CN2338712Y - High efficiency fin type shell-and-tube exchanger - Google Patents

High efficiency fin type shell-and-tube exchanger Download PDF

Info

Publication number
CN2338712Y
CN2338712Y CN 98219185 CN98219185U CN2338712Y CN 2338712 Y CN2338712 Y CN 2338712Y CN 98219185 CN98219185 CN 98219185 CN 98219185 U CN98219185 U CN 98219185U CN 2338712 Y CN2338712 Y CN 2338712Y
Authority
CN
China
Prior art keywords
tube
fin
heat exchanger
heat
pipe
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
Application number
CN 98219185
Other languages
Chinese (zh)
Inventor
臧海
杜西宁
贾诚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 98219185 priority Critical patent/CN2338712Y/en
Application granted granted Critical
Publication of CN2338712Y publication Critical patent/CN2338712Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model relates to a high efficiency fin-type tube casing type heat exchanger. The utility model is composed of a casing and a heat exchanger tube core, wherein, the heat exchanger tube core is composed of fin-type tubes and a tube plate, wherein, a plurality of fin tubes are fixed on the tube plate, and each fin-type tube is composed of fins and a heat exchanging tube. Practice verifies that the utility model has the advantages of small size, light weight and high heat efficiency, and can greatly improve the flow rate of the heat exchanging medium. Thereby, the utility model can be widely used for heat exchanging devices of gas and liquid, liquid and gas, and liquid with high viscosity in the industry, such as petroleum, chemistry, construction material, food, etc. The utility model is an ideal renewal generation product.

