CN205102639U - Shell -and -tube heat exchanger - Google Patents
Shell -and -tube heat exchanger Download PDFInfo
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- CN205102639U CN205102639U CN201520905022.2U CN201520905022U CN205102639U CN 205102639 U CN205102639 U CN 205102639U CN 201520905022 U CN201520905022 U CN 201520905022U CN 205102639 U CN205102639 U CN 205102639U
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Abstract
The utility model discloses a shell -and -tube heat exchanger relates to heat exchanger technical field for prevent the high temperature of tube sheet. This shell -and -tube heat exchanger includes: be equipped with the upper cover of hot -fluid entry, be equipped with the low head that the hot -fluid exported, be equipped with the heat transfer tube of cold flow body entry and cold fluid issuing to and set up last tube sheet, heat exchange tube and the floating tubesheet in heat transfer tube, wherein, the heat exchange tube is used for carrying the hot -fluid, shell -and -tube heat exchanger is still including keeping apart the tube sheet, it is located to keep apart the tube sheet cold flow body entry with between the cold fluid issuing, and with it sets up relatively to go up the tube sheet. It will to keep apart the tube sheet heat transfer tube separates and is two cavitys, and two the cavity intercommunication. Above -mentioned shell -and -tube heat exchanger is used for the heat transfer.
Description
Technical field
The utility model relates to technical field of heat exchangers, particularly relates to a kind of shell-and-tube heat exchanger.
Background technology
Shell-and-tube heat exchanger is the equipment of exchange heat between a kind of fluid realizing different temperatures, it has the features such as structure is simple, easy to operate, and can use under high temperature, high pressure, therefore, shell-and-tube heat exchanger all has a wide range of applications in fields such as oil, chemical industry, metallurgy.
Particularly, as shown in Figure 1, shell-and-tube heat exchanger comprises the upper cover 1 being provided with thermal fluid inlet 101, is provided with the low head 2 of hot fluid outlet ports 201, be provided with the heat exchanger tube 5 of cold fluid inlet 3 and cold fluid outlet 4, and be arranged on upper perforated plate 6, heat exchanger tube 7 and the floating tubesheet 8 in heat exchanger tube 5.
The course of work with the shell-and-tube heat exchanger of said structure is as follows: first hot fluid enters upper cover 1 by thermal fluid inlet 101, then, enters heat exchanger tube 7, finally, is flowed out by hot fluid outlet ports 201.Meanwhile, cold fluid enters in heat exchanger tube 5 by cold fluid inlet 3, and then, the hot fluid in heat exchanger tube 7 carries out exchange heat by the cold fluid in the tube wall of heat exchanger tube 7 and heat exchanger tube 5, and finally, cold fluid flows out from cold fluid outlet 4.
But present inventor finds, in the above-mentioned course of work, the hot fluid in upper cover 1 can contact with upper perforated plate 6, makes the temperature of upper perforated plate 6 too high, causes upper perforated plate 6 to lose efficacy, and then causes shell-and-tube heat exchanger normally to work.
Utility model content
The purpose of this utility model is to provide a kind of shell-and-tube heat exchanger, for preventing the temperature of upper perforated plate too high, maintains the normal work of shell-and-tube heat exchanger.
For achieving the above object, shell-and-tube heat exchanger provided by the utility model adopts following technical scheme:
A kind of shell-and-tube heat exchanger comprises: the upper cover being provided with thermal fluid inlet, be provided with the low head of hot fluid outlet ports, be provided with the heat exchanger tube of cold fluid inlet and cold fluid outlet, and the upper perforated plate be arranged in heat exchanger tube, heat exchanger tube and floating tubesheet, wherein, described heat exchanger tube is for carrying hot fluid, described shell-and-tube heat exchanger also comprises isolation tube sheet, described isolation tube sheet is between described cold fluid inlet and described cold fluid outlet, and be oppositely arranged with described upper perforated plate, described heat exchanger tube is divided into two cavitys by described isolation tube sheet, and two described cavitys are communicated with.
