AU711980B2

AU711980B2 - Refrigerant tubes for heat exchangers

Info

Publication number: AU711980B2
Application number: AU58344/96A
Authority: AU
Inventors: Yuichi Furakawa; Shinji Ito; Koichi Take; Yuji Yamamoto
Original assignee: Showa Aluminum Corp
Current assignee: Resonac Holdings Corp
Priority date: 1995-07-07
Filing date: 1996-07-03
Publication date: 1999-10-28
Anticipated expiration: 2016-07-03
Also published as: CN1140828A; BR9602985A; ZA965732B; MX9602646A; EP0762070B1; CZ293383B6; CN1111717C; CZ9602008A3; IN188905B; MY119070A; CA2180598A1; ATE199456T1; ES2154366T3; AU5834496A; AR002691A1; DE69611868D1; EP0762070A1; KR970007278A; TW296425B; KR100414852B1

Description

0 1 1- P/00/0 1 1 Regulation 3.2

AUSTRALIA

Patents Act 1 990

ORIGINAL

COMPLETE SPECIFICATION STANDARD PATENT Invention Title: REFRIGERANT TUBES FOR HEAT EXCHANGERS 0.

.*so 0* eq.

softa The following statement is a full description of this invention, including the best method of performing it known to us: GH&CO REF: P17370-V:CAS:RK TITLE OF THE INVENTION REFRIGERANT TUBES FOR HEAT EXCHANGERS BACKGROUND OF THE INVENTION The present invention relates to tubes for passing a refrigerant therethrough, refrigerant tubes, for heat exchangers, and more particularly to refrigerant tubes for condensers and evaporators for use in air-cooling systems for motor vehicles.

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 15 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 20 pipe connected to the lower end of the right header, a l 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,

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S oS 7141 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 15 for use in the condenser have pressure resistance since

OOSO

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 20 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 2 passages in the interior of the tube. Air flows -2- 3 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.

It is therefore desirable to provide a refrigerant tube for use in heat exchangers which achieves a high heat exchange efficiency.

SUMMARY OF THE INVENTION The present invention provides a heat exchanger refrigerant tube comprising a flat aluminium tube having parallel refrigerant passages 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 flat aluminum tube being formed by joining upper and lower aluminum sheets so as to define a hollow portion by the two aluminum sheets, the reinforcing walls being formed by a ridge projecting inward from one of the upper and lower walls integrally therewith and joined to flat inner surface of the other wall, the reinforcing walls being each formed with a plurality of communication *o holes for causing the parallel refrigerant passages to communicate with one another therethrough, the communication holes are formed by cutouts formed in an edge of the ridge at a predetermined spacing and having their openings closed by the other wall, each of the reinforcing walls being 10 to 40% in opening ratio which is the proportion of an area of all the communication holes in the reinforcing wall to a surface area of the reinforcing wall.

4 The refrigerant preferably passes through the parallel refrigerant passages by flowing 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 9 ratio is limited to the range of 10 to 40% because if the *9 99 ratio is less than 10%, the thermal conductance does not a increase and further because the conductance no longer 20 increases even if the ratio exceeds 40%, entailing an increase only in coefficient of friction. The opening *999 ratio in the range of 10 to 40% is preferably 10 to .9 more preferably about ~The communication holes are preferably so sized in 25 cross section as to permit the refrigerant to smoothly flow therethrough between the adjacent passages, to be

S.

999 free of the likelihood of becoming clogged with a flow of S.9: solder during brazing and to in no way impair the pressure resistance of the tube. The pitch of the communication holes is preferably 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 Sdirection of the tube is preferably up to 4 mm. A lower 17370V/704 I M

M

5 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 is difficulty 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.

In the claims which follow and the preceding summary of the invention, except where the context requires otherwise due to express language or necessary implication, the word "comprising" is used in the sense of "including"; that is, the features specified may be associated with further features in various embodiments 15 of the invention.

