CN206094996U - Shell -and -tube heat exchanger - Google Patents
Shell -and -tube heat exchanger Download PDFInfo
- Publication number
- CN206094996U CN206094996U CN201620509213.1U CN201620509213U CN206094996U CN 206094996 U CN206094996 U CN 206094996U CN 201620509213 U CN201620509213 U CN 201620509213U CN 206094996 U CN206094996 U CN 206094996U
- Authority
- CN
- China
- Prior art keywords
- tube
- heat exchanger
- baffle
- shell
- heat transfer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
- F28D7/16—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 in parallel spaced relation
- F28D7/1607—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 in parallel spaced relation with particular pattern of flow of the heat exchange media, e.g. change of flow direction
-
- 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
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
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
Description
技术领域technical field
本实用新型属于换热器领域,特别涉及一种管壳式换热器。The utility model belongs to the field of heat exchangers, in particular to a shell-and-tube heat exchanger.
背景技术Background technique
换热器是能量系统中使用最为广泛的单元设备之一,在生产中占有重要的地位。由于管壳式换热器具有结构可靠、技术成熟以及使用范围广等优点,因而在工业生产中广泛应用。管壳式换热器主要包括外壳、传热管束和折流板,其中折流板,是其最重要的部件之一,一方面用来支撑传热管束,减少传热管束的挠度,另一方面折流板可改变壳体内流体的流速和流向,增加壳程流体湍流扰动,从而有效的提高换热器的换热效率。目前,普通折流板都会导致壳体内出现一定的滞留死区,影响了换热器的换热效率。Heat exchanger is one of the most widely used unit equipment in energy system, and plays an important role in production. Due to the advantages of reliable structure, mature technology and wide application range, shell and tube heat exchangers are widely used in industrial production. The shell and tube heat exchanger mainly includes the shell, the heat transfer tube bundle and the baffle. The baffle is one of its most important parts. On the one hand, it is used to support the heat transfer tube bundle and reduce the deflection of the heat transfer tube bundle. On the one hand, the baffle can change the flow velocity and flow direction of the fluid in the shell, increase the turbulence of the shell-side fluid, and thus effectively improve the heat exchange efficiency of the heat exchanger. At present, ordinary baffles will lead to a certain stagnation dead zone in the shell, which affects the heat transfer efficiency of the heat exchanger.
实用新型内容Utility model content
为了解决现有的折流板容易导致壳体内出现较多的滞留死区的问题,本实用新型实施例提供了一种管壳式换热器。所述技术方案如下:In order to solve the problem that the existing baffles easily lead to more stagnation dead zones in the shell, the embodiment of the utility model provides a shell-and-tube heat exchanger. Described technical scheme is as follows:
本实用新型实施例提供了一种管壳式换热器,所述换热器包括:壳体、传热管束和多个折流板组件,所述传热管束和所述多个折流板组件均安装在所述壳体内,所述多个折流板组件沿所述壳体的长度方向等距间隔布置,每个所述折流板组件均包括多个呈螺旋结构布置的三角折流板,每个所述三角折流板上均设有多个管孔,所述传热管束通过对应的所述管孔插装在所述折流板组件内;The embodiment of the utility model provides a shell-and-tube heat exchanger, the heat exchanger includes: a shell, a heat transfer tube bundle and a plurality of baffle assemblies, the heat transfer tube bundle and the plurality of baffles The components are installed in the housing, and the plurality of baffle components are arranged at equal intervals along the length direction of the housing, and each of the baffle components includes a plurality of triangular baffles arranged in a spiral structure plate, each of the triangular baffles is provided with a plurality of tube holes, and the heat transfer tube bundle is inserted into the baffle assembly through the corresponding tube holes;
每个所述三角折流板均为曲面板状构件,每个所述三角折流板的曲率均为所述壳体内径的0.5倍至1.5倍。Each of the triangular baffles is a curved plate member, and the curvature of each of the triangular baffles is 0.5 to 1.5 times the inner diameter of the housing.
