CN112344766A - Three-way spiral shell-and-tube heat exchanger - Google Patents
Three-way spiral shell-and-tube heat exchanger Download PDFInfo
- Publication number
- CN112344766A CN112344766A CN202011368945.0A CN202011368945A CN112344766A CN 112344766 A CN112344766 A CN 112344766A CN 202011368945 A CN202011368945 A CN 202011368945A CN 112344766 A CN112344766 A CN 112344766A
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- Prior art keywords
- medium
- heat exchange
- exchange cavity
- spiral heat
- cylinder body
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 230000000149 penetrating effect Effects 0.000 claims description 10
- 238000000034 method Methods 0.000 abstract description 7
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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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
- F28D7/02—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 helically coiled
- F28D7/022—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 helically coiled the conduits of two or more media in heat-exchange relationship being helically coiled, the coils having a cylindrical configuration
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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
- F28F9/001—Casings in the form of plate-like arrangements; Frames enclosing a heat exchange core
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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
- F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
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- 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
本发明公开了一种三通式螺旋管壳换热器，包括筒体和设置在筒体两端的端盖，在一侧端盖上，对称设有第一介质进口接管和第一介质出口接管以及第二介质进口接管和第二介质出口接管，所述筒体上，上部设有进水口，下部设有出水口，所述筒体内，设有换热片组，所述换热片组包含非密封的内支撑罩和外支撑罩，在内支撑罩和外支撑罩之间，设置有第一介质螺旋换热腔和第二介质螺旋换热腔。本发明的三通式螺旋管壳换热器，第一第二介质分别通过管道进入第一第二介质螺旋换热腔的上部，再从第一第二介质螺旋换热腔的下部回流回来，过程中与水进行热交换，实现了三通换热，第一第二介质螺旋换热腔内均对流好，不易产生死区，换热效率高，实用性强。
The invention discloses a three-way type spiral shell-and-tube heat exchanger, which comprises a cylinder body and end caps arranged at both ends of the cylinder body. On one end cap, a first medium inlet pipe and a first medium outlet pipe are symmetrically arranged and the second medium inlet pipe and the second medium outlet pipe, the upper part of the cylinder is provided with a water inlet, and the lower part is provided with a water outlet; The unsealed inner support cover and the outer support cover are provided with a first medium spiral heat exchange cavity and a second medium spiral heat exchange cavity between the inner support cover and the outer support cover. In the three-way type spiral shell heat exchanger of the present invention, the first and second media respectively enter the upper part of the first and second medium spiral heat exchange chambers through pipes, and then return from the lower part of the first and second medium spiral heat exchange chambers, During the process, heat exchange with water is carried out to achieve three-way heat exchange. The first and second medium spiral heat exchange chambers have good convection, which is not easy to produce dead zones, and has high heat exchange efficiency and strong practicability.
Description
Technical Field
The invention belongs to the field of heat exchanger manufacturing, and particularly relates to a three-way spiral shell-and-tube heat exchanger.
Background
The shell-and-tube heat exchanger is also called a tubular heat exchanger, and is a dividing wall type heat exchanger which takes the wall surface of a tube bundle sealed in a shell as a heat transfer surface. However, most of the existing shell-and-tube heat exchangers can only realize heat exchange of two fluids, and have the problems of dead zones and poor backflow, so people hope to find a better way to solve the problems.
Disclosure of Invention
Aiming at the technical problem, the invention provides a three-way spiral shell-and-tube heat exchanger.
In order to achieve the technical purpose, the invention adopts the following technical scheme:
the three-way spiral shell-and-tube heat exchanger comprises a cylinder body and end covers arranged at two ends of the cylinder body, wherein a first medium inlet connecting tube, a first medium outlet connecting tube, a second medium inlet connecting tube and a second medium outlet connecting tube are symmetrically arranged on one end cover, a water inlet is arranged at the upper part of the cylinder body, a water outlet is arranged at the lower part of the cylinder body, a heat exchange plate group is arranged in the cylinder body and comprises an inner supporting cover and an outer supporting cover which are not sealed, a first medium spiral heat exchange cavity and a second medium spiral heat exchange cavity are arranged between the inner supporting cover and the outer supporting cover, the pitch and the radius of the spiral heat exchange cavity of a second medium are smaller than those of the first medium spiral heat exchange cavity, the periphery of the first medium spiral heat exchange cavity is in contact with the outer supporting cover and fixed through the outer supporting cover, and the periphery of the second medium spiral heat exchange cavity is in contact with the inner supporting, the upper end of the outer support cover is communicated with a water inlet on the cylinder body, and the lower end of the outer support cover is communicated with a water outlet on the cylinder body; a first medium distributing pipe is connected to a first medium inlet connecting pipe on the end cover and communicated with the upper part of the first medium spiral heat exchange cavity in a penetrating and perforating communication mode, and a first medium return pipe is connected to a first medium outlet connecting pipe on the end cover and communicated with the lower part of the first medium spiral heat exchange cavity in a penetrating and perforating communication mode; and a second medium outlet connecting pipe on the end cover is connected with a second medium return pipe and is communicated with the lower part of the second medium spiral heat exchange cavity in a penetrating and perforating way.
Preferably, the inner and outer non-sealed supporting covers are both composed of two symmetrically arranged protecting plates, and a gap for water flow to pass through is arranged between the two ends of each protecting plate.
Preferably, the walls of the first medium spiral heat exchange cavity and the second medium spiral heat exchange cavity are both provided with a raised grain structure to increase the heat exchange area.
Due to the adoption of the technical scheme, the invention has the following technical effects:
according to the three-way type spiral shell-and-tube heat exchanger, the first medium and the second medium respectively enter the upper part of the first medium spiral heat exchange cavity through the pipeline and then return from the lower part of the first medium spiral heat exchange cavity, heat exchange is carried out with water in the process, three-way heat exchange is realized, the heat exchange area is large, convection is good in the first medium spiral heat exchange cavity and the second medium spiral heat exchange cavity, dead zones are not easy to generate, the heat exchange efficiency is high, the overall strength is good, the practicability is high, and the three-way type spiral shell-and-tube heat exchanger is worthy.
Drawings
The invention will now be described, by way of example, with reference to the accompanying drawings, in which:
FIG. 1 is a schematic structural diagram of an embodiment of the present invention;
FIG. 2 is a schematic perspective view of a heat exchanger plate set;
fig. 3 is a cross-sectional view of fig. 2.
Detailed Description
All of the features disclosed in this specification, or all of the steps in any method or process so disclosed, may be combined in any combination, except combinations of features and/or steps that are mutually exclusive.
Any feature disclosed in this specification may be replaced by alternative features serving equivalent or similar purposes, unless expressly stated otherwise. That is, unless expressly stated otherwise, each feature is only an example of a generic series of equivalent or similar features.
As shown in fig. 1-3, a three-way spiral shell-and-tube heat exchanger includes a cylinder 1 and end caps 2 disposed at two ends of the cylinder 1, a first medium inlet connection tube 3, a first medium outlet connection tube 4, a second medium inlet connection tube 5 and a second medium outlet connection tube 6 are symmetrically disposed on the end cap 1 at one side, a water inlet 7 is disposed at the upper portion of the cylinder 1, a water outlet 8 is disposed at the lower portion of the cylinder, a heat exchanger set 9 is disposed in the cylinder 1, the heat exchanger set includes an inner support cover 10 and an outer support cover 11 which are not sealed, a first medium spiral heat exchange cavity 12 and a second medium spiral heat exchange cavity 13 are disposed between the inner support cover 10 and the outer support cover 11, the pitch and radius of the second medium spiral heat exchange cavity 13 are both smaller than those of the first medium spiral heat exchange cavity 12, the periphery of the first medium spiral heat exchange cavity 12 is in contact with the outer support cover 11 and is fixed by the outer support cover 11, the inner periphery of the second medium spiral heat exchange cavity 13 is in contact with the inner support cover 10 and is fixed through the inner support cover 10, the upper end of the outer support cover 11 is communicated with the water inlet 7 on the cylinder body 1, and the lower end of the outer support cover is communicated with the water outlet 8 on the cylinder body 1; a first medium distributing pipe 14 is connected to the first medium inlet connecting pipe 3 on the end cover 2 and is communicated with the upper part of the first medium spiral heat exchange cavity 12 in a penetrating and perforating communication mode, and a first medium return pipe 15 is connected to the first medium outlet connecting pipe 4 on the end cover 2 and is communicated with the lower part of the first medium spiral heat exchange cavity 12 in a penetrating and perforating communication mode; a second medium distributing pipe 16 is connected to the second medium inlet connecting pipe 5 on the end cover 2 and is communicated with the upper part of the second medium spiral heat exchange cavity 13 in a penetrating and perforating communication mode, and a second medium return pipe 17 is connected to the second medium outlet connecting pipe 6 on the end cover 2 and is communicated with the lower part of the second medium spiral heat exchange cavity 13 in a penetrating and perforating communication mode.
The inner and outer non-sealed supporting covers 10 and 11 are formed by two symmetrically arranged protecting plates, and gaps for water flow to pass through are arranged between the two ends of the two protecting plates.
The walls of the first medium spiral heat exchange cavity 12 and the second medium spiral heat exchange cavity 13 are both provided with a wave grain structure to increase the heat exchange area.
According to the three-way type spiral shell-and-tube heat exchanger, the first medium and the second medium respectively enter the upper part of the first medium spiral heat exchange cavity through the pipeline and then return from the lower part of the first medium spiral heat exchange cavity, heat exchange is carried out with water in the process, three-way heat exchange is realized, the heat exchange area is large, convection is good in the first medium spiral heat exchange cavity and the second medium spiral heat exchange cavity, dead zones are not easy to generate, the heat exchange efficiency is high, the overall strength is good, the practicability is high, and the three-way type spiral shell-and-tube heat exchanger is worthy.
The invention is not limited to the foregoing embodiments. The invention extends to any novel feature or any novel combination of features disclosed in this specification and any novel method or process steps or any novel combination of features disclosed.
Claims (3)
1. The three-way spiral shell-and-tube heat exchanger is characterized by comprising a cylinder body and end covers arranged at two ends of the cylinder body, wherein a first medium inlet connecting tube, a first medium outlet connecting tube, a second medium inlet connecting tube and a second medium outlet connecting tube are symmetrically arranged on one end cover, a water inlet is arranged at the upper part of the cylinder body, a water outlet is arranged at the lower part of the cylinder body, a heat exchange sheet set is arranged in the cylinder body and comprises an inner supporting cover and an outer supporting cover which are not sealed, a first medium spiral heat exchange cavity and a second medium spiral heat exchange cavity are arranged between the inner supporting cover and the outer supporting cover, the pitch and the radius of the spiral heat exchange cavity of a second medium are smaller than those of the first medium spiral heat exchange cavity, the periphery of the first medium spiral heat exchange cavity is in contact with the outer supporting cover and is fixed through the outer supporting cover, the periphery of the second medium spiral heat exchange cavity is in contact with the inner supporting cover, the upper end of the outer support cover is communicated with a water inlet on the cylinder body, and the lower end of the outer support cover is communicated with a water outlet on the cylinder body; a first medium distributing pipe is connected to a first medium inlet connecting pipe on the end cover and communicated with the upper part of the first medium spiral heat exchange cavity in a penetrating and perforating communication mode, and a first medium return pipe is connected to a first medium outlet connecting pipe on the end cover and communicated with the lower part of the first medium spiral heat exchange cavity in a penetrating and perforating communication mode; and a second medium outlet connecting pipe on the end cover is connected with a second medium return pipe and is communicated with the lower part of the second medium spiral heat exchange cavity in a penetrating and perforating way.
2. A three-way spiral shell and tube heat exchanger as claimed in claim 1, wherein the inner and outer non-sealed support shells are each formed by two symmetrically arranged protection plates, and a gap for water flow is provided between both ends of the two protection plates.
3. A three-way spiral shell and tube heat exchanger as claimed in claim 1, wherein the walls of the first and second media spiral heat exchange chambers are provided with corrugated structures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011368945.0A CN112344766B (en) | 2020-11-30 | 2020-11-30 | Three-way spiral shell and tube heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011368945.0A CN112344766B (en) | 2020-11-30 | 2020-11-30 | Three-way spiral shell and tube heat exchanger |
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| Publication Number | Publication Date |
|---|---|
| CN112344766A true CN112344766A (en) | 2021-02-09 |
| CN112344766B CN112344766B (en) | 2025-04-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202011368945.0A Active CN112344766B (en) | 2020-11-30 | 2020-11-30 | Three-way spiral shell and tube heat exchanger |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101321989B1 (en) * | 2012-06-11 | 2013-10-28 | (주)마이텍 | A fin heat exchanger by heat transfer between spiral channel and double pipe |
| CN203454868U (en) * | 2013-07-10 | 2014-02-26 | 湖北壮志石化设备科技有限公司 | Heat exchanger with efficient heat exchange tubes supported by triangular enclosed spiral baffle plate group |
| CN206037788U (en) * | 2016-08-30 | 2017-03-22 | 南通贝思特石墨设备有限公司 | Graphite heat exchanger of high -efficient heat transfer |
| CN209655859U (en) * | 2018-12-26 | 2019-11-19 | 广州市壹套节能设备有限责任公司 | A kind of heat-exchanging component and high-performance heat exchanger |
| CN211234048U (en) * | 2019-11-21 | 2020-08-11 | 南京扬子检修安装有限责任公司 | Novel spiral baffle heat exchanger |
| CN213778710U (en) * | 2020-11-30 | 2021-07-23 | 江苏埃米诺装备制造有限公司 | High-efficiency three-way pipe shell heat exchanger |
-
2020
- 2020-11-30 CN CN202011368945.0A patent/CN112344766B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101321989B1 (en) * | 2012-06-11 | 2013-10-28 | (주)마이텍 | A fin heat exchanger by heat transfer between spiral channel and double pipe |
| CN203454868U (en) * | 2013-07-10 | 2014-02-26 | 湖北壮志石化设备科技有限公司 | Heat exchanger with efficient heat exchange tubes supported by triangular enclosed spiral baffle plate group |
| CN206037788U (en) * | 2016-08-30 | 2017-03-22 | 南通贝思特石墨设备有限公司 | Graphite heat exchanger of high -efficient heat transfer |
| CN209655859U (en) * | 2018-12-26 | 2019-11-19 | 广州市壹套节能设备有限责任公司 | A kind of heat-exchanging component and high-performance heat exchanger |
| CN211234048U (en) * | 2019-11-21 | 2020-08-11 | 南京扬子检修安装有限责任公司 | Novel spiral baffle heat exchanger |
| CN213778710U (en) * | 2020-11-30 | 2021-07-23 | 江苏埃米诺装备制造有限公司 | High-efficiency three-way pipe shell heat exchanger |
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| Publication number | Publication date |
|---|---|
| CN112344766B (en) | 2025-04-01 |
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