BACKGROUND OF THE INVENTION
1. Field of the Invention
[0001] The present invention relates to a refrigerant distributor for a heat exchanger and
a heat exchanger having the refrigerant distributor.
2. Description of the Related Art
[0002] A conventional micro-channel heat exchanger 2' generally comprises micro-channels
or flat tubes 5, fins 4 disposed between the adjacent micro-channels or flat tubes
5, an inlet manifold 3 and an outlet manifold (not shown) disposed at ends of the
micro-channels or flat tubes 5 respectively, and a refrigerant distributor 1' disposed
in the inlet manifold 3 as shown in Figs. 1-2. The refrigerant distributor 1' is disposed
at a side of the heat exchanger 2' to distribute refrigerant. The distributor 1' may
have a portion extending out of the inlet manifold 3 as shown in Fig. 1 or may have
no portion extending out of the inlet manifold 3.
[0003] In the conventional micro-channel heat exchanger 2', and especially in a micro-channel
evaporator, since refrigerant is two-phase refrigerant containing gas and liquid,
if an inappropriate refrigerant distributor is employed, the refrigerant can not be
uniformly distributed to the micro-channels or flat tubes 5.
[0004] The distributor 1' is composed of a cylindrical pipe that is inserted into the inlet
manifold 3, and a plurality of outlets 8 with the same size are arranged in the cylindrical
pipe at the same intervals in a longitudinal direction of the pipe as shown in Figs.
1-2. Refrigerant flows from the outlets 8 of the distributor 1' near the inlet 7 at
a high flow rate so that more refrigerant is distributed, but refrigerant flows from
the outlets 8 of the distributor 1' far from the inlet 7 at a low flow rate so that
less refrigerant is distributed.
[0005] The above distributor is disadvantageous in that since the flow rate gradually decreases
in a refrigerant flow direction R in which refrigerant flows in the distributor 1',
if a diameter (i.e., a cross-section area) of the pipe is uniform along its length,
a volume flow rate of the refrigerant Q is expressed as Q=VA, where V represents a
flow speed, and A represents a cross-section area of a distributor.
[0006] Therefore, the flow speed of the refrigerant gradually reduces in the refrigerant
flow direction R and thus the flow rate of the refrigerant flowing from the outlets
with the same size is decreased. More refrigerant is distributed from the outlets
near the inlet, and less refrigerant is distributed from the outlets far from the
inlet. Furthermore, after the flow speed reduces, the gas and liquid tend to be separated
from each other to cause non-uniform distribution of the refrigerant.
[0007] From
WO 94/14021 A1 a plate heat exchanger comprising a plurality of plates with plate holes that communicate
with refrigerant passages is known. In one embodiment the plate heat exchanger comprises
a tapered tube with holes which extends through the plate holes to introduce the refrigerant.
The tapered tube has a cross-sectional area that decreases from a refrigerant manifold
end to the opposite end of the tube.
[0008] EP 1 798 506 A2 shows a heat exchanger with an injecting pipe that comprises several openings. In
one embodiment the free flow cross-section of the injecting pipe decreases in the
flow direction.
[0009] In
DE 33 10 236 A1 a refrigerant distributor for an evaporator is disclosed. The refrigerant distributor
comprises several adjacently arranged inlet openings for a refrigerant consisting
of a distributor head attached to the evaporator and which has a longitudinal bore
and several cross-bores extending from the longitudinal bore. In one embodiment the
longitudinal bore is conical and has a decreasing cross-section in the flow direction.
This document discloses the features of the preamble of claim 1.
[0010] JP H05 264126 A discloses a tube for providing a refrigerant to a heat exchanger. The tube connects
a plurality of orifices in a longitudinal direction, leading to the micro-channels
of the heat exchanger. The inner free cross-sectional area of the tube is reduced
in the direction away from the inlet pipe by either introducing an insert or by reducing
the perimeter of the cross-sectional area by pressing and braising a side of the pipe.
SUMMARY OF THE INVENTION
[0011] It is an object of the present invention to provide a refrigerant distributor for
a heat exchanger and a heat exchanger having the refrigerant distributor which can
relatively uniformly distribute refrigerant.
[0012] In accordance with an aspect of the present application, there is provided a refrigerant
distributor for a heat exchanger. The distributor comprises: a pipe having an inlet
disposed generally at one end of the pipe, refrigerant flowing into the pipe through
the inlet, wherein a cross-section of a flow passage within the pipe gradually decreases
from the one end to the other end of the pipe, and wherein the pipe is configured
in such a manner that a cylindrical pipe is divided into a plurality of segments and
is at least partially pressed so that a cross-section of one of the plurality of segments
is narrower than that of the preceding one of the plurality of segments from the one
end to the other end of the pipe, and wherein the cross-sections of the pipe have
the same perimeter, but the cross-section area of the pipe gradually reduces in the
refrigerant flow direction, and wherein the cylindrical pipe is pressed to be more
flat gradually in the refrigerant flow direction.
