Information
-
Patent Grant
-
6349761
-
Patent Number
6,349,761
-
Date Filed
Wednesday, December 27, 200024 years ago
-
Date Issued
Tuesday, February 26, 200222 years ago
-
Inventors
-
Original Assignees
-
Examiners
- Bennett; Henry
- McKinnon; Terrell
Agents
-
CPC
-
US Classifications
Field of Search
US
- 165 150
- 165 151
- 165 152
- 165 153
- 165 181
- 165 182
- 165 DIG 503
-
International Classifications
-
Abstract
A fin-tube heat exchanger with a vortex generator is disclosed. The heat exchanger includes at least one heat transfer tube extending therethrough. A vortex generator is formed on the fin and includes a plurality of protuberance ribs projected from the fin and centralized with the heat transfer tube. An air flow inlet is defined between adjacent two of the protuberance ribs and an air flow outlet is defined between other adjacent two of the protuberance ribs. The air flow is guided from the air flow inlet, through channels defined between the vortex generator and the at least one heat transfer tube, and passes out of the air flow outlet, thereby speeding the air flow and promoting the heat transfer efficiency of a stagnation area behind the tube, and generating vortexes at the protuberance ribs and the air flow outlet for draining outer air into the surface for better air mixing and promoting the heat transfer efficiency of the fin.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a fin-tube fin of a heat exchanger, especially to a fin-tube fin having a vortex generator.
2. Description of the Prior Art
Traditional air conditioner generally contains a compressor, a condenser, an expansion valve, and an evaporator. Normally, a fin-tube heat exchanger is used as the heat exchanger of an air conditioner as shown in
FIG. 1. A
traditional fin-tube heat exchanger
1
comprises a plurality of fins
11
spaced apart from adjacent ones a proper distance for passing an air flow
13
through gaps between the fins
11
. A plurality of heat transfer tubes
12
extend through the fins
11
and each heat transfer tube
12
contains coolant flowing therein for heat dissipation. The main function of the heat exchanger is to facilitate heat exchange between the coolant in the heat transfer tubes
12
and the air around the heat transfer tubes
12
. The main function of the fins
11
is to increase the contacting area between the coolant and the air around.
It has been a long term effort in the air conditioner industry to promote the function of the heat exchanger in consideration of power conservation. Some of the published patents have disclosed technique about promoting the heat exchange efficiency of the fins but most of the designs focus on the improvement of the traditional louver type or slit type of fins. For example, in U.S. Pat. No. 4,817,709, issued on Apr. 4, 1989, a fin structure having a slant plate formed by stamping is disclosed. Specifically, the fin has a wavy shape in which several triangular slant plates are formed by stamping and enable the air flow to generate counter-rotating vortexes at two sides of the triangular slant plate. The triangular slant plate is specifically suitable for the wavy-shaped fin not for general shape. Moreover, the heat transfer efficiency caused by the counter-rotating vortexes at two sides of the triangular slant plate is doubtful.
In U.S. Pat. No. 5,207,270, issued on May 4, 1993, a fin-tube heat exchanger is disclosed which has curved angular protuberances and straight protuberances around heat transfer tubes of each fin of the fin-tube heat exchanger. The curved angular protuberances cooperate with the straight protuberances for improving the heat transfer efficiency of the heat exchanger. In U.S. Pat. No. 5,203,403, issued on Apr. 20, 1993, a fin-tube heat exchanger is disclosed which has elliptic protuberances formed around heat transfer tubes of each fin of the fin-tube heat exchanger for promoting the heat transfer efficiency. However, the manufacturing of the heat exchanger is very complicated and high cost therefore need to be improved.
SUMMARY OF THE INVENTION
The primary purpose of the present invention is to provide a new structure of a fin geometry of a heat exchanger which is simple and easily manufactured yet effective in heat transfer. The fin geometry has a vortex generator having a plurality of ribs formed around heat transfer tubes of the fin by which the air flow passing through the heat exchanger can form a vortex effect around the heat transfer tubes for strengthening the mixture of air around thus considerably improving the heat dissipation efficiency of the fin.