在本实用新型的另一种实现方式中,所述三角折流板的多个所述管孔在所述换热器的横截面上的投影面积之和为对应的所述三角折流板在所述换热器的横截面上的投影面积的30%至40%。In another implementation manner of the present invention, the sum of the projected areas of the plurality of tube holes of the triangular baffle on the cross section of the heat exchanger is 30% to 40% of the projected area on the cross section of the heat exchanger.
在本实用新型的又一种实现方式中,每个所述三角折流板均包括第一侧边、 第二侧边、外弧边和内弧边,各所述三角折流板的所述第一侧边分别与最近的所述三角折流板的所述第二侧边之间的夹角为15°至90°。In yet another implementation of the present utility model, each of the triangular baffles includes a first side, a second side, an outer arc and an inner arc, and each of the triangular baffles An included angle between the first side and the second side of the nearest triangular baffle is 15° to 90°.
在本实用新型的又一种实现方式中,所述三角折流板的所述内弧边处设有凹陷,同一所述折流板组件的所述三角折流板上的凹陷在所述换热器的横截面上构成中心孔,所述中心孔的直径为所述管孔的直径的1倍至2倍。In yet another implementation of the present invention, the inner arc edge of the triangular baffle is provided with a depression, and the depression on the triangular baffle of the same baffle assembly is located on the A central hole is formed on the cross section of the heater, and the diameter of the central hole is 1 to 2 times the diameter of the tube hole.
在本实用新型的又一种实现方式中,所述壳体内安装有用于支撑所述三角折流板的多个拉杆,每个所述拉杆的两端分别固定安装在所述换热器内两端的管板上且与所述壳体的长度方向平行布置,各个所述三角折流板分别套装在各自对应的三根所述拉杆外,每两个相邻所述三角折流板之间均设有与所述拉杆一一对应的定距管,所述三个定距管分别位于所述外弧边的弧顶处、所述第一侧边的中部和所述第二侧边的中部,每个所述定距管均套装在各自对应的所述拉杆外,所述定距管与所述壳体的长度方向平行。In yet another implementation of the present utility model, a plurality of pull rods for supporting the triangular baffles are installed in the housing, and the two ends of each pull rod are fixedly installed on two ends of the heat exchanger. The tube plate at the end is arranged parallel to the length direction of the shell, and each of the triangular baffles is respectively set outside the three corresponding tie rods, and each two adjacent triangular baffles are provided with There are spacer tubes corresponding to the pull rods one by one, and the three spacer tubes are respectively located at the top of the outer arc, the middle of the first side and the middle of the second side, Each of the distance tubes is sleeved on the respective corresponding pull rods, and the distance tubes are parallel to the length direction of the housing.
在本实用新型的又一种实现方式中,所述壳体的两端各通过所述管板分别连接有管箱,所述传热管束的一端与一个所述管箱连通,所述传热管束的另一端与另一个所述管箱连通,在两个所述管箱上分别设有管程出口和管程进口,所述管程出口和所述管程进口分别通过各自对应的所述管箱与所述传热管束连通。In yet another implementation of the present utility model, both ends of the housing are respectively connected to tube boxes through the tube sheets, one end of the heat transfer tube bundle communicates with one of the tube boxes, and the heat transfer The other end of the tube bundle communicates with the other tube box, and the two tube boxes are respectively provided with a tube pass outlet and a tube pass inlet, and the tube pass outlet and the tube pass inlet respectively pass through the respective corresponding The tube box communicates with the heat transfer tube bundle.
在本实用新型的又一种实现方式中,所述壳体两端的外周壁上分别设有壳程出口和壳程进口,所述壳程出口和所述壳程进口连通。In yet another implementation manner of the present invention, a shell-side outlet and a shell-side inlet are respectively provided on the outer peripheral walls at both ends of the housing, and the shell-side outlet and the shell-side inlet are connected.
