CN205860828U - Deflection bar type corrugated tube heat exchanger - Google Patents

Deflection bar type corrugated tube heat exchanger Download PDF

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Publication number
CN205860828U
CN205860828U CN201620649725.8U CN201620649725U CN205860828U CN 205860828 U CN205860828 U CN 205860828U CN 201620649725 U CN201620649725 U CN 201620649725U CN 205860828 U CN205860828 U CN 205860828U
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China
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heat exchanger
cavity
inner shell
perforated plate
tube
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CN201620649725.8U
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Chinese (zh)
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卢健
聂忠峰
王智
王雪林
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Nanjing Jutuo Chemical Technology Co Ltd
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Nanjing Jutuo Chemical Technology Co Ltd
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Abstract

The utility model discloses deflection bar type corrugated tube heat exchanger, be provided with inner shell and the tube side end socket molectron being arranged in inner shell and lower perforated plate in the enclosure, tube side end socket molectron includes tube side upper cover and upper perforated plate;It is provided with the duct passed through for coolant between upper cover molectron and inner shell, between lower perforated plate and the low head of inner shell, forms the second cavity, between lower perforated plate and the upper cover of inner shell, form the 3rd cavity;The two ends of heat exchanger tube extend through upper perforated plate and lower perforated plate;Heat exchanger tube is made up of at least two sections of points of heat exchanger tubes, the adjacent two sections of points of heat exchanger tubes of the same heat exchanger tube closing inner space by gas distributor;Rod baffle is arranged in the region between upper perforated plate and lower perforated plate;The 4th cavity connecting coolant import is formed between shell, inner shell and lower perforated plate;Connection the 3rd cavity and the coolant through hole of the 4th cavity is had on the housing of inner shell.The thermal efficiency of the present utility model is high, be difficult to generate dirt, be difficult to leakage and cost is low.

