EP0762070A1 - Refrigerant tubes for heat exchangers - Google Patents
Refrigerant tubes for heat exchangers Download PDFInfo
- Publication number
- EP0762070A1 EP0762070A1 EP96110844A EP96110844A EP0762070A1 EP 0762070 A1 EP0762070 A1 EP 0762070A1 EP 96110844 A EP96110844 A EP 96110844A EP 96110844 A EP96110844 A EP 96110844A EP 0762070 A1 EP0762070 A1 EP 0762070A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tube
- walls
- reinforcing
- communication holes
- heat exchanger
- 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.)
- Granted
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/048—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21C—MANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
- B21C23/00—Extruding metal; Impact extrusion
- B21C23/02—Making uncoated products
- B21C23/04—Making uncoated products by direct extrusion
- B21C23/08—Making wire, bars, tubes
- B21C23/10—Making finned tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21C—MANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
- B21C37/00—Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape
- B21C37/06—Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape of tubes or metal hoses; Combined procedures for making tubes, e.g. for making multi-wall tubes
- B21C37/15—Making tubes of special shape; Making tube fittings
- B21C37/151—Making tubes with multiple passages
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- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
- F28D1/0308—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
- F28D1/0316—Assemblies of conduits in parallel
-
- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
- F28D1/0391—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits a single plate being bent to form one or more conduits
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- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
-
- 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
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/0071—Evaporators
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- 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
- F28D2021/0084—Condensers
Definitions
- the present invention relates to tubes for passing a refrigerant therethrough, i.e., refrigerant tubes, for heat exchangers, and more particularly to refrigerant tubes for condensers and evaporators for use in air-cooling systems for motor vehecles.
- the object of the present invention is to provide a refrigerant tube for use in heat exchangers which achieves a high heat exchange efficiency.
- the refrigerant to be passed through the parallel refrigerant passages flows through the communication holes widthwise of the tube to spread to every part of all the passages, whereby portions of the refrigerant become mixed together. Accordingly no temperature difference occurs in the refrigerant between the passages, with the result that the refrigerant undergoes condensation at the upstream side and at the downstream side alike, flowing uniformly to achieve an improved heat exchange efficiency.
- the opening ratio which is the proportion of all the communication holes in the reinforcing wall to this wall influences thermal conductance. When within the range of 10 to 40 %, the opening ratio results in satisfactory thermal conductance, whereby the heat exchange efficiency of the refrigerant tube can be further improved.
- the opening ratio is limited to the range of 10 to 40% because if the ratio is less than 10%, the thermal conductance does not increase and further because the conductance no longer increases even if the ratio exceeds 40%, entailing an increase only in coefficient of friction.
- the opening ratio in the range of 10 to 40% is preferably 10 to 30%, more preferably about 20%.
- the communication holes are so sized in cross section as to permit the refrigerant to smoothly flow therethrough between the adjacent passages, to be free of the likelihood of becoming clogged with a flow of solder during brazing and to in no way impair the pressure resistance of the tube.
- the pitch of the communication holes is such that the holes will not lower the pressure resistance of the tube while permitting the refrigerant to smoothly flow across the reinforcing walls.
- the communication holes formed in the plurality of reinforcing walls are preferably in a staggered arrangement when seen from above.
- FIG. 19 shows a condenser comprising flat refrigerant tubes embodying the invention.
- the condenser comprises a pair of headers 61, 62 arranged at left and right in parallel and spaced apart from each other, parallel flat refrigerant tubes 63 each joined at its opposite ends to the two headers 61, 62, corrugated fins 64 arranged in air flow clearances between the adjacent refrigerant tubes 63 and brazed to the adjacent refrigerant tubes 63, an inlet pipe 65 connected to the upper end of the left header 61, an outlet pipe 66 connected to the lower end of the right 62, a left partition 67 provided inside the left header 61 and positioned above the midportion thereof, and a right partition 68 provided inside the right header 62 and positioned below the midportion thereof, the number of refrigerant tubes 63 between the inlet pipe 65 and the left partition 67, the number of refrigerant tubes 63 between the left partition 67 and the right partition 68 and the number of regrigerant tubes
- the refrigerant tubes 63 for use in the above condenser are concerned with the present invention.
- Refrgigerant tubes embodying the invention will be described below.
- the following embodiments are all 10 to 40% in opening ratio which is the proportion of all communication holes in each reinforcing wall to the reinforcing wall.
- the communication holes formed in a plurality of reinforcing walls are all in a staggered arrangement.
- a refrigerant tube T1 for heat exchangers is formed by a flat aluminum tube 7 having parallel refrigerant passages 6 in its interior and comprising flat upper and lower walls 1, 2, left and right vertical side walls 3, 4 connected respectively between the left side edges of the upper and lower walls 1, 2 and between the right side edges thereof, and a plurality of reinforcing walls 5 connected between the upper and lower walls 1, 2, extending longitudinally of the tube and spaced apart from one another by a predetermined distance.
- the reinforcing walls 5 are each formed with a plurality of rectangular communiction holes 8 for causing the parallel refrigerant passages 6 to communicate with each other therethrough,
- the reinforcing walls 5 are formed by parallel ridges 11 projecting inward from the lower wall 2 and joined to the inner surface of the upper wall 1.
- the rectangular communication holes 8 are formed by rectangular cutouts 12 provided in the upper edge of each ridge 11 at a predetermined spacing and having their openings closed by the upper wall 1.
- the refrigerant tube T1 is produced by the following method.
- the lower roll 17 is provided, at its respective outer ends, with large-diameter portions 18 each having an outer end face flush with that of the second small-diameter portion 16 and having a smaller width than the portion 16.
- the peripheral surfaces of the rolling rolls 13, 17 form a flat portion 19 providing the lower wall 2 by thinning the sheet blank to a specified thickness.
- the rolls 13, 17 also form ridges 11 projecting from the flat portion 19 integrally therewith by means of the annular grooves 14.
- Further formed at the respective side edges of the flat portion 19 are upright portions 20 each including an inner stepped part 20a with the same height as the ridges 11, and a thin wall 20b extending upward from the outer edge of the stepped part 20a.
