CN205759760U - A kind of multi-fluid kettle type reboiler - Google Patents
A kind of multi-fluid kettle type reboiler Download PDFInfo
- Publication number
- CN205759760U CN205759760U CN201620470802.3U CN201620470802U CN205759760U CN 205759760 U CN205759760 U CN 205759760U CN 201620470802 U CN201620470802 U CN 201620470802U CN 205759760 U CN205759760 U CN 205759760U
- Authority
- CN
- China
- Prior art keywords
- fluid
- bobbin carriage
- tube bundle
- hot
- shaped heat
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of multi-fluid kettle type reboiler, including overall bobbin carriage and autoclave housing, it is tightly connected by tube sheet between the two, the upper end of described autoclave housing is provided with vapor phase exit, and its underpart is sequentially provided with cold flow import and liquid-phase outlet, described overall bobbin carriage is separated into several chamber by bobbin carriage dividing plate, neighbouring chamber forms sub-thread hot-fluid bobbin carriage, the corresponding one group of U-shaped heat-exchanging tube bundle of each sub-thread hot-fluid bobbin carriage, each group U-shaped heat-exchanging tube bundle is combined into overall U-shaped heat-exchanging tube bundle, the heat exchanger tube of this entirety U-shaped heat-exchanging tube bundle is evenly arranged on described tube sheet, it is provided with hot-fluid import and hot outlets on described each sub-thread hot-fluid bobbin carriage.This utility model compact conformation, heat transfer efficiency is high, and tube side fluid is evenly distributed, and can effectively reduce the thermal (temperature difference) stress of tube sheet and the dividing plate caused by a plurality of fluids skewness, and U-shaped heat-exchanging tube bundle can fully absorb housing and interbank thermal (temperature difference) stress.
Description
Technical field
This utility model belongs to technical field of heat exchangers, relates to a kind of kettle type reboiler for multi-fluid heat exchange.
Background technology
At present, multi-fluid kettle type reboiler can be divided into two kinds, and one is multi-fluid fixed tube sheet type kettle type reboiler.Another kind is multi-fluid U-tube formula kettle type reboiler.
Multi-fluid fixed tube sheet type kettle type reboiler compact conformation, floor space are little, but absorption tube shell-side fluid thermal (temperature difference) stress ability is little.Existing multi-fluid U-tube formula kettle type reboiler can absorb shell journey fluid temperature difference stress, but respectively restraining the most independent in housing layout, heat transfer efficiency is low, tube sheet not stringing area big, tube sheet thermo parameters method is uneven, structure is complicated, metal consumption is high, floor space is big.Additionally, the thermal (temperature difference) stress that existing many logistics kettle type reboiler hot-fluid entrance point tube sheet and dividing plate are caused by a plurality of fluids skewness is bigger.
Utility model content
This utility model provides a kind of multi-fluid kettle type reboiler, can effectively reduce tube sheet and the thermal (temperature difference) stress of dividing plate that a plurality of fluids skewness causes, for multi-fluid boiling heat transfer.
The purpose of this utility model has the technical scheme that
A kind of multi-fluid kettle type reboiler, including overall bobbin carriage and autoclave housing, it is tightly connected by tube sheet between the two, the upper end of described autoclave housing is provided with vapor phase exit, and its underpart is sequentially provided with cold flow import and liquid-phase outlet, described overall bobbin carriage is separated into several chamber by bobbin carriage dividing plate, neighbouring chamber forms sub-thread hot-fluid bobbin carriage, the corresponding one group of U-shaped heat-exchanging tube bundle of each sub-thread hot-fluid bobbin carriage, each group U-shaped heat-exchanging tube bundle is combined into overall U-shaped heat-exchanging tube bundle, the heat exchanger tube of this entirety U-shaped heat-exchanging tube bundle is evenly arranged on described tube sheet, it is provided with hot-fluid import and hot outlets on described each sub-thread hot-fluid bobbin carriage.
Described each sub-thread hot-fluid import bobbin carriage is equipped with heat flux distribution device.
This utility model compact conformation, heat transfer efficiency is high, tube side fluid is evenly distributed, can effectively reduce the thermal (temperature difference) stress of tube sheet and the dividing plate caused by a plurality of fluids skewness, U-shaped heat-exchanging tube bundle fully absorbs housing and interbank thermal (temperature difference) stress, it is possible to resolve existing multi-fluid kettle type reboiler heat transfer efficiency is low,
Floor space is big, tube sheet and the difficult problem such as heat exchanger tube joint thermal (temperature difference) stress is big.
This utility model is safe and reliable, metal consumption is low, floor space is little.
Accompanying drawing explanation
Fig. 1 is this utility model structure diagram;
Fig. 2 is the side view of Fig. 1;
Fig. 3 is the tube sheet side cross-sectional view of this utility model bobbin carriage;
Fig. 4 is the heat flux distribution plate side cross-sectional view of utility model bobbin carriage.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
With reference to Fig. 1,2,3,4, label in each figure: overall bobbin carriage 1, heat flux distribution plate 2, tube sheet 3,
Autoclave housing 4, overall U-shaped heat-exchanging tube bundle 5, tube bundle support plate 6, overflow plate 7, bearing 8, bobbin carriage dividing plate 9, shell side cold flow import C, shell side vapor phase exit D, shell side liquid-phase outlet E, hot-fluid 1 tube side import A1, hot-fluid 1 tube side outlet B1;Hot-fluid 2 tube side import A2, hot-fluid 2 tube side outlet B2;Hot-fluid 3 tube side import A3, hot-fluid 3 tube side outlet B3.
A kind of multi-fluid kettle type reboiler, including overall bobbin carriage 1 and autoclave housing 4, it is tightly connected by tube sheet 3 between the two, the upper end of described autoclave housing is provided with vapor phase exit D, and its underpart is sequentially provided with cold flow import C and liquid-phase outlet E, described overall bobbin carriage 1 is separated into several chamber by bobbin carriage dividing plate 9, neighbouring chamber forms sub-thread hot-fluid bobbin carriage, the corresponding one group of U-shaped heat-exchanging tube bundle of each sub-thread hot-fluid bobbin carriage, each group U-shaped heat-exchanging tube bundle is combined into overall U-shaped heat-exchanging tube bundle 5, the heat exchanger tube of this entirety U-shaped heat-exchanging tube bundle 5 is evenly arranged on described tube sheet 3, U heat exchange bundle absorbs the thermal stress that the shell journey hot and cold stream temperature difference causes, heat exchanger tube being evenly arranged on tube sheet of overall U-shaped heat-exchanging tube bundle 5 makes tube sheet uniform stressed as far as possible.It is provided with hot-fluid import and hot outlets on described each sub-thread hot-fluid bobbin carriage.Multiply hot-fluid is flowed into by overall bobbin carriage 1 hot-fluid import, flows through U-shaped heat-exchanging tube bundle and flowed out by overall bobbin carriage 1 hot outlets after shell side cold flow heat exchange after heat flux distribution plate 2 is uniformly distributed;Cold flow is flowed into by shell side import C, and after seething with excitement with tube side hot-fluid heat exchange in housing, vapor phase fluid is flowed out by shell side gaseous phase outlet D, and liquid phase fluid is flowed out by the outlet of shell side liquid phase E.
Described each sub-thread hot-fluid import bobbin carriage is equipped with heat flux distribution device 2, it is ensured that being uniformly distributed of fluid in bobbin carriage, so that tube sheet and bobbin carriage baffle temperature field are uniform as far as possible, decreases tube sheet and the thermal (temperature difference) stress of bobbin carriage dividing plate.
The tube bundle support plate 6 that described overall U-shaped heat-exchanging tube bundle 5 is installed in autoclave housing 4 supports,
And it is provided with overflow plate 7 in the autoclave housing 4 of this entirety U-shaped heat-exchanging tube bundle 5 rear end.Tube bundle support plate 6 is used for supporting each group of U-shaped heat-exchanging tube bundle, and overflow plate is used for ensureing housing liquid level, is to ensure that the essential condition of the safe and reliable operation of kettle type reboiler.
Claims (4)
1. a multi-fluid kettle type reboiler, including overall bobbin carriage and autoclave housing, it is tightly connected by tube sheet between the two, the upper end of described autoclave housing is provided with vapor phase exit, and its underpart is sequentially provided with cold flow import and liquid-phase outlet, it is characterized in that: described overall bobbin carriage (1) is separated into several chamber by bobbin carriage dividing plate (9), neighbouring chamber forms sub-thread hot-fluid bobbin carriage, the corresponding one group of U-shaped heat-exchanging tube bundle of each sub-thread hot-fluid bobbin carriage, each group U-shaped heat-exchanging tube bundle is combined into overall U-shaped heat-exchanging tube bundle (5), the heat exchanger tube of this entirety U-shaped heat-exchanging tube bundle (5) is evenly arranged on described tube sheet (3), it is provided with hot-fluid import and hot outlets on described each sub-thread hot-fluid bobbin carriage.
A kind of multi-fluid kettle type reboiler the most according to claim 1, it is characterised in that: described each sub-thread hot-fluid import bobbin carriage is equipped with heat flux distribution device (2).
A kind of multi-fluid kettle type reboiler the most according to claim 1, it is characterised in that: the tube bundle support plate (6) that described overall U-shaped heat-exchanging tube bundle (5) is installed in autoclave housing (4) supports.