Description

High-efficiency fin type shell-and-tube heat exchange of heat pipe
The utility model relates to a kind of high-efficiency fin type shell-and-tube heat exchange of heat pipe, adopts the shell-and-tube heat exchanger of the finned tube manufacturing of strengthening.
At present, China almost the shell-and-tube heat exchanger more than 90% be the light pipe pipe bundle heat exchanger, application is extensive, the existing history that goes up a century, this heat exchanger volume is huge, heat exchange efficiency is low, weight is big, in order to improve the flow regime of fluid, increased a large amount of deflection plates, increased the resistance of fluid, energy consumption is serious, because above this heat exchanger of various shortcoming does not satisfy the development of modern technologies far away, though invented finned sheet exchanger now again, the node pipe heat exchanger, still, the pressure that these heat exchangers are tried out is low, range of application is little, and very difficult large tracts of land is promoted the use of and replaced present pandemic light pipe shell-and-tube heat exchanger.
The purpose of this utility model is: the high-efficiency fin type shell-and-tube that a kind of volume is little, in light weight, heat exchange efficiency is high, the resistance of fluid is little, energy consumption is little heat exchange of heat pipe is provided.Can be widely used in industries such as oil, chemical industry, building materials, weaving, food, be specially adapted to require in resistance is little, liquid viscosity is high, installing space the is little complex appts.
The utility model high-efficiency fin type shell-and-tube heat exchange of heat pipe is achieved in that its structure of high-efficiency fin type shell-and-tube heat exchange of heat pipe is made of: housing and heat exchanger tube core: its heat exchanger tube core: be made up of fin-type pipe and tube sheet, dozens of fin-type pipe is fixed on the tube sheet; Its fin-type pipe: form by fin and heat exchanger tube; Its housing: by head and organization.Its head: be that end sealing is semicircle, itself and body connection place are ring flange, have dividing plate that its inner chamber is divided into two chambeies up and down in it, and promptly high-temperature medium enters chamber and high-temperature medium outlet plenum, and its high-temperature medium enters the chamber and is provided with high-temperature medium inlet tube interface; The high-temperature medium outlet plenum is provided with high-temperature medium outlet interface: its body: be end sealing tubular, establish cryogenic media inlet or outlet duct interface on it, the heat exchanger tube core is housed in the cavity, itself and head connection place are ring flange, support are arranged below its body.
Further elaborate as follows below by embodiment and accompanying drawing:
Accompanying drawing 1: the utility model structural representation
Accompanying drawing 2: the utility model fin-type pipe enlarged drawing
Accompanying drawing 3: the straight shape fin-type tube bank of the utility model high-efficiency fin type shell-and-tube heat exchange of heat pipe schematic diagram;
Its structure of the utility model high-efficiency fin type shell-and-tube heat exchange of heat pipe, as shown in Figure 1: constitute by housing and heat exchanger tube core; Its heat exchanger tube core: be made up of fin-type pipe (5) and tube sheet (3), dozens of fin-type pipe (5) is fixed on the tube sheet (3); Its fin-type pipe (5): be made up of fin (14) and heat exchanger tube (13), its fin (14) is vertical straight fins or vertical straight ripple formula fin, as shown in Figure 2; Its housing: form by head (1) and body (6).Its head (1): be that end sealing is semicircle, itself and body connection place are ring flange (10), have dividing plate (12) that its inner chamber is divided into two chambeies up and down in it, promptly high-temperature medium enters chamber C and high-temperature medium outlet plenum D, and its high-temperature medium enters chamber C and is provided with high-temperature medium inlet tube interface (11); High-temperature medium outlet plenum D is provided with high-temperature medium outlet interface (2): its body: be end sealing tubular, establish cryogenic media inlet or outlet duct interface (8), (4) on it, the heat exchanger tube core is housed in the body, itself and head (1), tube sheet (3) connection place are ring flange (9), there is sealing gasket (15) ring flange (10), (9) with tube sheet (3) connection place, by bolt ring flange (10), (9) and tube sheet (3) are connected as one, support (7) are arranged below its body.
Big and small a series of high-efficiency fin type shell-and-tube heats exchange of heat pipe that the inventor makes, its heat exchanger tube core are restrained for the U-shaped fin-type or straight shape fin-type is restrained two kinds, as Fig. 1, shown in Figure 4;
Practice confirms: we compare (one) with traditional light pipe shell-and-tube heat exchanger and the utility model of identical heat exchange area, get the heat exchanger that heat exchange area is 260 square metres and compare, and are listed as follows:
Item argument Tradition light pipe formula heat exchanger The finned tube shell-and-tube heat exchanger The percentage that the finned tube shell-and-tube reduces than light pipe formula
The housing external diameter 800mm 600mm 25%
The heat exchanger tube radical 680 168 75%
Heat exchanger tube weight 3868kg 2321kg 40%
The heat exchanger gross weight 8410kg 5040kg 40%
As can be seen from the table:
A) the finned tube shell-and-tube heat exchanger is saved space 25% than light pipe formula heat exchanger;
B) finned tube shell-and-tube heat exchanger heat exchanger tube quantity only is 1/4 of light pipe heat exchanger,
Reduced nearly 3/4;
C) the finned tube shell-and-tube heat exchanger is owing to the boring amount of the minimizing tube sheet of pipe has reduced
3/4, heat exchanger tube and tube sheet welding capacity have also reduced 3/4;
D) the finned tube shell-and-tube heat exchanger is owing to the minimizing of volume, at same equal pressure, same
Under the temperature conditions, the tube plate thickness attenuate, ring flange and miscellaneous part are corresponding to be subtracted
Gently, it is nearly 40% that the equipment overall weight of making has descended, the steel of unit heat exchange area
The material consumption has reduced more than 40%.
Because the minimizing of heat exchanger tube, under the condition of same traffic, its high-temperature stream side (being generally high-temperature medium in the pipe) longitudinal finned tube flow velocity can improve nearly four times, improve flow regime widely, improved heat transfer efficiency, opposite, the shell fluid area increases, the pressure that has reduced big discharge capacity one side falls, and can reduce resistance dissipative greatly, energy-conservation 50-80%.
(2) comparison under traditional light pipe shell-and-tube heat exchanger and the high-efficiency fin pipe shell-and-tube heat exchanger volume same case: be 600mm equally with the diameter, the heat exchanger that length is identical is an example, its major parameter such as following table:
Item argument Tradition light pipe formula heat exchanger The finned tube shell-and-tube heat exchanger The finned tube shell-and-tube is the percentage of light pipe formula
The heat exchanger tube radical 360 168 -54%
Heat exchange area 140 square metres 260 square metres +85%
Heat exchanger tube weight 2046kg 2321kg +13%
The tube side circulation area 318 square centimeters 148 square centimeters -53%
Gross weight of equipment 4640kg 5040kg +8%
Annotate: two kinds of heat exchanger heat-exchanging tubes are arranged and are taked maximum stringing amount to carry out stringing with reference to GB.
To sum up table is as can be seen:
Under the equal volume situation, the heat exchanger tube quantity of high-efficiency fin tubular type heat exchange of heat pipe is lower by 54% than the quantity of light pipe formula heat exchanger, has saved a large amount of heat exchange tube materials, helps the reduction of cost; The tube side circulation area is still low by 53% than light pipe heat exchanger, and under the situation of same traffic, its high temperature fluid flow velocity can improve more than the twice, has improved mixed heat transfer boundary condition, has improved heat exchange efficiency.
High-efficiency fin pipe heat exchanger area has increased by 85% than light pipe formula heat exchanger, its heat exchanger tube weight has only increased by 13%, and (actual heat exchanger tube is to reduce, the just fin weight that increases), gross weight of equipment has only increased by 8%, its unit heat exchange area steel consumption only is 19kg/ square metre, and light pipe heat exchanger steel consumption is 33kg/ square metre, is equivalent to the nearly twice of finned tube exchanger.
In sum, high-efficiency fin type shell-and-tube heat exchange of heat pipe has following advantage:
1) floor space little, in light weight, be specially adapted to the narrow place of construction area.
2) unit heat exchange area steel quantity consumption is low, has reduced steel consumption, has saved valuable natural resources.
3) heat exchange area big (comparing under the equal volume condition), heat exchanger tube is few, has reduced a large amount of machining and welding job amount.
4) increase substantially the flow velocity of heat transferring medium, augmentation of heat transfer improves heat exchange efficiency.
5) profile is the same with the light pipe shell-and-tube heat exchanger, no matter be that new equipment starts, still old plant modification is all very convenient.
6) can be widely used in solution-air, the liquid of industries such as oil, chemical industry, building materials, food
In the heat-exchanger rig of-gas and high-viscous liquid.
Therefore, high-efficiency fin type shell-and-tube heat exchange of heat pipe is a kind of desirable renewal product.

