a shell-and-tube heat exchanger with multi-shell side countercurrent speed-up.
背景技术Background technique
壳管式换热器广泛用于化工、食品、制冷空调等领域,是在一个圆筒形壳体内设置许多平行的管子,让两种流体分别从管内空间和管外空间流过并进行热量交换。对于目前广泛使用的单壳程管壳式换热器,当换热器传热量较大时导致壳体直径较大和单壳程流通截面很大,导致壳侧流体的速度很低,造成换热器整体换热系数不高,换热效率低。Shell and tube heat exchangers are widely used in chemical industry, food, refrigeration and air conditioning and other fields. Many parallel tubes are arranged in a cylindrical shell to allow two fluids to flow through the space inside the tube and the space outside the tube and exchange heat. . For the single shell-side shell-and-tube heat exchangers widely used at present, when the heat transfer capacity of the heat exchanger is large, the diameter of the shell and the cross-section of the single-shell side are large, resulting in a low velocity of the shell-side fluid, resulting in heat transfer. The overall heat transfer coefficient of the device is not high, and the heat transfer efficiency is low.
发明内容Contents of the invention
本发明的目的正是为了解决上述单壳程管壳式换热器所存在的不足,提供一种体积小、换热效率高的一种箱壳式多壳程逆流增速型管壳式换热器。The purpose of the present invention is to solve the shortcomings of the above-mentioned single-shell-side shell-and-tube heat exchanger, and to provide a box-shell multi-shell-side countercurrent speed-up type shell-and-tube heat exchanger with small volume and high heat exchange efficiency. heater.
为实现上述目的,本发明采用的技术方案如下:To achieve the above object, the technical scheme adopted in the present invention is as follows:
本发明的箱壳式多壳程逆流增速型管壳式换热器,包括壳体、壳体一端设有管板Ⅰ,管箱连接在管板Ⅰ的外侧且内部设置隔板,壳体的另一端设有端盖,壳体内设有换热管,管箱上设有管接口Ⅰ和管接口Ⅱ,在壳体的上部和下部分别设置管接口Ⅲ和管接口Ⅳ。所述的换热器壳体为上圆下方结构或上方下圆结构,壳体内设置至少一层纵向逆流增速导流板,将壳体内部分为至少两个壳程,使形成的管外流体流程数与管内流体流程数相同且沿轴向流动方向相反。通过壳体内设置的纵向逆流增速导流板将单程壳程分为多壳程,增加了壳程流体流通的长度,并使壳侧的流体沿纵向和管内的流体形成逆流,通过壳体内设置的横向增速扰动导流板增加了壳侧流体的流速和扰动。The shell-and-tube heat exchanger of the present invention includes a shell-and-tube heat exchanger with multi-shell-side countercurrent speed-up, which includes a shell, and a tube plate I is provided at one end of the shell. The other end of the casing is provided with an end cover, the shell is provided with heat exchange tubes, the pipe box is provided with pipe joints I and pipe joints II, and the upper and lower parts of the shell are respectively provided with pipe joints III and pipe joints IV. The shell of the heat exchanger has an upper circle and a lower circle structure or an upper and lower circle structure, and at least one layer of longitudinal countercurrent speed-up deflectors are arranged in the shell, which divides the inside of the shell into at least two shell sides, so that the formed fluid outside the tube The flow number is the same as the flow number of the fluid in the tube and the flow direction is opposite along the axial direction. The single-pass shell pass is divided into multiple shell passes through the vertical counterflow speed-up deflector set in the shell, which increases the length of the fluid circulation in the shell pass, and makes the fluid on the shell side flow countercurrently with the fluid in the tube along the longitudinal direction, and passes through the set in the shell The lateral speed-increasing turbulence deflector increases the velocity and turbulence of the shell-side fluid.
所述纵向逆流增速导流板在壳体内的固定方式为:纵向逆流增速导流板一端可与管板通过焊接固定,也可以通过插入壳体的轴向插槽内固定或其它固定方式。The fixing method of the longitudinal countercurrent speed-up deflector in the shell is: one end of the longitudinal counter-flow speed-up deflector can be fixed with the tube plate by welding, or can be fixed by inserting into the axial slot of the shell or by other fixing methods .
