CN206177097U - Multiple exit tube heat exchanger of controllable temperature - Google Patents

Multiple exit tube heat exchanger of controllable temperature Download PDF

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Publication number
CN206177097U
CN206177097U CN201621225074.6U CN201621225074U CN206177097U CN 206177097 U CN206177097 U CN 206177097U CN 201621225074 U CN201621225074 U CN 201621225074U CN 206177097 U CN206177097 U CN 206177097U
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China
Prior art keywords
shell
outlet
shell side
export
medium
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Application number
CN201621225074.6U
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Chinese (zh)
Inventor
璧典寒
赵亮
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Changchun Zhongan Hongcheng Weiye Energy Saving Technology Co Ltd
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Changchun Zhongan Hongcheng Weiye Energy Saving Technology Co Ltd
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Priority to CN201621225074.6U priority Critical patent/CN206177097U/en
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Abstract

The utility model provides a multiple exit tube heat exchanger of controllable temperature, includes: and a housing, two baffles that are close to both ends in the shell, a set of medium circulation pipe of welding on the baffle, the medium import and the export at shell both ends, establish import of the medium on the shell lateral wall and export between two baffles, guide plate between two interior baffles on the shell, the shell both ends are advanced, form the tube side between the export, the shell lateral wall is enterprising, form the shell side between the export, it exports to increase by one or more than one shell side middle section between the import of shell side on the shell lateral wall and the terminal export of shell side, the medium conveying pipe who connects each export of shell side collects and is connected to on a tee bend or the electric flow control valve of expert more. Electric flow control valve disposes flow controller, the utility model discloses an actively the effect is: can control shell side and the heat transfer total amount of tube side and the exit temperature of governing valve on best node. An influence falls to minimumly for central heating system, to the secondary network electric heat pump peaking unit evaporimeter. The reduction is to former influence of once netting hydraulic balance.