Claims (3)

1, a kind of high-efficiency fin type shell-and-tube heat exchange of heat pipe: constitute by housing and heat exchanger tube core; It is characterized in that: its heat exchanger tube core: be made up of fin-type pipe (5) and tube sheet (3), dozens of fin-type pipe (5) is fixed on the tube sheet (3); Its fin-type pipe (5): form by fin (14) and heat exchanger tube (13);
2, high-efficiency fin type shell-and-tube heat exchange of heat pipe as claimed in claim 1, it is characterized in that: its housing: form by head (1) and body (6), its head (1): be that end sealing is semicircle, itself and body connection place are ring flange (10), there is dividing plate (12) that its inner chamber is divided into two chambeies up and down in it, be that high-temperature medium enters chamber C and high-temperature medium outlet plenum D, its high-temperature medium enters chamber C and is provided with high-temperature medium inlet tube interface (11); High-temperature medium outlet plenum D is provided with high-temperature medium outlet interface (2); Its body: be end sealing tubular, establish cryogenic media inlet or outlet duct interface (8), (4) on it, the heat exchanger tube core is housed in the body;
3, as claim 1 and 2 described high-efficiency fin type shell-and-tube heats exchange of heat pipe, it is characterized in that: its fin (14) is vertical straight fins or vertical straight ripple formula fin;
CN 98219185 1998-10-09 1998-10-09 High efficiency fin type shell-and-tube exchanger Expired - Fee Related CN2338712Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 98219185 CN2338712Y (en) 1998-10-09 1998-10-09 High efficiency fin type shell-and-tube exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 98219185 CN2338712Y (en) 1998-10-09 1998-10-09 High efficiency fin type shell-and-tube exchanger