本发明可在纵向逆流增速导流板与壳体间形成的流道内设置横向增速扰动导流板,所述横向增速扰动导流板形状与壳体内形成的管外流体流道截面形状相同,横向增速导流板一端留有通道缺口,并在导流板板面上开有若干用于支撑换热管的管孔。In the present invention, a horizontal speed-increasing disturbance deflector can be arranged in the flow channel formed between the longitudinal counterflow speed-up speed-up deflector and the housing, and the shape of the horizontal speed-up disturbance deflector is consistent with the cross-sectional shape of the fluid channel outside the pipe formed in the housing. Similarly, there is a channel gap at one end of the horizontal speed-increasing deflector, and a plurality of tube holes for supporting the heat exchange tubes are opened on the surface of the deflector.
本发明优选在换热器壳体内设置一层纵向逆流增速导流板,所述的换热管为直管式换热管,在壳体的另一端设有管板Ⅱ,换热管贯穿管板Ⅰ和管板Ⅱ与两端的管箱和端盖连通。In the present invention, a layer of longitudinal counterflow speed-increasing deflectors is preferably arranged in the heat exchanger shell. The heat exchange tubes are straight tube heat exchange tubes. Tube sheet I and tube sheet II communicate with the tube boxes and end caps at both ends.
所述的换热管也可以为U型管型换热管,壳体与端盖焊接或采用法兰连接。The heat exchange tube may also be a U-shaped heat exchange tube, and the shell and the end cover are welded or flanged.
所述换热管即可是套管形式也可是非套管形式。当为双热源时,换热管由外套管和穿装在外套管管腔中的内套管组成,当外套管和内套管为直管时,两端都设置外管板和内管板,其中一端外管板和内管板之间设置隔板和两个管接口;当外套管和内套管为U型管时,只在一端设置外管板和内管板,外管板和内管板之间设置隔板和两个管接口。可实现双热源同步换热。The heat exchange tubes can be in the form of sleeves or in the form of non-sleeves. When it is a double heat source, the heat exchange tube is composed of an outer tube and an inner tube installed in the cavity of the outer tube. When the outer tube and the inner tube are straight tubes, both ends are provided with an outer tube plate and an inner tube plate. , where a partition and two pipe joints are set between the outer tube sheet and the inner tube sheet at one end; A partition and two pipe joints are arranged between the inner tube sheets. It can realize dual heat source synchronous heat exchange.
本发明的一种箱壳式多壳程逆流增速型管壳式换热器,将壳体设计为上圆下方结构或上方下圆结构,可实现壳管式换热器中壳程内流体沿轴向方向与管内流体形成逆向和快速流动换热、减小流体间传热温差、提高换热效率,并可实现双热源同步复合利用,其特出的壳体结构使换热管排列时更加紧凑,可有效的减小换热器体积,并减少制冷剂充注量。The shell-and-tube heat exchanger of the present invention is a shell-and-tube multi-shell-side countercurrent speed-increasing type. The shell is designed as a structure with an upper circle and a lower circle or a structure with an upper circle and a lower circle, so that the fluid in the shell-side of the shell-and-tube heat exchanger can be realized. It forms a reverse and rapid flow heat exchange with the fluid in the tube along the axial direction, reduces the heat transfer temperature difference between the fluids, improves the heat exchange efficiency, and can realize the synchronous composite utilization of dual heat sources. Its special shell structure makes the heat exchange tubes arranged It is more compact, which can effectively reduce the volume of the heat exchanger and reduce the refrigerant charge.
附图说明Description of drawings
图1为本发明的实施例1的结构示意图。Fig. 1 is a schematic structural diagram of
图2为图1中A-A向剖视图。Fig. 2 is a sectional view along A-A in Fig. 1 .
图3为本发明的实施例2的结构示意图。Fig. 3 is a schematic structural diagram of
图4为图3中A-A向剖视图。Fig. 4 is a sectional view along A-A in Fig. 3 .
图5为本发明的实施例3的结构示意图。FIG. 5 is a schematic structural diagram of
图6为图5中A-A向剖视图。Fig. 6 is a sectional view along A-A in Fig. 5 .
图7为本发明的实施例4的结构示意图。Fig. 7 is a schematic structural diagram of
图8为图7中A-A向剖视图。Fig. 8 is a sectional view along A-A in Fig. 7 .
图9为本发明的实施例5的结构示意图。Fig. 9 is a schematic structural diagram of
图10为图9中A-A向剖视图。Fig. 10 is a sectional view along A-A in Fig. 9 .
图11为本发明的实施例6的结构示意图。Fig. 11 is a schematic structural diagram of
图12为图1中A-A向剖视图。Fig. 12 is a sectional view along A-A in Fig. 1 .
图13为本发明的实施例7的结构示意图。Fig. 13 is a schematic structural diagram of
图14为图13中A-A向剖视图。Fig. 14 is a cross-sectional view along line A-A in Fig. 13 .
图15为本发明的实施例8的结构示意图。Fig. 15 is a schematic structural diagram of
图16为图15中A-A向剖视图。Fig. 16 is a cross-sectional view along line A-A in Fig. 15 .
图17为本发明的实施例9的结构示意图。Fig. 17 is a schematic structural diagram of
图18为图17中A-A向剖视图。Fig. 18 is a sectional view along line A-A in Fig. 17 .
图19为本发明的实施例10的结构示意图。Fig. 19 is a schematic structural diagram of
图20为图19中A-A向剖视图。Fig. 20 is a sectional view along A-A in Fig. 19 .
具体实施方式Detailed ways
本发明以下将结合实施例作进一步描述,但并不限制本发明。The present invention will be further described below in conjunction with examples, but the present invention is not limited.
实施例1Example 1
如图1所示,箱壳式多壳程逆流增速型管壳式换热器,包括壳体5、壳体两端设有管板Ⅰ3和管板Ⅱ8,管箱2连接在管板Ⅰ3的外侧且内部设置隔板,壳体的另一端设有端盖11,壳体内设有换热管6,所述的换热管为直管式换热管,换热管贯穿管板Ⅰ3和管板Ⅱ8与两端的管箱和端盖连通。管箱2上设有管接口Ⅰ1和管接口Ⅱ9,在壳体的上部和下部分别设置管接口Ⅲ4和管接口Ⅳ10。所述的换热器壳体为上圆下方结构,即其上方为半圆柱形,下方为四棱柱。壳体内设置一层纵向逆流增速导流板7,将壳体内部分为两个壳程,使形成的管外流体流程数与管内流体流程数相同且沿轴向流动方向相反。As shown in Figure 1, the shell-and-tube heat exchanger of the multi-shell side countercurrent speed-up type shell-and-tube heat exchanger includes the
工作流程如下:一种介质从管接口9进入换热器管箱2,经换热管换热后从管接口1流出换热器,另一种工质从管接口4进入壳体内,从管接口10流出壳体,两种介质在流通过程中形成逆流换热。The working process is as follows: one medium enters the
实施例2Example 2
如图2所示,该实施例是在实施例的结构的基础上,换热管为U型管。As shown in Fig. 2, this embodiment is based on the structure of the embodiment, and the heat exchange tube is a U-shaped tube.