BRIEF DESCRIPTION OF THE DRAWINGS ~A preferred embodiment of the present invention will *9 :now be described, by way of example only, with reference to the accompanying drawings in which: .9 i 20 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; 25 FIG. 3 is an enlarged view in section-taken along the line 3-3 in FIG. 1;

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.9 FIG. 4 is a cross sectional view showing how to S 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. 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; -6 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 0 @0~0

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S S S. 0050 @500 0@ 0* 0S 00 00 *0 0 0000 0

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55 *0 0 S. 6S 55 0 5* @0 5 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 15 Evaluation Test i, the relationship between the ooou o average quality X of refrigerant and the thermal conductance hA; FIG. 15 is a graph showing the result of Evaluation Test 2, the relationship between the 20 average quality X of refrigerant and the heat transfer coefficient h; ao..

FIG. 16 is a graph showing the result of Evaluation Test 3, 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 FIG. 17 is a graph showing the result of Evaluation Test 4, the relationship between the opening ratio and the heat transfer coefficient h at an average quality X of refrigerant of 20%, 50% or and the relationship between the opening ratio and the coefficient of friction f when the average quality X of refrigerant is FIG. 18 is a graph showing the result of Evaluation Test 5, the relationship between the refrigerant pressure loss APr and the quantity of heat radiated through unit front area, Q/Fa, as established 15 for condensers comprising refrigerant tubes; and oleo FIG. 19 is a front view showing a condenser wherein flat refrigerant tubes are used.

S C CDESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 19 shows a condenser comprising flat

SC.

20 refrigerant tubes embodying the invention. The condenser comprises a pair of headers 61, 62 arranged c. 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 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 63 between the right partition 68 and the outlet pipe 66 decreasing in this order. A refrigerant flowing into the inlet pipe 15 65 in a gas phase flows zigzag through the condenser o before flowing out from the outlet pipe 66 in a liquid phase.

S *The refrigerant tubes 63 for use in the above condenser are concerned with the present invention.

20 Refrgigerant tubes embodying the invention will be described below. The following embodiments are all to 40% in opening ratio which is the proportion of all communication holes in each reinforcing wall to the 5S reinforcing wall. The communication holes formed in a plurality of reinforcing walls are all in a staggered -9arrangement.

Embodiiment 1 This embodiment is shown in FIGS. 1 to 3. A refrigerant tube T1 for heat exchangers is formed by a S flat aluminum tube 7 having parallel refrigerant passages 6 in its interior and comprising flat upper and lower walls i, 2, left and right vertical side walls 3, 4 connected respectively between the left side edges of the upper and lower walls i, 2 and between the right i0 side edges thereof, and a plurality of reinforcing walls 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 15 rectangular communiction holes 8 for causing the parallel refrigerant passages 6 to communicate with each other S S e ".therethrough, The flat aluminum tube 7 is prepared from upper and lower two aluminum sheets 9, 10 by vertically 20 bending the lower sheet 10 at its opposite side edges, joining the bent side edges to the respective side edges of the upper aluminum sheet 9 so as to define a hollow eeso portion by the two aluminum sheets 9, S 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 i. 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 i.

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 13, 17. The upper roll 13 has parallel annular grooves 14 arranged at 15 a spacing, first small-diameter portions 15 formed at 5550 the respective outer sides of the arrangement of *grooves 14 and each having a periphery of the same

S.

diameter as the bottom faces of the grooves 14, and second small-diameter portions 16 positioned externally 20 of the respective first small-diameter portions 15 and

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having a smaller diameter and a greater width than the portions 15. The lower roll 17 is provided, at its

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e respective outer ends, with large-diameter portions 18 each having an outer end face flush with that of the 25 second small-diameter portion 16 and having a smaller eeee 25 second small-diameter portion 16 and having a smaller -11width 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. Thus, the rolling operation produces a rolled aluminum sheet 21.

As shown in FIGS. 5 and 6, the rolled aluminum sheet 21 is then passed between a pair of upper and 15 lower rolls 22, 24. The upper roll 22 has rectangular protrusions 23 arranged at a predetermined spacing at a position corresponding to each of the parallel annular

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:grooves 14 in the upper roll 13 for the preceding step.

This rolling operation forms rectangular cutouts 12 in 20 the upper edges of the respective ridges 11 at the predetermined spacing, whereby the lower aluminum sheet is obtained.

rego The multiplicity of protrusions 23 are in a a.

staggered arrangement so that the cutouts 12 are formed in the upper edges of the parallel ridges in a in the upper edges of the parallel ridges 11 in a -12staggered arrangement when seen from above.

