CN206274230U - A kind of superconduction fluidised form heat exchanger - Google Patents
A kind of superconduction fluidised form heat exchanger Download PDFInfo
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- CN206274230U CN206274230U CN201621395810.2U CN201621395810U CN206274230U CN 206274230 U CN206274230 U CN 206274230U CN 201621395810 U CN201621395810 U CN 201621395810U CN 206274230 U CN206274230 U CN 206274230U
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Abstract
The utility model discloses a kind of superconduction fluidised form heat exchanger; it belongs to field of heat exchange; including framework; the framework is divided into upper and lower two-layer, and the upper strata is set to water body side frame, and the side will be arranged on flue outside; the lower floor is set to flue gas body side frame; the side is arranged on inside flue, is provided between the water body side frame and flue gas body side frame into water header, is provided with protective cover around the water inlet header and is connected with framework;In the framework several columns light pipe is provided with perpendicular to water inlet header, the light pipe is that the pipe of closing is not connected with water inlet header, heat-exchange working medium is provided with light pipe, the heat-exchange working medium is preferably acetone or methyl alcohol, outer tube is cased with outside light pipe in the water body side frame, there is water in space between the light pipe and outer tube and connected with the water inlet header, the water body side frame top is provided with water outlet header, and the water outlet header and the space between light pipe and outer tube connect.
Description
Technical field
The utility model is related to field of heat exchange, and in particular to a kind of superconduction fluidised form heat exchanger.
Background technology
The average thermal efficiency of industry coal-boiler only has 67%, 25% heat energy by fume emission to air in the middle of, row
Cigarette temperature is up to more than 200 DEG C, both pollutes environment, and the fume afterheat resource of preciousness is wasted again.Therefore many large-sized boilers
The shell-tube type economizer of cast iron or stainless steel is mounted on, is fed water for Mist heat recovering preboiler.
But because the sulfur content of coal is higher, oxysulfide would generally be produced during burning, i.e. shape after being combined with vapor
Into sulfuric acid vapor.When the set point (referred to as acid dew point) of the metal pipe-wall temperature less than sulfuric acid vapor of economizer, will be in its table
Face forms liquid sulfuric acid (referred to as condensing).
For a long time, the corrosion that traditional shell-tube type economizer is caused due to condensation, or even perforated phenomenon occurs often, sternly
Ghost image rings the operation safety of boiler, so current boiler is all to alleviate condensation and corrosion phenomenon by improving exhaust gas temperature
Produce, flue-gas temperature remains high.In addition the bulky of this kind of economizer, flue gas resistance are big, easy dust stratification, stifled ash, heat exchange
Efficiency is reduced year by year, and service life is short, often wants deashing, therefore medium small boiler to be rarely employed, when large-sized boiler uses one section
Between after, it is basic without high-temperature flue gas of leaving take away heat, waste the energy because fouling is serious.Under boiler smoke temperature is every
15~18 DEG C of drop can improve boiler efficiency 1%, therefore reduction boiler smoke temperature has turned into an important way of boiler energy-saving
Footpath, while must solve the problem of heat exchanger tube low-temperature corrosion again, then heat pipe type of coal saver is just applied and given birth to.
Radial heat pipe being used existing heat pipe type of coal saver, its structure type is more:Many radial heat pipe elements lie in a horizontal plane in
In the flue be made up of economizer housing, each branch heat-pipe elements structure in same level (or vertical) face is in a row;In heat pipe
Housing is stretched out at pipe two ends, adjacent row or is separated by corresponding heat pipe inner tube in a row and is concatenated by seamless elbow and be integrated;First, last two
Heat exhausting pipe has one end not concatenated with elbow, but is connected in parallel by header is integrated respectively.The vertical radial heat pipe of flue gas is from cigarette
Road flows through, and water flows into header side, and uniformly flows into first row (or the end row) heat pipe being connected with the header, then flows successively through each
Heat exhausting pipe, finally flows out from opposite side.Flue gas and heat pipe outer tube and fin contacts, it is completely separated with heat pipe inner tube;Heat pipe inner tube
Weld seam between two ends and seamless elbow is also completely outside flue.
