CN110030851A - A kind of bushing type floating head heat exchanger - Google Patents
A kind of bushing type floating head heat exchanger Download PDFInfo
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- CN110030851A CN110030851A CN201910388633.7A CN201910388633A CN110030851A CN 110030851 A CN110030851 A CN 110030851A CN 201910388633 A CN201910388633 A CN 201910388633A CN 110030851 A CN110030851 A CN 110030851A
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- tube
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- floating head
- shaped heat
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- 238000005192 partition Methods 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims description 13
- 238000007665 sagging Methods 0.000 claims 3
- 230000002093 peripheral effect Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
Classifications
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- 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
- F28D7/10—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 one within the other, e.g. concentrically
- F28D7/14—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 one within the other, e.g. concentrically both tubes being bent
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- 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
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- 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
- F28F9/0241—Header boxes; End plates floating elements floating end plates
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/34—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely
- F28F1/36—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely the means being helically wound fins or wire spirals
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明涉及套管式换热器,具体为一种套管式浮头换热器。本发明用以实现两种高温差、高压差、甚至不允许直接接触两种介质的换热要求,同时能实现三种介质的自由换热。一种套管式浮头换热器包括依次密封连接的前端管箱、前端管板、中间管箱、中间管板、壳体、后封头,壳体内部有浮头管板,U形换热管的两端管头与前端管板密封连接,U形换热管的直管穿过中间管板、浮头管板,浮头管板上密封连接有罩住U形换热管的弯管部分的浮头盖,中间管板与浮头管板之间连接有套于U形换热管的直管上的套管;换热器内部形成管程、中间管程、壳程三个相互隔离、独自构成回路的介质流程;前端管箱中间设有管程隔板,中间管箱中间设有中间管程隔板。
The invention relates to a casing type heat exchanger, in particular to a casing type floating head heat exchanger. The invention is used to realize the heat exchange requirements of two kinds of high temperature difference, high pressure difference, and even not allowing direct contact with two kinds of media, and can realize free heat exchange of three kinds of media at the same time. A casing type floating head heat exchanger comprises a front end tube box, a front end tube sheet, a middle tube box, a middle tube sheet, a shell and a rear head which are sealed and connected in sequence, and the shell is provided with a floating head tube sheet and a U-shaped heat exchange tube. The two ends of the tube head are sealed with the front tube sheet, the straight tube of the U-shaped heat exchange tube passes through the middle tube sheet and the floating head tube sheet, and the floating head tube sheet is sealed and connected with a floating head covering the elbow part of the U-shaped heat exchange tube. The cover, the middle tube sheet and the floating head tube sheet are connected with a casing sleeved on the straight pipe of the U-shaped heat exchange tube; the tube side, the middle pipe side and the shell side are formed inside the heat exchanger, which are isolated from each other and form a circuit independently. There is a tube-side partition in the middle of the front-end tube box, and an intermediate tube-pass partition in the middle of the middle tube box.
Description
技术领域technical field
本发明涉及套管式换热器,具体为一种套管式浮头换热器。The invention relates to a casing type heat exchanger, in particular to a casing type floating head heat exchanger.
背景技术Background technique
换热器在现代化工生产中发挥着重要的作用。面对化工工业的突飞猛进,各种先进的工艺流程应运而生,同时一系列复杂的工况让现有的化工设备接受着考验。当根据工艺流程为设备选型时,往往会遇到两种高温差、高压差、甚至不允许两种介质直接接触的换热工况。此时,为实现工艺流程,通常会增加多套设备或引入第三种介质来逐步实现工艺流程,无形中增加了项目的投资成本。因此,需要一种新型换热设备来弥补现有设备面对多种复杂工况,设备性能不足的缺陷。Heat exchangers play an important role in modern industrial production. In the face of the rapid development of the chemical industry, various advanced technological processes have emerged, and a series of complex working conditions have put the existing chemical equipment to the test. When the equipment is selected according to the process flow, two kinds of high temperature difference, high pressure difference, and even heat exchange conditions that do not allow direct contact between the two media are often encountered. At this time, in order to realize the technological process, usually multiple sets of equipment are added or a third medium is introduced to gradually realize the technological process, which invisibly increases the investment cost of the project. Therefore, a new type of heat exchange equipment is needed to make up for the shortcomings of the existing equipment that faces a variety of complex working conditions and the equipment performance is insufficient.