The above method of producing the lower aluminum sheet 10 requires two steps for forming the ridges 11 having the cutouts 12. As shown in FIG. 7, however, these ridges 11 with the cutouts 12 can be formed by a single step by using in combination with the lower roller 17 of the first step an upper roll 26 which is formed in each of parallel annular grooves 14 with protrusions 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, the upper aluminum :i 15 sheet 9 has at each of its opposite side edge portions eb..

an upper surface in the form of a slope 27 slanting outwardly downward. With reference to FIG. 2, each side 4 edge portion of the upper aluminum sheet 9 is placed on the stepped part 20a of the upright portion 20 of the 20 lower aluminum sheet 10, and the thin wall 20b (indicated in a broken line) is crimped onto the slope 27 of the upper aluminum sheet 9. Subsequently, the lower surface of the upper sheet 9 is brazed to the stepped parts 4* 44 the upright portions 20 of the lower sheet 10 and to the top ends of the ridges thereof, whereby the the top ends of the ridges 11 thereof, whereby the -13refrigerant 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. The lower 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 the lower wall 2.

Embodiment 2 FIG. 9 shows this embodiment, a refrigerant tube T2 for use in heat exchangers. The tube T2 has the same construction as Embodiment 1 except that 15 the tube T2 has left and right side walls 28, 29 of o double structure, communication holes 30 in the form of "an inverted trapezoid,and a plurality of relatively low upward projections 31 integral with the lower wall 2, extending longitudinally thereof and spaced apart from 20 one another for giving a heat transfer surface of increased

S

area. The holes 30 can be provided by forming trapezoidal cutouts 32 in the upper edges of the ridges 11.

e r a The tube T2 comprises a flat aluminum tube 33, which is prepared by bending opposite side edges of upper and lower two aluminum sheets 34, 35, fitting the -14bent side edges of one of the two aluminum sheets 34, 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 sheets 34, Stated more specifically, the side walls 28, 29 are formed by the following method. Upright portions 36 having the same height as the reinforcing walls 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. As indicated in a broken line in FIG. 9, on the other hand, 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 15 of the upright portion 36 and projecting downward slightly beyond the lower surface of the lower wall 2.

4 The downward projections 37a of the depending portions S 37 are crimped onto the respective slopes 38 of the lower aluminum sheet 35, and the portions where the 20 upper and lower aluminum sheets 34, 35 are in contact with each other are brazed.

9.

r Embodiment 3 oe FIG. 10 shows this embodiment, 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 15 communication holes 5 is formed by the combination of a too pair of trapezoidal cutouts 45a, 45b. Such cutouts 45b are formed respectively in the lower edge of the do downward ridge 44a and the upper edge of the upward ridge 44b at a predetermined spacing.

9**9 20 Embodiment 4 FIG. 11 shows this embodiment, a heat exchange refrigerant tube T4, which has two kinds of 4@6* reinforcing walls 46. The walls 46 of one kind are each 66 formed by a downward ridge 46a inwardly projecting from an upper wall 1 and joined to a flat inner surface of a an upper wall 1 and joined to a flat inner surface of a -16lower 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 i. 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 i, 2. With the exception of this feature, the present embodiment is the same as Embodiment 3.

Embodiment FIG. 12 shows this embodiment, a heat exchanger refrigerant tube T5. The tube T5 has 15 reinforcing walls 48 which are formed by downward ridges eo :i0 48a inwardly projecting from an upper wall 1 and joined :%Soo a flat inner surface of a lower wall 2. Trapezoidal

S.

communication holes 49 are formed by providing trapezoidal cutouts 49a in the lower edges of the ridges 48a 20 at a predetermined spacing and closing the openings of 0° O the cutouts 49a with the lower wall 2. The present embodiment is the same as Embodiment 3 except for this 0005 **Gee feature.

Embodiment 6 25 FIG. 13 shows this embodiment, a heat -17exchange 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. Except for this feature, 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.

o oo oooo Examples of the invention will be described oooo 15 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.

