CN104930878A - Heat exchanger and heat energy recovery device - Google Patents

Heat exchanger and heat energy recovery device Download PDF

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Publication number
CN104930878A
CN104930878A CN201510259218.3A CN201510259218A CN104930878A CN 104930878 A CN104930878 A CN 104930878A CN 201510259218 A CN201510259218 A CN 201510259218A CN 104930878 A CN104930878 A CN 104930878A
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CN
China
Prior art keywords
heat exchanger
pipe
cross over
interior pipe
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.)
Pending
Application number
CN201510259218.3A
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Chinese (zh)
Inventor
陈明华
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.)
Suzhou Jin Ke Plastic Cement Science And Technology Ltd
Original Assignee
Suzhou Jin Ke Plastic Cement Science And Technology Ltd
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 Suzhou Jin Ke Plastic Cement Science And Technology Ltd filed Critical Suzhou Jin Ke Plastic Cement Science And Technology Ltd
Priority to CN201510259218.3A priority Critical patent/CN104930878A/en
Publication of CN104930878A publication Critical patent/CN104930878A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a heat exchanger which characterized in that the heat exchanger comprises an inner tube and an outer tube; the inner tube is placed in a space formed by the outer tube; the outer surface of the inner tube and an inner wall of the outer tube form a first flow channel; an inner wall of the inner tube forms a second flow channel; and the cross section of the inner tube is a centrosymmetric or axisymmetric graph.