- the multiplicity of protrusions 23 are in a staggered arrangement so that the cutouts 12 are formed in the upper edges of the parallel ridges 11 in a staggered arrangement when seen from above.
- the side walls 28, 29 are formed by the following method.
- Upright portions 36 having the same height as the reinforcing walls 5 are provided respectively at opposite sides of the lower aluminum sheet 35, and a slope 38 slanting outwardly upward is formed at the bottom edge of each upright portion 36.
- a depending portion 37 is formed at each of opposite sides of the upper aluminum sheet 34, the portion 37 being in contact with with the outer side face of the upright portion 36 and projecting downward slightly beyond the lower surface of the lower wall 2.
- the downward projections 37a of the depending portions 37 are crimped onto the respective slopes 38 of the lower aluminum sheet 35, and the portions where the upper and lower aluminum sheets 34, 35 are in contact with each other are brazed.
- FIG. 10 shows this embodiment, i.e., a refrigerant tube T3 for use in heat exchangers, which comprises a flat aluminum tube 39.
- the tube 39 is prepared from an aluminum sheet 40 in the form of a brazing sheet having a brazing filler metal layer on one surface thereof, by folding the sheet at the midportion of its width like a hairpin with the brazing layer out so as to form a hollow portion, bending opposite side edges to an arcuate shape and joining the side edges in butting contact with each other.
- the tube 39 therefore has circular-arc left and right side walls 41, 42.
- the butt joint 43 thus made is oblique in cross section so as to form the joint 43 over an increased area.
- Each of reinforcing walls 44 is formed by joining a downward ridge 44a inwardly projecting from the upper wall 1 to an upward ridge 44b inwardly projecting from the lower wall 2.
- Each of trapezoidal communication holes 5 is formed by the combination of a pair of trapezoidal cutouts 45a, 45b. Such cutouts 45a, 45b are formed respectively in the lower edge of the downward ridge 44a and the upper edge of the upward ridge 44b at a predetermined spacing.
- FIG. 11 shows this embodiment, i.e., a heat exchange refrigerant tube T4, which has two kinds of reinforcing walls 46.
- the walls 46 of one kind are each formed by a downward ridge 46a inwardly projecting from an upper wall 1 and joined to a flat inner surface of a lower wall 2.
- the walls 46 of the other kind are each formed by an upward ridge 46b inwardly projecting from the lower wall 2 and joined to a flat inner surface of the upper wall 1.
- the two kinds of walls 46 are arranged alternately.
- Trapezoidal communication holes 47 are formed by trapezoidal cutouts 47a, 47b provided respectively in the lower edge of the downward ridge 46a and in the upper edge of the upward ridge 46b and have their openings closed by one of the upper and lower walls 1, 2.
- the present embodiment is the same as Embodiment 3.
- FIG. 12 shows this embodiment, i.e., a heat exchanger refrigerant tube T5.
- the tube T5 has reinforcing walls 48 which are formed by downward ridges 48a inwardly projecting from an upper wall 1 and joined to a flat inner surface of a lower wall 2.
- Trapezoidal communication holes 49 are formed by providing trapezoidal cutouts 49a in the lower edges of the ridges 48a at a predetermined spacing and closing the openings of the cutouts 49a with the lower wall 2.
- the present embodiment is the same as Embodiment 3 except for this feature.
- FIG. 13 shows this embodiment, i.e., a heat exchange refrigerant tube T4, which comprises a flat aluminum tube 50.
- the tube 50 is prepared from upper and lower two aluminum sheets 51, 53 by bending opposite side edges of the sheets to an arcuate shape toward each other so as to form a hollow portion, butting the sheets against each other edge to edge and joining the butted edges.
- the present embodiment is the same as Embodiment 3.
- the left and right butt joints 53, 54 are oblique in cross section as is the case with Embodiment 3.
- the aluminum sheet having the ridges, etc. and used in the foregoing embodiments can be replaced by an aluminum extrudate of specified cross section.
- Example 2 The same refrigerant tube as that of Example 1 except that the tube is 0.8 mm in the height of communication holes and 40% in opening ratio.
- the refrigerant tubes of Example 1 and Comparative Example were used to determine the relationship between the average quality X of refrigerant (the fraction of vapor mass in refrigerant) and the thermal conductance hA (h: heat transfer coefficient, A: the area of heat transfer surface inside the refrigerant tube).
- the method of determination was as follows. The refrigerant tube was placed in a cooling water channel, a refrigerant comprising HFC134a was passed through the tube, and cooling water was passed through the channel.
- the mass velocity G of the refrigerant was set at 400 kg/m 2 ⁇ s, the refrigerant inlet temperature at 65 o C, and the heat flux between the refrigerant and the cooling water at 8 kW/m 2 .
- the flow rate of the cooling water was so set as to give a Reynolds number of 1500.
- the thermal conductance hA was measured at varying values of average quality X.
- the refrigerant tubes of Examples 1 to 4 and Comparative Example were used to determine, by the same method as in Evaluation Test 1, the relationship between the opening ratio and the heat transfer coefficient h at an average quality X of refrigrant of 20%, 50% or 80%, and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant was 50% (Reynolds number: 10 4 ).
- FIG. 17 shows the result.
- FIG. 17 indicates that at any value of average quality X, the heat transfer coefficient h is greater when the reinforcing walls are formed with communication holes than when no holes are formed, and that the heat transfer coefficient h is especially great at an opening ratio of 20%.
- FIG. 19 Three kinds of condensers of the multiflow type shown in FIG. 19 were fabricated using the refrigerant tube of Example 2 or Comparative Example. More specifically, 37 refrigerant tubes, and corrugated fins, 22 mm in width, 7 mm in height and 1 mm in fin pitch, were used for making a core portion measuring 326 mm in width, 330.5 mm in height and 0.108 m 2 in front area, and opposite ends of each tube were connected to right and left headers. No partition was provided in opposite headers in the condenser of the type I (single pass).
