GB2476154A - Tubular heat exchanger for a motor vehicle air conditioner - Google Patents
Tubular heat exchanger for a motor vehicle air conditioner Download PDFInfo
- Publication number
- GB2476154A GB2476154A GB1020563A GB201020563A GB2476154A GB 2476154 A GB2476154 A GB 2476154A GB 1020563 A GB1020563 A GB 1020563A GB 201020563 A GB201020563 A GB 201020563A GB 2476154 A GB2476154 A GB 2476154A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stampings
- heat exchanger
- tube
- inner tube
- exchanger according
- 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.)
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Links
- 239000003507 refrigerant Substances 0.000 claims abstract description 38
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 229910003460 diamond Inorganic materials 0.000 claims abstract description 3
- 239000010432 diamond Substances 0.000 claims abstract description 3
- 241000826860 Trapezium Species 0.000 claims abstract 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 239000012530 fluid Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 description 3
- 240000006829 Ficus sundaica Species 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
- F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
- F28F1/424—Means comprising outside portions integral with inside portions
- F28F1/426—Means comprising outside portions integral with inside portions the outside portions and the inside portions forming parts of complementary shape, e.g. concave and convex
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/008—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
- F28D2021/0085—Evaporators
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Air-Conditioning For Vehicles (AREA)
Abstract
A tubular heat exchanger for a motor vehicle air conditioner comprises an internal tube 12 through which a fluid flows and an outer tube 14 radially enclosing the internal tube thereby forming a space therebetween and through which a fluid flows. The internal tube has a plurality of stampings 16 on its surface and are spaced from one another and extend part way along the length of the tube. The stampings may be substantially rectangular with their longitudinal axis extending at an angle of 0 degrees to plus or minus 45 degrees. The stampings are arranged around the circumference of the internal tube, may be spaced in the longitudinal direction by 15mm to 30mm, their depth may be between 1mm and 3mm, the sum of their area may between 10 and 60 percent. The stampings may widen in a circumferential direction (fig 7), may be curved (fig 8) and may be, triangular, diamond (fig 9) trapezium or circular shaped. A gaseous refrigerant from an evaporator flows through the internal tube and a liquid refrigerant from the condenser flows through the space between the internal and outer tube.
Description
Tubular heat exchanger for motor vehicle air conditioners
Description
The present invention relates to a tubular heat exchanger for a motor vehicle air conditioner and in particular a double-walled heat exchanger tube with an inner tube through which a fluid or a gas can flow and an outer tube, which radially encloses the inner tube subject to the forming of an intermediate space through which a flow can flow.
Double-walled heat exchanger tubes for motor vehicle air conditioners are thoroughly known. Thus, DE 10 2005 052 972 Al for example describes a double-walled tube with an outer tube and an inner tube inserted in the outer tube, wherein the inner tube is provided with several rectilinear or helically twisted grooves continuously running in longitudinal direction. Such grooves enlarge the cross-sectional area of a channel running between inner and outer tube so that the flow resistance of the refrigerant flowing in that outer * channel and typically subjected to high pressure can be reduced. * 30
* 3y reducing the flow resistance the flow rate of :. the high-pressure refrigerant flowing through the channel :::; can be increased, so that a heat transfer from the high-temperature refrigerant, that is the refrigerant subjected to high pressure to the low-temperature refrigerant flowing in the inner tube, that is the low-pressure refrigerant, can be improved.
The known continuous grooves running rectilinearly or helically however are accompanied by a comparatively high pressure loss, which is disadvantageous to the overall performance of the air conditioning system.
In the case of applications in the field of a
motor vehicle air conditioner it is a disadvantage that the tube diameter as well as the tube length are limited IS within predetermined ranges because of prevailing installation space requirements. Consequently it proves particularly difficult, especially with an already existing vehicle package, to realize a demanded degree of heat exchange with predetermined tube diameter and predetermined tube length.
It is therefore the object of the present invention to make available a tubular, particularly a double-walled heat exchanger for a motor vehicle air conditioner, which with a predetermined tube outer S... geometry or with predetermined tube length and predetermined tube diameters makes possible an p individually adaptable heat exchange between its flow channels. Preferably, the tubular heat exchanger according to the invention is to be producible without *SS S . additional expenditure worth mentioning and adaptable to existing geometrical requirements. Preferably, the heat exchanger should also be characterized by a lower pressure loss.