Another purpose of the present invention is to provide a new structure of a fin of a heat exchanger which utilizes a pattern of ribs of a vortex generator of the fin to create a vortex effect for increasing the mixture of air and promoting the heat transfer efficiency of a stagnation area behind the heat transfer tube while not increasing the pressure drop significantly. With this new structure, the function of the heat exchanger is promoted and the total operational efficiency of the air conditioner is thus increased.
According to one aspect of the present invention, there is provided a heat exchanger comprising a plurality of fins spaced from each other in parallel and adjacent ones of the fins allowing an air flow to pass through a gap therebetween. A plurality of heat transfer tubes extends through the fins. A vortex generator comprises a plurality of protuberance ribs formed on the fin and centralized with the heat transfer tube. An air flow inlet is defined between adjacent two of the protuberance ribs and an air flow outlet is defined between other adjacent two of the protuberance ribs.
In operation, the air flow is guided from the air flow inlet, through channels defined between the vortex generator and the heat transfer tube, and passes out of the air flow outlet, thereby speeding the air flow and promoting the heat transfer efficiency of a stagnation area behind the tube, and generating vortexes at the protuberance ribs and the air flow outlet for draining outer air into the surface for better air mixing.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1
is a perspective view of a traditional fin-tube heat exchanger;
FIG. 2
is a perspective view of a fin-tube heat exchanger in accordance with a first embodiment of the present invention;
FIG. 3
is an enlarged view of a portion of a fin of FIG.
2
and the heat transfer tube and vortex generator fixed on the fin;
FIG. 4
is a schematic view showing that a vortex generator is configured around a heat transfer tube for guiding air flow to form vortex around the heat transfer tube;
FIG. 5
is a cross-sectional view taken from line
1
—
1
of
FIG. 3
;
FIGS. 6A
to
6
F illustrate different designs of the protuberance ribs of the first embodiment of
FIG. 2
;
FIG. 7
is a plan view of a fin-tube heat exchanger in accordance with a second embodiment of the present invention;
FIG. 8
is a plan view of a fin-tube heat exchanger in accordance with a third embodiment of the present invention;
FIG. 9
is a cross-sectional view taken from line
2
—
2
of
FIG. 8
;
FIGS. 10A
to
10
F illustrate different designs of the protuberance ribs of the third embodiment of
FIG. 8
; and
FIG. 11
is a plan view of a fin-tube heat exchanger in accordance with a fourth embodiment of the present invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to
FIG. 2
, a fin-tube heat exchanger
2
in accordance with the present invention also comprises a plurality of fins
21
spaced away adjacent ones and a plurality of heat transfer tubes
22
extending through the fins
21
. An air flow may pass through a gap between adjacent fins
21
. A vortex generator
3
is formed around the heat transfer tube
22
for guiding the air flow
23
to create vortex around the heat transfer tube
22
in order to promote the dissipation efficiency of the fin
21
.
FIG. 3
is a partial enlarged view of
FIG. 2
, illustrating the fin
21
, the heat transfer tube
22
and the vortex generator
3
.
FIG. 4
is a schematic view showing that the vortex generator
3
is configured around the heat transfer tube
22
for guiding the air flow
23
to form vortex
25
around the heat transfer tube
22
.
FIG. 5
is a cross-sectional view taken from line
1
—
1
of FIG.
3
. In the first embodiment, the vortex generator
3
comprises two front protuberance ribs
31
a
,
31
b
and two rear protuberance ribs
31
c
,
31
d
. The front protuberance ribs
31
a
,
31
b
are symmetric with respect to the air flow
23
. Similarly, the rear protuberance ribs
31
c
,
31
d
are also symmetric with respect to the air flow
23
. Each protuberance rib
31
a
,
31
b
,
31
c
,
31
d
has a arc shape. The protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
are arranged around the heat transfer tube
22
. Specifically, the heat transfer tube
22
is the physical center of the four protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
. The protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
are projected from one face of the fin
21
and each protuberance rib forms an arc shape along an extended direction II of the fin
21
.
The protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
are spaced away from each other, wherein an air flow inlet
24
a
is defined between the two front protuberance ribs
31
a
,
31
b
, while an air flow outlet
24
b
is defined between the two rear protuberance ribs
31
c
,
31
d.
When the air flow
23
is guided from the inlet
24
a
to the outlet
24
b
, due to the affection of the protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
, the air flow
23
will be strengthened and passes through channels defined between the heat transfer tube
22
and the protuberance ribs
31
a
,
31
b
,
31
c
,
31
d
and force the wake lagged in the stagration area ,i.e., the outlet
24
b
, to move forward thereby increasing the heat transmission efficiency between the heat transfer tube
22
and the protuberance ribs
31
a
,
31
b
,
31
c
,
31
d.
Meanwhile, co-rotating or counter-rotating vertex
25
are formed at two sides of the air flow
23
and the outlet
24
b
for draining outer air into the fin
21
in order to promote the heat transfer effect.
Since the heat transfer effect is the poorest at the stagnation area, i.e., the outlet
24
b
, it has been improved considerably by the vortex generator
3
yet not increasing the pressure drop significantly.
The design of the first embodiment of the present invention is quite different from the traditional louver or slit fin, because the traditional structure promotes the heat transfer efficiency by damaging the heat boundary layer which causes a drawback of increasing the pressure drop significantly. The vortex generator can promote the heat transfer efficiency without introducing considerable pressure drop. In applications, the vortex generator is suitable for both plain and wavy fin.
The protuberance rib
31
a
,
31
b
,
31
c
,
31
d
may have different structures.
FIGS. 6A
to
6
F illustrate different structures of the protuberance ribs in cross-sectional views.
FIG. 6A
illustrates a protuberance rib
32
having two vertical side walls
321
and a horizontal top wall
322
connected between the vertical side walls
321
.
FIG. 6B
illustrates a protuberance rib
33
having two sloped side walls
331
and a horizontal top wall
332
connected between the sloped side walls
331
.
FIG. 6C
illustrates a protuberance rib
34
having a vertical side wall
321
connected to a curved wall
342
.
FIG. 6D
illustrates a protuberance rib
35
having two sloped walls
351
,
352
connected to form a triangular shape.
FIG. 6E
illustrates a protuberance rib
36
having a vertical wall
361
and a sloped wall
362
connected to the vertical wall
361
, wherein the sloped wall
362
is located between the vertical wall
361
and the heat transfer tube
22
.
FIG. 6F
illustrates a protuberance rib
37
having a vertical wall
371
and a sloped wall
372
connected to the vertical wall
371
, wherein the vertical wall
371
is located between the sloped wall
372
and the heat transfer tube
22
.
FIG. 7
is a plan view of a fin-tube heat exchanger in accordance with a second embodiment of the present invention. In the second embodiment, most of the structure is the same as that of the first embodiment except that the number of the protuberance ribs
38
in the second embodiment is increased compared to that of the first embodiment. For example, the number of the protuberance ribs
38
may be eight and each protuberance rib
38
has a corresponding one symmetric to the virtual line of the air flow. The air flow path, the vortex generating theory, and the heat transfer effect are the same to those of the first embodiment thus the description thereof is omitted herein.
FIG. 8
is a plan schematic view of a fin-tube heat exchanger in accordance with a third embodiment of the present invention. In the third embodiment, the fin
21
has four inner protuberance ribs
41
a
,
41
b
,
41
c
,
41
d
formed around the heat transfer tube
22
and centralized with the heat transfer tube
22
. The arrangement and shapes of the four inner protuberance ribs
41
a
,
41
b
,
41
c
,
41
d
are the same as those of the first embodiment shown in FIG.