- the condenser of the type II had a partition inside the left header above the midportion thereof, another partition inside the right header below the midportion thereof, 20 refrigerant tubes positioned above the partition of the left header, 11 refrigerant tubes arranged between the two partitions, and 6 refrigerant tubes positioned below the partition of the tight header (three passes).
- the condenser of the type III had two partitions positioned respectively in an upper portion and a lower portion of the left header, two partitions positioned inside the right header, one at an intermediate level between the two partitions of the left header and the other at a level below the lower partition of the left header, 12 refrigerant tubes positioned above the upper partition of the left header, 9 refirgerant tubes between the upper partition of the left header and the upper partition of the right header, 7 refrigerant tubes positioned between the upper partition of the right header and the lower partition of the left header, 5 refrigerant tubes positioned between the lower partition of the left header and the lower partition of the right header, and 4 refrigerant tubes positioned below the lower partition of the right header (five passes).
- the condensers were checked for the relationship between the refrigerant pressure loss ⁇ Pr and the quantity of heat radiated per unit front area, Q/Fa.
- FIG. 18 shows the result.
- FIG. 18 shows that the capacitor comprising the refrigerant tube wherein the reinforcing walls are formed with communication holes at an opening ratio of 20% exhibits an improved performance over the condenser comprising the refrigerant tube having no communication holes in the reinforcing walls and achieves an improvement even when the pressure loss is the same.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
Description
- The present invention relates to tubes for passing a refrigerant therethrough, i.e., refrigerant tubes, for heat exchangers, and more particularly to refrigerant tubes for condensers and evaporators for use in air-cooling systems for motor vehecles.
- The term "aluminum" as used herein and in the claims includes pure aluminum and aluminum alloys.
- JP-B-45300/1991 discloses a condenser for use in air-cooling systems for motor vehicles which comprises a pair of headers arranged at right and left in parallel and spaced apart from each other, parallel flat refrigerant tubes each joined at its opposite ends to the two headers, corrugated fins arranged in air flow clearances between the adjacent refrigerant tubes and brazed to the adjacent refrigerant tubes, an inlet pipe connected to the upper end of the left header, an outlet pipe connected to the lower end of the right header, a left partition provided inside the left header and positioned above the midportion thereof, and a right partition provided inside the right header and positioned below the midportion thereof, the number of refrigerant tubes between the inlet pipe and the left partition, the number of refrigerant tubes between the left partition and the right partition and the number of refrigerant tubes between the right partition and the outlet pipe decreasing from above downward. A refrigerant flowing into the inlet pipe in a vapor phase flows zigzag through the condenser before flowing out from the outlet pipe in a liquid phase. Condensers of the construction described are called parallel flow or multiflow condenser, realize higher efficiencies, lower pressure losses and supercompactness and are in wide use recently in place of conventional serpentime condensers.
- It is required that the flat refrigerant tube for use in the condenser have pressure resistance since the refrigerant is introduced thereinto in the form of a gas of high pressure. To meet this requirement and to achieve a high heat exchange efficiency, the refrigerant tube used is in the form of a flat aluminum tube which comprises upper and lower walls, and a reinforcing wall connected between the upper and lower walls and extending longitudinally.
- However, the reinforcing wall provided in the refrigerant tube forms independent parallel refrigerant passages in the interior of the tube. Air flows orthogonal to the parallel refrigerant passages, so that the heat exchange efficiency is consequently higher in the refrigerant passage at the air inlet side than in the passage at the air outlet side. Accordingly, gaseous refrigerant is rapidly condensed to a liquid in the refrigerant passage at the upstream side, whereas the refrigerant still remains in the passage at the downstream side. When the entire structure of the tube is considered, the refrigerant therefore flows unevenly, failing to achieve a high heat exchange efficiency.
- The object of the present invention is to provide a refrigerant tube for use in heat exchangers which achieves a high heat exchange efficiency.
- The present invention provides a refrigerant tube which fulfills the above object and which comprises a flat tube having parallel refrigerant passages in its interior and comprising upper and lower walls and a plurality of reinforcing walls connected between the upper and lower walls, the reinforcing walls extending longitudinally of the tube and spaced apart from one another by a predetermined distance, the reinfocing walls being each formed with a plurality of communication holes for causing the parallel refrigerant passages to communicate with one another therethrough, each of the reinforcing walls being 10 to 40% in opening ratio which is the proportion of all the communication holes in the reinforcing wall to the reinforcing wall.
- The refrigerant to be passed through the parallel refrigerant passages flows through the communication holes widthwise of the tube to spread to every part of all the passages, whereby portions of the refrigerant become mixed together. Accordingly no temperature difference occurs in the refrigerant between the passages, with the result that the refrigerant undergoes condensation at the upstream side and at the downstream side alike, flowing uniformly to achieve an improved heat exchange efficiency. The opening ratio which is the proportion of all the communication holes in the reinforcing wall to this wall influences thermal conductance. When within the range of 10 to 40 %, the opening ratio results in satisfactory thermal conductance, whereby the heat exchange efficiency of the refrigerant tube can be further improved. The opening ratio is limited to the range of 10 to 40% because if the ratio is less than 10%, the thermal conductance does not increase and further because the conductance no longer increases even if the ratio exceeds 40%, entailing an increase only in coefficient of friction. The opening ratio in the range of 10 to 40% is preferably 10 to 30%, more preferably about 20%.
- The communication holes are so sized in cross section as to permit the refrigerant to smoothly flow therethrough between the adjacent passages, to be free of the likelihood of becoming clogged with a flow of solder during brazing and to in no way impair the pressure resistance of the tube. The pitch of the communication holes is such that the holes will not lower the pressure resistance of the tube while permitting the refrigerant to smoothly flow across the reinforcing walls.
- The communication holes formed in the plurality of reinforcing walls are preferably in a staggered arrangement when seen from above.
- The pitch of the reinforcing walls in the widthwise direction of the tube is preferably up to 4 mm. A lower heat exchange efficiency will result if the pitch is in excess of 4 mm.
- The height of the reinforcing walls is preferably up to 2 mm. If the wall height is over 2 mm, not only difficulty is encountered in fabricating a compacted heat exchanger, but the resistance to the passage of air also increases to result in an impaired heat exchange efficiency.