Said structure has following drawback:1. header specification is larger, generally Φ 800, for manufacture installation brings difficulty;
2. after fume side leakage, whole pipe must all be changed, and cause maintenance cost to increase, and maintenance difficulty is big.For the design of above-mentioned drawback
A kind of superconduction fluidised form heat exchanger, and in the market without such device.
The content of the invention
For the problems of in the prior art, the utility model provides a kind of superconduction fluidised form heat exchanger, by changing
Water side and fume side tube construction, improve heat exchange efficiency, reduce production and install and operating cost.
To achieve these goals, the technical solution adopted in the utility model is as follows:A kind of superconduction fluidised form heat exchanger, including
Framework, the framework is divided into upper and lower two-layer, and the upper strata is set to water body side frame, and the lower floor is set to flue gas body side frame, the water
It is provided between body side frame and flue gas body side frame into water header, is provided with protective cover around the water inlet header and is connected with framework;
Several columns light pipe is provided with perpendicular to water inlet header in the framework, heat-exchange working medium, the water are provided with the light pipe
Outer tube is cased with outside light pipe in body side frame, is had water in the space between the light pipe and outer tube and is connected with the water inlet header,
The water body side frame top is provided with water outlet header, and the water outlet header and the space between light pipe and outer tube connect.
Used as preferred technical scheme, the light pipe in the flue gas body side frame is provided with fin.
Used as preferred technical scheme, light pipe and fin in the flue gas body side frame have enamel.
Used as preferred technical scheme, the light pipe uses the pipe of Φ 42*3, the outer tube to use the pipe of Φ 89*6.
Used as preferred technical scheme, the framework is provided with the hanger for conveniently removing and installing.
The utility model is beneficial in that:
1. traditional water inlet header is changed to common header, be reduced in size, reduce production and installation difficulty.
2. after the light pipe leakage of fume side, the light pipe of fume side need to be only changed, reduce operation and maintenance cost.
3. heat exchange efficiency is improved after the heat exchanger internal structure changes, and can realize that module is given birth to according to heat exchange efficiency
Produce, reduce cost.
4. the light pipe of fume side and fin enamel are processed, and can also improve its service life.
Brief description of the drawings
Fig. 1 is a kind of overall structure figure of superconduction fluidised form heat exchanger;
Fig. 2 is a kind of top view of superconduction fluidised form heat exchanger;
Fig. 3 is a kind of broken section enlarged drawing of superconduction fluidised form heat exchanger.
In figure:1- frameworks, 2- flue gases body side frame, 3- water inlets header, 4- water body side frame, 5- water outlets header, 6- outer tubes, 7- are protected
Shield, 8- light pipes.
Specific embodiment
For the ease of it will be appreciated by those skilled in the art that being further described to the utility model below in conjunction with the accompanying drawings.
As shown in Figure 1-Figure 3, a kind of superconduction fluidised form heat exchanger, including framework 1, the framework 1 is provided with convenient dismounting peace
The hanger of dress, framework 1 is used for supporting the heat exchanger tube of inside, and 1 point of the framework is upper and lower two-layer, and the upper strata is set to water side frame
Frame 4, the side will be arranged on flue outside, and the lower floor is set to flue gas body side frame 2, and the side is arranged on inside flue, the water side
It is provided between framework 4 and flue gas body side frame 2 into water header 3, is provided with protective cover 7 around the water inlet header 3 and connects with framework 1
Connect;
Several columns light pipe 8 is provided with perpendicular to water inlet header 3 in the framework 1, the light pipe 8 uses the pipe of Φ 42*3,
The light pipe 8 is not connected for the pipe of closing with water inlet header 3, and heat-exchange working medium is provided with light pipe 8, and the heat-exchange working medium is preferably
Acetone or methyl alcohol, are cased with outer tube 6 outside the light pipe 8 in the water body side frame 4, the outer tube 6 uses the pipe of Φ 89*6, institute
Stating has water and is connected with the water inlet header 3 in the space between light pipe 8 and outer tube 6, the top of the water body side frame 4 is provided with water outlet
Header 5, the water outlet header 5 and the space between light pipe 8 and outer tube 6 connect.