Description

A kind of heat exchanger and heat-energy recovering apparatus
Technical field
The present invention relates to a kind of environmental protection and energy saving technical field, particularly relate to a kind of heat exchanger heat energy in waste gas or waste liquid being carried out effectively reclaim.
Background technology
In existing process for machining and manufacturing, usually use heating or baking step, the useless flue gas of discharging in the process or waste water can take away the 20-50% of the heat that heater provides.Flue gas is the main path of general energy consumption equipment waste energy, and such as boiler exhaust gas power consumption is large about 15%, and the main power consumption such as the forming machine of other equipment such as dyeing, dryer and kiln is all pass through fume emission.Therefore plurality of devices is all provided with the heat exchanger heat energy in waste gas and waste liquid being carried out to effectively recovery.
The heat exchanger used in prior art uses two kinds of technical schemes usually, and one is directly reclaim waste water or useless flue gas, as technical scheme disclosed in patent CN200820091816.X; Two is the heat energy utilizing refrigerant to absorb waste water or useless flue gas.Problem existing in prior art is to realize heat exchange efficiency, and promote heat exchange area, its heat reclamation device structure is all very complicated.Baroque consequence causes the efficiency of heat exchange can decline along with the use of heat exchanger.This is because impurity, dust or dirt in waste water or waste gas can be deposited in heat exchange area, cannot discharge; And the structure of complexity to cause this heat exchanger to be difficult to cleaned.Therefore usual in prior art it is considered that how to improve heat exchange area, the change but ignoring heat exchange area causes greatly impurity dust or dirt more easily to stay heat exchange zone field surface, causes heat exchanger effectiveness in actual use procedure to decline.
In view of this, need badly in prior art and want a kind of new heat exchanger, the function reducing manufacturing cost process complexity and easily cleaning can be realized simultaneously.
Summary of the invention
In order to overcome the defect existed in prior art, the invention provides a kind of heat exchanger heat energy in waste gas or waste liquid being carried out effectively reclaim.
In order to realize foregoing invention object, the present invention discloses a kind of heat exchanger, it is characterized in that, comprise: pipe and an outer tube in one, this interior pipe is positioned in the space that outer tube formed, the outer surface of this interior pipe and the inwall of outer tube form a first flow, and the inwall of this interior pipe forms one second runner, and the cross section of this interior pipe is a Central Symmetry or zhou duicheng tuxing.
Further, this first flow is used for flowing through clean gas or liquid; Second runner is used for flowing through waste gas or waste liquid.
Further, this outer tube is made up of calcium silicates or fibre cement or quartz sand or plastics or metal, and this interior pipe is made of metal.
Further, this heat exchanger also comprises at least one cross over pipe, and this cross over pipe is made up of at least three ports, and the first end of this cross over pipe is connected with one end of this outer tube.
Further, this heat exchanger also comprises at least one isolated tube, and this isolated tube is between this interior pipe and this cross over pipe, and this isolated tube is connected with the second end of this cross over pipe.
Further, this interior pipe is formed by aluminium alloy extrusions or silver type material or copper profile extrusion.
The present invention discloses a kind of heat-energy recovering apparatus simultaneously, comprise: at least one heat exchanger, pipe and an outer tube in this heat exchanger one, this interior pipe is positioned in the space that outer tube formed, the outer surface of this interior pipe and the inwall of outer tube form a first flow, and the inwall of this interior pipe forms one second runner; At least one cross over pipe, this cross over pipe is used for being connected with this heat exchanger, and this cross over pipe comprises at least two ports, and the opening direction of the first port of this cross over pipe is vertical with the opening direction of this second port.
Further, this cross over pipe also comprises one the 3rd port, and the opening direction of the 3rd port is contrary with the opening direction of this first port, and vertical with the opening direction of this second port.
Further, this heat-energy recovering apparatus also comprises an isolated tube, and this isolated tube is between the outer surface and the inwall of this cross over pipe of this interior pipe.
Further, this interior pipe cross section is a Central Symmetry or zhou duicheng tuxing; This first flow is used for flowing through clean gas or liquid; Second runner is used for flowing through waste gas or waste liquid.
Compared with prior art, the invention has the advantages that: without any contact point between two runners of the first, this heat exchanger, clean gas/liquid can not be caused by waste gas/waste liquor contamination.The second, its structure is simple, is made up of, can realizes arbitrary shape and be applicable to any environment basic module.Three, manufacturing process simply, therefore manufacturing cost decline more remarkable in prior art.Four, easy cleaning, will cause heat exchanger effectiveness to decline because of long-term accumulation dirt.
Accompanying drawing explanation
Can be further understood by following detailed Description Of The Invention and institute's accompanying drawings about the advantages and spirit of the present invention.
Fig. 1 is the structural representation of heat exchanger involved in the present invention;
Fig. 2 is the AA sectional view of heat exchanger involved in the present invention;
Fig. 3 is the sectional view of the second embodiment of heat exchanger involved in the present invention;
Fig. 4 is the stereogram of the 3rd embodiment of heat exchanger involved in the present invention;
Fig. 5 is the explosive view of heat exchanger involved in the present invention;
Fig. 6 is the mounting means schematic diagram of heat exchanger involved in the present invention;
Fig. 7 is a kind of working state schematic representation of heat exchanger involved in the present invention.
Detailed description of the invention
The heat exchanger of a kind of specific embodiment of the present invention is described in detail below in conjunction with accompanying drawing.But, the present invention should be understood as and be not limited to this embodiment described below, and technical concept of the present invention can combine with other known technologies or function other technologies identical with those known technologies and implements.