Description

Deflection bar type corrugated tube heat exchanger
Technical field
This utility model belongs to technical field of chemical, is a kind of vertical heat exchanger, specifically a kind of baffling Rod-type corrugated tube heat exchanger.
Background technology
At present, shell-and-tube exchanger commonly uses.The shortcoming of conventional heat exchanger is that the thermal efficiency is low, easy generates dirt Dirt and easily leakage.For operation pressure ratio compared with big and that temperature is high heat exchanger, it is the most that it manufactures material, and must be with not Rust steel or steel alloy, thus manufacturing price is the most costly.On the whole, it is main scarce that current shell-and-tube exchanger exists Point is: the thermal efficiency is low, easily generate dirt, easily leak and involve great expense.
Utility model content
The purpose of this utility model be low for the existing heat exchanger thermal efficiency, easily generate dirt, leakage point is many and makes The problems such as high price is expensive, it is provided that a kind of thermal efficiency height, the deflection bar type corrugated tube being difficult to generate dirt, be difficult to leak and cost is low are warm Exchanger, concrete technical scheme is as follows:
Deflection bar type corrugated tube heat exchanger, including shell, is provided with Heating medium, heating agent outlet, coolant on shell Import and refrigerant exit, the inner chamber at shell is provided with inner shell and the tube side end socket molectron being arranged in inner shell cavity and down tube Plate, tube side end socket molectron includes tube side upper cover and the upper perforated plate being arranged on tube side upper cover, tube side upper cover and upper pipe The first cavity it is formed with between plate;
Upper cover molectron is arranged on the upper end of inner shell, and and inner shell between be provided with the duct passed through for coolant, down tube Plate is sealably mounted at the lower end of inner shell, is formed with the second cavity, lower perforated plate and inner shell between lower perforated plate and the low head of inner shell Upper cover between formed the 3rd cavity;
Being additionally provided with rod baffle, some heat exchanger tubes and at least one gas distributor in inner shell cavity, described some are changed The upper end of heat pipe is run through upper perforated plate and connects the first cavity, and the lower end of described some heat exchanger tubes is run through lower perforated plate and connects second Cavity;Arbitrary gas distributor at least one gas distributor above-mentioned has at least one and closes inner chamber, in described some heat exchanger tubes At least heat exchanger tube be made up of at least two sections of points of heat exchanger tubes, adjacent two sections of points of heat exchanger tubes of same heat exchanger tube pass through one Closing cavity connects;Rod baffle is arranged in the region between upper perforated plate and lower perforated plate;
Having gap between inner shell and shell, described spacer ring is arranged around inner shell, makes between shell, inner shell and lower perforated plate Form the 4th cavity;Coolant inlet communication the 4th cavity, is provided with connection the 3rd cavity and the 4th cavity on the housing of inner shell Coolant through hole, coolant through hole is arranged in the housing of inner shell relative to the region between lower perforated plate and upper perforated plate;Refrigerant exit connects 3rd cavity, Heating medium connects the first cavity, heating agent outlet the second cavity.
In use, coolant enters into the 4th cavity by coolant import to this utility model, then by the housing of inner shell On coolant through hole enter in the cavity of inner shell, carry out energy exchange with the heating agent in heat exchanger tube, owing to whole inner shell is arranged In the enclosure, the housing of inner shell is inside and outside all by the pressure of coolant so that the external and internal pressure difference of the housing of inner shell is less, can have Effect ground reduces the thickness of the housing of inner shell, when inner shell uses alloy steel or stainless steel Steel material to make, in can being effectively reduced The manufacturing expense of shell, thus reduces the manufacturing cost of whole heat exchanger.
This utility model rod baffle substitutes deflection plate, reduces shell side resistance, is more beneficial for the housing of reduction inner shell Thickness.
In this utility model, the split-type structural that heat exchange tube design Cheng Youfen heat exchanger tube is formed, same heat exchanger tube Dividing heat exchanger tube to be coupled together by gas distributor, each point of heat exchanger tube can use different materials according to residing different region Make, to reduce the integral manufacturing expense of heat exchanger as much as possible.
Further, described coolant through hole is disposed relative to upper perforated plate, closer on the housing of the inner shell of lower perforated plate, can make Coolant contacts with heat exchanger tube fully, carries out energy exchange with the heating agent in heat exchanger tube.
Further, being provided only with a gas distributor in inner shell cavity, this gas distributor is provided with one and closes cavity, described Some heat exchanger tubes, by upper point heat exchanger tube and two pieces points of heat exchanger tubes compositions of lower point of heat exchange, above divide heat exchanger tube to lead to lower point of heat exchanger tube Cross the connection of closing cavity.One gas distributor is only set, the complexity of heat exchanger can be effectively reduced;It it is two sections by heat exchange tube design Formula structure, to reduce making and the installation of heat exchanger further.