Description

A kind of multiple exit shell-and-tube heat exchanger of controllable temperature
Technical field
This utility model belongs to technical field of heat exchangers, and in particular to a kind of multiple exit shell-and-tube heat exchanger of controllable temperature.
Background technology
Shell-and-tube heat exchanger used in central heating secondary network electric heating pump peak regulation system, goes out according to only one shell side The conventional structure of mouth, it is as follows with once net water heat exchange existing problems.One is due to restraining heat-transfer surface in conventional shell-and-tube heat exchanger Product is substantially stationary, constant in the medium temperature and flow of tube side import, and the heat exchange medium temperature and flow of shell side import is not In the case of change, the heat exchange medium temperature for wanting to control shell-side outlet is relatively difficult.If electric heating pump vaporizer inflow temperature Too high, medium is easily in high temperature, high pressure conditions in vaporizer, affects very big to the service life of electric heating pump assembly;Two is for steady Determine the inflow temperature of electric heating pump vaporizer, need the inlet and outlet pipe in electric heating pump vaporizer to concatenate an electric three passes and adjust Valve, is mixed using the relatively low vaporizer water outlet of temperature with shell side water outlet, the inflow temperature of vaporizer is controlled with this, due to being typically for The once net of hot heat exchange station and the confession of secondary network, backwater caliber are larger, and concatenation electric three-way regulating valves are easily limited by space is transformed System.
Utility model content
The purpose of this utility model is to provide a kind of multiple exit shell-and-tube heat exchanger of controllable temperature, overcomes existing shell to exchange heat What device was present(Shell side)The deficiency that heat exchange medium temperature can not be adjusted voluntarily.
Shell-and-tube heat exchanger of the present utility model includes two panels dividing plate, the welding of tubular closure, inside the shell near two ends One group of medium circulation tube that shell two ends cavity volume is connected on dividing plate, the medium entrance for being located at shell two ends and outlet, it is located at two Heat transferring medium inlet and outlet, inside the shell between piece dividing plate on side wall of outer shell be crisscross arranged between two panels dividing plate several pieces lead Stream plate, the passage between the import and export of shell two ends forms tube side, and the passage on side wall of outer shell between import and export forms shell side, institute The improvement of work is:Between shell side import and shell side end outlet on side wall of outer shell(Shell side is interval)Increase by one or one with Upper shell side stage casing outlet, medium delivery pipe for connecting each interval outlet of shell side is collected and is connected to a threeway or is powered dynamic more On flow control valve.Electric flow control valve configures flow controller;Described flow controller, goes out including shell side end is located at Temperature sensor in mouth, the outlet of shell side stage casing, electric flow control valve outlet or medium delivery pipe, treatment temperature transducing signal And the control module of output regulation and control electric flow control valve electric current.
Increase a shell side stage casing outlet between shell side import and shell side end outlet on side wall of outer shell, connect shell side Stage casing exports to collect with the medium delivery pipe of shell side end outlet and is connected on an electric three-way flow control valve.
A kind of porous shell-and-tube heat exchanger method of operation of controllable temperature of the present invention is as follows:Temperature medium middle first passes through connecting line Into the tube side water inlet of multiple exit shell-and-tube heat exchanger, middle temperature medium heat is passed to by tube bank outer wall by tube bank inwall reverse The low-temperature heat exchange medium of flowing, thus the middle temperature medium temperature in tube side be minimized, become cryogenic media, via multiple exit pipe The tube side outlet of shell heat exchanger flows out.
At the same time, low-temperature heat exchange medium enters the shell side water inlet of multiple exit shell-and-tube heat exchanger by connecting line, leads to The middle temperature media for heat exchange of tube bank outer wall and tube bank inwall reverse flow is crossed, and under the regulation of electric three-way regulating valves, a part After low-temperature heat exchange medium is by restraining the less low-temperature heat exchange region heat exchange of heat exchange area, flow out from shell side stage casing outlet, and One water inlet of electric three-way regulating valves is entered by connecting line;Another part low-temperature heat exchange medium is by restraining heat-transfer surface After the maximum middle temperature heat exchange area heat exchange of product, flow out from shell side outlet water at tail end mouth, adjusted into electric three passes by connecting line Another water inlet of valve.Low-temperature heat exchange medium after gentle low-temperature heat exchange region is heated up in, the entrance of lower temperature is electronic One water inlet of three-way control valve, another water inlet of the entrance electric three-way regulating valves of higher temperature, after two-way heats up Low-temperature heat exchange medium mixed inside electric three-way regulating valves after, then by electric three-way regulating valves outlet flow out, Complete the shell side of a multiple exit shell-and-tube heat exchanger and the heat exchange of tube side, and the regulation process to shell side leaving water temperature.
Good effect of the present utility model is
1st, it is to restrain the less low-temperature heat exchange region of heat exchange area, shell side outlet water at tail end mouth that shell side stage casing outlet is corresponding Corresponding is to restrain the maximum middle temperature heat exchange area of heat exchange area, by electric three-way regulating valves to multiple exit shell-and-tube heat exchanger The regulation of shell side stage casing outlet and shell side outlet water at tail end mouth flow, can by the heat exchange total amount of shell side and tube side, and electronic three The outlet temperature of logical regulating valve is controlled on optimal node.
2nd, the stability of the vaporizer inflow temperature of electric heating pump regulating units, is related to the safety fortune of electric heating pump regulating units OK, after using multiple exit shell-and-tube heat exchanger and the once net backwater indirect heat exchange mode of temp. controllable, by once net return water temperature Impact of the transient change to secondary network electric heating pump regulating units vaporizer is preferably minimized.
3rd, because electric heating pump regulating units need to be connected on once net on middle temperature water return pipeline, if resistance is excessive influencing whether Original hydraulic equilibrium once netted, because the resistance ratios plate type heat exchanger of the multiple exit shell-and-tube heat exchanger of controllable temperature it is low by more than 50%, can Reduce to greatest extent once netting hydraulically balanced impact to original.
Description of the drawings
A kind of temperature-adjustable shell-and-tube heat exchanger schematic diagram of Fig. 1 this utility model.
How logical electric flow control valve electric controller used in a kind of temperature-adjustable shell-and-tube heat exchanger of Fig. 2 this utility model Block diagram.
Specific embodiment
Refering to Fig. 1, Fig. 2, a kind of multiple exit shell-and-tube heat exchanger of controllable temperature, including:Tubular closure 2, inside the shell is leaned on The two panels dividing plate 3 of two close end, it is welded on dividing plate and connects one group of medium circulation tube 4 of shell two ends cavity volume, is located at shell two ends Tube side import 1 and tube side outlet 6, be located at shell side import 11 between two panels dividing plate 3 on the side wall of shell 2 and shell-side outlet 7, outer Several pieces shell side deflectors 5 being crisscross arranged in shell between two panels dividing plate 3, improvements introduced is:Shell on the side wall of shell 2 Increase a shell side stage casing outlet 10, connection shell side stage casing outlet 10 and shell side end between journey import 11 and shell side end outlet 7 The medium delivery pipe 9 for bringing out mouth 7 is collected and is connected on the two entrances end of an electric three-way flow control valve 8.Electric flow Regulating valve configures flow controller;Described flow controller, including be located at shell side end outlet, shell side stage casing outlet, it is electronic Temperature sensor in Flow-rate adjustment valve outlet port or medium delivery pipe, treatment temperature transducing signal and output regulation and control electric flow are adjusted The control module of section valve electric current.