在本实用新型的又一种实现方式中,所述传热管束包括多个传热管,各所述传热管插装在各自对应的所述管孔中,各所述传热管相互平行布置。In yet another implementation of the present utility model, the heat transfer tube bundle includes a plurality of heat transfer tubes, each of the heat transfer tubes is inserted into the corresponding tube hole, and each of the heat transfer tubes is parallel to each other. layout.
在本实用新型的又一种实现方式中,所述折流板组件为碳钢构件或不锈钢构件。In yet another implementation manner of the present utility model, the baffle assembly is a carbon steel component or a stainless steel component.
本实用新型实施例提供的技术方案带来的有益效果是:The beneficial effects brought by the technical solution provided by the embodiment of the utility model are:
在本实施例所提供的换热器工作时,换热流体在壳体与传热管束之间流动,当换热流体在流经折流板组件时,换热流体在各个三角折流板的作用下,形成旋转涡流,从而使得旋转的换热流体能够流经壳体与传热管束之间的每个区域,大大减少了滞留死区的产生,进而提高了换热器的换热效率。When the heat exchanger provided in this embodiment is in operation, the heat exchange fluid flows between the shell and the heat transfer tube bundle. When the heat exchange fluid flows through the baffle assembly, the heat exchange fluid passes through Under the action, a rotating vortex is formed, so that the rotating heat exchange fluid can flow through each area between the shell and the heat transfer tube bundle, greatly reducing the stagnation dead zone, and thus improving the heat exchange efficiency of the heat exchanger.
附图说明Description of drawings
为了更清楚地说明本实用新型实施例中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍。显而易见地,下面描述中的附图仅仅是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to illustrate the technical solutions in the embodiments of the present utility model more clearly, the following will briefly introduce the drawings required for the description of the embodiments. Apparently, the drawings in the following description are only some embodiments of the present utility model, and those skilled in the art can also obtain other drawings according to these drawings without creative work.
图1是本实用新型实施例提供的换热器的结构示意图;Fig. 1 is a schematic structural view of a heat exchanger provided by an embodiment of the present invention;
图2是本实用新型实施例提供的三角折流板的结构示意图;Fig. 2 is a schematic structural view of a triangular baffle provided by an embodiment of the present invention;
图3是本实用新型实施例提供的折流板组件的左视图;Fig. 3 is a left view of the baffle assembly provided by the embodiment of the present invention;
图中各符号表示含义如下:The meanings of the symbols in the figure are as follows:
1-壳体,11-壳程出口,12-壳程进口,2-传热管束,21-传热管,3-折流板组件,31-三角折流板,311-第一侧边,312-第二侧边,313-外弧边,314-内弧边,32-管孔,33-中心孔,4-管板,5-管箱,51-管程出口,52-管程进口。1-shell, 11-shell side outlet, 12-shell side inlet, 2-heat transfer tube bundle, 21-heat transfer tube, 3-baffle assembly, 31-triangular baffle, 311-first side, 312-second side, 313-outer arc edge, 314-inner arc edge, 32-tube hole, 33-center hole, 4-tube plate, 5-tube box, 51-tube pass outlet, 52-tube pass inlet .
具体实施方式detailed description
为使本实用新型的目的、技术方案和优点更加清楚,下面将结合附图对本实用新型实施方式作进一步地详细描述。In order to make the purpose, technical solutions and advantages of the present utility model clearer, the implementation of the present utility model will be further described in detail below in conjunction with the accompanying drawings.