4
. Four outer protuberance ribs
42
a
,
42
b
,
42
c
,
42
d
are also formed around and centralized with the heat transfer tube
22
and respectively correspond to the inner protuberance ribs
41
a
,
41
b
,
41
c
,
41
d
. Each outer protuberance rib
42
a
,
42
b
,
42
c
,
42
d
is spaced from each corresponding inner protuberance rib
41
a
,
41
b
,
41
c
,
41
d
a predetermined distance. The outer protuberance ribs
42
a
,
42
b
,
42
c
,
42
d
are projected from one side of the fin
21
, while the corresponding inner protuberance ribs
41
a
,
41
b
,
41
c
,
41
d
are projected from an opposite side of the fin
21
. The cross-sectional view thereof may be referred to FIG.
9
.
Except to the addition of the outer protuberance ribs
42
a
,
42
b
,
42
c
,
42
d
, the air flow path, the vortex generating theory, and the heat transmission effect are similar to those of the first embodiment. For example, there are two inner protuberance ribs
41
a
,
41
b
function as front inner protuberance ribs and an air flow inlet
43
a
is defined between the two front protuberance ribs
41
a
,
41
b
. Similarly, there are other two inner protuberance ribs
41
c
,
41
d
function as rear inner protuberance ribs and an air flow outlet
43
b
is defined between the two rear inner protuberance ribs
41
c
,
41
d.
Referring to
FIG. 9
, the inner protuberance ribs
41
a
,
41
d
are symmetric to the heat transfer tube
22
and the corresponding outer protuberance ribs
42
a
,
42
d
are also symmetric to the heat transfer tube
22
. The inner and outer protuberance ribs
41
a
,
42
a
forms a wave shape and same of the inner and outer protuberance ribs
41
d
,
42
d
. The corresponding pair of the inner and outer protuberance ribs may have different structures as shown in the cross-sectional views of
FIGS. 10A
to
10
F.
FIG. 10A
illustrates an inner protuberance rib
43
having two vertical side walls
431
and a horizontal top wall
432
connected between the vertical side walls
431
.
FIG. 10B
illustrates an inner protuberance rib
44
having two sloped side walls
441
and a horizontal top wall
442
connected between the sloped side walls
441
.
FIG. 10C
illustrates an inner protuberance rib
45
having a vertical side wall
451
connected to a curved wall
452
.
FIG. 10D
illustrates an inner protuberance rib
46
having two sloped walls
461
,
462
connected to form a triangular shape.
FIG. 10E
illustrates an inner protuberance rib
47
having a vertical wall
471
and a sloped wall
472
connected to the vertical wall
471
, wherein the sloped wall
472
is located between the vertical wall
471
and the heat transfer tube
22
.
FIG. 10F
illustrates an inner protuberance rib
48
having a vertical wall
481
and a sloped wall
482
connected to the vertical wall
481
, wherein the vertical wall
481
is located between the sloped wall
482
and the heat transfer tube
22
. The above mentioned inner protuberance ribs each has its corresponding outer protuberance rib projected to an opposite direction, while another pair of inner and outer protuberance ribs are symmetric to the heat transfer tube
22
as shown in
FIGS. 10A
to
10
F.
FIG. 11
is a plan view of a fin-tube heat exchanger in accordance with a fourth embodiment of the present invention. Similar to the third embodiment, a plurality of inner protuberance ribs
50
and outer protuberance ribs
51
are formed around and centralized with the heat transfer tube
22
. The only difference is that the number of the protuberance ribs
50
,
51
in this embodiment is more than that of the third embodiment.
In practice, the present invention can be used in air conditioners and air-cooled heat exchangers. The fin may be plain type or wavy type. The vortex generator of the present invention can cause a pair of co-rotating or counter-rotating vortex vortexes for draining outer new air into the surface of the heat exchanger in order to improve the heat transfer efficiency of the stagnation-lagged area behind the heat transfer tube thereby promoting the total heat transfer efficiency of the heat exchanger.