A kind of multi-fluid kettle type reboiler the most according to claim 1, it is characterised in that: it is provided with overflow plate (7) in the autoclave housing (4) of described overall U-shaped heat-exchanging tube bundle (5) rear end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620470802.3U CN205759760U (en) | 2016-05-23 | 2016-05-23 | A kind of multi-fluid kettle type reboiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620470802.3U CN205759760U (en) | 2016-05-23 | 2016-05-23 | A kind of multi-fluid kettle type reboiler |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205759760U true CN205759760U (en) | 2016-12-07 |
Family
ID=58114710
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620470802.3U Expired - Fee Related CN205759760U (en) | 2016-05-23 | 2016-05-23 | A kind of multi-fluid kettle type reboiler |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205759760U (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106839823A (en) * | 2017-03-24 | 2017-06-13 | 南京聚拓化工科技有限公司 | A kind of HP boiler water deflection bar type preheater and chemical reaction equipment |
CN107569866A (en) * | 2017-10-13 | 2018-01-12 | 茂名瑞派石化工程有限公司 | A kind of new kettle type reboiler and its manufacturing process |
CN107883791A (en) * | 2017-11-10 | 2018-04-06 | 清华大学 | Heat-exchanger rig for variable working condition |
CN108398046A (en) * | 2018-03-14 | 2018-08-14 | 哈尔滨汽轮机厂辅机工程有限公司 | A kind of photo-thermal autoclave evaporator tube bank fixed structure |
CN108801036A (en) * | 2018-06-22 | 2018-11-13 | 沈阳汇博热能设备有限公司 | A kind of kettle type reboiler tube bank limiting device |
CN109458860A (en) * | 2018-12-08 | 2019-03-12 | 大连福佳·大化石油化工有限公司 | Extraction device heat exchanger improves structure |
CN110075554A (en) * | 2019-05-08 | 2019-08-02 | 上海蓝滨石化设备有限责任公司 | A kind of concatenated multi-fluid reboiler in still dome |
CN116907251A (en) * | 2023-09-06 | 2023-10-20 | 浙江浙能迈领环境科技有限公司 | Shell-and-tube heat exchanger structure for methanol supply |
-
2016
- 2016-05-23 CN CN201620470802.3U patent/CN205759760U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106839823A (en) * | 2017-03-24 | 2017-06-13 | 南京聚拓化工科技有限公司 | A kind of HP boiler water deflection bar type preheater and chemical reaction equipment |
CN107569866A (en) * | 2017-10-13 | 2018-01-12 | 茂名瑞派石化工程有限公司 | A kind of new kettle type reboiler and its manufacturing process |
CN107883791A (en) * | 2017-11-10 | 2018-04-06 | 清华大学 | Heat-exchanger rig for variable working condition |
CN108398046A (en) * | 2018-03-14 | 2018-08-14 | 哈尔滨汽轮机厂辅机工程有限公司 | A kind of photo-thermal autoclave evaporator tube bank fixed structure |
CN108801036A (en) * | 2018-06-22 | 2018-11-13 | 沈阳汇博热能设备有限公司 | A kind of kettle type reboiler tube bank limiting device |
CN109458860A (en) * | 2018-12-08 | 2019-03-12 | 大连福佳·大化石油化工有限公司 | Extraction device heat exchanger improves structure |
CN110075554A (en) * | 2019-05-08 | 2019-08-02 | 上海蓝滨石化设备有限责任公司 | A kind of concatenated multi-fluid reboiler in still dome |
CN116907251A (en) * | 2023-09-06 | 2023-10-20 | 浙江浙能迈领环境科技有限公司 | Shell-and-tube heat exchanger structure for methanol supply |
CN116907251B (en) * | 2023-09-06 | 2023-11-21 | 浙江浙能迈领环境科技有限公司 | Shell-and-tube heat exchanger structure for methanol supply |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205759760U (en) | A kind of multi-fluid kettle type reboiler | |
CN202582275U (en) | Multi-fluid shell-and-tube heat exchanger | |
WO2007034290A8 (en) | Nuclear reactor, in particular a liquid-metal-cooled nuclear reactor | |
WO2009024854A3 (en) | Nuclear reactor with compact primary heat exchanger | |
CN203501860U (en) | Built-in sleeve type heater | |
CN204388660U (en) | A kind of shell-and-tube three mediums composite heat-exchanger | |
CN208026096U (en) | A kind of Novel condensation heat exchanger | |
CN201335611Y (en) | Condenser with spiral traverse baffle suitable for heating high pressure gas (steam) | |
CN202582237U (en) | Plate-shell type condenser | |
CN102829646A (en) | Inner finned tube condenser | |
CN201356988Y (en) | Energy-saving type alcohol recovery tower | |
CN204438882U (en) | Vertical reinforcement thin tubesheet heat regenerator | |
CN202346974U (en) | External heat collector | |
CN202955676U (en) | Heat-conduction oil vapor generator | |
CN102072678A (en) | Water bath type gasifying device | |
CN109210825A (en) | A kind of intelligent type heat exchanger with adjusting temperature function | |
CN105135907A (en) | High-temperature-resistant single-tube-pass heat exchange method and heat exchanger | |
CN201311221Y (en) | Header type integral heat pipe | |
CN105222617B (en) | A kind of low flow resistance heat exchanger for natural cycle system | |
CN203064550U (en) | Large-scale storage tank heating device | |
CN202487183U (en) | Floating-head type lead bismuth heat exchange device | |
CN202869316U (en) | Heat exchanger integrating material heating, maintaining and cooling functions | |
CN204240646U (en) | A kind of coverboard full-liquid type heat exchanger | |
CN202915770U (en) | Lamella heat exchanger | |
CN102980332B (en) | Heat recovery shell and tube condenser |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
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: 20161207 |