Further, the upper end that heat exchanger tube is arranged in inner shell cavity, a lower point heat exchanger tube is above divided to be arranged in inner shell cavity Lower end, above divides heat exchanger tube to use alloy pipe to make, and lower point of heat exchanger tube uses carbon steel pipe to make.A upper point heat exchanger tube is arranged in heat exchange The high-temperature region of device, uses resistant to elevated temperatures alloy pipe to make, and lower point of heat exchanger tube is arranged in the low-temperature space of heat exchanger, uses common Carbon steel pipe makes, and on the premise of ensureing heat exchanger effective efficiency, reduces the manufacturing cost of heat exchanger.
Further, the housing of inner shell is divided into the upper shell and lower house being tightly connected, and upper shell is positioned at the upper end of lower house, Described upper shell uses alloy steel material to make, and lower house uses carbon steel material to make.The housing of inner shell is also classified into upper and lower two Segmentation structure, wherein upper shell is in high-temperature region, have employed steel alloy and makes, and lower house is in low-temperature space, uses carbon steel system Make, to be effectively reduced the manufacturing expense of heat exchanger.
Further, described some heat exchanger tubes use corrugated tube to make.Described point of heat exchanger tube uses corrugated tube to make, and divides and changes The top and bottom of heat pipe are provided with construction section.Heat exchanger tube and point heat exchanger tube use corrugated tube to make, and have the advantage that
1, the thermal efficiency is high.Owing to heat exchanger tube uses corrugated form, pipe inner runner section continuously suddenlys change, and causes fluid Even if being in high turbulence state in the case of flow velocity is the lowest the most all the time, it is difficult to form laminar flow, make the main heat of convection heat transfer' heat-transfer by convection Resistance is effectively overcome, and the inside and outside heat transfer of pipe is strengthened simultaneously, thus heat transfer coefficient is the highest, can reach 2-3 times of straight pipe type.
2, it is difficult to generate dirt.Due to the high turbulence of fluid in runner, the microgranule in fluid is made to be difficult to deposit fouling, i.e. A small amount of dirt has been made to generate, the strain produced owing to there is shell journey thermal (temperature difference) stress on corrugated tube, make that there is elastic characteristic Corrugated tube curvature generation micro-variations, so that corrugated tube heat exchanger has nature antiscale and the ability of natural scale removal.Medium exists Tube wall is washed away strongly by the inside and outside great turbulence level of pipe, and additionally the smooth arc of bellows surface also can suppress generation and the life of incrustation scale Long.
3, leakage prevention is strong.Because each ripple of every heat exchanger tube all has the function that self-compensation situation expands with heat and contract with cold, because of What this need not expansion joint etc arranges the thermal (temperature difference) stress reducing shell journey, has stronger adaptation thermal expansion ability, thus subtracts Lack the possibility of the leakage losses such as the equipment caused because expanding with heat and contract with cold snaps.
Further, described rod baffle includes that horizontal rod baffle and longitudinal rod baffle, horizontal rod baffle and longitudinal rod baffle are equal Horizontally disposed, horizontal rod baffle and longitudinal rod baffle are mutually perpendicular to.Mutual horizontal rod baffle and longitudinal rod baffle are set, can protect The card disturbance to coolant, it is ensured that heat transfer effect.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the present utility model.
Fig. 2 is the enlarged drawing in the region being labeled as A in Fig. 1.
Fig. 3 is the schematic diagram of heat exchanger tube in this utility model.
In figure: 1-Heating medium;2-heating agent air inlet pipe;3-refrigerant exit;4-coolant escape pipe;5-coolant import;Between 6- Gap;7-upper shell;Upper point of heat exchanger tube of 8-;9-gas distributor;10-lower house;Lower point of heat exchanger tube of 11-;12-shell;14-coolant leads to Hole;15-heating agent escape pipe;16-heating agent exports;17-longitudinal direction rod baffle;The horizontal rod baffle of 18-;19-tube side upper cover;On 20- Tube sheet;21-lower perforated plate;22-the first cavity;23-the second cavity;24-the 3rd cavity;25-the 4th cavity;26-connecting rod;In 27- The upper cover of shell;The low head of 28-inner shell;91-closes cavity.
Detailed description of the invention
Following combination accompanying drawing and enforcement example are to this utility model further instruction.
Refer to Fig. 1 and Fig. 2, deflection bar type corrugated tube heat exchanger, including shell 12, shell 12 is provided with heating agent Import 1, heating agent outlet 16, coolant import 5 and refrigerant exit 3, the inner chamber at shell 12 is provided with inner shell and is arranged on inner shell chamber Internal tube side end socket molectron and lower perforated plate 21, tube side end socket molectron includes tube side upper cover 19 and is arranged on tube side envelope Upper perforated plate 20 on 19, is formed with the first cavity 22 between tube side upper cover 19 and upper perforated plate 20;