Publications (1)

Publication Number Publication Date
CN2338712Y true CN2338712Y (en) 1999-09-15

Family

ID=33971342

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 98219185 Expired - Fee Related CN2338712Y (en) 1998-10-09 1998-10-09 High efficiency fin type shell-and-tube exchanger

Country Status (1)

Country Link
CN (1) CN2338712Y (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101270690B (en) * 2008-04-02 2010-06-09 北京航空航天大学 Fuel oil and lubricating oil heat exchanger of light aircraft engine
CN101957150A (en) * 2010-10-12 2011-01-26 岳阳市中达机电有限公司 High-efficiency oil cooler
CN102692147A (en) * 2012-05-23 2012-09-26 张家港市科华化工装备制造有限公司 Cooler
CN106679457A (en) * 2017-01-20 2017-05-17 广州立之力机械设备有限公司 Heat exchanger
CN110873481A (en) * 2018-08-31 2020-03-10 临沂市云旭新能源科技有限公司 Water source heat pump condenser

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101270690B (en) * 2008-04-02 2010-06-09 北京航空航天大学 Fuel oil and lubricating oil heat exchanger of light aircraft engine
CN101957150A (en) * 2010-10-12 2011-01-26 岳阳市中达机电有限公司 High-efficiency oil cooler
CN102692147A (en) * 2012-05-23 2012-09-26 张家港市科华化工装备制造有限公司 Cooler
CN106679457A (en) * 2017-01-20 2017-05-17 广州立之力机械设备有限公司 Heat exchanger
CN110873481A (en) * 2018-08-31 2020-03-10 临沂市云旭新能源科技有限公司 Water source heat pump condenser

Similar Documents

Publication Publication Date Title
CN101245971A (en) Enclosed cavity type heat exchanger
CN103063058A (en) Novel horizontal cooler
CN2338712Y (en) High efficiency fin type shell-and-tube exchanger
CN1140764C (en) Axial flow-type heat exchanger with convergent-divergent tube, full counterflow and dual shell passes and its heat-exchange method
CN2562864Y (en) Polymerization still
CN201488600U (en) Finned tube heat exchanger
CN101726195A (en) Stainless steel finned tube heat exchanger for residual heat recovery
RU2386096C2 (en) Honeycomb heat exchanger with flow swirling
CN201225853Y (en) Wide channel plate heat exchanger with detachable intensified element on one side
CN102410747B (en) Multi-level boost energy-saving heat exchanger
CN2212769Y (en) Reinforced transfer heat steam-water heat exchanger
CN109405590B (en) High-efficient heat exchanger of netted pipe layer of hexagon mesh screen
CN113218218A (en) Copper-aluminum composite material inner and outer finned tube heat exchanger
CN210426197U (en) Braided filler type superhigh temperature and superhigh pressure heat exchanger
CN210123213U (en) Novel micro-channel heat exchanger with single collecting pipe
CN112595148A (en) S-shaped tube bundle cross-flow type tube-shell heat exchanger based on foam metal
CN111336841A (en) Enclosed stack type micro-channel heat exchanger
CN101865623B (en) Helical flat pipe for waste heat boiler
CN215893343U (en) Combined double-shell-pass U-shaped tubular heat exchanger
CN2206440Y (en) Multifunctional heat exchanger
CN2484536Y (en) Fin corrugated-tube type heat exchanger
CN202432893U (en) Single-expansion-tube preheater
CN2123055U (en) Corrugated helically coiled shell and tube exchanger
CN219869237U (en) High-efficiency shell-and-tube heat exchanger suitable for light hydrocarbon recovery process
CN218545382U (en) Finned tube heat exchanger suitable for large-scale non-afterburning compressed air energy storage power station

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee