CN205425903U - Round trip shell and tube type heat exchanger with compensation circle - Google Patents
Round trip shell and tube type heat exchanger with compensation circle Download PDFInfo
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- CN205425903U CN205425903U CN201520906540.6U CN201520906540U CN205425903U CN 205425903 U CN205425903 U CN 205425903U CN 201520906540 U CN201520906540 U CN 201520906540U CN 205425903 U CN205425903 U CN 205425903U
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Abstract
Description
技术领域technical field
本实用新型涉及一种化工传热过程中的冷热流体热交换设备,尤其是一种具有补偿圈的双程管壳式换热器。The utility model relates to a cold and hot fluid heat exchange device in the heat transfer process of a chemical industry, in particular to a double-pass shell-and-tube heat exchanger with a compensation ring.
背景技术Background technique
换热器作为传热过程中冷、热流体热交换的主要设备,在化工生产中的诸多领域得到广泛应用,目前的换热器根据其热交换方式主要分为三种:一是混合式换热器,应用于可使冷、热流体直接混合进行热交换的场合,设备简单、换热效果好,但仅限于两流体互相混合的情况,换热机理较为复杂、传热的同时往往伴有传质过程;二是蓄热式换热器,是在蓄热器中实现热交换,生产中通常采用两个并联蓄热器交替使用,结构简单、耐高温,但设备体积庞大,不能避免两种流体的混合;三是间壁式换热器,因化学生产中遇到的多是间壁两侧流体的热交换,因此间壁式换热器是化工生产中应用最多的换热器。As the main equipment for heat exchange between cold and hot fluids in the heat transfer process, heat exchangers are widely used in many fields in chemical production. The current heat exchangers are mainly divided into three types according to their heat exchange methods: one is the hybrid heat exchanger. Heater is used in occasions where cold and hot fluids can be directly mixed for heat exchange. The equipment is simple and the heat exchange effect is good, but it is limited to the situation where the two fluids are mixed with each other. The heat exchange mechanism is more complicated, and heat transfer is often accompanied by The mass transfer process; the second is the regenerative heat exchanger, which realizes heat exchange in the heat accumulator. In production, two parallel heat accumulators are usually used alternately. The structure is simple and high temperature resistant, but the equipment is bulky and cannot be avoided. The third is the partition wall heat exchanger, because most of the heat exchange between the fluids on both sides of the partition wall is encountered in chemical production, so the partition wall heat exchanger is the most widely used heat exchanger in chemical production.
管壳式换热器是典型的间壁式换热器,在化工生产中得到了广泛应用,由于两流体的温度不同,壳体和输送管的温度也不同,因此壳体和输送管热膨胀量也有所差别,当两流体的温度相差较大时,由于热应力引起设备变形,甚至弯曲或破裂。The shell-and-tube heat exchanger is a typical partition heat exchanger, which has been widely used in chemical production. Because the temperature of the two fluids is different, the temperature of the shell and the delivery pipe are also different, so the thermal expansion of the shell and the delivery pipe also varies. The difference is that when the temperature difference between the two fluids is large, the equipment will be deformed, even bent or broken due to thermal stress.
实用新型内容Utility model content
本实用新型旨在解决上述问题,提供了一种具有补偿圈的双程管壳式换热器,它克服了一般管壳式换热器当两流体的温度相差较大时,由于热应力引起设备变形,甚至弯曲或破裂的弊端,其采用的技术方案如下:The utility model aims to solve the above problems, and provides a double-pass shell-and-tube heat exchanger with a compensation ring, which overcomes the thermal stress caused by the general shell-and-tube heat exchanger when the temperature difference between the two fluids is large. The disadvantages of equipment deformation, even bending or cracking, the technical solutions adopted are as follows:
一种具有补偿圈的双程管壳式换热器,包括隔板、管程出口接头、左管板、壳体、补偿圈、壳程入口接头、右封头、右管板、输送管、横向挡板、壳程出口接头、管程入口接头、左封头,所述的隔板放置于左封头内部,将左封头内部分为上下两个封闭空间,右端与左管板连接,所述的管程出口接头和管程入口接头均设置在左封头上,所述的壳程入口接头和壳程出口接头均设置在壳体上,所述的左管板左端靠左封头定位,右端靠壳体定位,所述的右管板左端靠壳体定位,右端靠右封头定位,所述的壳体左端与左封头连接,右端与右封头连接,所述的输送管穿过横向挡板、左管板和右管板上开设的圆柱孔,左端管口伸出左管板左端,右端管口伸出右管板右端,所述的横向挡板与壳体连接,所述的补偿圈焊接在壳体上,在壳体与输送管热膨胀不同时,发生弹性变形,以适应壳体与输送管不同的热膨胀程度。A double-pass shell-and-tube heat exchanger with a compensation ring, including a diaphragm, a tube-side outlet joint, a left tube plate, a shell, a compensation ring, a shell-side inlet joint, a right head, a right tube plate, a delivery pipe, Transverse baffle, shell-side outlet joint, tube-side inlet joint, and left head. The partition is placed inside the left head, dividing the inside of the left head into upper and lower closed spaces, and the right end is connected to the left tube plate. Both the tube side outlet joint and the tube side inlet joint are arranged on the left head, the shell side inlet joint and the shell side outlet joint are both arranged on the shell, and the left end of the left tube plate is close to the left head Positioning, the right end is positioned against the shell, the left end of the right tube plate is positioned against the shell, the right end is positioned against the right head, the left end of the shell is connected to the left head, the right end is connected to the right head, the conveying The tube passes through the cylindrical hole opened on the transverse baffle, the left tube plate and the right tube plate, the left end of the nozzle protrudes from the left end of the left tube plate, and the right end of the nozzle protrudes from the right end of the right tube plate, and the transverse baffle is connected to the shell , the compensation ring is welded on the housing, and elastically deforms when the thermal expansion of the housing and the delivery pipe is different, so as to adapt to the different degrees of thermal expansion of the housing and the delivery pipe.
所述的右封头为弧形结构,降低流体与内表面的冲击,所述的右封头内部设有一个用来定位右管板的环形凸台。The right head has an arc-shaped structure to reduce the impact of the fluid and the inner surface, and an annular boss for positioning the right tube sheet is provided inside the right head.
本实用新型具有如下优点:单位体积具有的换热面积较大、换热效果较好,结构简单、克服了一般管壳式换热器当两流体的温度相差较大时,由于热应力引起设备变形,甚至弯曲或破裂的问题。The utility model has the following advantages: the heat exchange area per unit volume is larger, the heat exchange effect is better, the structure is simple, and it overcomes the general shell-and-tube heat exchanger when the temperature difference between the two fluids is large. Deformation, even bending or cracking problems.
附图说明Description of drawings
图1:本实用新型一种具有补偿圈的双程管壳式换热器的结构示意图;Figure 1: A structural schematic diagram of a double-pass shell-and-tube heat exchanger with a compensation ring in the utility model;
符号说明:Symbol Description:
1.隔板、2.管程出口接头、3.左管板、4.壳体、5.补偿圈、6.壳程入口接头、7.右封头、8.右管板、9.输送管、10.横向挡板、11.壳程出口接头、12.管程入口接头、13.左封头。1. Partition plate, 2. Tube side outlet joint, 3. Left tube plate, 4. Shell, 5. Compensation ring, 6. Shell side inlet joint, 7. Right head, 8. Right tube plate, 9. Conveying Tube, 10. Transverse baffle, 11. Shell side outlet joint, 12. Tube side inlet joint, 13. Left head.