- The present invention will be described in greater detail with reference to the accompanying drawings.
-
- FIG. 1 is a view in cross section showing a flat refrigerant tube of
Embodiment 1 of the present invention; - FIG. 2 is an enlarged fragmentary view of the tube shown in FIG. 1;
- FIG. 3 is an enlarged view in section taken along the line 3-3 in FIG. 1;
- FIG. 4 is a cross sectional view showing how to produce an aluminum sheet by rolling for fabricating the refrigerant tube of
Embodiment 1 of the invention; - FIG. 5 is a cross sectional view showing how to form cutouts in the upper edges of ridges of the aluminum sheet shown in FIG. 4;
- FIG. 6 is a view in section taken along the line 6-6 in FIG. 5;
- FIG. 7 is a view in longitudinal section showing how to form the ridges and the cutouts in the upper edges thereof by a single step;
- FIG. 8 is an enlarged fragmentary perspective view showing the refrigerant tube of
Embodiment 1 of the invention while it is being fabricated; - FIG. 9 is a cross sectional view of a flat refrigerant tube according to
Embodiment 2 of the invention; - FIG. 10 is a cross sectional view of a flat refrigerant tube according to
Embodiment 3 of the invention; - FIG. 11 is a cross sectional view of a flat refrigerant tube according to Embodiment 4 of the invention;
- FIG. 12 is a cross sectional view of a flat refrigerant tube according to
Embodiment 5 of the invention; - FIG. 13 is a cross sectional view of a flat refrigerant tube according to
Embodiment 6 of the invention; - FIG. 14 is a graph showing the result of
Evaluation Test 1, i.e., the relationship between the average quality X of refrigerant and the thermal conductance hA; - FIG. 15 is a graph showing the result of
Evaluation Test 2, i.e., the relationship between the average quality X of refrigerant and the heat transfer coefficient h; - FIG. 16 is a graph showing the result of
Evaluation Test 3, i.e., the relationship between the opening ratio and the thermal conductance hA at an average quality X of refrigerant of 20%, 50% or 80%, and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant is 50%; - FIG. 17 is a graph showing the result of Evaluation Test 4, i.e., the relationship between the opening ratio and the heat transfer coefficient h at an average quality X of refrigerant of 20%, 50% or 80%, and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant is 50%;
- FIG. 18 is a graph showing the result of
Evaluation Test 5, i.e., the relationship between the refrigerant pressure loss ΔPr and the quantity of heat radiated through unit front area, Q/Fa, as established for condensers comprising refrigerant tubes; and - FIG. 19 is a front view showing a condenser wherein flat refrigerant tubes are used.
- FIG. 19 shows a condenser comprising flat refrigerant tubes embodying the invention. The condenser comprises a pair of
headers flat refrigerant tubes 63 each joined at its opposite ends to the twoheaders fins 64 arranged in air flow clearances between theadjacent refrigerant tubes 63 and brazed to theadjacent refrigerant tubes 63, aninlet pipe 65 connected to the upper end of theleft header 61, anoutlet pipe 66 connected to the lower end of the right 62, aleft partition 67 provided inside theleft header 61 and positioned above the midportion thereof, and aright partition 68 provided inside theright header 62 and positioned below the midportion thereof, the number ofrefrigerant tubes 63 between theinlet pipe 65 and theleft partition 67, the number ofrefrigerant tubes 63 between theleft partition 67 and theright partition 68 and the number ofregrigerant tubes 63 between theright partition 68 and theoutlet pipe 66 decreasing in this order. A refrigerant flowing into theinlet pipe 65 in a gas phase flows zigzag through the condenser before flowing out from theoutlet pipe 66 in a liquid phase. - The
refrigerant tubes 63 for use in the above condenser are concerned with the present invention. Refrgigerant tubes embodying the invention will be described below. The following embodiments are all 10 to 40% in opening ratio which is the proportion of all communication holes in each reinforcing wall to the reinforcing wall. The communication holes formed in a plurality of reinforcing walls are all in a staggered arrangement. - This embodiment is shown in FIGS. 1 to 3. A refrigerant tube T1 for heat exchangers is formed by a
flat aluminum tube 7 havingparallel refrigerant passages 6 in its interior and comprising flat upper andlower walls vertical side walls 3, 4 connected respectively between the left side edges of the upper andlower walls walls 5 connected between the upper andlower walls walls 5 are each formed with a plurality ofrectangular communiction holes 8 for causing theparallel refrigerant passages 6 to communicate with each other therethrough, - The
flat aluminum tube 7 is prepared from upper and lower twoaluminum sheets lower sheet 10 at its opposite side edges, joining the bent side edges to the respective side edges of theupper aluminum sheet 9 so as to define a hollow portion by the twoaluminum sheets - The reinforcing
walls 5 are formed byparallel ridges 11 projecting inward from thelower wall 2 and joined to the inner surface of theupper wall 1. Therectangular communication holes 8 are formed byrectangular cutouts 12 provided in the upper edge of eachridge 11 at a predetermined spacing and having their openings closed by theupper wall 1. - The refrigerant tube T1 is produced by the following method.