While the present invention has been described with reference to specific embodiments, the description is illustrative of the invention and is not to be construed as limiting the invention. Therefore, various modifications to the present invention can be made to the preferred embodiments by those skilled in the art without departing from the true spirit and scope of the invention as defined by the appended claims.
Claims
- 1. A heat exchanger comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising a plurality of protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, each of the protuberance ribs having an arcuate contour in a plane normal to the respective heat transfer tube, the plurality of arcuate protuberance ribs together forming a circular pattern concentrically spaced from the respective heat transfer tube, an air flow inlet being defined between an adjacent two of the protuberance ribs and an air flow outlet being defined between another adjacent two of the protuberance ribs; wherein the air flow is guided from the air flow inlet, through channels defined between the plurality of protuberance ribs and the heat transfer tube, and passes out of the air flow outlet, thereby speeding the air flow, and generating vortexes at the protuberance ribs and the air flow outlet for drawing outer air to the heat exchanger for air mixing.
- 2. A heat exchanger, comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising a plurality of protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, an air flow inlet being defined between an adjacent two of the protuberance ribs and an air flow outlet being defined between another adjacent two of the protuberance ribs, each protuberance rib having a vertical wall connected to a sloped wall and the vertical wall being located between a respective heat transfer tube and the sloped wall; wherein the air flow is guided from the air flow inlet, through channels defined between the plurality of protuberance ribs and the heat transfer tube, and passes out of the air flow outlet, thereby speeding the air flow, and generating vortexes at the protuberance ribs and the air flow outlet for drawing outer air to the heat exchanger for air mixing.
- 3. A heat exchanger, comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising a plurality of protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, an air flow inlet being defined between an adjacent two of the protuberance ribs and an air flow outlet being defined between another adjacent two of the protuberance ribs, each protuberance rib having a vertical wall connected to a sloped wall and the sloped wall being located between a respective heat transfer tube and the vertical wall; wherein the air flow is guided from the air flow inlet, through channels defined between the plurality of protuberance ribs and the heat transfer tube, and passes out of the air flow outlet, thereby speeding the air flow, and generating vortexes at the protuberance ribs and the air flow outlet for drawing outer air to the heat exchanger for air mixing.
- 4. A heat exchanger comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising (a) a plurality of inner protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, each of the inner protuberance ribs extending from a first surface of the corresponding fin in a first direction and having an arcuate contour in a plane normal to the respective heat transfer tube, the plurality of arcuate inner protuberance ribs together forming a circular pattern concentrically spaced from the respective heat transfer tube, a first air flow inlet being defined between an adjacent two of the inner protuberance ribs and a first air flow outlet being defined between another adjacent two of the inner protuberance ribs; and (b) a plurality of outer protuberance ribs formed on the corresponding fin around the centrally disposed heat transfer tube and in respective radial alignment with the inner protuberance ribs, each of the outer protuberance ribs extending from a second surface of the corresponding fin in a second direction, the second direction being opposite the first direction, each of the outer protuberance ribs having an arcuate contour in a plane normal to the respective heat transfer tube, the plurality of arcuate outer protuberance ribs together forming a circular pattern concentrically spaced from the circular pattern of the inner protuberance ribs, a second air flow inlet being defined between an adjacent two of the outer protuberance ribs and a second air flow outlet being defined between another adjacent two of the outer protuberance ribs; wherein the air flow is respectively guided from the first and second air flow inlets, through channels defined between the inner and outer protuberance ribs and between the inner protuberance ribs and the heat transfer tube, and respectively pass out of the first and second air flow outlets, thereby speeding the air flow and drawing wake lagged air in the first and second air flow outlets away from the first and second air flow outlet, and generating vortexes at the inner and outer protuberance ribs and the first and second air flow outlets for drawing outer air to the heat exchanger for air mixing.