实施例Example
本实用新型实施例提供的一种管壳式换热器,如图1所示,该换热器包括壳体1、传热管束2和多个折流板组件3,传热管束2和多个折流板组件3均安装在壳体1内,多个折流板组件3沿壳体1的长度方向等距间隔布置,每个折流板组件3均包括多个呈螺旋结构布置的三角折流板31,每个三角折流板31上均设有多个管孔32,传热管束2通过对应的管孔32插装在折流板组件3内。A shell-and-tube heat exchanger provided by the embodiment of the utility model, as shown in Figure 1, the heat exchanger includes a shell 1, a heat transfer tube bundle 2 and a plurality of baffle assemblies 3, Each baffle assembly 3 is installed in the casing 1, and a plurality of baffle assemblies 3 are arranged at equal intervals along the length direction of the casing 1, and each baffle assembly 3 includes a plurality of triangles arranged in a spiral structure. The baffles 31 are provided with a plurality of tube holes 32 on each triangular baffle 31 , and the heat transfer tube bundle 2 is inserted into the baffle assembly 3 through the corresponding tube holes 32 .
在本实施例所提供的换热器工作时,换热流体在壳体1与传热管束2之间流动,当换热流体在流经折流板组件3时,换热流体在各个三角折流板31的作用下,成为旋转涡流,从而使得旋转的换热流体能够流经壳体1与传热管束2之间的每个区域,大大减少了滞留死区的产生,进而提高了换热器的换热效率。When the heat exchanger provided in this embodiment is working, the heat exchange fluid flows between the shell 1 and the heat transfer tube bundle 2. Under the action of the flow plate 31, it becomes a rotating vortex, so that the rotating heat exchange fluid can flow through each area between the shell 1 and the heat transfer tube bundle 2, which greatly reduces the generation of stagnation dead zone, and thus improves the heat exchange. The heat exchange efficiency of the device.
优选地,折流板组件3为碳钢构件或不锈钢构件,从而延缓了折流板组件3的腐蚀,提高了换热器的使用寿命。并且,碳钢材质或不锈钢材质的折流板组件3还具有良好的导热性。需要说明的是,折流板组件3的材质并不局限于上述优选方案,在其他实施例中,还可以为其他材质,本实用新型在此不做限制。Preferably, the baffle assembly 3 is a carbon steel member or a stainless steel member, thereby delaying the corrosion of the baffle assembly 3 and improving the service life of the heat exchanger. Moreover, the baffle assembly 3 made of carbon steel or stainless steel also has good thermal conductivity. It should be noted that the material of the baffle assembly 3 is not limited to the above-mentioned preferred solution, in other embodiments, it can also be made of other materials, and the present invention is not limited here.
图2为三角折流板的结构示意图,在本实施例中,每个三角折流板31均为 曲面板状构件,每个三角折流板31的曲率均为壳体1内径的0.5倍至1.5倍,从而使得由多个三角折流板31组成的折流板组件3能够为螺旋状结构,进而有利于换热流体形成旋转涡流,提高了换热器的换热效率。Fig. 2 is a structural schematic diagram of a triangular baffle. In this embodiment, each triangular baffle 31 is a curved plate member, and the curvature of each triangular baffle 31 is 0.5 times to the inner diameter of the housing 1. 1.5 times, so that the baffle assembly 3 composed of a plurality of triangular baffles 31 can have a spiral structure, which is beneficial to the heat exchange fluid to form a rotating vortex, and improves the heat exchange efficiency of the heat exchanger.
需要说明的是,三角折流板31的曲率可以根据实际需求而进行相应的改变,本实用新型对此不做限制。It should be noted that the curvature of the triangular baffle 31 can be changed according to actual needs, and the present invention does not limit this.
图3为折流板组件的左视图,如图3所示,优选地,三角折流板31的多个管孔32在换热器的横截面上的投影面积之和为对应的三角折流板31在换热器的横截面上的投影面积的30%至40%,从而保证了三角折流板31能够有较大的面积作用于换热流体,进而提高了换热器的可靠性。Fig. 3 is a left view of the baffle assembly, as shown in Fig. 3, preferably, the sum of the projected areas of the plurality of tube holes 32 of the triangular baffle 31 on the cross section of the heat exchanger is the corresponding triangular baffle The projected area of the plate 31 on the cross-section of the heat exchanger is 30% to 40%, thereby ensuring that the triangular baffle 31 can have a larger area to act on the heat exchange fluid, thereby improving the reliability of the heat exchanger.
在本实施例中,每个三角折流板31均包括第一侧边311、第二侧边312、外弧边313和内弧边314,各三角折流板31的第一侧边分别与最近的三角折流板31的第二侧边之间的夹角为15°至90°,从而限定了三角折流板31的布置方式,即两个三角折流板31之间的间距大小,进而控制了换热流体的流量。In this embodiment, each triangular baffle 31 includes a first side 311, a second side 312, an outer arc 313 and an inner arc 314, and the first sides of each triangular baffle 31 are respectively connected to The included angle between the second sides of the nearest triangular baffles 31 is 15° to 90°, thereby limiting the arrangement of the triangular baffles 31, that is, the distance between two triangular baffles 31, In turn, the flow rate of the heat exchange fluid is controlled.
优选地,三角折流板31的内弧边314处设有凹陷,同一折流板组件3的三角折流板31上的凹陷在换热器的横截面上构成中心孔33,中心孔33的直径为管孔32的直径的1倍至2倍。在上述实现方式中,换热器在工作时,小部分的换热流体可以通过中心孔33在壳体1与传热管束2之间流动,以达到分流的效果,从而降低了换热流体对折流板组件3的冲击,进而降低了换热器的振动。Preferably, the inner arc edge 314 of the triangular baffle 31 is provided with a depression, and the depression on the triangular baffle 31 of the same baffle assembly 3 forms a central hole 33 on the cross section of the heat exchanger, and the center hole 33 The diameter is 1 to 2 times the diameter of the pipe hole 32 . In the above implementation mode, when the heat exchanger is in operation, a small part of the heat exchange fluid can flow between the shell 1 and the heat transfer tube bundle 2 through the central hole 33 to achieve the effect of splitting, thereby reducing the heat exchange fluid folding The impact of the flow plate assembly 3 further reduces the vibration of the heat exchanger.
具体地,壳体1内安装有用于支撑三角折流板31的多个拉杆(图未示),每个拉杆的两端分别固定安装在管板4的两端且与壳体1的长度方向平行布置,各个三角折流板31分别套装在各自对应的拉杆外,每两个相邻三角折流板31之间均设有与拉杆一一对应的定距管(图未示),三个定距管分别位于外弧边313的弧顶处、第一侧边311的中部和第二侧边312的中部,每个定距管均套装在各自对应的拉杆外,定距管与壳体1的长度方向平行,定距管的长度可以等于沿壳体1的长度方向间隔布置的两个相邻三角折流板31之间的间距,从而限定了三角折流板31在壳体1的长度方向上的间距。Specifically, a plurality of pull rods (not shown) for supporting the triangular baffle 31 are installed in the shell 1, and the two ends of each pull rod are respectively fixedly installed on the two ends of the tube sheet 4 and aligned with the longitudinal direction of the shell 1. Arranged in parallel, each triangular baffle 31 is respectively set outside the respective corresponding tie rods, and a distance tube (not shown) corresponding to the tie rods is provided between every two adjacent triangular baffles 31, three The spacer tubes are located at the arc top of the outer arc edge 313, the middle of the first side 311 and the middle of the second side 312, and each spacer tube is set outside the corresponding pull rod, and the spacer tube and the housing The length direction of 1 is parallel, and the length of the spacer tube can be equal to the distance between two adjacent triangular baffles 31 arranged at intervals along the length direction of the housing 1, thereby limiting the distance between the triangular baffles 31 in the housing 1. spacing along the length.
在本实施例中,壳体1的两端各通过管板分别连接管箱5,传热管束2的一端与一个管箱5连通,传热管束2的另一端与另一个管箱5连通,在两个管箱上分别设有管程出口51和管程进口52,管程出口51和管程进口52分别通过各自对应的管箱5与传热管束2连通,从而形成了传热管束2内的换热流体的循 环流通。In this embodiment, both ends of the shell 1 are respectively connected to the tube box 5 through the tube sheet, one end of the heat transfer tube bundle 2 communicates with one tube box 5, and the other end of the heat transfer tube bundle 2 communicates with another tube box 5, The tube side outlet 51 and the tube side inlet 52 are respectively provided on the two tube boxes, and the tube side outlet 51 and the tube side inlet 52 communicate with the heat transfer tube bundle 2 through the respective tube boxes 5, thereby forming the heat transfer tube bundle 2 Circulation of the heat exchange fluid inside.
在本实施例中,壳体1两端的外周壁上分别设有壳程出口11和壳程进口12,壳程出口11和壳程进口12连通,从而形成了壳体和传热管束2之间的换热流体的循环流通。In this embodiment, a shell side outlet 11 and a shell side inlet 12 are respectively provided on the outer peripheral walls of the two ends of the housing 1, and the shell side outlet 11 and the shell side inlet 12 are connected, thereby forming a gap between the housing and the heat transfer tube bundle 2. Circulation of the heat exchange fluid.
在本实施例中,传热管束2包括多个传热管21,各传热管21插装在各自对应的管孔32中,各传热管相互平行布置,从而提高了换热器的换热效率。值得说明的是,传热管21的数量需要和换热器的整体设计相对应,在其他实施例中,传热管21的数量可以根据实际需求而变动,本实用新型对此不作限制。In this embodiment, the heat transfer tube bundle 2 includes a plurality of heat transfer tubes 21, and each heat transfer tube 21 is inserted into a corresponding tube hole 32, and each heat transfer tube is arranged in parallel to each other, thereby improving the heat transfer efficiency of the heat exchanger. Thermal efficiency. It is worth noting that the number of heat transfer tubes 21 needs to correspond to the overall design of the heat exchanger. In other embodiments, the number of heat transfer tubes 21 can vary according to actual needs, which is not limited by the present invention.
以上所述仅为本实用新型的较佳实施例,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 descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present utility model shall be included in this utility model. within the scope of protection of utility models.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620509213.1U CN206094996U (en) | 2016-05-30 | 2016-05-30 | Shell -and -tube heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620509213.1U CN206094996U (en) | 2016-05-30 | 2016-05-30 | Shell -and -tube heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206094996U true CN206094996U (en) | 2017-04-12 |
Family
ID=58471730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620509213.1U Expired - Fee Related CN206094996U (en) | 2016-05-30 | 2016-05-30 | Shell -and -tube heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206094996U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109253637A (en) * | 2017-07-14 | 2019-01-22 | 中国石油化工股份有限公司 | A kind of heat exchanger with spiral-flow type lattice board |
| CN109579573A (en) * | 2018-12-07 | 2019-04-05 | 西安交通大学 | A kind of spiral lattice board shell-and-tube heat exchanger |
| CN110595234A (en) * | 2019-09-30 | 2019-12-20 | 郑州大学 | A Longitudinal Flow Shell Program Heat Exchanger with Multiple U-shaped Heat Exchange Tubes |
| WO2022117129A1 (en) | 2020-12-01 | 2022-06-09 | Vysoké Učení Technické V Brně | Tubular shell heat exchanger with cross flow |
| WO2022135623A1 (en) | 2020-12-22 | 2022-06-30 | Vysoké Učení Technické V Brně | Tubular shell heat exchanger with sheet baffles |
| JPWO2022163792A1 (en) * | 2021-01-29 | 2022-08-04 | ||