具体实施方式detailed description
下面结合附图和实例对本实用新型作进一步说明:Below in conjunction with accompanying drawing and example the utility model is described further:
如图1所示,本实用新型一种具有补偿圈的双程管壳式换热器,包括隔板(1)、管程出口接头(2)、左管板(3)、壳体(4)、补偿圈(5)、壳程入口接头(6)、右封头(7)、右管板(8)、输送管(9)、横向挡板(10)、壳程出口接头(11)、管程入口接头(12)、左封头(13),所述的隔板(1)放置于左封头(13)内部,将左封头(13)内部分为上下两个封闭空间,右端与左管板(3)连接,所述的管程出口接头(2)和管程入口接头(12)均设置在左封头(13)上,所述的壳程入口接头(6)和壳程出口接头(11)均设置在壳体(4)上,所述的左管板(3)左端靠左封头(13)定位,右端靠壳体(4)定位,所述的右管板(8)左端靠壳体(4)定位,右端靠右封头(7)定位,所述的壳体(4)左端与左封头(13)连接,右端与右封头(7)连接,所述的输送管(9)穿过横向挡板(10)、左管板(3)和右管板(8)上开设的圆柱孔,左端管口伸出左管板(3)左端,右端管口伸出右管板(8)右端,所述的横向挡板(10)与壳体(4)连接,所述的补偿圈(5)焊接在壳体(4)上,在壳体(4)与输送管(10)热膨胀不同时,发生弹性变形,以适应壳体(4)与输送管(10)不同的热膨胀程度。As shown in Figure 1, the utility model has a double-pass shell-and-tube heat exchanger with a compensation ring, including a partition (1), a tube-side outlet joint (2), a left tube plate (3), a shell (4 ), compensation ring (5), shell side inlet joint (6), right head (7), right tube sheet (8), conveying pipe (9), transverse baffle (10), shell side outlet joint (11) , the tube inlet joint (12), the left head (13), the partition (1) is placed inside the left head (13), and the inside of the left head (13) is divided into upper and lower closed spaces, The right end is connected with the left tube sheet (3), the tube side outlet joint (2) and the tube side inlet joint (12) are all arranged on the left head (13), and the shell side inlet joint (6) and The shell-side outlet joints (11) are all arranged on the shell (4), the left end of the left tube plate (3) is positioned against the left head (13), the right end is positioned against the shell (4), and the right tube plate (3) is positioned against the shell (4). The left end of the plate (8) is positioned against the shell (4), the right end is positioned against the right head (7), the left end of the shell (4) is connected to the left head (13), and the right end is connected to the right head (7) , the conveying pipe (9) passes through the cylindrical hole provided on the transverse baffle (10), the left tube plate (3) and the right tube plate (8), and the nozzle on the left end stretches out from the left end of the left tube plate (3), The nozzle at the right end protrudes from the right end of the right tube plate (8), the transverse baffle (10) is connected to the shell (4), the compensation ring (5) is welded on the shell (4), and the (4) When the thermal expansion is different from that of the delivery pipe (10), elastic deformation occurs to adapt to the different degrees of thermal expansion of the housing (4) and the delivery pipe (10).
所述的右封头(7)为弧形结构,降低流体与内表面的冲击,所述的右封头(7)内部设有一个用来定位右管板(8)的环形凸台。The right head (7) has an arc-shaped structure to reduce the impact of the fluid and the inner surface. The inside of the right head (7) is provided with an annular boss for positioning the right tube sheet (8).
本实用新型使用时,热流体由管程入口接头(12)流入左封头(13)的下部空间,经下部的输送管(9)流入右封头(7)的下部空间,再经上部的输送管(9)流入左封头(13)的上部空间,最终经管程出口接头(2)流出;冷流体由壳程入口接头(6)流入壳体(4)右端的内部空间,并沿着右管板(8)、横向挡板(10)、输送管(9)之间的空隙流动,然后沿着两横向挡板(10)与输送管(9)之间的空隙流动,由于壳体(4)内有数块横向挡板(10),所以冷流体在壳体中做折流流动,其中横向挡板(10)的数量可根据需要进行选择,最终由壳体(4)左端的壳程出口接头(11)流出。在此过程中,热流体两次流经输送管(9),实现了管程流体的双程流动,冷流体在壳体(4)内沿横向挡板(10)做折流流动,增大了单位体积的换热面积、换热效果好,补偿圈(5)焊接在壳体上,在壳体(4)与输送管(9)热膨胀不同时,发生弹性变形,以适应壳体(4)与输送管(9)不同的热膨胀程度,从而克服了一般管壳式换热器当两流体的温度相差较大时,由于热应力引起设备变形,甚至弯曲或破裂的问题。When the utility model is in use, the hot fluid flows into the lower space of the left head (13) from the pipe-side inlet joint (12), flows into the lower space of the right head (7) through the lower delivery pipe (9), and then passes through the upper The conveying pipe (9) flows into the upper space of the left head (13), and finally flows out through the tube-side outlet joint (2); the cold fluid flows into the inner space of the right end of the shell (4) from the shell-side inlet joint (6), and flows along the The right tube sheet (8), the transverse baffle (10), and the gap between the conveying pipe (9) flow, and then flow along the gap between the two transverse baffles (10) and the conveying pipe (9), due to the (4) There are several horizontal baffles (10) inside, so the cold fluid flows in the casing, and the number of horizontal baffles (10) can be selected according to the needs, and finally the shell at the left end of the casing (4) Outlet outlet joint (11) flows out. During this process, the hot fluid flows through the delivery pipe (9) twice, realizing the two-way flow of the tube-side fluid, and the cold fluid flows along the transverse baffle (10) in the shell (4), increasing the The heat exchange area per unit volume is improved, and the heat exchange effect is good. The compensation ring (5) is welded on the shell, and when the thermal expansion of the shell (4) and the delivery pipe (9) are different, elastic deformation occurs to adapt to the shell (4) ) and the conveying pipe (9) have different degrees of thermal expansion, thereby overcoming the problem of deformation, even bending or cracking of the equipment due to thermal stress when the temperature difference between the two fluids is large in a general shell-and-tube heat exchanger.
