CN218097385U - Heat transfer jacket structure - Google Patents
Heat transfer jacket structure Download PDFInfo
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- CN218097385U CN218097385U CN202221611846.5U CN202221611846U CN218097385U CN 218097385 U CN218097385 U CN 218097385U CN 202221611846 U CN202221611846 U CN 202221611846U CN 218097385 U CN218097385 U CN 218097385U
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- 238000003466 welding Methods 0.000 claims abstract description 20
- 239000012530 fluid Substances 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims description 34
- 239000011229 interlayer Substances 0.000 claims description 23
- 238000009825 accumulation Methods 0.000 claims description 12
- 239000010410 layer Substances 0.000 claims description 6
- 239000011159 matrix material Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 241000521257 Hydrops Species 0.000 abstract 2
- 206010030113 Oedema Diseases 0.000 abstract 2
- 235000013405 beer Nutrition 0.000 description 6
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 230000002093 peripheral effect Effects 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 229910000679 solder Inorganic materials 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及传热夹套技术领域,具体指一种传热夹套结构。The utility model relates to the technical field of heat transfer jackets, in particular to a heat transfer jacket structure.
背景技术Background technique
露天发酵罐由于投资省、生产周期短、自动化管理方便和啤酒质量稳定等许多优点,在发酵过程中,为了及时散出发酵产生的热量,并使发酵罐内的温度均匀,在发酵罐的外壁装有冷却夹套。目前的啤酒发酵罐大都使用在一块约4~8mm的不锈钢厚板的外表面上焊接薄板的各种夹套,在夹套中通入冷却媒介,实现啤酒发酵的功能。发酵罐的内表面都是光滑平整的,罐体外面通过保温来减少冷能量的损失。Due to the low investment, short production cycle, convenient automatic management and stable beer quality, the open-air fermenter has many advantages. Equipped with cooling jacket. Most of the current beer fermentation tanks use various jackets welded with thin plates on the outer surface of a thick stainless steel plate of about 4 to 8 mm, and a cooling medium is passed into the jacket to realize the function of beer fermentation. The inner surface of the fermenter is smooth and flat, and the outside of the tank is insulated to reduce the loss of cold energy.
由于啤酒发酵时产生大量热能,需要在尽可能短的时间利用夹套内的冷却媒介迅速冷却啤酒。但是,现有的夹套中,由于罐壁较厚并且不锈钢导热热阻大,传热效果差,随着发酵罐体积越来越大,很难满足啤酒发酵的工艺要求。Since a large amount of heat energy is generated during beer fermentation, it is necessary to rapidly cool the beer with the cooling medium in the jacket in the shortest possible time. However, in the existing jacket, due to the thicker tank wall and the large thermal resistance of stainless steel, the heat transfer effect is poor. As the volume of the fermenter becomes larger and larger, it is difficult to meet the technological requirements of beer fermentation.
为了提高传热效率,申请人在先申请的专利申请号为CN200420037437.4(公布号为CN2750279Y)的中国实用新型专利《内置式激光焊传热夹套结构》以及专利申请号为CN201310151188.5(公布号为CN104120053A)的中国发明专利《一种蜂窝夹套发酵罐》公开了一种传热夹套结构,该传热夹套结构包括两块板,在两块板的板面上具有按一定几何形状排列的焊接区,而其它非焊接区部分呈凸弧状,使得其内腔剖面呈凹凸起伏的蜂窝状。In order to improve the heat transfer efficiency, the applicant's patent application number CN200420037437.4 (publication number CN2750279Y) and the Chinese utility model patent "built-in laser welding heat transfer jacket structure" and the patent application number CN201310151188.5 ( The Chinese invention patent "A Honeycomb Jacketed Fermentation Tank" with publication number CN104120053A) discloses a heat transfer jacket structure, which includes two plates, on which there are certain The welding area arranged in a geometric shape, while the other non-welding areas are in a convex arc shape, so that the inner cavity section is in a concave-convex honeycomb shape.