According to the invention, this object is solved through a heat exchanger according to Patent Claim 1 and by means of a motor vehicle air conditioner according to Patent Claim 13 and with a motor vehicle according to Patent Claim 14. Individual advantageous configurations of the invention are the subject of dependent patent claims.
The tubular heat exchanger according to the invention is designed for a motor vehicle air conditioner and comprises an inner tube through which a fluid or a gas and/or a fluid-gas mixture can flow. In addition, the coaxial heat exchanger comprises an outer tube, which radially encloses the inner tube subject to the formation of an intermediate space through which a flow can flow.
In the final assembly state of the heat exchanger in the refrigerant circuit of a vehicle air conditioner it is thereby more preferably provided that the inner tube fluidically interconnects an evaporator and a compressor of the air conditioner, while the channel formed between inner tube and outer tube makes available a fluidic connection between a condenser and an expansion device of the air conditioner. S...
By means of the coaxial heat exchanger a heat * * transfer of the high-pressure or high-temperature refrigerant flowing on the outside to the low-pressure or . .: low-temperature refrigerant flowing in the inner tube in the opposite direction can take place. Because of this, cooling down of the high-temperature, high-pressure *5 ** * S
S *5 * 6 * *
refrigerant can take place even before flowing through the expansion device connected downstream, with the help of which the refrigerant flowing to the evaporator is cooled down because of an isentropic or adiabatic expansion.
To specifically change, improve and/or manipulate the heat transfer between the refrigerant flowing in the outer channel and in the inner tube that can be achieved with the heat exchanger it is provided according to the invention that the inner tube comprises a quantity of stampings arranged spaced from one another and with their longitudinal extension, at least partially, extending in axial direction of the inner tube. With the help of these stanpings specific swirling of the respective refrigerant in both channels through which flow can flow of the coaxial heat exchanger tube can take place.
In this connection, a degree of swirling of the respective refrigerant flow that compared with the prior art can be specifically adjusted can be achieved through an arrangement of local starnpings in the inner tube which are spaced from one another. Depending on the orientation of the longitudinal extension of the stampings relative to the longitudinal axis of the inner or outer tube the degree of swirling of the respective refrigerant can be *. specifically changed and thus ultimately a demanded degree of heat transfer be achieved even without changing the tube diameter and the tube length.
I * . * * S.
According to an advantageous configuration of the invention the stampings of the inner tube are formed S. I. S * * S * S. I S I * *.
radially to the inside. The production of such starnpings turns out to be comparatively simple and can be produced in mass production by inserting a tube substantially running rectilinearly in a stamping tool provided for this purpose.
In this connection it is more preferably provided that the stampings protruding to the inside from the inner surface of the tube correspond to corresponding depressions provided on the outer surface of the tube. In this manner, both refrigerants flowing in the inner channel formed by the inner tube and in the outer channel formed by the inner and outer tube can be approximately swirled to the same degree.
According to a particularly advantageous further development of the invention it is additionally provided that the quantity, the size, the geometrical shape and the orientation of the stampings is matched for achieving a predetermined heat exchange between the preferentially gaseous refrigerant flowing in the inner tube and the liquid refrigerant preferentially flowing in opposite direction between inner and outer tube. In this connection, the heat capacity and additional physical state quantities such as for example a respective pressure and temperature of the refrigerant can be taken into account. Here, the invention is not restricted to the described constellation of the refrigerant flows.
Thus it cart also be provided that the gaseous refrigerant flows in the flow channel between inner and outer tube and the liquid refrigerant in the inner tube. * ** ** * S *
S S *, S * . a a.
Through specific changing of the quantity, the size, the geometrical shape and also the orientation of the stampings with respect to the main flow direction of the refrigerant the degree of the heat transfer between the two opposite refrigerant flows can also be variably adapted to the requirements of the respective refrigerant circuit and consequently optimized even with fixed predetermined tube length and fixed predetermined tube diameter. J0
According to a further development of the invention it is additionally provided that the quantity of the stampings which are arranged on an imaginary line running perpendicularly to the longitudinal axis of the t5 inner tube or intersect such an imaginary circumferential line, amounts to between 4 to 12, preferentially between 6 to 10. The extension of the stampings in tube circumferential direction in this case is to be more preferably selected smaller than the spacing of stampirigs in circumferential direction of the tube arranged adjacently. The spacing of adjacent stampings seen in circumferential direction amounts to at least 1.5 to 3 times the extension of the respective stampings in circumferential direction.
According to a further development of the invention it is additionally provided that stampings arranged adjacently to one another in axial direction have a spacing of at least 15 irim to 30 miTt. In that the stampings are not formed continuously but interrupted in axial direction, i.e. in tube longitudinal direction, altogether better swirling of the refrigerant than with a continuous groove can be achieved. Here, tests have shown S. *S * * * *. ) * * S S ** that a higher degree of heat transfer can be achieved within an axial spacing range of 15 mm to 30 mm.
According to a further advantageous configuration of the invention the depth of the stampings is between 1 mm and 3 mm, preferentially between 1.5 mm and 2.5 mm.
In this connection it is particularly provided that the depth of the stampings is a maximum of 15 % of the diameter of the inner tube. Such a limitation of the stamping depth on the one hand proves to be favorable in terms of manufacturing. On the other hand, this affects the stability of the tube only to a minor extent, at least only to a tolerable degree.
According to a further particularly advantageous configuration of the invention the sum of the areas of all stampings of the inner tube amounts to between 10 % and 60 %, preferentially between 20 % and 50 % of the outer surface area of the inner tube. Thus, tests have shown that the degree of the heat transfer is particularly influenced by the overall area of the stanipings, whereas in the stated interval of 10 to 60 % or 20 to 50 % the degree of the heat exchange that is optimal for the present application can be achieved. *S.S
According to a further advantageous configuration of the invention the stampings have a substantially rectangular geometry and extend with their longitudinal axis at an angle of 0° to +1-45°, preferentially of ÷1-10° to +1-35° relative to the longitudinal axis of the inner tube. With increasing S. * * S * . I. * * S S
S
inclination relative to the tube longitudinal axis of the starnpirigs of rectangular or oblong design a higher degree of swirling and thus an increased degree of heat exchange can typically be achieved between the flow channels. An inclination of 0° to +/-45° or of +1-10° to +/-35° proves to be advantageous for the intended operating purpose in the refrigerant circuit of a motor vehicle air conditioner.
With a further alternative or complementary configuration of the heat exchanger the stampings widen in circumferential direction seen in flow direction of the refrigerant. Thus the stampings can be designed for example divergently, triangularly or conically widening IS in axial direction of the tube. It is likewise conceivable that the stampings seen in circumferential direction of the tube widen contrary to the flow direction in the manner described before.
It is additionally conceivable that the stampings seen in flow direction follow a curved course.
They can for example be characterized by a substantially crescent-like geometry with a cross-sectional geometry that remains substantially the same but can also be variable, particularly with a divergent or convergent cross-sectional geometry. It is also conceivable that the stampings are substantially designed triangular, diamond, Lrapezium or substantially circular-shaped. * *
According to a further independent aspect the S. * : invention additionally relates to a motor vehicle air conditioner with a closed refrigerant circuit. The * * refrigerant circuit fluidically interconnects at least S. * S * *5 * S S* one compressor, one condenser, one expansion device, such as an expansion valve, and an evaporator of the air conditioner. In addition, the refrigerant circuit comprises a previously described heat exchanger according to the invention, wherein the inner tube of the coaxial heat exchanger fluidically interconnects the evaporator of the air conditioner with the compressor of the air conditioner and the outer tube of the coaxial heat exchanger the condenser and the expansion device of the air conditioner.
Depending on the design of the air conditioner and the coolant circuit, inverse coupling of inner tube and outer flow channel to the components evaporator and compressor and condenser and expansion device respectively is also possible in principle.
In addition, the invention relates to a motor vehicle which comprises the previously described air conditioner or a coaxial tube heat exchanger according to the invention.
Further objectives, features and advantageous application possibilities of the invention are represented in the following description of the various exemplary embodiments making reference to the drawings.
There, all features described in the text in isolation and also graphically depicted in the figures form the subject of the present invention both standing alone as well as in any conceivable practical combination thereof. * . * * * * **
It shows: * * *. ** * a * * * S. 5 * **
S
Fig. 1 a schematic cross-sectional representation through a coaxial tube heat exchanger according to the invention according to a first embodiment, Fig. 2 a representation of a second embodiment of the heat exchanger corresponding to Fig. 1, Fig. 3 an exemplary cross section of a heat exchanger in the sectional plane perpendicularly to the tube longitudinal axis, Fig. 4 a schematic lateral view of an inner tube with stampings arranged offset in circumferential direction and spaced from one another in axial direction, Fig. 5 a further schematic lateral view of an inner tube with stampings running obliquely relative to the tube longitudinal axis, Fig. 6 a configuration comparable to Fig. 4 however with an increased quantity of stampings, Fig. 7 a further inner tube with stampings widening in flow direction, *t.S Fig. 8 an exemplary embodiment with stampings following I..... . * . a curved course in flow direction and Fig. 9 an exemplary embodiment with stampings of diamond-shaped design and oriented variously relative to one another. * S
* * 10 ** I * I S * S. Fig. 1 to 3 shows a coaxial tube heat exchanger with an inner tube 12 and with an outer tube 14. While the outer tube 14 has a substantially continuous cylindrical shape, individual stampings 16 protruding to the inside are provided on the inner tube 12. The stampings 16 formed as depression in the outer surface of the inner tube 12 correspondingly thereto protrude from the inner surface of the inner tube 12.
The inner tube predominantly serves for a fluidic connection between an evaporator and a compressor of a motor vehicle air conditioner and thus connects the outlet of the evaporator with the suction side of the compressor. The outer tube 14 or the outer channel formed IS by the outer tube 14 and inner tube 12 is preferentially subjected to a through flow of a refrigerant subjected to high pressure flowing in a direction opposite to that of the vapor flowing in the inner tube 12.
Here, the high-temperature high-pressure refrigerant passes a defined heat quantity on to the vapor flowing in opposite direction in the inner tube 12.
In that the individual starnpings 16, 18 are formed spaced from one another in axial direction, i.e. in tube longitudinal direction, on the inner tube 12, an improved heat transfer can be made available compared with continuous grooves of continuous design in axial * * direction. * *
The stampings 16 schematically indicated in FIg.
1 are substantially rectangular in shape and with their longitudinal axis substantially extend parallel to the axial direction. In contrast with this, the stampirigs 18 ** 0* * * 0 * S 11 ** 0 * S * S 55 shown in Fig. 2 are inclined relative to the axial direction of the tube 20, but arranged parallel relative to one another. The angle assumed between the longitudinal direction of these stampings 18 and the tube axial direction preferentially amounts to 0° to +/_450, preferably +/1O° to +/-35°.
As is noticeable by means of the cross-sectional representation according to Fig. 3, a total of four stampings 16 for example seen in circumferential direction of an inner tube 20 are arranged along an imaginary circumferential line distributed over the circumference of the inner tube 12 at same, i.e. equidistant spacings.
In the configuration according to Fig. 4, substantially rectangular stampings 26, 28 but compared with the tube diameter each having a greater longitudinal extension compared with the configuration according to Fig. 1 and 2 are again provided. Here, too, the stampings 26 as well as the stampings 28 arranged spaced axially thereof are oriented parallel to one another and parallel to the tube longitudinal axis. The stampings 26 as well as the stampings 28 in this case are additionally arranged distributed over the circumference of the inner tube 22 at regular, equidistant spacings. *...
With respect to the Figures 4 to 9 it is S.....
* . additionally noted that the broken lines running in . : 30 circumferential direction merely represent a cut off or * interrupted tube.
S
S. S... * S * S. S * * 12 5 S * S * S.
The arrangement of the stampings 26 by groups and the arrangement of the stampings 28 in this case are turned in circumferential direction so that an imaginary axial extension of a stamping 26 comes to lie in the intermediate space free of stampings between two starnpings 28. Since the stamping density as well as the geometry of the individual stampings 26, 28 is substantially identical, this also applies the other way round. This means, an imaginary extension of a stamping 28 preferentially comes to lie in the middle between stampings 26 in circumferential direction arranged adjacent to one another.
The inner tube 32 according to Fig. 5 likewise Is comprises arrangements of stamoings 36, 38 preferentially distributed equidistantly over the circumference of the tube 32 likewise spaced from one another in axial direction. However, compared with the configuration according to Fig. 4, these are oriented slightly inclined relative to the longitudinal axis of the tube 32.