- With reference to FIG. 4, an aluminum sheet blank in the form of a brazing sheet covered with a brazing filler metal over the lower surface and having a thickness greater than that of upper and lower walls of the refrigerant tube to be produced is first rolled by a pair of upper and
lower rolls upper roll 13 has parallelannular grooves 14 arranged at a spacing, first small-diameter portions 15 formed at the respective outer sides of the arrangement ofgrooves 14 and each having a periphery of the same diameter as the bottom faces of thegrooves 14, and second small-diameter portions 16 positioned externally of the respective first small-diameter portions 15 and having a smaller diameter and a greater width than theportions 15. Thelower roll 17 is provided, at its respective outer ends, with large-diameter portions 18 each having an outer end face flush with that of the second small-diameter portion 16 and having a smaller width than theportion 16. The peripheral surfaces of the rolling rolls 13, 17 form aflat portion 19 providing thelower wall 2 by thinning the sheet blank to a specified thickness. Therolls ridges 11 projecting from theflat portion 19 integrally therewith by means of theannular grooves 14. Further formed at the respective side edges of theflat portion 19 areupright portions 20 each including an inner steppedpart 20a with the same height as theridges 11, and athin wall 20b extending upward from the outer edge of the steppedpart 20a. Thus, the rolling operation produces a rolledaluminum sheet 21. - As shown in FIGS. 5 and 6, the rolled
aluminum sheet 21 is then passed between a pair of upper andlower rolls upper roll 22 hasrectangular protrusions 23 arranged at a predetermined spacing at a position corresponding to each of the parallelannular grooves 14 in theupper roll 13 for the preceding step. This rolling operation formsrectangular cutouts 12 in the upper edges of therespective ridges 11 at the predetermined spacing, whereby thelower aluminum sheet 10 is obtained. - The multiplicity of
protrusions 23 are in a staggered arrangement so that thecutouts 12 are formed in the upper edges of theparallel ridges 11 in a staggered arrangement when seen from above. - The above method of producing the
lower aluminum sheet 10 requires two steps for forming theridges 11 having thecutouts 12. As shown in FIG. 7, however, theseridges 11 with thecutouts 12 can be formed by a single step by using in combination with thelower roller 17 of the first step anupper roll 26 which is formed in each of parallelannular grooves 14 withprotrusions 25 arranged at a predetermined spacing and having a height smaller than the depth of the grooves. - On the other hand, the flat
upper aluminum sheet 9 is prepared which comprises a brazing sheet having opposite surfaces each covered with a brazing filler metal layer. As seen in FIG. 8, theupper aluminum sheet 9 has at each of its opposite side edge portions an upper surface in the form of aslope 27 slanting outwardly downward. With reference to FIG. 2, each side edge portion of theupper aluminum sheet 9 is placed on the steppedpart 20a of theupright portion 20 of thelower aluminum sheet 10, and thethin wall 20b (indicated in a broken line) is crimped onto theslope 27 of theupper aluminum sheet 9. Subsequently, the lower surface of theupper sheet 9 is brazed to the steppedparts 20a of theupright portions 20 of thelower sheet 10 and to the top ends of theridges 11 thereof, whereby the refrigerant tube T1 is fabricated. - The peripheral surface of the upper rolling
roll 13 may be formed with indentations and projections which are triangular wavelike in cross section, or knurled. Thelower aluminum sheet 10 then obtained has projections and indentations extending longitudinally thereof over the entire inner surface, or has an inner surface formed with latticelike projections or indentations. This gives an increased surface area to thelower wall 2. - FIG. 9 shows this embodiment, i.e., a refrigerant tube T2 for use in heat exchangers. The tube T2 has the same construction as
Embodiment 1 except that the tube T2 has left andright side walls upward projections 31 integral with thelower wall 2, extending longitudinally thereof and spaced apart from one another for giving a heat transfer surface of increased area. Theholes 30 can be provided by formingtrapezoidal cutouts 32 in the upper edges of theridges 11. - The tube T2 comprises a
flat aluminum tube 33, which is prepared by bending opposite side edges of upper and lower twoaluminum sheets 34, 35, fitting the bent side edges of one of the twoaluminum sheets 34, 35 respectively over the bent side edges of the other aluminum sheet and joining the fitted portions so as to define a hollow portion by thesheets 34, 35. - Stated more specifically, the
side walls Upright portions 36 having the same height as the reinforcingwalls 5 are provided respectively at opposite sides of thelower aluminum sheet 35, and aslope 38 slanting outwardly upward is formed at the bottom edge of eachupright portion 36. As indicated in a broken line in FIG. 9, on the other hand, a dependingportion 37 is formed at each of opposite sides of the upper aluminum sheet 34, theportion 37 being in contact with with the outer side face of theupright portion 36 and projecting downward slightly beyond the lower surface of thelower wall 2. Thedownward projections 37a of the dependingportions 37 are crimped onto therespective slopes 38 of thelower aluminum sheet 35, and the portions where the upper andlower aluminum sheets 34, 35 are in contact with each other are brazed. - FIG. 10 shows this embodiment, i.e., a refrigerant tube T3 for use in heat exchangers, which comprises a
flat aluminum tube 39. Thetube 39 is prepared from analuminum sheet 40 in the form of a brazing sheet having a brazing filler metal layer on one surface thereof, by folding the sheet at the midportion of its width like a hairpin with the brazing layer out so as to form a hollow portion, bending opposite side edges to an arcuate shape and joining the side edges in butting contact with each other. Thetube 39 therefore has circular-arc left andright side walls - Each of reinforcing
walls 44 is formed by joining adownward ridge 44a inwardly projecting from theupper wall 1 to anupward ridge 44b inwardly projecting from thelower wall 2. Each of trapezoidal communication holes 5 is formed by the combination of a pair oftrapezoidal cutouts Such cutouts downward ridge 44a and the upper edge of theupward ridge 44b at a predetermined spacing. - FIG. 11 shows this embodiment, i.e., a heat exchange refrigerant tube T4, which has two kinds of reinforcing
walls 46. Thewalls 46 of one kind are each formed by adownward ridge 46a inwardly projecting from anupper wall 1 and joined to a flat inner surface of alower wall 2. Thewalls 46 of the other kind are each formed by anupward ridge 46b inwardly projecting from thelower wall 2 and joined to a flat inner surface of theupper wall 1. The two kinds ofwalls 46 are arranged alternately. Trapezoidal communication holes 47 are formed bytrapezoidal cutouts downward ridge 46a and in the upper edge of theupward ridge 46b and have their openings closed by one of the upper andlower walls Embodiment 3. - FIG. 12 shows this embodiment, i.e., a heat exchanger refrigerant tube T5. The tube T5 has reinforcing
walls 48 which are formed bydownward ridges 48a inwardly projecting from anupper wall 1 and joined to a flat inner surface of alower wall 2. Trapezoidal communication holes 49 are formed by providing trapezoidal cutouts 49a in the lower edges of theridges 48a at a predetermined spacing and closing the openings of the cutouts 49a with thelower wall 2. The present embodiment is the same asEmbodiment 3 except for this feature. - FIG. 13 shows this embodiment, i.e., a heat exchange refrigerant tube T4, which comprises a
flat aluminum tube 50. Thetube 50 is prepared from upper and lower twoaluminum sheets Embodiment 3. The left and right butt joints 53, 54 are oblique in cross section as is the case withEmbodiment 3. - The aluminum sheet having the ridges, etc. and used in the foregoing embodiments can be replaced by an aluminum extrudate of specified cross section.