Light pipe 8 in the flue gas body side frame 2 is provided with fin, and the light pipe 8 and fin in the flue gas body side frame 2 have
Enamel, can improve its service life.
It is specific to install and heat transfer process:
During installation, the flue gas body side frame 2 of water inlet header 3 bottom is arranged on inside flue, and the upper water side frame of header 3 of intaking
Frame 4 is arranged on flue outside.During work, high-temperature flue gas shift to light by flue gas body side frame 2, the heat-exchange working medium evaporation in light pipe 8
In the light pipe 8 that the top of pipe 8 enters in water body side frame 4, have due to being flowed in the space in water body side frame 4 between light pipe 8 and outer tube 6
Cooling water, therefore the condensation of the heat-exchange working medium in light pipe 8 can be back flowed back into the light pipe 8 of flue gas body side frame 2, and reciprocation cycle is changed
Heat.
It should be appreciated that the purposes of these embodiments is merely to illustrate the utility model and is not intended to limit of the present utility model
Protection domain.Additionally, it will also be appreciated that after technology contents of the present utility model have been read, those skilled in the art can be right
The utility model makes various changes, modification and/or modification, and all these equivalent form of value equally falls within right appended by the application will
Ask within the protection domain that book limited.
Claims (5)
1. a kind of superconduction fluidised form heat exchanger, including framework, it is characterised in that:The framework is divided into upper and lower two-layer, and the upper strata sets
It is water body side frame, the lower floor is set to flue gas body side frame, is provided between the water body side frame and flue gas body side frame into water header, institute
State and protective cover is provided with into around water header and is connected with framework;
Several columns light pipe is provided with perpendicular to water inlet header in the framework, heat-exchange working medium, the water side frame are provided with the light pipe
Outer tube is cased with outside light pipe in frame, is had water in the space between the light pipe and outer tube and is connected with the water inlet header, it is described
Water body side frame top is provided with water outlet header, and the water outlet header and the space between light pipe and outer tube connect.
2. a kind of superconduction fluidised form heat exchanger according to claim 1, it is characterised in that:Light pipe in the flue gas body side frame
It is provided with fin.
3. a kind of superconduction fluidised form heat exchanger according to claim 2, it is characterised in that:Light pipe in the flue gas body side frame
Has enamel with fin.
4. a kind of superconduction fluidised form heat exchanger according to claim 1, it is characterised in that:The light pipe uses the pipe of Φ 42*3
Son, the outer tube uses the pipe of Φ 89*6.
5. a kind of superconduction fluidised form heat exchanger according to claim 1, it is characterised in that:The framework is provided with convenient dismounting
The hanger of installation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621395810.2U CN206274230U (en) | 2016-12-19 | 2016-12-19 | A kind of superconduction fluidised form heat exchanger |
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CN201621395810.2U CN206274230U (en) | 2016-12-19 | 2016-12-19 | A kind of superconduction fluidised form heat exchanger |
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CN206274230U true CN206274230U (en) | 2017-06-23 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110567301A (en) * | 2019-08-23 | 2019-12-13 | 深圳市嘉名科技有限公司 | Heat dissipation plate and manufacturing method thereof |
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2016
- 2016-12-19 CN CN201621395810.2U patent/CN206274230U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110567301A (en) * | 2019-08-23 | 2019-12-13 | 深圳市嘉名科技有限公司 | Heat dissipation plate and manufacturing method thereof |
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