发明内容SUMMARY OF THE INVENTION
本发明提供一种套管式浮头换热器,用以实现两种高温差、高压差、甚至不允许直接接触两种介质的换热要求,同时能实现三种介质的自由换热。The invention provides a casing type floating head heat exchanger, which is used to realize the heat exchange requirements of two kinds of high temperature difference, high pressure difference, and even not allowing direct contact with two kinds of media, and can realize free heat exchange of three kinds of media at the same time.
本发明是采用如下技术方案实现的:一种套管式浮头换热器,包括依次密封连接的前端管箱、前端管板、中间管箱、中间管板、壳体、后封头,壳体与后封头连接的一端内部有浮头管板,U形换热管的两端管头与前端管板密封连接,U形换热管的直管穿过中间管板、浮头管板,浮头管板上密封连接有罩住U形换热管的弯管部分的浮头盖,中间管板与浮头管板之间连接有套于U形换热管的直管上的套管;换热器内部形成管程、中间管程、壳程三个相互隔离、独自构成回路的介质流程;前端管箱上有管程入口和管程出口,中间管箱上有中间管程入口和中间管程出口,壳体上有壳程入口和壳程出口;前端管箱中间设有管程隔板,中间管箱中间设有中间管程隔板;管程依次流经管程入口、前端管箱的管程隔板上部空间、U形换热管、前端管箱的管程隔板下部空间、管程出口;中间管程依次流经中间管程入口、中间管箱的中间管程隔板上部空间、套于U形换热管的上部直管上的套管内部、浮头盖内腔、套于U形换热管的下部直管上的套管内部、中间管箱的中间管程隔板下部空间、中间管程出口;壳程流经壳程入口、壳体与套管之间的空间、浮头盖与后封头之间的空间、壳程出口。The present invention is realized by adopting the following technical solutions: a casing-type floating head heat exchanger, comprising a front-end tube box, a front-end tube sheet, a middle tube box, a middle tube sheet, a shell, a rear head and a shell which are sealed and connected in sequence. The end connected with the rear head has a floating head tube sheet inside, the two ends of the U-shaped heat exchange tube are sealed with the front tube sheet, and the straight tube of the U-shaped heat exchange tube passes through the middle tube sheet, the floating head tube sheet, and the floating head tube. The plate is sealed and connected with a floating head cover covering the elbow part of the U-shaped heat exchange tube, and a sleeve on the straight pipe of the U-shaped heat exchange tube is connected between the intermediate tube plate and the floating head tube plate; inside the heat exchanger It forms a medium flow that is isolated from each other and forms a loop independently; the front-end tube box has a tube-side inlet and a tube-side outlet, and the middle tube box has a middle tube-side inlet and an intermediate tube-side outlet. The shell has a shell side inlet and a shell side outlet; a tube side separator is arranged in the middle of the front-end tube box, and a middle tube-side separator is arranged in the middle of the middle tube box; The upper space of the plate, the U-shaped heat exchange tube, the lower space of the tube side separator of the front-end tube box, and the tube side outlet; the middle tube side flows through the middle tube side inlet, the upper space of the middle tube side separator of the middle tube box, and is sleeved in the middle tube side. The inside of the casing on the upper straight tube of the U-shaped heat exchange tube, the inner cavity of the floating head cover, the inside of the casing on the lower straight tube of the U-shaped heat exchange tube, the space at the lower part of the middle tube side partition of the middle tube box, the middle Tube side outlet; the shell side flows through the shell side inlet, the space between the shell and the casing, the space between the floating head cover and the rear head, and the shell side outlet.
本发明所述套管式浮头换热器,实现了两种高温差、高压差、甚至不允许直接接触两种介质的换热要求,同时能实现三种介质的自由换热。具有结构紧凑、安全可靠、适用范围广、满足多种复杂工艺要求的特点。The sleeve-type floating head heat exchanger of the present invention realizes the heat exchange requirements of two kinds of high temperature difference, high pressure difference, and even does not allow direct contact with two kinds of media, and can realize free heat exchange of three kinds of media at the same time. It has the characteristics of compact structure, safety and reliability, wide application range, and meets various complex process requirements.
附图说明Description of drawings
图1为本发明的结构示意图;Fig. 1 is the structural representation of the present invention;
图2为U形换热管的结构示意图;Figure 2 is a schematic structural diagram of a U-shaped heat exchange tube;
图3为图2的一个局部左视图;Fig. 3 is a partial left side view of Fig. 2;
图4为图2的另一个局部左视图。FIG. 4 is another partial left side view of FIG. 2 .
图中:1-前端管箱,2-前端管板,3-中间管箱,4-中间管板,5-壳体,6-折流板,7-浮头管板,8-浮头盖,9-后封头,10-U形换热管,11-套管,12-管程隔板,13-中间管程隔板。In the picture: 1- Front end tube box, 2- Front end tube sheet, 3- Middle tube box, 4- Middle tube sheet, 5- Shell, 6- Baffle plate, 7- Floating head tube sheet, 8- Floating head cover, 9 - Rear head, 10-U-shaped heat exchange tube, 11-Sleeve, 12-Tube side separator, 13- Middle tube side separator.
具体实施方式Detailed ways
一种套管式浮头换热器,包括依次密封连接的前端管箱1、前端管板2、中间管箱3、中间管板4、壳体5、后封头9,壳体5与后封头9连接一端内部有浮头管板7,U形换热管10的两端管头与前端管板2密封连接,U形换热管10的直管穿过中间管板4、浮头管板7,浮头管板7上密封连接有罩住U形换热管10的弯管部分的浮头盖8,中间管板4与浮头管板7之间连接有套于U形换热管10的直管上的套管11;换热器内部形成管程、中间管程、壳程三个相互隔离、独自构成回路的介质流程;前端管箱1上有管程入口和管程出口,中间管箱3上有中间管程入口和中间管程出口,壳体5上有壳程入口和壳程出口;前端管箱1中间设有管程隔板12,中间管箱3中间设有中间管程隔板13;管程依次流经管程入口、前端管箱1的管程隔板12上部空间、U形换热管10、前端管箱1的管程隔板12下部空间、管程出口;中间管程依次流经中间管程入口、中间管箱3的中间管程隔板13上部空间、套于U形换热管10的上部直管上的套管11内部、浮头盖8内腔、套于U形换热管10的下部直管上的套管11内部、中间管箱3的中间管程隔板13下部空间、中间管程出口;壳程流经壳程入口、壳体5与套管11之间的空间、浮头盖8与后封头9之间的空间、壳程出口。A casing type floating head heat exchanger, comprising a front end tube box 1, a front end tube sheet 2, a middle tube box 3, a middle tube sheet 4, a shell 5, a rear head 9, the shell 5 and the rear seal, which are sequentially sealed and connected. There is a floating head tube sheet 7 inside the connecting end of the head 9, the two ends of the U-shaped heat exchange tube 10 are sealed with the front end tube sheet 2, and the straight pipe of the U-shaped heat exchange tube 10 passes through the middle tube sheet 4 and the floating head tube sheet 7. , the floating head tube plate 7 is sealed and connected with a floating head cover 8 covering the elbow portion of the U-shaped heat exchange tube 10, and a straight tube sleeved on the U-shaped heat exchange tube 10 is connected between the intermediate tube plate 4 and the floating head tube plate 7 The casing 11 on the upper part of the heat exchanger; the tube side, the middle pipe side, and the shell side are formed inside the heat exchanger, which are isolated from each other and form a separate circuit; the front end pipe box 1 has a pipe side inlet and a tube side outlet, and the middle pipe box 3 There are middle tube side inlet and middle tube side outlet, shell 5 has shell side inlet and shell side outlet; front end tube box 1 is provided with tube side separator 12, middle tube box 3 is provided with middle tube side separator 13; The tube pass flows through the tube pass inlet, the upper space of the tube pass partition 12 of the front end tube box 1, the U-shaped heat exchange tube 10, the lower space of the tube pass partition 12 of the front end tube box 1, and the tube pass outlet in turn; the middle tube pass It flows through the inlet of the middle tube side, the upper space of the middle tube side partition plate 13 of the middle tube box 3, the inside of the sleeve 11 sleeved on the upper straight pipe of the U-shaped heat exchange tube 10, the inner cavity of the floating head cover 8, and the inner cavity of the U-shaped heat exchange tube 10. The inside of the casing 11 on the lower straight pipe of the heat exchange tube 10, the lower space of the middle tube side partition plate 13 of the middle tube box 3, the middle tube side outlet; the shell side flows through the shell side inlet, between the shell 5 and the casing 11 , the space between the floating head cover 8 and the rear head 9, and the shell side outlet.
本换热器运行时,管程箱体的U形换热管10、中间管程腔体的套管11、壳程腔体的壳体5均可自由伸缩,不会因三种介质的温差而产生温差应力,对设备造成危害。当工况为两种不允许直接接触的工艺介质时,可将两介质分别通入管程和壳程,在中间管程通入中和介质,两种工艺介质被中间管程隔开,即使管程和壳程任何一个部位出现腐蚀泄露,会被中间管程中的介质中和,不会引起两种工艺介质的直接接触,安全可靠。当两工艺介质压差较大时,可在中间管程通入一定压力的无害介质,降低工艺介质的压力差值,以此实现用较薄的管板承受较大的压力工况,降低了设备成本。When the heat exchanger is running, the U-shaped heat exchange tube 10 of the tube-side box, the sleeve 11 of the intermediate tube-side cavity, and the shell 5 of the shell-side cavity can be freely expanded and contracted, and will not be affected by the temperature difference of the three media. The thermal stress is generated, which is harmful to the equipment. When the working conditions are two process media that do not allow direct contact, the two media can be passed into the tube side and the shell side respectively, and the neutralizing medium can be passed into the middle tube side, and the two process media are separated by the middle tube side. Corrosion leakage occurs in any part of the process and the shell side, which will be neutralized by the medium in the middle tube side, and will not cause direct contact between the two process media, which is safe and reliable. When the pressure difference between the two process media is large, a harmless medium with a certain pressure can be introduced into the middle tube side to reduce the pressure difference of the process medium, so as to realize the use of thinner tube sheets to withstand larger pressure conditions and reduce equipment cost.
多组U形换热管10穿过套管11形成管束,套管11外设折流板6,可对套管11起到支撑作用,同时可改变壳程介质的流向,提高换热效率。Multiple groups of U-shaped heat exchange tubes 10 pass through the casing 11 to form a tube bundle. The casing 11 is provided with a baffle 6, which can support the casing 11 and change the flow direction of the shell-side medium to improve the heat exchange efficiency.
U形换热管10的直管外壁上设置有翅片或槽道,翅片或槽道对U形换热管10具有一定的支撑固定作用,可减小设备运行时U形换热管10的振动,也可对中间管程介质起到扰流作用,增强设备换热效果。Fins or channels are arranged on the outer wall of the straight tube of the U-shaped heat exchange tube 10. The fins or channels have a certain supporting and fixing effect on the U-shaped heat exchange tube 10, which can reduce the size of the U-shaped heat exchange tube 10 when the equipment is running. The vibration can also play a turbulent role in the intermediate tube side medium and enhance the heat exchange effect of the equipment.
Claims (3)
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CN201910388633.7A CN110030851A (en) | 2019-05-10 | 2019-05-10 | A kind of bushing type floating head heat exchanger |
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CN113566611A (en) * | 2021-08-12 | 2021-10-29 | 上海蓝滨石化设备有限责任公司 | U-shaped pipe three-flow heat exchanger |
CN113566611B (en) * | 2021-08-12 | 2023-12-19 | 上海蓝滨石化设备有限责任公司 | U-shaped tube three-flow heat exchanger |
CN118776347A (en) * | 2024-08-12 | 2024-10-15 | 江苏东方瑞吉能源装备有限公司 | A multi-stream coiled tube heat exchanger and a method of using the same |
CN118776347B (en) * | 2024-08-12 | 2025-04-22 | 江苏东方瑞吉能源装备有限公司 | A multi-stream coiled tube heat exchanger and a method of using the same |
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