Because shell-and-tube heat exchanger provided by the utility model comprises isolation tube sheet, isolation tube sheet is between cold fluid inlet and cold fluid outlet, and be oppositely arranged with upper perforated plate, heat exchanger tube is divided into two cavitys by isolation tube sheet, and two cavitys are communicated with, therefore, isolation tube sheet can stop that the cold fluid flowed into from cold fluid inlet directly flows to cold fluid outlet, compared with prior art, there is more cold fluid can contact with upper perforated plate, thus can effectively prevent upper perforated plate temperature too high, maintain the normal work of shell-and-tube heat exchanger.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is shell-and-tube heat exchanger of the prior art;
Fig. 2 is the first shell-and-tube heat exchanger in the utility model embodiment;
Fig. 3 is the secundal viae shell heat exchanger in the utility model embodiment;
Fig. 4 is the third shell-and-tube heat exchanger in the utility model embodiment;
Fig. 5 is the 4th kind of shell-and-tube heat exchanger in the utility model embodiment;
Fig. 6 is the 5th kind of shell-and-tube heat exchanger in the utility model embodiment;
Fig. 7 is the 6th kind of shell-and-tube heat exchanger in the utility model embodiment.
Description of reference numerals:
1-upper cover; 101-thermal fluid inlet; 2-low head;
201-hot fluid outlet ports; 3-cold fluid inlet; 4-cold fluid outlet;
5-heat exchanger tube; 6-upper perforated plate; 7-heat exchanger tube;
8-floating tubesheet; 9-isolation tube sheet; 10-the first thermal insulation layer;
11-sealing ring; 12-guide shell; 13-the first outer deflection plate;
Deflection plate in 14-the first; 15-the second outer deflection plate; Deflection plate in 16-the second.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of this utility model protection.
The utility model embodiment provides a kind of shell-and-tube heat exchanger, as shown in Figure 2, this shell-and-tube heat exchanger comprises: the upper cover 1 being provided with thermal fluid inlet 101, be provided with the low head 2 of hot fluid outlet ports 201, be provided with the heat exchanger tube 5 of cold fluid inlet 3 and cold fluid outlet 4, and the upper perforated plate 6 be arranged in heat exchanger tube 5, heat exchanger tube 7 and floating tubesheet 8, wherein, heat exchanger tube 7 is for carrying hot fluid, this shell-and-tube heat exchanger also comprises isolation tube sheet 9, isolation tube sheet 9 is between cold fluid inlet 3 and cold fluid outlet 4, and be oppositely arranged with upper perforated plate 6, heat exchanger tube 5 is divided into two cavitys by isolation tube sheet 9, and two cavitys are communicated with.
Particularly, above-mentioned two cavitys can by the gap area between isolation tube sheet 9 and the inwall of heat exchanger tube 5, and also can offer through hole on isolation tube sheet 9, two cavitys are communicated with by this through hole.
The shell-and-tube heat exchanger provided due to the utility model embodiment comprises isolation tube sheet 9, isolation tube sheet 9 is between cold fluid inlet 3 and cold fluid outlet 4, and be oppositely arranged with upper perforated plate 6, heat exchanger tube 5 is divided into two cavitys by isolation tube sheet 9, and two cavitys are communicated with, therefore, isolation tube sheet 9 can stop that the cold fluid flowed into from cold fluid inlet 3 directly flows to cold fluid outlet 4, compared with prior art, there is more cold fluid can contact with upper perforated plate 6, thus can effectively prevent upper perforated plate 6 temperature too high, maintain the normal work of shell-and-tube heat exchanger.
It should be noted that, cold fluid inlet 3 should be tried one's best and to be arranged near upper perforated plate 6, and isolation tube sheet 9 should be tried one's best, close cold fluid inlet 3 is arranged, thus make the flow distance in the cavity of cold fluid between upper perforated plate 6 and isolation tube sheet 9 shorter, and then the exchange heat that the hot fluid in the cold fluid decreased in this cavity and heat exchanger tube 7 carries out, make the cooling fluid temperature that contacts with upper perforated plate 6 lower, thus upper perforated plate 6 temperature can be prevented further too high.