- Examples of the invention will be described below along with a comparative example. The refrigerant tubes of the examples and comparative example are so shaped as shown in FIG. 1 in cross section.
- A refrigerant tube which is 508 mm in length, 16.5 mm in the distance between
side walls lower walls walls 5, 2.4 mm in the pitch of reinforcingwalls 5, 0.3 mm in the thickness of reinforcingwalls 5, 1.6 mm in the pitch P ofcommunication holes 8, 0.8 mm in the length L ofcommunication holes 8, 0.2 mm in the height H ofcommunication holes - The same refrigerant tube as that of Example 1 except that this tube is 0.4 mm in the height of communication holes and 20% in opening ratio.
- The same refrigerant tube as that of Example 1 except that the tube is 0.6 mm in the height of communication holes and 30% in opening ratio.
- The same refrigerant tube as that of Example 1 except that the tube is 0.8 mm in the height of communication holes and 40% in opening ratio.
- The same refrigerant tube as that of Example 1 except that the tube has no communication holes in the reinforcing walls.
- The refrigerant tubes of Example 1 and Comparative Example were used to determine the relationship between the average quality X of refrigerant (the fraction of vapor mass in refrigerant) and the thermal conductance hA (h: heat transfer coefficient, A: the area of heat transfer surface inside the refrigerant tube). The method of determination was as follows. The refrigerant tube was placed in a cooling water channel, a refrigerant comprising HFC134a was passed through the tube, and cooling water was passed through the channel. After the lapse of a specified period of time, the mass velocity G of the refrigerant was set at 400 kg/m2·s, the refrigerant inlet temperature at 65o C, and the heat flux between the refrigerant and the cooling water at 8 kW/m2. The flow rate of the cooling water was so set as to give a Reynolds number of 1500. The thermal conductance hA was measured at varying values of average quality X.
- The result is shown in FIG. 14, which reveals that when the reinforcing walls are formed with communication holes, the thermal conductance hA is greater at any value of average quality X than when no holes are formed.
- The refrigerant tubes of Example 2 and Comparative Example were used to determine the relationship between the average quality X of refrigerant and the heat transfer coefficient h by the same method as in
Evaluation Test 1. FIG. 15 shows the result. - FIG. 15 reveals that at any value of average quality X, the heat transfer coefficient h is greater when the reinforcing walls are formed with communication holes than when no holes are formed.
- The refrigerant tubes of Examples 1 to 4 and Comparative Example were used to determine the relationship between the opening ratio and the thermal conductance hA at an average quality X of refrigerant of 20%, 50% or 80%, and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant was 50% (Reynolds number of refrigerant: 104), the relationships being determined by the same method as in
Evaluation Test 1. FIG. 16 shows the result. - FIG. 16 indicates that at any value of average quality X, the thermal conductance hA is greater when the reinforcing walls are formed with communication holes than when no holes are formed, and that the thermal conductance hA is especially great at an opening ratio of 20%.
- The refrigerant tubes of Examples 1 to 4 and Comparative Example were used to determine, by the same method as in
Evaluation Test 1, the relationship between the opening ratio and the heat transfer coefficient h at an average quality X of refrigrant of 20%, 50% or 80%, and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant was 50% (Reynolds number: 104). FIG. 17 shows the result. - FIG. 17 indicates that at any value of average quality X, the heat transfer coefficient h is greater when the reinforcing walls are formed with communication holes than when no holes are formed, and that the heat transfer coefficient h is especially great at an opening ratio of 20%.
- Three kinds of condensers of the multiflow type shown in FIG. 19 were fabricated using the refrigerant tube of Example 2 or Comparative Example. More specifically, 37 refrigerant tubes, and corrugated fins, 22 mm in width, 7 mm in height and 1 mm in fin pitch, were used for making a core portion measuring 326 mm in width, 330.5 mm in height and 0.108 m2 in front area, and opposite ends of each tube were connected to right and left headers. No partition was provided in opposite headers in the condenser of the type I (single pass). The condenser of the type II had a partition inside the left header above the midportion thereof, another partition inside the right header below the midportion thereof, 20 refrigerant tubes positioned above the partition of the left header, 11 refrigerant tubes arranged between the two partitions, and 6 refrigerant tubes positioned below the partition of the tight header (three passes). The condenser of the type III had two partitions positioned respectively in an upper portion and a lower portion of the left header, two partitions positioned inside the right header, one at an intermediate level between the two partitions of the left header and the other at a level below the lower partition of the left header, 12 refrigerant tubes positioned above the upper partition of the left header, 9 refirgerant tubes between the upper partition of the left header and the upper partition of the right header, 7 refrigerant tubes positioned between the upper partition of the right header and the lower partition of the left header, 5 refrigerant tubes positioned between the lower partition of the left header and the lower partition of the right header, and 4 refrigerant tubes positioned below the lower partition of the right header (five passes). The condensers were checked for the relationship between the refrigerant pressure loss ΔPr and the quantity of heat radiated per unit front area, Q/Fa. FIG. 18 shows the result.
- FIG. 18 shows that the capacitor comprising the refrigerant tube wherein the reinforcing walls are formed with communication holes at an opening ratio of 20% exhibits an improved performance over the condenser comprising the refrigerant tube having no communication holes in the reinforcing walls and achieves an improvement even when the pressure loss is the same.