In the configuration according to Fig. 6, the inner tube 42 comprises stampings 36, 38 which in terms of geometry and orientation correspond to the stampings 36, 38 shown in Fig. 5. However, the individual stampings 36, 38 seen in circumferential direction are arranged at a clearly shorter distance from one another. As a whole, the inner tube 42 compared with the inner tube 32 has an increased quantity of stampings 36, 38. In addition, the * 30 axial spacing of the stampings 36, 38 shown in Fig. 6 is shorter than the axial spacing of the inner tube stampirigs 36, 38 shown in Fig. 5. * I. * * S
* * 13 ** * * * S * S. Fig. 7 schematically shows additional conceivable stamping geometries. The stampings 56 are for instance designed as isosceles triangles which seen in tube longitudinal direction have approximately 2 to 4 times a greater extension than in circumferential direction. The inner tube 52 additionally comprises stampings 513 which widen funnel-like or conically in certain regions, which likewise seen in tube longitudinal direction have a greater extension than in circumferential direction of the tube 52.
The starnpings 66, 68 additionally represented in Fig. 8 by means of an inner tube 62 are designed curved relative to the tube longitudinal direction at least in J5 certain regions, wherein the stampings 68 seen in stamping longitudinal direction have a substantially constant cross-sectional profile, while the stampings 66, seen in tube longitudinal direction, from the left to the right, have a cross-sectional profile which seen in circumferential direction of the tube 62, is growing larger. In addition, the stampings 66, 68 differ in terms of their mutual orientation. While stampings 68 lying adjacently to one another are curved in the same direction, stampirigs 66 arranged adjacent to one another in circumferential direction have curves facing away from one another. *S.. * * * *..
Fig. 9 finally shows a further inner tube 72 *****.
* with diamond-shaped stampings 76, 78 wherein the ** * 30 stampings 76 are each oriented parallel to one another, * * * * while the stampings 78 arranged adjacent to one another in circumferential direction are arranged turned relative ** I. * S * * * 14 ** * * S S * S. to one another or mirror-symmetrically to the axial direction of the tube.
The quantity, the geometrical configuration, the mutual arrangement, the spacings and dimensioning of the individual stampings shown in Fig. 1 to 9 serve for the optimization and an adaptation of the degree of heat transfer between the fluids flowing in the outer and in the inner channel preferentially in opposite directions to suit the requirement, which fluids can be gaseous and/or liquid. Here, a required degree of heat exchange can also be achieved largely independently of the predetermined tube length and a predetermined overall tube diameter. * S **S *
* ***** * S ** * * S * * ** * *Sa..* * S aS I. 0$ * -a * b 0* * * * S * S. Li stofreferencenumbers 10 Heat exchanger 12 Inner tuber 14 Outer tube 16 Stamping 18 Stamping 20 Inner tube 22 Inner tube 26 Stamping 28 stamping 32 Inner tube 36 Stamping 38 Stamping 42 Inner tube 52 Inner tube 56 Stamping 58 Stamping 62 Inner tube 66 Stamping 68 Stamping 72 Inner tube 76 Stamping 78 Stamping * I * ***
S
* *S*.s * S *5 * * S S * I.
S
*SIiSS * S *S IS S. S * a 16 S. S * S S * S.
Claims (14)
- Patent claims 1. A tubular heat exchanger for a motor vehicle air conditioner with an inner tube (12; 22; 32; 42; 52; 62; 72) through which a liquid or gas can flow and an outer tube (14) radially enclosing the inner tube subject to the formation of an intermediate space through which a flow can flow, characterized in that the inner tube (12; 22; 32; 42; 52; 62; 72) comprises a quantity of stanipings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78) arranged spaced from one another and with their longitudinal extension extending at least partially in axial direction of the inner tube (12; 22; 32; 42; 52; 62; 72)
- 2. The heat exchanger according to Claim 1, wherein the stampings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78) are formed radially to the inside.
- 3. The heat exchanger according to any one of the preceding claims, wherein the quantity, the size, the geometrical shape and the orientation of the stampings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78) with predetermined geometry of inner *000 and/or outer tube is matched for achieving a 0*0...0 predetermined heat exchange between the gaseous refrigerant flowing in the inner tube (12; 22; 32; * * * * . 42; 52; 62; 72) and the liquid refrigerant flowing between the inner and outer tube (14). I. * -.* a 17 *0 * * S. *0
- 4. The heat exchanger according to any one of the preceding claims, wherein the quantity of the stampings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78), which are arranged on an imaginary circumferential line running perpendicularly to the longitudinal axis of the inner tube is 4 to 12, preferentially amounts to 6 to 10.