In addition, as shown in Figure 3, upper perforated plate 6 is provided with the first thermal insulation layer 10 towards the one side of thermal fluid inlet 101, thus can reduce the heat that the hot fluid in upper cover 1 transmits to upper perforated plate 6, and then can prevent the temperature of upper perforated plate 6 from raising.Preferably, the material of the first thermal insulation layer 10 is castable.Compared with other heat-barrier materials, castable can at high temperature keep good intensity, thus when the temperature of the hot fluid flowed into from thermal fluid inlet 101 is higher, can prevent the first thermal insulation layer 10 from splitting because of high temperature, thus the heat that the hot fluid in upper cover 1 transmits to upper perforated plate 6 can be reduced, and then can prevent the temperature of upper perforated plate 6 from raising.
Further, present inventor finds, in the actual use procedure of shell-and-tube heat exchanger, the material of the first thermal insulation layer 10 may come off from upper perforated plate 6, and the material after coming off easily enters in heat exchanger tube 7, causes heat exchanger tube 7 to block.For avoiding the appearance of this problem, outstanding first thermal insulation layer 10 certain length of import of heat exchanger tube 7.In addition, the material passing the part that upper perforated plate 6 stretches in upper cover 1 in heat exchanger tube 7 is preferably the good pottery of heat-proof quality, thus the heat that the hot fluid in upper cover 1 transmitted to upper perforated plate 6 by heat exchanger tube 7 can be reduced, prevent the temperature of upper perforated plate 6 too high further.
In addition, as shown in Figure 4, the outer peripheral face of isolation tube sheet 9 is arranged with sealing ring 11, isolation tube sheet 9 is connected with the inner wall sealing of heat exchanger tube 5 by sealing ring 11, thus the cold fluid flowed into from cold fluid inlet 3 can be prevented to be flowed directly to cold fluid outlet 4 by the gap between isolation tube sheet 9 and the inwall of heat exchanger tube 5, the temperature of upper perforated plate 6 can be prevented further too high.Now, in order to make two cavitys in heat exchanger tube 5 be communicated with, isolation tube sheet 9 is also provided with the through hole of connection two cavitys.
Further, in order to prevent the heat exchange efficiency of shell-and-tube heat exchanger from declining, the inwall of heat exchanger tube 5 is provided with the second thermal insulation layer.But in the practical work process of shell-and-tube heat exchanger, stream has hot fluid in heat exchanger tube 7, make heat exchanger tube 7 thermal expansion can occur, thus drive isolation tube sheet 9 to move.In the process of isolation tube sheet 9 movement, sealing ring 11 meeting and the second thermal insulation layer generation relative sliding or extruding, cause the second thermal insulation layer to be scratched by sealing ring 11.For avoiding the appearance of this problem, sealing ring 11 in the utility model embodiment is preferably elastic seal ring, thus when sealing ring 11 and the second thermal insulation layer generation relative sliding or when extruding, elastic deformation can be there is to play cushioning effect in sealing ring 11, thus the second thermal insulation layer can be avoided to be scratched by sealing ring 11, prevent the heat exchange efficiency of shell-and-tube heat exchanger from declining.
In addition, as shown in Figure 5, shell-and-tube heat exchanger also comprises the guide shell 12 be fixed on isolation tube sheet 9, and the two ends of guide shell 12 lay respectively in two cavitys, and the distance exporting to floating tubesheet 8 of guide shell 12 is less than the distance of cold fluid outlet 4 to floating tubesheet 8.Therefore, the cold fluid flowed out from the outlet of guide shell 12 can flow to cold fluid outlet 4 along from floating tubesheet 8 to the direction of isolation tube sheet 9.Flow direction due to the hot fluid in heat exchanger tube 7 is the direction of self-isolation tube sheet 9 to floating tubesheet 8, contrary with the flow direction of cold fluid, thus make to form countercurrent flow between hot fluid and cold fluid, effectively improve the heat exchange efficiency between hot fluid and cold fluid, make the heat exchange efficiency of shell-and-tube heat exchanger higher.Exemplarily, guide shell 12 through isolating for being communicated with the through hole of two cavitys on tube sheet 9, and can be fixed on isolation tube sheet 9 by the mode of welding.