- 5. A heat exchanger, comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising (a) a plurality of inner protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, a first air flow inlet being defined between an adjacent two of the inner protuberance ribs and a first air flow outlet being defined between another adjacent two of the inner protuberance ribs; and (b) a plurality of outer protuberance ribs formed on the corresponding fin around the centrally disposed heat transfer tube and in respective radial alignment with the inner protuberance ribs, a second air flow inlet being defined between an adjacent two of the outer protuberance ribs and a second air flow outlet being defined between another adjacent two of the outer protuberance ribs, each of the inner and outer protuberance ribs having a vertical wall connected to a curved wall; wherein the air flow is guided from the second and first air flow inlets, through channels defined between the inner and outer protuberance ribs and between the inner protuberance ribs and the heat transfer tube, and passes out of the first and second air flow outlets, thereby speeding the air flow and drawing wake lagged air in the first and second air flow outlets away from the first and second air flow outlet, and generating vortexes at the inner and outer protuberance ribs and the first and second air flow outlets for drawing outer air to the heat exchanger for air mixing.
- 6. A heat exchanger, comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising (a) a plurality of inner protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, a first air flow inlet being defined between an adjacent two of the inner protuberance ribs and a first air flow outlet being defined between another adjacent two of the inner protuberance ribs; and (b) a plurality of outer protuberance ribs formed on the corresponding fin around the centrally disposed heat transfer tube and in respective radial alignment with the inner protuberance ribs, a second air flow inlet being defined between an adjacent two of the outer protuberance ribs and a second air flow outlet being defined between another adjacent two of the outer protuberance ribs, each of the inner and outer protuberance ribs having a vertical wall connected to a sloped wall and the vertical wall being located between the heat transfer tube and the sloped wall; wherein the air flow is guided from the second and first air flow inlets, through channels defined between the inner and outer protuberance ribs and between the inner protuberance ribs and the heat transfer tube, and passes out of the first and second air flow outlets, thereby speeding the air flow and drawing wake lagged air in the first and second air flow outlets away from the first and second air flow outlet, and generating vortexes at the inner and outer protuberance ribs and the first and second air flow outlets for drawing outer air to the heat exchanger for air mixing.
- 7. A heat exchanger, comprising:a plurality of fins spaced from each other in parallel and allowing an air flow to pass through a gap therebetween; a plurality of heat transfer tubes extending through the fins; and a plurality of vortex generators respectively formed on the plurality of fins and corresponding to each of the plurality of heat transfer tubes, each of the vortex generators comprising (a) a plurality of inner protuberance ribs formed on a corresponding fin around a respective centrally disposed heat transfer tube, a first air flow inlet being defined between an adjacent two of the inner protuberance ribs and a first air flow outlet being defined between another adjacent two of the inner protuberance ribs; and (b) a plurality of outer protuberance ribs formed on the corresponding fin around the centrally disposed heat transfer tube and in respective radial alignment with the inner protuberance ribs, a second air flow inlet being defined between an adjacent two of the outer protuberance ribs and a second air flow outlet being defined between another adjacent two of the outer protuberance ribs, each of the inner and outer protuberance ribs having a vertical wall connected to a sloped wall and the sloped wall being located between the heat transfer tube and the vertical wall; wherein the air flow is guided from the second and first air flow inlets, through channels defined between the inner and outer protuberance ribs and between the inner protuberance ribs and the heat transfer tube, and passes out of the first and second air flow outlets, thereby speeding the air flow and drawing wake lagged air in the first and second air flow outlets away from the first and second air flow outlet, and generating vortexes at the inner and outer protuberance ribs and the first and second air flow outlets for drawing outer air to the heat exchanger for air mixing.
US Referenced Citations (3)
Number |
Name |
Date |
Kind |
4449581 |
Blystone et al. |
May 1984 |
A |
5706885 |
Kim |
Jan 1998 |
A |
5975199 |
Park et al. |
Nov 1999 |
A |
Foreign Referenced Citations (5)
Number |
Date |
Country |
2088544 |
Jun 1982 |
GB |
58-213192 |
Dec 1983 |
JP |
361006590 |
Jan 1986 |
JP |
61-83893 |
Apr 1986 |
JP |
62266391-A |
Nov 1987 |
JP |