| CN117305999A (en) * | 2023-10-16 | 2023-12-29 | 浙江精工集成科技股份有限公司 | A steam drafting device |
-
2016
- 2016-05-30 CN CN201620509213.1U patent/CN206094996U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109253637A (en) * | 2017-07-14 | 2019-01-22 | 中国石油化工股份有限公司 | A kind of heat exchanger with spiral-flow type lattice board |
| CN109579573A (en) * | 2018-12-07 | 2019-04-05 | 西安交通大学 | A kind of spiral lattice board shell-and-tube heat exchanger |
| CN110595234A (en) * | 2019-09-30 | 2019-12-20 | 郑州大学 | A Longitudinal Flow Shell Program Heat Exchanger with Multiple U-shaped Heat Exchange Tubes |
| WO2022117129A1 (en) | 2020-12-01 | 2022-06-09 | Vysoké Učení Technické V Brně | Tubular shell heat exchanger with cross flow |
| WO2022135623A1 (en) | 2020-12-22 | 2022-06-30 | Vysoké Učení Technické V Brně | Tubular shell heat exchanger with sheet baffles |
| JPWO2022163792A1 (en) * | 2021-01-29 | 2022-08-04 | ||
| WO2022163792A1 (en) * | 2021-01-29 | 2022-08-04 | 三菱パワー株式会社 | Heat exchanger |
| JP7511686B2 (en) | 2021-01-29 | 2024-07-05 | 三菱重工業株式会社 | Heat exchanger |
| US12352513B2 (en) | 2021-01-29 | 2025-07-08 | Mitsubishi Heavy Industries, Ltd. | Heat exchanger |
| CN117305999A (en) * | 2023-10-16 | 2023-12-29 | 浙江精工集成科技股份有限公司 | A steam drafting device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206094996U (en) | Shell -and -tube heat exchanger | |
| CN101551207B (en) | Shell-and-tube heat exchanger with oblate tube | |
| US20090242184A1 (en) | Spiral Tube Fin Heat Exchanger | |
| CN101706227A (en) | Shell-and-tube heat exchanger with un-notched traverse baffles | |
| CN201032431Y (en) | A shell-and-tube heat exchanger with curved bow-shaped baffles | |
| CN204007233U (en) | The U-shaped pipe heat exchanger of a kind of continuous helical deflecting plate | |
| CN204730708U (en) | A kind of helical deflecting plate pipe and shell type heat exchanger of unequal-interval | |
| CN105806102A (en) | A heat exchanger with a self-supporting structure guide device | |
| CN104949552A (en) | Shell-and-tube heat exchanger | |
| CN201892451U (en) | Bending traverse baffle heat exchanger | |
| CN106197120A (en) | A combined heat exchange element of a petal-shaped heat exchange tube and a round orifice plate | |
| CN108519007A (en) | A self-supporting double helical finned tube heat exchanger | |
| CN104697360B (en) | Shell side flow equalizing spiral support longitudinal flow heat exchanger | |
| CN201852513U (en) | Variable angle baffle heat exchanger | |
| CN202403572U (en) | Corrugated u-shaped tube bundle heat exchanger | |
| CN204461147U (en) | Shell side current-sharing spiral support longitudinal-flow heat exchanger | |
| CN106979716A (en) | A kind of three-dimensional deflection plate and shell-and-tube heat exchanger | |
| CN201413066Y (en) | Shell and tube spiral flat tube heat exchanger | |
| CN206146272U (en) | Crisscross concave surface pipe shell and tube type heat exchanger | |
| CN201589572U (en) | A shell-and-tube heat exchanger with no gap baffles | |
| CN210718754U (en) | Winding tube type heat exchanger with baffle plate | |
| CN104034188B (en) | Heat exchanger and strengthened heat exchange method | |
| CN205784743U (en) | A heat exchanger with a self-supporting structure guide device | |
| CN208398689U (en) | Self-supporting double-helix finned tube heat exchanger | |
| CN201497419U (en) | EGR cooler and spiral deflector thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170412 Termination date: 20180530 |