It should be noted that, from the above, the cold fluid flowed out from the outlet of guide shell 12 can flow to cold fluid outlet 4 along from floating tubesheet 8 to the direction of isolation tube sheet 9, now, in order to make cold fluid to flow to the flow distance before cold fluid outlet 4 longer, thus make to carry out exchange heat fully between cold fluid and hot fluid, need to make cold fluid outlet 4 as far as possible near isolation tube sheet 9.
But in the practical work process of shell-and-tube heat exchanger, stream has hot fluid in heat exchanger tube 7, make heat exchanger tube 7 thermal expansion can occur, thus drive isolation tube sheet 9 to move to floating tubesheet 8 direction from upper perforated plate 6.When the displacement of isolation tube sheet 9 is longer, and isolation tube sheet 9 and cold fluid outlet 4 between distance shorter time, cold fluid inlet 3 and cold fluid outlet 4 can all be positioned at the same side isolating tube sheet 9, cause the cold fluid flowed into from cold fluid inlet 3 directly to be flowed out by cold fluid outlet 4, make can not carry out exchange heat between cold fluid and hot fluid.For avoiding the appearance of this problem, need to arrange certain distance between cold fluid outlet 4 and isolation tube sheet 9, this distance needs the displacement being greater than isolation tube sheet 9.
In addition, as shown in Figure 6, at least one first outer deflection plate 13 of being parallel to each other and at least one deflection plate 14 in first is also provided with between upper perforated plate 6 and isolation tube sheet 9, in first outer deflection plate 13 and first, deflection plate 14 is ring baffle plate, and the first outer deflection plate 13 is oppositely arranged with isolation tube sheet 9, in the first outer deflection plate 13 and first, deflection plate 14 alternate intervals arranges.Therefore, the cold fluid flowed into from cold fluid inlet 3 can in the first deflection plate 13 and first deflection plate 14 stop under carry out baffling, prevent the cold fluid flowed into from cold fluid inlet 3 from flowing directly into the entrance of guide shell 12, contribute to more cold fluid to contact with upper perforated plate 6, thus upper perforated plate 6 temperature can be prevented further too high.
Exemplarily, as shown in Figure 6, the first outer deflection plate 13 is fixed on heat exchanger tube 7 by the mode of expanded joint, and in first, deflection plate 14 is fixed on guide shell 12 by the mode of expanded joint.Wherein, the internal diameter of the first outer deflection plate 13 is greater than the external diameter of guide shell 12, make the passage existed between the first outer deflection plate 13 and guide shell 12 for making cold fluid pass through, in first, the external diameter of deflection plate 14 is less than the internal diameter of heat exchanger tube 5, makes the passage existed between the inwall of deflection plate 14 and heat exchanger tube 5 in first for making cold fluid pass through.
Further, in order to make the baffling effect of the cold fluid between upper perforated plate 6 and isolation tube sheet 9 better, preferably, the internal diameter of the first outer deflection plate 13 is less than the external diameter of deflection plate 14 in first, thus after passage between the inwall making cold fluid flow through deflection plate 14 and heat exchanger tube 5 in first, cold fluid can be stopped by the first outer deflection plate 13, thus changes the flow direction of cold fluid.Similarly, after cold fluid flows through the passage between the first outer deflection plate 13 and guide shell 12, cold fluid can be stopped by deflection plate 14 in first, thus changes the flow direction of cold fluid.
Further, in order to make the cold fluid between upper perforated plate 6 and isolation tube sheet 9, there is comparatively uniform flow velocity and carry out heat exchange equably to make the hot fluid in itself and heat exchanger tube 7, preferably, the width of passage in first between deflection plate 14 and the inwall of heat exchanger tube 5 is identical with the width of the passage between the first outer deflection plate 13 and guide shell 12.
In addition, the outer peripheral face of the first outer deflection plate 13 is arranged with sealing ring 11, first outer deflection plate 13 is connected with the inner wall sealing of heat exchanger tube 5 by sealing ring 11, thus can prevent cold fluid from passing through from the gap between the first deflection plate 13 and the inwall of heat exchanger tube 5, and then improve the baffling effect of cold fluid.Further, when being provided with the second thermal insulation layer on the inwall of heat exchanger tube 5, movement or the extruding of the first outer deflection plate 13 also may scratch the second thermal insulation layer.For avoiding the appearance of this problem, sealing ring 11 in the utility model embodiment is preferably elastic seal ring, thus when sealing ring 11 and the second thermal insulation layer generation relative sliding or when extruding, elastic deformation can be there is to play cushioning effect in sealing ring 11, thus avoid the second thermal insulation layer to be scratched by sealing ring 11, prevent the heat exchange efficiency of shell-and-tube heat exchanger from declining.
Similarly, as shown in Figure 7, at least one second outer deflection plate 15 of being parallel to each other and at least one deflection plate 16 in second is also provided with between floating tubesheet 8 and isolation tube sheet 9, in second outer deflection plate 15 and second, deflection plate 16 is ring baffle plate, and the second outer deflection plate 15 is oppositely arranged with isolation tube sheet 9, in the second outer deflection plate 15 and second, deflection plate 16 alternate intervals arranges.Therefore, cold fluid can in the second outer deflection plate 15 and second deflection plate 16 stop under carry out baffling, make the flow distance of cold fluid longer, and the flow dead of cold fluid can be reduced and improve the turbulent extent of cold fluid, thus the heat exchange efficiency that improve between hot fluid and cold fluid, make the heat exchange efficiency of shell-and-tube heat exchanger higher.
Exemplarily, as shown in Figure 7, the second outer deflection plate 15 is fixed on heat exchanger tube 7 by the mode of expanded joint, and in second, deflection plate 16 is fixed on guide shell 12 by the mode of expanded joint.Wherein, the internal diameter of the second outer deflection plate 15 is greater than the external diameter of guide shell 12, make the passage existed between the second outer deflection plate 15 and guide shell 12 for making cold fluid pass through, in second, the external diameter of deflection plate 16 is less than the internal diameter of heat exchanger tube 5, makes the passage existed between the inwall of deflection plate 16 and heat exchanger tube 5 in second for making cold fluid pass through.
Further, comparatively even in order to make the cold fluid between isolation tube sheet 9 and floating tubesheet 8 distribute, preferably, the internal diameter of the second outer deflection plate 15 is less than the external diameter of deflection plate 16 in second, thus after passage between the inwall making cold fluid flow through deflection plate 16 and heat exchanger tube 5 in second, cold fluid can be stopped by the second outer deflection plate 15, thus changes the flow direction of cold fluid.Similarly, after cold fluid flows through the passage between the second outer deflection plate 15 and guide shell 12, cold fluid can be stopped by deflection plate 16 in second, thus changes the flow direction of cold fluid.
Further, in order to make the cold fluid between isolation tube sheet 9 and floating tubesheet 8, there is comparatively uniform flow velocity and carry out heat exchange equably to make the hot fluid in itself and heat exchanger tube 7, preferably, the width of passage in second between deflection plate 16 and the inwall of heat exchanger tube 5 is identical with the width of the passage between the second outer deflection plate 15 and guide shell 12.
Similarly, the outer peripheral face of the second outer deflection plate 15 also can be arranged with sealing ring 11, second outer deflection plate 15 is connected with the inner wall sealing of heat exchanger tube 5 by sealing ring 11, thus can prevent cold fluid from passing through from the gap between the second deflection plate 15 and the inwall of heat exchanger tube 5, and then improve the baffling effect of cold fluid.Further, when being provided with the second thermal insulation layer on the inwall of heat exchanger tube 5, the movement of the second outer deflection plate 15 also may scratch the second thermal insulation layer.For avoiding the appearance of this problem, sealing ring 11 in the utility model embodiment is preferably elastic seal ring, thus when sealing ring 11 and the second thermal insulation layer generation relative sliding or when extruding, elastic deformation can be there is to play cushioning effect in sealing ring 11, thus avoid the second thermal insulation layer to be scratched by sealing ring 11, prevent the heat exchange efficiency of shell-and-tube heat exchanger from declining.
In addition, heat exchanger tube 5 can also be provided with multiple cold fluid inlet 3, make the distribution flowing into the cold fluid after heat exchanger tube 5 from each cold fluid inlet 3 comparatively even, thus upper perforated plate 6 can be contacted equably with cold fluid, make the temperature of upper perforated plate 6 comparatively even, prevent upper perforated plate 6 local temperature too high, thus can prevent there is larger thermal stress in upper perforated plate 6, and then upper perforated plate 6 can be avoided to lose efficacy.Preferably, each cold fluid inlet 3 being axially uniformly distributed on the outside of heat exchanger tube 5 around heat exchanger tube 5.Exemplarily, when the number of cold fluid inlet 3 is 4, the angle between each cold fluid inlet 3 is 90 degree.
Similarly, heat exchanger tube 5 can also be provided with multiple cold fluid outlet 4, it has the distribution similar with above-mentioned cold fluid inlet 3, repeats no more herein.In addition, for the ease of the connection of other pipelines and cold fluid inlet 3, cold fluid outlet 4, cold fluid inlet 3 and cold fluid outlet 4 can interlaced arrangement.
In addition, when being provided with the second thermal insulation layer on the inwall of heat exchanger tube 5, the shell-and-tube heat exchanger that the utility model embodiment provides in use, shell-and-tube heat exchanger is needed vertically to place, the i.e. axis of heat exchanger tube 5 and horizontal plane, thus heat exchanger tube 7 can be avoided to bend because of Action of Gravity Field, and then can prevent the heat exchanger tube 7 after bending from being scratched by the second thermal insulation layer, cause the heat exchange efficiency of shell-and-tube heat exchanger to decline.
In addition, be also provided with and raise the nose above water to breathe to export in heat exchanger tube 5, and raise the nose above water to breathe to be provided with sealing ring between outlet with hot fluid outlet ports 201, alternatively, sealing ring is metallic packing ring, and the sealing that floating head is exported between hot fluid outlet ports 201 has higher reliability.
It should be noted that when shell-and-tube heat exchanger works, first should pass into cold fluid, and then pass into hot fluid, thus upper perforated plate 6 temperature when shell-and-tube heat exchanger just works can be prevented too high, avoid upper perforated plate 6 to lose efficacy.
The above; be only detailed description of the invention of the present utility model; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; change can be expected easily or replace, all should be encompassed within protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of described claim.
Claims (10)
1. a shell-and-tube heat exchanger, comprise: the upper cover being provided with thermal fluid inlet, be provided with the low head of hot fluid outlet ports, be provided with the heat exchanger tube of cold fluid inlet and cold fluid outlet, and be arranged on upper perforated plate, heat exchanger tube and the floating tubesheet in heat exchanger tube, described heat exchanger tube is for carrying hot fluid, it is characterized in that, described shell-and-tube heat exchanger also comprises isolation tube sheet, and described isolation tube sheet between described cold fluid inlet and described cold fluid outlet, and is oppositely arranged with described upper perforated plate; Described heat exchanger tube is divided into two cavitys by described isolation tube sheet, and two described cavitys are communicated with.
2. shell-and-tube heat exchanger according to claim 1, is characterized in that, described upper perforated plate is provided with the first thermal insulation layer towards the one side of described thermal fluid inlet.
3. shell-and-tube heat exchanger according to claim 1, is characterized in that, the outer peripheral face of described isolation tube sheet is arranged with sealing ring, and described isolation tube sheet is connected with the inner wall sealing of described heat exchanger tube by described sealing ring; Described isolation tube sheet is provided with the through hole of connection two described cavitys.
4. shell-and-tube heat exchanger according to claim 3, is characterized in that, the inwall of described heat exchanger tube is provided with the second thermal insulation layer, and described sealing ring is elastic seal ring.
5. the shell-and-tube heat exchanger according to claim 3 or 4, is characterized in that, described shell-and-tube heat exchanger also comprises the guide shell be fixed on described isolation tube sheet, and the two ends of described guide shell lay respectively in two described cavitys; The distance exporting to described floating tubesheet of described guide shell is less than the distance of described cold fluid outlet to described floating tubesheet.
6. shell-and-tube heat exchanger according to claim 5, it is characterized in that, between described upper perforated plate and described isolation tube sheet, be also provided with at least one first outer deflection plate of being parallel to each other and at least one deflection plate in first, in described first outer deflection plate and described first, deflection plate is ring baffle plate; And described first outer deflection plate and described isolation tube sheet are oppositely arranged, in described first outer deflection plate and described first, deflection plate alternate intervals arranges.
7. shell-and-tube heat exchanger according to claim 6, is characterized in that, the internal diameter of described first outer deflection plate is less than the external diameter of deflection plate in described first.
8. shell-and-tube heat exchanger according to claim 5, it is characterized in that, between described floating tubesheet and described isolation tube sheet, be also provided with at least one second outer deflection plate of being parallel to each other and at least one deflection plate in second, in described second outer deflection plate and described second, deflection plate is ring baffle plate; And described second outer deflection plate and described isolation tube sheet are oppositely arranged, in described second outer deflection plate and described second, deflection plate alternate intervals arranges.
9. shell-and-tube heat exchanger according to claim 8, is characterized in that, the internal diameter of described second outer deflection plate is less than the external diameter of deflection plate in described second.
10. shell-and-tube heat exchanger according to claim 1, is characterized in that, described heat exchanger tube is provided with multiple cold fluid inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520905022.2U CN205102639U (en) | 2015-11-13 | 2015-11-13 | Shell -and -tube heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520905022.2U CN205102639U (en) | 2015-11-13 | 2015-11-13 | Shell -and -tube heat exchanger |
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| Publication Number | Publication Date |
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| CN205102639U true CN205102639U (en) | 2016-03-23 |
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| CN201520905022.2U Active CN205102639U (en) | 2015-11-13 | 2015-11-13 | Shell -and -tube heat exchanger |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107525420A (en) * | 2017-09-30 | 2017-12-29 | 芜湖精达机械制造有限公司 | A kind of U-shaped tubing heat exchanger |
| CN108387117A (en) * | 2018-03-16 | 2018-08-10 | 华南理工大学 | Double convection current pipe heat exchangers inside and outside one kind |
| CN110595231A (en) * | 2019-09-04 | 2019-12-20 | 山西亚乐士环保技术股份有限公司 | Floating pipe type heat exchanger |
| CN113218214A (en) * | 2021-05-11 | 2021-08-06 | 徐振江 | Shell and tube heat exchanger |
| CN113432464A (en) * | 2021-05-20 | 2021-09-24 | 田方 | Multi-channel heat exchanger |
-
2015
- 2015-11-13 CN CN201520905022.2U patent/CN205102639U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107525420A (en) * | 2017-09-30 | 2017-12-29 | 芜湖精达机械制造有限公司 | A kind of U-shaped tubing heat exchanger |
| CN108387117A (en) * | 2018-03-16 | 2018-08-10 | 华南理工大学 | Double convection current pipe heat exchangers inside and outside one kind |
| CN108387117B (en) * | 2018-03-16 | 2024-05-24 | 华南理工大学 | Internal and external double convection tube type heat exchanger |
| CN110595231A (en) * | 2019-09-04 | 2019-12-20 | 山西亚乐士环保技术股份有限公司 | Floating pipe type heat exchanger |
| CN113218214A (en) * | 2021-05-11 | 2021-08-06 | 徐振江 | Shell and tube heat exchanger |
| CN113432464A (en) * | 2021-05-20 | 2021-09-24 | 田方 | Multi-channel heat exchanger |
| CN113432464B (en) * | 2021-05-20 | 2023-12-08 | 江苏一山特种装备有限公司 | Multi-channel heat exchanger |
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