实施例3Example 3
如图3所示,该实施例是在图3所示结构的基础上,在壳体5内设置横向增速扰动导流板12。所述横向增速扰动导流板形状与壳体内形成的管外流体流道截面形状相同,横向增速导流板一端留有通道缺口,并在导流板板面上开有若干用于支撑换热管的管孔。As shown in FIG. 3 , this embodiment is based on the structure shown in FIG. 3 , and a transverse speed-increasing
实施例4Example 4
如图4所示,该实施方式是在实施例1的结构的基础上,所述的换热管为套管式换热管,换热管是由外套管13和穿装在外套管管腔中的内套管14组成;增加内管板17、18;在外管板3和内管板17之间设置管接口Ⅴ15和Ⅵ16。As shown in Figure 4, this embodiment is based on the structure of Example 1. The heat exchange tube is a sleeve-type heat exchange tube, and the heat exchange tube is composed of an
实施例5Example 5
如图5 所示,该实施例是在实施例4的结构的基础上,在壳体5内设置横向增速扰动导流板12。所述横向增速扰动导流板形状与壳体内形成的管外流体流道截面形状相同,横向增速导流板一端留有通道缺口,并在导流板板面上开有若干用于支撑换热管的管孔。As shown in Figure 5, this embodiment is on the basis of the structure of
实施例6Example 6
如图6所示,箱壳式多壳程逆流增速型管壳式换热器,包括壳体5、壳体两端设有管板Ⅰ3和管板Ⅱ8,管箱2连接在管板Ⅰ3的外侧且内部设置隔板,壳体的另一端设有端盖11,壳体内设有换热管6,所述的换热管为直管式换热管,换热管贯穿管板Ⅰ3和管板Ⅱ8与两端的管箱和端盖连通。管箱2上设有管接口Ⅰ1和管接口Ⅱ9,在壳体的上部和下部分别设置管接口Ⅲ4和管接口Ⅳ10。所述的换热器壳体为上方下圆结构,即其上方为四棱柱形,下方为半圆柱形。壳体内设置一层纵向逆流增速导流板7,将壳体内部分为两个壳程,使形成的管外流体流程数与管内流体流程数相同且沿轴向流动方向相反。As shown in Figure 6, the shell-and-tube heat exchanger with multi-shell side countercurrent speed-up type includes a
工作流程如下:一种介质从管接口9进入换热器管箱2,经换热管换热后从管接口1流出换热器,另一种工质从管接口4进入壳体内,从管接口10流出壳体,两种介质在流通过程中形成逆流换热。The working process is as follows: one medium enters the
实施例7Example 7
如图7所示,该实施方式是在实施例6的结构的基础上,换热管为U型换热管。As shown in FIG. 7 , this embodiment is based on the structure of Example 6, and the heat exchange tubes are U-shaped heat exchange tubes.
实施例8Example 8
如图8所示,该实施例是在实施例6的结构的基础上,在壳体5内设置横向增速扰动导流板12。所述横向增速扰动导流板形状与壳体内形成的管外流体流道截面形状相同,横向增速导流板一端留有通道缺口,并在导流板板面上开有若干用于支撑换热管的管孔。As shown in FIG. 8 , this embodiment is based on the structure of
实施例9Example 9
如图9所示,该实施例是在实施例6的结构的基础上,所述的换热管为套管式换热管,换热管是由外套管13和穿装在外套管管腔中的内套管14组成;增加内管板17、18;在外管板3和内管板17之间设置管接口Ⅴ15和管接口Ⅵ16。As shown in Figure 9, this embodiment is based on the structure of
实施例10Example 10
如图10 所示,该实施例是在实施例9的结构的基础上,在壳体5内设置横向增速扰动导流板12。所述横向增速扰动导流板形状与壳体内形成的管外流体流道截面形状相同,横向增速导流板一端留有通道缺口,并在导流板板面上开有若干用于支撑换热管的管孔。As shown in Figure 10, this embodiment is on the basis of the structure of
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| CN102288053A (en) * | 2011-08-01 | 2011-12-21 | 王英慧 | Shell and tube sewage heat exchanger |
| CN103759574A (en) * | 2013-12-10 | 2014-04-30 | 柳州五菱宝马利汽车空调有限公司 | Double semilunar split collecting and distributing tube for automotive parallel flow evaporator |
| CN104807351A (en) * | 2015-04-17 | 2015-07-29 | 广东申菱空调设备有限公司 | Pure counterflow shell-and-tube heat exchanger and manufacturing method thereof |
| CN107289675A (en) * | 2016-03-31 | 2017-10-24 | 杭州三花研究院有限公司 | Heat exchanger and vehicle heat management system |
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| CN109506500A (en) * | 2018-11-21 | 2019-03-22 | 浙江英科新能源有限公司 | A kind of shell-and-tube heat-exchange device |
| CN109945694A (en) * | 2019-01-21 | 2019-06-28 | 易达科技(深圳)有限公司 | Anti-corrosion heat exchanger and heat pump system |
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| CN113513930A (en) * | 2021-06-16 | 2021-10-19 | 河海大学 | High-temperature phase-change shell-and-tube heat exchanger |
| CN115388679A (en) * | 2022-08-05 | 2022-11-25 | 常州大学 | Multi-pass countercurrent sleeve type heat exchanger |
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