In the present embodiment, the shell 12 cylindrical shape in closed at both ends, cylindrically, the two ends of inner shell use inner shell entirety Ellipse head is closed.Inner shell is made up of upper shell 7 and lower house 10, and upper shell and lower house are welded to connect, wherein upper casing position In the upper end of lower house, upper shell uses chrome-nickel Steel material to make, and lower house uses carbon steel material to make.It is appreciated that According to concrete heat-exchange temperature and heat transferring medium, upper shell can also use the alloy steel material of type to make;Certainly inner shell is also Integral manufacturing can be used, and overall employing alloy steel material makes.
Upper cover molectron is arranged on the upper end of inner shell, and and inner shell between be provided with the duct passed through for coolant, down tube Plate 21 is sealably mounted between the low head 28 of the lower end of inner shell, lower perforated plate and inner shell and is formed with the second cavity 23, lower perforated plate The 3rd cavity 24 is formed between 21 and the upper cover 27 of inner shell;
In the present embodiment, tube side upper cover 19 is fixed on the inwall of upper cover 27 of inner shell by connecting rod 26, tube side Gap is had, the duct passed through as coolant between upper cover 19 and the inwall of inner shell.
Being additionally provided with rod baffle, some heat exchanger tubes and at least one gas distributor in inner shell cavity, described some are changed The upper end of heat pipe is run through upper perforated plate and connects the first cavity, and the lower end of described some heat exchanger tubes is run through lower perforated plate and connects second Cavity;Arbitrary gas distributor at least one gas distributor above-mentioned has at least one and closes inner chamber, in described some heat exchanger tubes At least heat exchanger tube be made up of at least two sections of points of heat exchanger tubes, adjacent two sections of points of heat exchanger tubes of same heat exchanger tube pass through one Closing cavity connects.
Please refer to Fig. 3, in the present embodiment, being provided only with a gas distributor 9, this gas distributor 9 is provided with an envelope Closing cavity 91, all heat exchanger tubes are divided into point heat exchanger tube 8 and lower point of heat exchanger tube 11, above divide the lower end of heat exchanger tube and lower point of heat exchange The upper end of pipe all connects the closing cavity 91 of gas distributor 9, makes point heat exchanger tube connect with lower point of heat exchanger tube.Upper point of heat exchanger tube uses Chrome-nickel steel pipe manufacturing, lower point of heat exchanger tube uses carbon steel pipe to make.
In the present embodiment, all heat exchanger tubes all use corrugated tube to make, wherein upper point of heat exchanger tube 8 and lower point of heat exchanger tube 11 Two ends be provided with construction section, for being connected with upper perforated plate, lower perforated plate and gas distributor, connected mode uses welds, Ke Yili Solving, according to different needs, connected mode can also use expanded joint.In figure 3, upper end 81 and the lower end 82 of heat exchanger tube 8 are above divided For construction section, lower point of heat exchanger tube 11 is similar with the structure of upper point heat exchanger tube 8.
It is appreciated that gas distributor can also arrange two, three, four, and more, and the concrete quantity that arranges can root Convenient and reasonable setting according to installation and maintenance.
Be appreciated that every heat exchanger tube can also for becoming three sections, four sections, or even more multistage divides heat exchanger tube, and according to specifically Heat transferring medium and heat-exchange temperature use different materials to make, to reach matter the multistage heat exchanger tube of same heat exchanger tube Amount and the reasonable balance of cost.
Rod baffle is divided into multi-tier arrangement from bottom to up in the present embodiment, and every layer is fixed on an annulus, and garden ring passes through Connecting rod concatenates up and down, and is fixed on the inwall of inner shell.Certainly the most also can by single for the above-mentioned annulus inwall being fixed on inner shell, Or directly rod baffle is fixed on the inwall of inner shell.
Having gap 6 between inner shell and shell, described gap 6 is arranged around inner shell, makes shell 12, inner shell and down tube The 4th cavity 25 is formed between plate 21;Coolant import 5 connects the 4th cavity, is provided with connection the 3rd cavity on the housing of inner shell 24 and the 4th coolant through hole 14 of cavity 25, coolant through hole 14 be arranged in the housing of inner shell relative to lower perforated plate 21 and upper perforated plate 20 it Between region;In the present embodiment, coolant through hole 14 is disposed relative to upper perforated plate, region closer to lower perforated plate 21, coolant Through hole 14 has several, and around lower house 10 circumferentially.
Refrigerant exit 3 connects the 3rd cavity 24 by coolant escape pipe 4, and Heating medium 1 connects the by heating agent air inlet pipe 2 One cavity 22, heating agent outlet 16 connects the second cavity 23 by heating agent escape pipe 15.
In the present embodiment, rod baffle includes horizontal rod baffle 18 and longitudinal rod baffle 17, horizontal rod baffle and longitudinally folding Flow post is the most horizontally disposed, and is mutually perpendicular to.

Claims (8)

1. deflection bar type corrugated tube heat exchanger, including shell, is provided with Heating medium, heating agent outlet, coolant enters on shell Mouth and refrigerant exit, it is characterised in that the inner chamber at shell is provided with inner shell and the tube side end socket group being arranged in inner shell cavity Component and lower perforated plate, tube side end socket molectron includes tube side upper cover and the upper perforated plate being arranged on tube side upper cover, on tube side The first cavity it is formed with between end socket and upper perforated plate;
Upper cover molectron is arranged on the upper end of inner shell, and and inner shell between be provided with the duct passed through for coolant, lower perforated plate is close Feud is arranged on the lower end of inner shell, is formed with the second cavity between lower perforated plate and the low head of inner shell, and lower perforated plate is upper with inner shell The 3rd cavity is formed between end socket;
Rod baffle, some heat exchanger tubes and at least one gas distributor, described some heat exchanger tubes it are additionally provided with in inner shell cavity Upper end run through upper perforated plate and connect the first cavity, the lower end of described some heat exchanger tubes runs through lower perforated plate and to connect second empty Chamber;Arbitrary gas distributor at least one gas distributor above-mentioned has at least one and closes inner chamber, in described some heat exchanger tubes At least heat exchanger tube is made up of at least two sections of points of heat exchanger tubes, and adjacent two sections of points of heat exchanger tubes of same heat exchanger tube pass through an envelope Close cavity connection;Rod baffle is arranged in the region between upper perforated plate and lower perforated plate;
Having gap between inner shell and shell, described spacer ring is arranged around inner shell, makes to be formed between shell, inner shell and lower perforated plate 4th cavity;Coolant inlet communication the 4th cavity, is provided with connection the 3rd cavity and the 4th cavity cold on the housing of inner shell Matchmaker's through hole, coolant through hole is arranged in the housing of inner shell relative to the region between lower perforated plate and upper perforated plate;
Refrigerant exit connection the 3rd cavity, Heating medium connects the first cavity, heating agent outlet the second cavity.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that described coolant through hole is arranged in Relative to upper perforated plate, closer on the housing of the inner shell of lower perforated plate.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that only arrange in inner shell cavity Having a gas distributor, this gas distributor is provided with one and closes cavity, and described some heat exchanger tubes are by upper point heat exchanger tube and lower point Two pieces points of heat exchanger tube compositions of heat exchange, above divide heat exchanger tube to connect by closing cavity with lower point of heat exchanger tube.
Deflection bar type corrugated tube heat exchanger the most according to claim 3, it is characterised in that in above dividing heat exchanger tube to be arranged in Upper end in shell cavity, lower point of heat exchanger tube is arranged in the lower end in inner shell cavity, above divides heat exchanger tube to use alloy pipe to make, under Heat exchanger tube is divided to use carbon steel pipe to make.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that the housing of inner shell is divided into sealing The upper shell connected and lower house, upper shell is positioned at the upper end of lower house, and described upper shell uses alloy steel material to make, lower casing Body uses carbon steel material to make.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that described some heat exchanger tubes are adopted Make of corrugated tube.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that described point of heat exchanger tube uses ripple Stricture of vagina pipe makes, and the top and bottom of point heat exchanger tube are provided with construction section.
Deflection bar type corrugated tube heat exchanger the most according to claim 1, it is characterised in that described rod baffle includes laterally Rod baffle and longitudinal rod baffle, horizontal rod baffle and longitudinal rod baffle are the most horizontally disposed, horizontal rod baffle and longitudinal rod baffle phase The most vertical.
CN201620649725.8U 2016-06-27 2016-06-27 Deflection bar type corrugated tube heat exchanger Active CN205860828U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620649725.8U CN205860828U (en) 2016-06-27 2016-06-27 Deflection bar type corrugated tube heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620649725.8U CN205860828U (en) 2016-06-27 2016-06-27 Deflection bar type corrugated tube heat exchanger

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CN205860828U true CN205860828U (en) 2017-01-04

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109984602A (en) * 2018-01-02 2019-07-09 青岛海尔施特劳斯水设备有限公司 Water dispenser
CN110411238A (en) * 2019-07-18 2019-11-05 德州职业技术学院(德州市技师学院) A kind of pure electric automobile cooling system heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109984602A (en) * 2018-01-02 2019-07-09 青岛海尔施特劳斯水设备有限公司 Water dispenser
CN109984602B (en) * 2018-01-02 2023-12-12 青岛海尔施特劳斯水设备有限公司 water dispenser
CN110411238A (en) * 2019-07-18 2019-11-05 德州职业技术学院(德州市技师学院) A kind of pure electric automobile cooling system heat exchanger
CN110411238B (en) * 2019-07-18 2020-11-20 德州职业技术学院(德州市技师学院) Heat exchanger for pure electric vehicles cooling system

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