具体地,如图1所示,两块板体1之间形成有夹层11,该夹层11中布置有多个用于将两块板体1焊接在一起的焊点12,两块板体1的相邻周缘相互焊接形成有用于对夹层11周部进行封闭的焊缝13,位于外侧的板体1上具有与夹层11相贯通的排液口14,夹套停止工作时,夹套结构底层通道111内低于排液口的部分无法排尽而导致存在积液,随着水的挥发,氯离子浓度会逐渐提高,随着夹套的反复工作及停止工作中,底层通道111内的氯离子浓度逐渐升高,氯离子浓度达到一定比例,对最下面一道焊缝会有腐蚀,泄漏风险增大。Specifically, as shown in FIG. 1, an
实用新型内容Utility model content
本实用新型所要解决的技术问题是针对现有技术的现状,提供一种能够尽可能减少积液残留的传热夹套结构。The technical problem to be solved by the utility model is to provide a heat transfer jacket structure that can reduce the residual liquid accumulation as much as possible in view of the current state of the prior art.
本实用新型解决上述技术问题所采用的技术方案为:一种传热夹套结构,包括有两块板体,两块板体之间形成有夹层,两块板体的相邻周缘相互焊接形成有用于对夹层周部进行封闭的焊缝,位于外侧的所述板体上具有与所述夹层相贯通的排液口,其特征在于:所述板体底部的焊缝包括有依次连接的U形段和水平直线段,该U形段与两块板体之间包围形成有位于所述夹层底部的积液槽,所述的排液口位于所述U形段的正上方,且排液口的最低点低于所述的水平直线段。The technical scheme adopted by the utility model to solve the above technical problems is: a heat transfer jacket structure, including two plates, an interlayer is formed between the two plates, and the adjacent peripheral edges of the two plates are welded to each other to form There is a welding seam for sealing the periphery of the interlayer, and the outer plate body has a liquid discharge port that communicates with the interlayer. It is characterized in that: the weld seam at the bottom of the plate body includes sequentially connected U U-shaped section and a horizontal straight section, surrounded by the U-shaped section and the two boards, there is a liquid accumulation groove at the bottom of the interlayer, and the liquid discharge port is located directly above the U-shaped section, and the liquid discharge The lowest point of the mouth is lower than said horizontal straight line segment.
为了在不影响排液的同时减少积液量,将所述积液槽的长度记为L1,将所述排液口的直径记为D,1/3≤D/L1≤1/8。In order to reduce the amount of liquid accumulation without affecting the liquid discharge, the length of the liquid accumulation groove is marked as L1, and the diameter of the liquid discharge port is marked as D, 1/3≦D/L1≦1/8.
优选地,所述L1的值为180~220mm。Preferably, the value of L1 is 180-220mm.
优选地,所述D的值为40~50mm。Preferably, the value of D is 40-50 mm.
为了保证积液量大幅度下降,将所述板体的长度记为L2,1/20≤L1/L2≤1/50。In order to ensure a significant reduction in the amount of effusion, the length of the plate body is recorded as L2, 1/20≤L1/L2≤1/50.
优选地,所述L2的值为6000~8000mm。Preferably, the value of L2 is 6000-8000mm.
为了提高夹层中流体的传热效率,所述的夹层中布置有多个用于将两块板体焊接在一起的焊点。In order to improve the heat transfer efficiency of the fluid in the interlayer, a plurality of welding points for welding the two plates are arranged in the interlayer.
为了保证底层通道的流体顺畅排出,所述的焊点呈矩阵状间隔布置,位于最下面一排的焊点、水平直线段与两块板体之间包围形成有底层通道,将该底层通道的高度记为H,将所述排液口的直径记为D,H<D<2H。In order to ensure the smooth discharge of the fluid in the bottom channel, the solder joints are arranged at intervals in a matrix, and a bottom channel is formed between the solder joints in the bottom row, the horizontal straight line section and the two plates. The height is denoted as H, and the diameter of the discharge port is denoted as D, where H<D<2H.
优选地,所述H的值为30~35mm。Preferably, the value of H is 30-35mm.
与现有技术相比,本实用新型的优点在于:通过将板体底部的焊缝设计成依次连接的U形段和水平直线段,该U形段与两块板体之间包围形成有位于夹层底部的积液槽,排液时,夹层中冷媒或热媒通过U形段正上方的排液口排出,由于排液口的最低点低于水平直线段,底层通道内的液体会排空而避免出现积液,只有部分液体会残留在积液槽中,避免大范围腐蚀,减小泄漏风险。Compared with the prior art, the utility model has the advantage that: by designing the welding seam at the bottom of the plate body as a U-shaped section and a horizontal straight line section connected in sequence, a U-shaped section and two plates are enclosed and formed between the two plates. The liquid accumulation tank at the bottom of the interlayer, when draining, the refrigerant or heat medium in the interlayer is discharged through the liquid discharge port directly above the U-shaped section. Since the lowest point of the liquid discharge port is lower than the horizontal straight section, the liquid in the bottom channel will be emptied To avoid effusion, only part of the liquid will remain in the effusion tank, avoiding extensive corrosion and reducing the risk of leakage.
附图说明Description of drawings
图1为背景技术中传热夹套结构的结构示意图;Fig. 1 is the structural representation of heat transfer jacket structure in the background technology;
图2为本实用新型传热夹套结构的实施例的结构示意图。Fig. 2 is a structural schematic diagram of an embodiment of the heat transfer jacket structure of the present invention.
具体实施方式detailed description
以下结合附图实施例对本实用新型作进一步详细描述。The utility model is described in further detail below in conjunction with the accompanying drawings.
如图2所示,为本实用新型传热夹套结构的一个优选实施例。该传热夹套结构包括有两块板体1。As shown in Figure 2, it is a preferred embodiment of the structure of the heat transfer jacket of the present invention. The heat transfer jacket structure includes two
其中,两块板体1之间形成有夹层11,该夹层11中呈矩阵状间隔布置有多个用于将两块板体1焊接在一起的焊点12,两块板体1的相邻周缘相互焊接形成有用于对夹层11周部进行封闭的焊缝13,位于外侧的板体1上具有与夹层11相贯通的排液口14。Wherein, an
本实施例中,板体1底部的焊缝13包括有依次连接的U形段131和水平直线段132,位于最下面一排的焊点12、水平直线段132与两块板体1之间包围形成有底层通道111,U形段131与两块板体1之间包围形成有积液槽112,该积液槽112位于夹层11的底部,低于上述底层通道111,另外,排液口14位于U形段131的正上方,且排液口14的最低点低于水平直线段132。In this embodiment, the
将积液槽112的长度记为L1,将板体1的长度记为L2,将排液口14的直径记为D,将底层通道111的高度记为H,1/20≤L1/L2≤1/50,1/3≤D/L1≤1/8且H<D<2H。积液槽112长度控制尽量短,只要保障积液槽112处的鼓胀及排液口14有空间即可,根据多年的制造经验,L1的值优选为180~220mm,L2的值优选为6000~8000mm,D的值优选为40~50mm,H的值优选为30~35mm。The length of the
本实施例的工作原理如下:使用时,将位于内侧的板体1作为反应器、搅拌器等设备的换热面,其内为容器空间,位于外侧的板体1作为反应器、搅拌器等设备的罐体壁,其外则为大气空间;The working principle of this embodiment is as follows: when in use, the
(1)工作时,将冷媒或热媒充入两块板体1之间的夹层11中,可与容器空间内的流体进行换热,夹层11中焊点12的设计可阻扰流体流动形成湍流,提高传热效率;(1) During work, the refrigerant or heat medium is filled into the
(2)工作结束后,打开排液口14,夹层11中冷媒或热媒通过排液口14排出,由于排液口14的最低点低于水平直线段132,底层通道111内的液体会排空而避免出现积液,只有部分液体会残留在积液槽112中,避免大范围腐蚀,减小泄漏风险。(2) After the work is finished, open the
Claims (9)
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