Claims (13)
- A heat exchanger refrigerant tube comprising a flat tube having parallel refrigerant passages in its interior and comprising upper and lower walls and a plurality of reinforcing walls connected between the upper and lower walls, the reinforcing walls extending longitudinally of the tube and spaced apart from one another by a predetermined distance, the reinforcing walls being each formed with a plurality of communication holes for causing the parallel refrigerant passages to communicate with one another therethrough, each of the reinforcing walls being 10 to 40% in opening ratio which is the proportion of all the communication holes in the reinforcing wall to the reinforcing wall.
- A heat exchanger refrigerant tube as defined in claim 1 wherein the opening ratio is 10 to 30%.
- A heat exchanger refrigerant tube as defined in claim 1 wherein the opening ratio is about 20%.
- A heat exchanger refrigerant tube as defined in claim 1, 2 or 3 wherein the communication holes are rectangular or trapezoidal in shape.
- A heat exchanger refrigerant tube as defined in claim 1, 2 or 3 wherein the communication holes formed in the plurality of reinforcing walls are in a staggered arrangement when seen from above.
- A heat exchanger refrigerant tube comprising a flat aluminum tube having parallel refrigerant passages in its interior and comprising upper and lower walls and a plurality of reinforcing walls, the reinforcing walls extending longitudinally of the tube and spaced apart from one another by a predetermined distance, the flat aluminum tube being formed of an aluminum sheet, the reinforcing walls each comprising a ridge projecting from the aluminum sheet and integral therewith, the reinforcing walls being each formed with a plurality of communication holes for causing the parallel refrigerant passages to communicate with one another therethrough, each of the reinforcing walls being being 10 to 40% in opening ratio which is the proportion of all the communication holes in the reinforcing wall to the reinforcing wall, the communication holes in the plurality of reinforcing walls being in a staggered arrangement when seen from above.
- A heat exchanger refrigerant tube as defined in claim 6 wherein the aluminum sheet comprises a brazing sheet having a brazing filler metal layer over at least one of opposite surfaces thereof.
- A heat exchanger refrigerant tube as defined in claim 6 wherein the flat aluminum tube is prepared by bending opposite side edges of at least one of upper and lower two aluminum sheets, and joining the bent side edges to respective side edges of the other aluminum sheet so as to define a hollow portion by the two aluminum sheets.
- A heat exchanger refrigerant tube as defined in claim 6 wherein the flat aluminum tube is prepared by bending opposite side edges of upper and lower two aluminum sheets, fitting the bent side edges of one of the two aluminum sheets respectively over the bent side edges of the other aluminum sheet, and joining the fitted portions so as to define a hollow portion by the two aluminum sheets.
- A heat exchanger refrigerant tube as defined in claim 6 wherein the flat anuminum tube is prepared from the aluminum sheet by folding the sheet at the middle of its width so as to form a hollow portion, bending at least one of opposite side edges of the sheet, butting the bent side edge against the other side edge and joining the side edges.
- A heat exchanger refrigerant tube as defined in claim 2 wherein each of the reinforcing walls is formed by a downward ridge projecting inward from the upper wall integrally therewith and an upward ridge projecting inward from the lowerwall integrally therewith and joined to the downward ridge, and the communication holes are formed by combination of opposed pairs of cutouts formed in a lower edge of the downward ridge and an upper edge of the upward ridge and arranged at a predetermined spacing.
- A heat exchanger refrigerant tube as defined in claim 6 wherein the reinforcing walls include those formed by downward ridges projecting inward from the upper wall integrally therewith and joined to a flat inner surface of the lower wall, and those formed by upward ridges projecting inward from the lower wall integrally therewith and joined to a flat inner surface of the upper wall, the two kinds of reinforcing walls being arranged alternately, and the communication holes are formed by cutouts formed in lower edges of the downward ridges and upper edges of the upward ridges at a predetermined spacing and having their openings closed by one of the upper and lower walls.
- A heat exchanger refrigerant tube as defined in claim 6 wherein each of the reinforcing walls is formed by a ridge projecting inward from one of the upper and lower walls integrally therewith and joined to a flat inner surface of the other wall, and the communication holes are formed by cutouts formed in an edge of the ridge at a predetermined spacing and having their openings closed by one of the upper and lower walls.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17200795 | 1995-07-07 | ||
JP7172007A JPH0926278A (en) | 1995-07-07 | 1995-07-07 | Heat exchanger refrigerant flow pipe and car air-conditioner condenser |
JP172007/95 | 1995-07-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0762070A1 true EP0762070A1 (en) | 1997-03-12 |
EP0762070B1 EP0762070B1 (en) | 2001-02-28 |
Family
ID=15933798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96110844A Expired - Lifetime EP0762070B1 (en) | 1995-07-07 | 1996-07-04 | Refrigerant tubes for heat exchangers |
Country Status (17)
Country | Link |
---|---|
EP (1) | EP0762070B1 (en) |
JP (1) | JPH0926278A (en) |
KR (1) | KR100414852B1 (en) |
CN (1) | CN1111717C (en) |
AR (1) | AR002691A1 (en) |
AT (1) | ATE199456T1 (en) |
AU (1) | AU711980B2 (en) |
BR (1) | BR9602985A (en) |
CA (1) | CA2180598C (en) |
CZ (1) | CZ293383B6 (en) |
DE (1) | DE69611868T2 (en) |
ES (1) | ES2154366T3 (en) |
IN (1) | IN188905B (en) |
MX (1) | MX9602646A (en) |
MY (1) | MY119070A (en) |
TW (1) | TW296425B (en) |
ZA (1) | ZA965732B (en) |
Cited By (2)
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EP0838641A3 (en) * | 1996-10-24 | 1999-09-22 | Showa Aluminum Corporation | Evaporator |
WO2008064228A1 (en) * | 2006-11-22 | 2008-05-29 | Johnson Controls Technology Company | Multichannel evaporator with flow mixing microchannel tubes |
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DE10201511A1 (en) * | 2002-01-17 | 2003-07-31 | Behr Gmbh & Co | Welded multi-chamber tube |
WO2004015350A1 (en) * | 2002-08-09 | 2004-02-19 | Showa Denko K.K. | Flat tube and process for producing heat exchanger with use of the flat tube |
TWI468535B (en) * | 2012-11-20 | 2015-01-11 | Truan Sheng Lui | Method for inhibiting the diffusion of silicon by means of coarse aluminum crystals |
JP6243232B2 (en) * | 2014-01-17 | 2017-12-06 | 株式会社ティラド | Method of manufacturing fin for heat exchanger, fin and heat exchanger |
CN103968700B (en) * | 2014-05-26 | 2016-08-24 | 赵耀华 | A kind of high efficient heat exchanging water pipe and heat pipe radiant heating/refrigeration system |
CN108253827B (en) * | 2016-12-28 | 2020-06-23 | 神讯电脑(昆山)有限公司 | Aluminum extrusion type hot plate and manufacturing method thereof |
CN109097074B (en) * | 2018-10-15 | 2023-09-19 | 中冶焦耐(大连)工程技术有限公司 | Single-channel water supply bottom water-cooling coke quenching car and working method thereof |
CN109357545B (en) * | 2018-11-28 | 2024-05-31 | 博格华纳排放系统(宁波)有限公司 | Cooler for vehicle |
CN110670799B (en) * | 2019-10-10 | 2021-11-09 | 李居强 | Structural plate with cavity and manufacturing method thereof |
CN111192221B (en) * | 2020-01-07 | 2024-04-16 | 中南大学 | Aluminum electrolysis fire hole image repairing method based on deep convolution generation countermeasure network |
US11255610B2 (en) * | 2020-01-22 | 2022-02-22 | Cooler Master Co., Ltd. | Pulse loop heat exchanger and manufacturing method of the same |
JP2021125367A (en) * | 2020-02-05 | 2021-08-30 | 昭和電工株式会社 | Battery module |
WO2022145003A1 (en) * | 2020-12-28 | 2022-07-07 | 三菱電機株式会社 | Dehumidifying device |
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EP0338704A1 (en) * | 1988-04-13 | 1989-10-25 | Mitsubishi Aluminum Kabushiki Kaisha | Heat exchanger core |
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JP2718193B2 (en) * | 1989-07-08 | 1998-02-25 | 株式会社デンソー | Heat exchanger |
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US5323851A (en) * | 1993-04-21 | 1994-06-28 | Wynn's Climate Systems, Inc. | Parallel flow condenser with perforated webs |
-
1995
- 1995-07-07 JP JP7172007A patent/JPH0926278A/en active Pending
-
1996
- 1996-07-02 IN IN1218CA1996 patent/IN188905B/en unknown
- 1996-07-02 MY MYPI96002708A patent/MY119070A/en unknown
- 1996-07-03 AU AU58344/96A patent/AU711980B2/en not_active Ceased
- 1996-07-04 EP EP96110844A patent/EP0762070B1/en not_active Expired - Lifetime
- 1996-07-04 AT AT96110844T patent/ATE199456T1/en not_active IP Right Cessation
- 1996-07-04 ES ES96110844T patent/ES2154366T3/en not_active Expired - Lifetime
- 1996-07-04 CZ CZ19962008A patent/CZ293383B6/en not_active IP Right Cessation
- 1996-07-04 DE DE69611868T patent/DE69611868T2/en not_active Expired - Fee Related
- 1996-07-05 BR BR9602985A patent/BR9602985A/en not_active IP Right Cessation
- 1996-07-05 CN CN96108774A patent/CN1111717C/en not_active Expired - Fee Related
- 1996-07-05 AR ARP960103459A patent/AR002691A1/en unknown
- 1996-07-05 ZA ZA965732A patent/ZA965732B/en unknown
- 1996-07-05 TW TW085108124A patent/TW296425B/zh active
- 1996-07-05 CA CA002180598A patent/CA2180598C/en not_active Expired - Fee Related
- 1996-07-05 MX MX9602646A patent/MX9602646A/en not_active IP Right Cessation
- 1996-07-06 KR KR1019960027365A patent/KR100414852B1/en not_active IP Right Cessation
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DE2209325B2 (en) * | 1970-05-18 | 1977-12-08 | Noranda Metal Industries Ine, Bellingham, Wash. (V.StA.) | HEAT EXCHANGE PIPE |
DE3731669A1 (en) * | 1987-09-21 | 1989-04-06 | Sueddeutsche Kuehler Behr | Flat heat exchanger tube |
EP0338704A1 (en) * | 1988-04-13 | 1989-10-25 | Mitsubishi Aluminum Kabushiki Kaisha | Heat exchanger core |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0838641A3 (en) * | 1996-10-24 | 1999-09-22 | Showa Aluminum Corporation | Evaporator |
WO2008064228A1 (en) * | 2006-11-22 | 2008-05-29 | Johnson Controls Technology Company | Multichannel evaporator with flow mixing microchannel tubes |
US7802439B2 (en) | 2006-11-22 | 2010-09-28 | Johnson Controls Technology Company | Multichannel evaporator with flow mixing multichannel tubes |
Also Published As
Publication number | Publication date |
---|---|
IN188905B (en) | 2002-11-16 |
CA2180598A1 (en) | 1997-01-08 |
CZ293383B6 (en) | 2004-04-14 |
DE69611868D1 (en) | 2001-04-05 |
CN1140828A (en) | 1997-01-22 |
KR100414852B1 (en) | 2004-03-31 |
AU5834496A (en) | 1997-01-23 |
JPH0926278A (en) | 1997-01-28 |
CN1111717C (en) | 2003-06-18 |
KR970007278A (en) | 1997-02-21 |
MX9602646A (en) | 1997-06-28 |
EP0762070B1 (en) | 2001-02-28 |
AU711980B2 (en) | 1999-10-28 |
ATE199456T1 (en) | 2001-03-15 |
ES2154366T3 (en) | 2001-04-01 |
TW296425B (en) | 1997-01-21 |
CZ9602008A3 (en) | 1997-04-16 |
DE69611868T2 (en) | 2001-06-13 |
AR002691A1 (en) | 1998-03-25 |
ZA965732B (en) | 1997-01-23 |
CA2180598C (en) | 2007-06-05 |
MY119070A (en) | 2005-03-31 |
BR9602985A (en) | 1998-04-28 |
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