Claims (2)

1. the multiple exit shell-and-tube heat exchanger of a kind of controllable temperature, including:Tubular closure, inside the shell near two ends two panels every Plate, be welded on dividing plate one group of medium circulation tube for connecting shell two ends cavity volume, the medium entrance for being located at shell two ends and outlet, The heat transferring medium inlet and outlet that is located between two panels dividing plate on side wall of outer shell, inside the shell are crisscross arranged between two panels dividing plate Several pieces deflectors, the passage between the import and export of shell two ends forms tube side, and the passage on side wall of outer shell between import and export is formed Shell side, is characterized in that:Increase one or more shell sides between shell side import and shell side end outlet on side wall of outer shell Stage casing exports, and connection shell side stage casing exports to collect to be connected to a threeway or be powered to moving more with the medium delivery pipe of end outlet flows Electric flow control valve configuration flow controller on adjustable valve;Described flow controller, including be located at shell side end outlet, Shell side stage casing outlet, electric flow control valve outlet or medium delivery pipe in temperature sensor, treatment temperature transducing signal and The control module of output regulation and control electric flow control valve electric current.
2. a kind of multiple exit shell-and-tube heat exchanger of controllable temperature according to claim 1, is characterized in that:On side wall of outer shell Increase a shell side stage casing outlet, the outlet of connection shell side stage casing and shell side end outlet between shell side import and shell side end outlet Medium delivery pipe collect and be connected on an electric three-way flow control valve.
CN201621225074.6U 2016-11-15 2016-11-15 Multiple exit tube heat exchanger of controllable temperature Active CN206177097U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621225074.6U CN206177097U (en) 2016-11-15 2016-11-15 Multiple exit tube heat exchanger of controllable temperature

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621225074.6U CN206177097U (en) 2016-11-15 2016-11-15 Multiple exit tube heat exchanger of controllable temperature

Publications (1)

Publication Number Publication Date
CN206177097U true CN206177097U (en) 2017-05-17

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621225074.6U Active CN206177097U (en) 2016-11-15 2016-11-15 Multiple exit tube heat exchanger of controllable temperature

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CN (1) CN206177097U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107388859A (en) * 2017-09-07 2017-11-24 华中科技大学 Heat exchanger assembly and flow self-regulating heat exchanger
CN109373788A (en) * 2018-09-04 2019-02-22 徐召辉 A kind of energy-efficient formula dividing wall type heat exchanger
CN110579120A (en) * 2019-08-30 2019-12-17 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof
CN110736366A (en) * 2019-10-17 2020-01-31 沪东重机有限公司 body two-section type heat exchanger and heat exchange method
CN115435615A (en) * 2022-09-26 2022-12-06 江苏曙光压力容器有限公司 Corrugated pipe heat exchanger with heat transfer enhancement effect

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107388859A (en) * 2017-09-07 2017-11-24 华中科技大学 Heat exchanger assembly and flow self-regulating heat exchanger
CN107388859B (en) * 2017-09-07 2023-06-02 华中科技大学 Heat exchanger assembly and self-adjusting flow heat exchanger
CN109373788A (en) * 2018-09-04 2019-02-22 徐召辉 A kind of energy-efficient formula dividing wall type heat exchanger
CN110579120A (en) * 2019-08-30 2019-12-17 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof
CN110579120B (en) * 2019-08-30 2020-11-24 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof
CN110736366A (en) * 2019-10-17 2020-01-31 沪东重机有限公司 body two-section type heat exchanger and heat exchange method
CN115435615A (en) * 2022-09-26 2022-12-06 江苏曙光压力容器有限公司 Corrugated pipe heat exchanger with heat transfer enhancement effect
CN115435615B (en) * 2022-09-26 2023-12-22 江苏曙光压力容器有限公司 Corrugated pipe heat exchanger with heat transfer enhancement effect

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