- 5. The heat exchanger according to any one of the preceding claims, wherein starnpings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78) arranged in axial direction adjacently to one another have a spacing of at least 15 mm to 30 mm.
- 6. The heat exchanger according to any one of the preceding claims, wherein the depth of the stampings is between 1 mm and 3 mm, preferentially between 1.5 mm and 2.5 mm.
- 7. The heat exchanger according to any one of the preceding claims, wherein the depth of the stampings (16; 18; 26, 28; 36, 38; 46, 48; 56, 58; 66, 68; 76, 78) is a maximum of 15% of the diameter of the inner tube (12; 22; 32; 42; 52; 62; 72)
- 8. The heat exchanger according to any one of the preceding claims, wherein the sum of the areas of S..' all stampings (16; 18; 26, 28; 36, 38; 46, 48; 56, S...,.* 58; 66, 68; 76, 78) is between 10 % and 60%, preferentially between 20 % and 50 % of the outer * . S * surface area of the inner tube (12; 22; 32; 42; 52; * . ue, S. ** * . S * 18 S. S S ** * S.
- 9. The heat exchanger according to any one of the preceding claims, wherein the stampings (16; 18; 26, 28; 36, 38) have a substantially rectangular geometry and with their longitudinal axis extend at S an angle of 00 to +/-45°, preferentially of +/*100 to +/-35° relative to the longitudinal axis of the inner tube (12; 22; 32; 42; 52; 62; 72)
- 10. The heat exchanger according to any one of the preceding claims 1 to 8, wherein the starnpings (56, 58) widen in circumferential direction seen in flow direction.
- 11. The heat exchanger according to any one of the preceding Claims 1 to 8 or 9, wherein the stampings (66, 68) seen in flow direction follow a curved course.
- 12. The heat exchanger according to any one of the preceding claims, wherein the stampings (76, 78) are designed triangular, diamond, trapezium or circular-shaped.
- 13. A motor vehicle air conditioner with a closed refrigerant circuit which fluidically interconnects at least one compressor, one condenser, one expansion device and one evaporator (20) of the air conditioner and comprises a heat exchanger according to any one of the preceding claims, wherein the inner tube (12; 22; 32; 42; 52; 62; 72) fluidically . interconnects the evaporator with the compressor and the outer tube the condenser and the expansion * * ** ** * * * * * * ** device.
- 14. A motor vehicle with an air conditioner according to Claim 13 or with a heat exchanger according to any one of the preceding Claims 1 to 12. * * *SS. * S s. * * * S * ** ***S.*. * S. *s * 20 * S I. * * . S I *
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009057232A DE102009057232A1 (en) | 2009-12-05 | 2009-12-05 | Tubular heat exchanger for automotive air conditioning |
Publications (2)
Publication Number | Publication Date |
---|---|
GB201020563D0 GB201020563D0 (en) | 2011-01-19 |
GB2476154A true GB2476154A (en) | 2011-06-15 |
Family
ID=43531464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1020563A Withdrawn GB2476154A (en) | 2009-12-05 | 2010-12-03 | Tubular heat exchanger for a motor vehicle air conditioner |
Country Status (4)
Country | Link |
---|---|
US (1) | US20110132028A1 (en) |
CN (1) | CN102087077A (en) |
DE (1) | DE102009057232A1 (en) |
GB (1) | GB2476154A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104501314B (en) * | 2014-12-26 | 2017-02-22 | 海信(山东)空调有限公司 | Vehicle-mounted air conditioner |
EP3182046A1 (en) | 2015-12-15 | 2017-06-21 | SAB Werkzeugbau GmbH | Heat exchanger for equipment or motor vehicles |
Citations (6)
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- 2009-12-05 DE DE102009057232A patent/DE102009057232A1/en not_active Withdrawn
-
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Also Published As
Publication number | Publication date |
---|---|
CN102087077A (en) | 2011-06-08 |
GB201020563D0 (en) | 2011-01-19 |
US20110132028A1 (en) | 2011-06-09 |
DE102009057232A1 (en) | 2011-06-09 |
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Legal Events
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WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |