CN210718772U - Double flow double shell side full countercurrent heat exchanger - Google Patents
Double flow double shell side full countercurrent heat exchanger Download PDFInfo
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- CN210718772U CN210718772U CN201921352902.6U CN201921352902U CN210718772U CN 210718772 U CN210718772 U CN 210718772U CN 201921352902 U CN201921352902 U CN 201921352902U CN 210718772 U CN210718772 U CN 210718772U
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- 239000012530 fluid Substances 0.000 claims abstract description 66
- 238000000034 method Methods 0.000 claims description 4
- 238000005192 partition Methods 0.000 abstract description 7
- 230000008676 import Effects 0.000 abstract 3
- 238000007789 sealing Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 6
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Abstract
Description
技术领域technical field
本实用新型涉及换热器技术领域,特别是涉及一种双股流双壳程全逆流换热器。The utility model relates to the technical field of heat exchangers, in particular to a double-flow double-shell-pass full countercurrent heat exchanger.
背景技术Background technique
换热器是一种实现冷热流体热量传递的重要工业设备,应用于各种流程性工业领域。常见的换热器一般仅有两种流体进行换热,如果有三种及以上流体同时换热,需要串联或并联多台换热器,从而使设备投资大大增加,动力消耗和热量损失也相应增大,同时也增大了设备占地面积。Heat exchanger is an important industrial equipment that realizes heat transfer of cold and hot fluids, and is used in various process industries. Common heat exchangers generally only have two kinds of fluids for heat exchange. If there are three or more fluids for heat exchange at the same time, multiple heat exchangers need to be connected in series or in parallel, which greatly increases equipment investment and increases power consumption and heat loss accordingly. It also increases the footprint of the equipment.
专利CN206724759U公开了一种多股流换热器,包括筒体、设于筒体内的多根换热管、进流管、出流管、进液室、出液室和隔板。该专利通过在进液室和出液室内设置隔板,将进液室和出液室分为相互独立的多个腔室,多个腔室对应相同数量的换热管,通入不同的介质,达到同时与筒体内腔中的流体进行换热的效果。上述技术方案中换热器为单壳程,两股管程流体同时与一种壳程流体进行热交换,导致总传热温差增小,两股管程流体不能与壳程流体充分换热。Patent CN206724759U discloses a multi-stream heat exchanger, which includes a cylindrical body, a plurality of heat exchange tubes arranged in the cylindrical body, an inflow pipe, an outflow pipe, a liquid inlet chamber, a liquid outlet chamber and a partition plate. This patent divides the liquid inlet chamber and the liquid outlet chamber into multiple independent chambers by arranging partitions in the liquid inlet chamber and the liquid outlet chamber, and the multiple chambers correspond to the same number of heat exchange tubes, which are connected to different media. , to achieve the effect of heat exchange with the fluid in the inner cavity of the cylinder at the same time. In the above technical solution, the heat exchanger is a single shell side, and two pipe side fluids exchange heat with one shell side fluid at the same time, resulting in an increase in the total heat transfer temperature difference, and the two pipe side fluids cannot fully exchange heat with the shell side fluid.
实用新型内容Utility model content
为了克服上述现有技术的不足,本实用新型提供了一种双股流双壳程全逆流换热器。In order to overcome the above-mentioned deficiencies of the prior art, the utility model provides a double-flow double-shell-pass full countercurrent heat exchanger.
本实用新型所采用的技术方案是:一种双股流双壳程全逆流换热器,主要包括壳体、换热管、半弓形折流板、管板、管箱、管程分程隔板、壳程分程隔板、壳程流体进出口接管、第一股管程流体进出口接管以及第二股管程流体进出口接管,其特征在于:所述壳体内设有一块壳程分程隔板,壳程分程隔板与一端管板垂直焊接,与另一端管板保持一定间距,同时与壳体保持密封,从而将壳程分成双壳程;两端的管箱内均设置有管程分程隔板,每个管箱上均设置有管程流体进出口接管,从而将管箱及换热管束分为第一股管程和第二股管程,第一股管程流体进口接管设置在靠近壳程流体出口接管管箱上,并与壳程流体出口接管位于换热器同侧,而管程的流体出口接管设置在另一端管箱的对应位置上;第二股管程流体进出口接管在两端管箱上的位置正好与第一股管程流体进出口接管左右相反。The technical scheme adopted by the utility model is: a double-flow double-shell-pass full countercurrent heat exchanger, which mainly includes a shell, a heat exchange tube, a semi-arctic baffle, a tube sheet, a tube box, and a tube-pass splitter. The plate, the shell-side split-pass baffle, the shell-side fluid inlet and outlet connections, the first tube-side fluid inlet and outlet connections, and the second tube-side fluid inlet and outlet connections, are characterized in that: the shell is provided with a shell-side splitter The shell-side split-pass separator is vertically welded with one end of the tube sheet, and maintains a certain distance with the other end of the tube sheet, and at the same time is sealed with the shell, so that the shell side is divided into two shell paths; the tube boxes at both ends are provided with The tube side is divided into a partition, and each tube box is provided with a tube side fluid inlet and outlet connection, so that the tube box and the heat exchange tube bundle are divided into the first tube side and the second tube side. The first tube side fluid The inlet pipe is arranged on the pipe box close to the shell side fluid outlet, and is located on the same side of the heat exchanger as the shell side fluid outlet pipe, and the fluid outlet pipe of the tube side is arranged at the corresponding position of the other end of the pipe box; the second pipe The position of the inlet and outlet pipes of the process fluid on the pipe boxes at both ends is just opposite to the left and right of the inlet and outlet pipes of the first pipe side.
所述的第一股管程和第二股管程中,每股管程流体与相对应壳程流体流向均为逆流,与壳程流体温差大的流体走第一股管程,与壳程流体温差小的流体走第二股管程。In the first tube side and the second tube side, the flow direction of each tube side fluid and the corresponding shell side fluid is countercurrent, and the fluid with a large temperature difference with the shell side fluid goes to the first tube side, and the shell side fluid flows in the opposite direction. The fluid with small temperature difference of fluid goes to the second pipe pass.
所述的第一股管程和第二股管程的换热管数量,根据两股管程流体的流量和换热量而定,再根据每股管程的管子数确定壳程分程隔板和管程分程隔板的相应位置,壳程分程隔板和管程分程隔板均处于同一平面内。The number of heat exchange tubes of the first tube side and the second tube side is determined according to the flow rate and heat exchange of the two tube side fluids, and then the shell side separation distance is determined according to the number of tubes in each tube side. The corresponding positions of the plate and the tube-side split-pass separator, the shell-side split-pass separator and the tube-side split-pass separator are all in the same plane.
所述的壳程分程隔板和管程分程隔板同为水平布置或者竖直布置。The shell-side split-pass baffles and the tube-side split-pass baffles are both arranged horizontally or vertically.
与现有技术相比,本实用新型的有益效果:一是该换热器采用壳程分程隔板,可实现双壳程流动,可提高壳程流体速度,并延长流体在壳程的流动时间,同时每股管程流体和相对应的壳程流体均为逆流,提高了换热器的整体换热效率;二是与壳程流体温差大的管程流体走第一股管程,与壳程流体温差较小的管程流体走第二股管程,使换热器的总传热温差增大,可实现两股管程流体与壳程流体充分换热。Compared with the prior art, the beneficial effects of the present utility model are as follows: First, the heat exchanger adopts a shell-side split-pass baffle, which can realize double-shell-side flow, increase the fluid velocity on the shell-side, and prolong the flow of the fluid on the shell-side. At the same time, each tube-side fluid and the corresponding shell-side fluid are countercurrent, which improves the overall heat exchange efficiency of the heat exchanger; second, the tube-side fluid with a large temperature difference with the shell-side fluid goes to the first tube-side, and the The tube-side fluid with a smaller temperature difference between the shell-side fluids goes to the second tube-side, which increases the total heat transfer temperature difference of the heat exchanger, and can achieve full heat exchange between the two-tube-side fluid and the shell-side fluid.
附图说明Description of drawings
图1为双股流双壳程全逆流换热器的结构示意图。Figure 1 is a schematic structural diagram of a double-flow double-shell-pass full countercurrent heat exchanger.
附图标记:1-管程分程隔板;2-第一管程流体进口接管;3-壳体流体出口接管;4-换热管;5-壳程分程隔板;6-半弓形折流板;7-拉杆及定距管;8-壳体;9-兼做法兰管板;10-管箱法兰;11-第一管程流体出口接管;12-管箱;13-第二管程流体进口接管;14-壳体流体进口接管;15-第二管程流体出口接管。Reference numerals: 1-tube-side split-pass baffle; 2-first tube-side fluid inlet nozzle; 3-shell fluid outlet nozzle; 4-heat exchange tube; 5-shell-side split-pass baffle; 6-semi-bow Baffle plate; 7-tie rod and spacer pipe; 8-shell; 9-double as flanged tube plate; 10-pipe box flange; 11-first pipe side fluid outlet pipe; 12-pipe box; 13-section The second tube side fluid inlet pipe; 14 - the shell fluid inlet pipe; 15 - the second pipe side fluid outlet pipe.
具体实施方式Detailed ways
下面结合附图对本实用新型进一步说明。The present utility model will be further described below in conjunction with the accompanying drawings.
双股流双壳程全逆流换热器,采用固定管板式换热器,首先,将壳程分程隔板和一端管板焊接固定,然后通过拉杆及定距管在壳程分程隔板的两侧布置并固定半弓形折流板,半弓形折流板的缺口采用左右布置,接着将换热管逐个穿过所述管板和半弓形折流板,然后将整个管束及半弓形折流板装入壳体,并将所述管板与壳体焊接;在壳体另一端焊接固定另一块管板,并将每个换热管的另一端逐个引入该管板,然后将所有换热管的两端与对应的管板进行焊接固定;最后安装壳程流体进出口接管以及支座,完成整个壳体的装配。接着把管箱分程隔板装入管箱并焊接固定,在两端管箱上分别焊接管程流体进出口接管,然后将两端管箱分别通过管箱法兰和壳体法兰与壳体相连接,管箱分程隔板正对着管板上的隔板槽。The double-flow double-shell-pass full counter-flow heat exchanger adopts a fixed tube-sheet heat exchanger. First, the shell-side split-pass separator and one end of the tube sheet are welded and fixed, and then the shell-side split-pass separator is fixed by means of tie rods and spacer tubes. Arrange and fix the half-arc-shaped baffles on both sides, and the gaps of the half-arc-shaped baffles are arranged on the left and right sides, and then pass the heat exchange tubes through the tube sheets and the half-arc-shaped baffles one by one, and then fold the whole tube bundle and the half-arc-shaped baffles one by one. The flow plate is loaded into the shell, and the tube plate is welded to the shell; another tube plate is welded and fixed at the other end of the shell, and the other end of each heat exchange tube is introduced into the tube plate one by one, and then all the heat exchange tubes are welded together. The two ends of the heat pipe are welded and fixed with the corresponding tube sheet; finally, the shell side fluid inlet and outlet pipes and supports are installed to complete the assembly of the entire shell. Next, put the pipe box dividing plate into the pipe box and fix it by welding. Weld the pipe-side fluid inlet and outlet pipes on the pipe boxes at both ends, and then connect the pipe boxes at both ends through the pipe box flange and the shell flange and the shell respectively. The tubes are connected to each other, and the splitter of the tube box is facing the separator groove on the tube plate.
以上所述仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the within the protection scope of the present invention.
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CN201921352902.6U CN210718772U (en) | 2019-08-20 | 2019-08-20 | Double flow double shell side full countercurrent heat exchanger |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN113893569A (en) * | 2020-07-07 | 2022-01-07 | 中国石油化工股份有限公司 | Static crystallization apparatus and static crystallization method |
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CN113893569A (en) * | 2020-07-07 | 2022-01-07 | 中国石油化工股份有限公司 | Static crystallization apparatus and static crystallization method |
CN113893569B (en) * | 2020-07-07 | 2023-08-04 | 中国石油化工股份有限公司 | Static crystallization apparatus and static crystallization method |
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Granted publication date: 20200609 Termination date: 20210820 |