Example 1 A refrigerant tube which is 508 mm in length, 20 16.5 mm in the distance between side walls 3, 4, 1 mm in the height between upper and lower walls i, 2, six in the number of reinforcing walls 5, 2.4 mm in the pitch -of reinforcing walls 5, 0.3 mm in the thickness of reinforcing walls 5, 1.6 mm in the pitch P of communication holes 8, 0.8 mm in the length L of communication -18holes 8, 0.2 mm in the height H of communication holes 8, and 10% in opening ratio.

Example 2 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.

Example 3 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.

Example 4 The same refrigerant tube as that of Example 1 except that the tube is 0.8 mm in the height of e eo eo. communication holes and 40% in opening ratio.

eooe 15 Comparative Example The same refrigerant tube as that of Example 1 except that the tube has no communication holes in the reinforcing walls.

Evaluation Test 1 20 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 heat transfer coefficient, A: the area of heat transfer surface inside the refriger- -19ant tube). The method of determination was as follows.

The refrigerant tube was placed in a cooling water channel, a refrigerant comprising HFCI34a 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 2 at 400 kg/m2- s, the refrigerant inlet temperature at 650 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 result is shown in FIG. 14, which reveals 9**9 that when the reinforcing walls are formed with 9**e o o 15 communication holes, the thermal conductance hA is greater at any value of average quality X than when no holes are formed.

Evaluation Test 2 The refrigerant tubes of Example 2 and 20 Comparative Example were used to determine the relation- *999 ship between the average quality X of refrigerant and the heat transfer coefficient h by the same method as 9 in Evaluation Test i. FIG. 15 shows the result.

9999 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.

Evaluation Test 3 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 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 i. FIG. 16 shows the result.

FIG. 16 indicates that at any value of average oo 15 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 Evaluation Test 4 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 c between the opening ratio and the heat transfer coefficient h at an average quality X of refrigrant of -21or 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 Evaluation Test 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 o oo 15 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 in front area, and opposite ends of each tube were connected to right 20 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 -22partition 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 parti- 15 tion 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 20 (five passes). The condensers were checked for the relationship between the refrigerant pressure loss APr 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 -23formed with communication holes at an opening ratio of 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.

or ooee o oo oo -24-

Claims

1. A heat exchanger refrigerant tube comprising a flat aluminium tube having parallel refrigerant passages 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 flat aluminimum tube being formed by joining upper and lower aluminum sheets so as to define a hollow portion by the two aluminum sheets, the reinforcing walls being 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, the reinforcing walls being each formed with a plurality of communication holes for causing the parallel refrigerant passages to communicate with one another therethrough, the communication holes are formed by cutouts formed in an edge of the ridge at a predetermined spacing and having their openings closed by the other wall, each of the reinforcing walls being 10 to 40% in opening ratio which is the proportion of an area of all :the communication holes in the reinforcing wall to a "surface area of the reinforcing wall.

2. A heat exchanger refrigerant tube as defined in .I 25 claim 1 wherein the opening ratio is 10 to

3. A heat exchanger refrigerant tube as defined in claim 1 wherein the opening ratio is about

4. A heat exchanger refrigerant tube as defined in any one of claims 1-3 wherein the communication holes are 30 rectangular or trapezoidal in shape.

5. A heat exchanger refrigerant tube as defined in any one of claims 1-3 wherein the communication holes formed in the plurality of reinforcing walls are in a staggered arrangement relative to an adjacent reinforcing wall.

6. A heat exchanger refrigerant tube as defined in claim 1 wherein the aluminum sheet comprises a brazing 26 sheet having a brazing filler metal layer over at least one of opposite surfaces thereof.

7. A heat exchanger refrigerant tube substantially as herein described with reference to one or more of the accompanying drawings. Dated this 27th day of April 1999 SHOWA ALUMINUM CORPORATION By their Patent Attorney GRIFFITH HACK CO. 99*e 9*9 .9 0. to t o 9 to 0 o .*9 99* o 0* 9 27 PAGES 27 TO 29 ARE INTENTIONALLY BLANK 0e** S S. S S S S. 9* S S S S 55 S S: 17370V/704