In the following description, in order to clear displaying structure of the present invention and working method, to be described by many Directional words, but by the Word Understanding such as "front", "rear", "left", "right", " outward ", " interior ", " outwards ", " inwardly ", " axis ", " radial direction " for convenience of term, and word of limitation should do not should be understood to.Wherein " interior " should be understood to the direction near axis, accordingly, should be understood to the direction away from axis outward.
The object of the present invention is to provide and to be a kind ofly made up of basic module, can arbitrary shape be realized and be applicable to the heat exchanger of any environment.This heat exchanger can also effectively overcome in prior art the technical barrier being difficult to clean.
Fig. 1 is the structural representation of heat exchanger involved in the present invention.As shown in Figure 1, this heat exchanger is a two-tube tubing heat exchanger.This heat exchanger comprises outer tube 10 and interior pipe 20.Wherein interior pipe 20 is concentrically inserted in the inwall of outer tube 10.Fig. 2 is the AA sectional view of heat exchanger involved in the present invention.Form a runner between interior pipe 20 and outer tube 10, interior pipe 20 itself is by being another runner 40.Two runners are isolated from one another by interior pipe 20, only realize heat exchange, and do not come in contact.
Interior pipe 2 and outer tube 10 constitute a heat exchanger, and the head and the tail two ends of this heat exchanger respectively connect a cross over pipe 50.As shown in Figure 4, cross over pipe 50 is preferably a kind of three-way pipe.Three ends all can be connected with heat exchanger, thus this two-tube tubing heat exchanger can become three-dimensional structure from the straight line of plane, is satisfied with arbitrary field of employment.
As shown in Figure 5, a of cross over pipe 50 end coordinates with the outer surface of the outer tube of heat exchanger, fit system can be threaded, thermal welding, the connection such as fluid sealant.The inner tube length of this heat exchanger is slightly longer than outer tube, and therefore, pipe 20 has extended to the c end of cross over pipe, and the runner therefore between pipe 20 and outer tube 10 becomes the runner between interior pipe 20 and cross over pipe.An isolated tube 30 is had between the c of interior pipe 20 and cross over pipe holds.The inner surface of isolated tube 30 is close to the outer surface of interior pipe, and the outer surface of isolated tube 30 is close to the inner surface of the c end of cross over pipe, and therefore clean air or liquid can only flow to b end from a end of cross over pipe, and can not hold to c.By the mutual linking of several cross over pipes and heat exchanger, the heat reclamation device of arbitrary shape can be realized.
Symmetric figure or zhou duicheng tuxing centered by the cross section of interior pipe 20.Fig. 2 is wherein a kind of embodiment, and under this embodiment, pipe 20 is made up of the projection of some center radiation shapes, and the sectional view of interior pipe 20 can be considered as a N limit shape.Fig. 3 is another kind of embodiment.It will be appreciated by those skilled in the art that the span of N can be selected according to actual needs, when the numerical value of N is larger, the area of heat exchange is also larger.Heat exchanger provided by the present invention, clean air or liquid flow through from the runner between interior pipe and outer tube, and carry the waste gas of a large amount of heat energy or waste water flows through from the runner that interior pipe 20 inwall is formed.By interior pipe is designed to centrosymmetric image or zhou duicheng tuxing, inner pipe wall easy cleaning can be made.Arbitrary section due to inwall is all shape about the same, therefore any one limit of interior pipe is all almost parallel with axis, therefore can stretch in interior pipe with the scrub-brush of common common long handle, rotate or move up and down hairbrush and by frictional force, dirt can be removed.
Fig. 4 is the 3rd embodiment of heat exchanger provided by the present invention.Compared with the one the second embodiments, the cross section of the interior pipe in the 3rd embodiment is similarly a centrosymmetric image or zhou duicheng tuxing, but its jut rotates by certain angle, forms a helical form figure.
Interior pipe 20 is made up of aluminium, copper, silver-colored contour thermal conductive metallic material, is preferably extruded aluminium alloy extrusions, and like this, the tube wall of pipe can be accomplished very thin, and processing technology is relatively simple.Outer tube 10 can be made up of the material that the thermal conductivity factors such as calcium silicates, fibre cement, quartz sand, plastic raw materials are low.Those skilled in the art also can by outer tube 10 metal material manufacture, outer surface covering and heat insulating layer.Same, isolated tube 30 is also made up of the material that heat conduction is low.
Fig. 6 is a kind of working state schematic representation of heat exchanger involved in the present invention.As shown in Figure 6, this heat exchanger has been used on Hopper Dryer.Hopper Dryer utilizes metallic resistance silk to add hot-air, and utilizes a blower fan that hot-air is blown into Hopper Dryer inside by airduct, thus realizes the drying of material.This Hopper Dryer comprises blower fan 1 and an air outlet 2.Blower fan 1 is inner by the air heat after-blow material bin of fresh drying, and air outlet 2 discharges the waste gas with a large amount of heat energy and steam.Waste gas and fresh air realize heat exchange after this heat exchanger, and the heat energy in waste gas is conducted to after in fresh air and is discharged.Except Hopper Dryer, heat exchanger provided by the present invention can also be applicable in the plurality of devices such as smelting stove, hot water apparatus, aircondition, oil cooler.
Compared with prior art, the invention has the advantages that: without any contact point between two runners of the first, this heat exchanger, clean gas/liquid can not be caused by waste gas/waste liquor contamination.The second, its structure is simple, is made up of, can realizes arbitrary shape and be applicable to any environment basic module.Three, manufacturing process simply, therefore manufacturing cost decline more remarkable in prior art.Four, easy cleaning, will cause heat exchanger effectiveness to decline because of long-term accumulation dirt.
Just preferred embodiment of the present invention described in this description, above embodiment is only in order to illustrate technical scheme of the present invention but not limitation of the present invention.All those skilled in the art, all should be within the scope of the present invention under this invention's idea by the available technical scheme of logical analysis, reasoning, or a limited experiment.