上面以举例方式对本实用新型进行了说明,但本实用新型不限于上述具体实施例,凡基于本实用新型所做的任何改动或变型均属于本实用新型要求保护的范围。The utility model has been described above with examples, but the utility model is not limited to the above-mentioned specific embodiments, and any changes or modifications made based on the utility model all belong to the protection scope of the utility model.
Claims (2)
- null1. a round trip shell-and-tube heat exchanger with compensating ring,It is characterized in that: include dividing plate (1)、Tube side outlet connection (2)、Left tube sheet (3)、Housing (4)、Compensating ring (5)、Shell side inlet joint (6)、Right end socket (7)、Right tube plate (8)、Conveying pipe (9)、Transverse baffle (10)、Shell-side outlet joint (11)、Tube-side inlet joint (12)、Left end socket (13),It is internal that described dividing plate (1) is positioned over left end socket (13),It is divided into upper and lower two to close space by internal for left end socket (13),Right-hand member is connected with left tube sheet (3),Described tube side outlet connection (2) and tube-side inlet joint (12) are arranged on left end socket (13),Described shell side inlet joint (6) and shell-side outlet joint (11) are arranged on housing (4),Described left tube sheet (3) left end keep left end socket (13) location,Right-hand member positions by housing (4),Described right tube plate (8) left end positions by housing (4),Right-hand member keep right end socket (7) location,Described housing (4) left end is connected with left end socket (13),Right-hand member is connected with right end socket (7),Described conveying pipe (9) passes transverse baffle (10)、The cylindrical hole offered on left tube sheet (3) and right tube plate (8),The left end mouth of pipe stretches out left tube sheet (3) left end,The right-hand member mouth of pipe stretches out right tube plate (8) right-hand member,Described transverse baffle (10) is connected with housing (4),Described compensating ring (5) is welded on housing (4).
- A kind of round trip shell-and-tube heat exchanger with compensating ring the most according to claim 1, it is characterized in that: described right end socket (7) is arcuate structure, described right end socket (7) is internal is provided with one for the annular boss positioning right tube plate (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520906540.6U CN205425903U (en) | 2015-11-13 | 2015-11-13 | Round trip shell and tube type heat exchanger with compensation circle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520906540.6U CN205425903U (en) | 2015-11-13 | 2015-11-13 | Round trip shell and tube type heat exchanger with compensation circle |
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| Publication Number | Publication Date |
|---|---|
| CN205425903U true CN205425903U (en) | 2016-08-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520906540.6U Expired - Fee Related CN205425903U (en) | 2015-11-13 | 2015-11-13 | Round trip shell and tube type heat exchanger with compensation circle |
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| Country | Link |
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| CN (1) | CN205425903U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107990756A (en) * | 2017-12-28 | 2018-05-04 | 无锡宏盛换热器制造股份有限公司 | Water cooler |
| CN110914630A (en) * | 2017-05-26 | 2020-03-24 | 阿法拉伐奥米有限公司 | Shell and tube installation with bypass |
-
2015
- 2015-11-13 CN CN201520906540.6U patent/CN205425903U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110914630A (en) * | 2017-05-26 | 2020-03-24 | 阿法拉伐奥米有限公司 | Shell and tube installation with bypass |
| US11073347B2 (en) | 2017-05-26 | 2021-07-27 | Alfa Laval Olmi S.P.A. | Shell-and-tube equipment with bypass |
| CN110914630B (en) * | 2017-05-26 | 2022-03-01 | 阿法拉伐奥米有限公司 | Shell and Tube Equipment with Bypass |
| CN107990756A (en) * | 2017-12-28 | 2018-05-04 | 无锡宏盛换热器制造股份有限公司 | Water cooler |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20171113 |