Claims (10)

1. a heat exchanger, it is characterized in that, comprise: pipe and an outer tube in one, described interior pipe is positioned in the space that outer tube formed, the described outer surface of interior pipe and the inwall of outer tube form a first flow, the inwall of described interior pipe forms one second runner, and the cross section of described interior pipe is a Central Symmetry or zhou duicheng tuxing.
2. heat exchanger as claimed in claim 1, it is characterized in that, described first flow is used for flowing through clean gas or liquid; Second runner is used for flowing through waste gas or waste liquid.
3. heat exchanger as claimed in claim 1, is characterized in that, described outer tube is made up of calcium silicates or fibre cement or quartz sand or plastics or metal, and described interior pipe is made of metal.
4. heat exchanger as claimed in claim 1, it is characterized in that, described heat exchanger also comprises at least one cross over pipe, and described cross over pipe is made up of at least three ports, and the first end of described cross over pipe is connected with one end of described outer tube.
5. heat exchanger as claimed in claim 4, it is characterized in that, described heat exchanger also comprises at least one isolated tube, and described isolated tube is between described interior pipe and described cross over pipe, and described isolated tube is connected with the second end of described cross over pipe.
6. heat exchanger as claimed in claim 3, is characterized in that, described interior pipe is formed by aluminium alloy extrusions or silver type material or copper profile extrusion.
7. a heat-energy recovering apparatus, is characterized in that, comprising:
At least one heat exchanger, pipe and an outer tube in described heat exchanger one, described interior pipe is positioned in the space that outer tube formed, and the described outer surface of interior pipe and the inwall of outer tube form a first flow, inwall formation one second runner of described interior pipe;
At least one cross over pipe, described cross over pipe is used for being connected with described heat exchanger, and described cross over pipe comprises at least two ports, and the opening direction of the first port of described cross over pipe is vertical with the opening direction of described second port.
8. heat-energy recovering apparatus as claimed in claim 7, it is characterized in that, described cross over pipe also comprises one the 3rd port, and the opening direction of described 3rd port is contrary with the opening direction of described first port, and vertical with the opening direction of described second port.
9. heat-energy recovering apparatus as claimed in claim 8, it is characterized in that, described heat-energy recovering apparatus also comprises an isolated tube, and described isolated tube is between the outer surface and the inwall of described cross over pipe of described interior pipe.
10. heat-energy recovering apparatus as claimed in claim 7, it is characterized in that, described interior pipe cross section is a Central Symmetry or zhou duicheng tuxing; Described first flow is used for flowing through clean gas or liquid; Second runner is used for flowing through waste gas or waste liquid.
CN201510259218.3A 2015-05-20 2015-05-20 Heat exchanger and heat energy recovery device Pending CN104930878A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510259218.3A CN104930878A (en) 2015-05-20 2015-05-20 Heat exchanger and heat energy recovery device

Publications (1)

Publication Number Publication Date
CN104930878A true CN104930878A (en) 2015-09-23

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020507740A (en) * 2017-02-09 2020-03-12 スアル.ツェーゼット エス.エル.オー. Annular heat exchanger
CN114199040A (en) * 2021-11-17 2022-03-18 卢霞丽 Condenser for industrial heat exchange

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000265908A (en) * 1999-03-12 2000-09-26 Toyota Autom Loom Works Ltd Egr gas cooling device
CN2798016Y (en) * 2005-07-01 2006-07-19 舒增鳌 Coaxial type sleeve heat-exchanger
JP2010014312A (en) * 2008-07-02 2010-01-21 Hitachi Cable Ltd Double tube type supercooler
CN101776405A (en) * 2010-02-01 2010-07-14 上海醇华电子有限公司 Double-pipe heat exchanger
CN102853711A (en) * 2012-08-17 2013-01-02 贝恩医疗设备(广州)有限公司 Heat exchange joint and heat exchange device
CN204678929U (en) * 2015-05-20 2015-09-30 苏州锦珂塑胶科技有限公司 A kind of heat exchanger and heat-energy recovering apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000265908A (en) * 1999-03-12 2000-09-26 Toyota Autom Loom Works Ltd Egr gas cooling device
CN2798016Y (en) * 2005-07-01 2006-07-19 舒增鳌 Coaxial type sleeve heat-exchanger
JP2010014312A (en) * 2008-07-02 2010-01-21 Hitachi Cable Ltd Double tube type supercooler
CN101776405A (en) * 2010-02-01 2010-07-14 上海醇华电子有限公司 Double-pipe heat exchanger
CN102853711A (en) * 2012-08-17 2013-01-02 贝恩医疗设备(广州)有限公司 Heat exchange joint and heat exchange device
CN204678929U (en) * 2015-05-20 2015-09-30 苏州锦珂塑胶科技有限公司 A kind of heat exchanger and heat-energy recovering apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020507740A (en) * 2017-02-09 2020-03-12 スアル.ツェーゼット エス.エル.オー. Annular heat exchanger
CN114199040A (en) * 2021-11-17 2022-03-18 卢霞丽 Condenser for industrial heat exchange

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Application publication date: 20150923

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