[0013] In accordance with another aspect of the present application, there is provided a
heat exchanger. The heat exchanger comprises a refrigerant distributor disposed at
a side of the heat exchanger to distribute refrigerant, wherein the refrigerant distributor
is one of the distributors mentioned above.
[0014] With the above configuration, refrigerant can be distributed relatively uniformly.
BRIEF DESCRIPTION OF THE DRAWINGS
[0015] The advantages of the present invention will become apparent and more readily appreciated
from the following description of the embodiments, taken in conjunction with the accompanying
drawing.
Fig. 1 is a conventional micro-channel heat exchanger.
Fig. 2 is a sectional view taken along line A-A of Fig. 1.
Fig. 3 is a schematic view showing a micro-channel heat exchanger according to an
example not part of the invention.
Fig. 5 is a schematic view showing a refrigerant distributor for a micro-channel heat
exchanger according to an embodiment of the present application.
Fig. 6 is a schematic view showing a micro-channel heat exchanger according to an
example not part of the invention.
Fig. 7 is a schematic view showing a refrigerant distributor for a micro-channel heat
exchanger according to an example not part of the invention.
Fig. 8 is a schematic view showing a micro-channel heat exchanger according to the
third embodiment of the present application.
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0016] The embodiments are described below in order to explain the present invention, but
do not pose a limitation on the scope of the invention.
Exemple 1
[0017] A micro-channel heat exchanger 2 according to the first embodiment of the present
application comprises micro-channels or flat tubes 5, fins 4 disposed between the
adjacent micro-channels or flat tubes 5, an inlet manifold 3 and an outlet manifold
(not shown) disposed at ends of the micro-channels or flat tubes 5 respectively, and
a refrigerant distributor 1 disposed in the inlet manifold 3 as shown in Fig. 3. The
refrigerant distributor 1 is disposed at a side of the heat exchanger 2 to distribute
refrigerant.
[0018] The refrigerant distributor 1 for the heat exchanter1 comprises: a pipe 9 having
an inlet 7 disposed generally at one end of the pipe. Refrigerant flows into the pipe
through the inlet in use. A cross-section of a flow passage within the pipe 9 gradually
decreases from the one end to the other end of the pipe.
[0019] The pipe 9 comprises a plurality of segments 91, and a cross-section area of one
of the plurality of segments 91 is less than that of the preceding one of the plurality
of segments 91 from the one end to the other end of the pipe.
[0020] With the above distributor, the flow rate of the refrigerant gradually decreases
in the refrigerant flow direction R, but a cross-section area of the pipe also reduces
in the refrigerant flow direction R. It can be known from the formula Q=VA that a
flow speed of refrigerant is substantially uniform along the entire length of the
distributor and generally uniform amount of refrigerant is distributed from the outlets
with the same size. Therefore, the distributor can ensure that amounts of refrigerant
passing through the respective outlets are uniform.
Embodiment
[0021] A heat exchanger according to the second embodiment of the present invention is the
same as that of the first embodiment except a distributor 1. Only the distributor
1 is described below in detail.
[0022] The distributor 1 according to the second embodiment comprises a pipe 9. The pipe
9 is configured in such a manner that a cylindrical pipe is divided into a plurality
of segments 91 and is at least partially pressed so that a cross-section of one of
the plurality of segments 91 is narrower than that of the preceding one of the plurality
of segments from the one end to the other end of the pipe. In other words, the cylindrical
pipe is pressed to be more flat gradually in the refrigerant flow direction R. The
cross-sections of the pipe have the same perimeter, but the cross-section area of
the pipe gradually reduces in the refrigerant flow direction R as shown in Fig. 5.
[0023] With the above configuration of the distributor, the flow rate of the refrigerant
gradually decreases in the refrigerant flow direction R, but the cross-section area
of the pipe also reduces in the refrigerant flow direction R. It can be known from
the formula Q=VA that a flow speed of refrigerant is substantially uniform along the
entire length of the distributor and generally uniform amount of refrigerant is distributed
from the outlets with the same size. Therefore, the distributor can ensure that amounts
of refrigerant passing through the respective outlets are uniform.
Example
[0024] A micro-channel heat exchanger 2 according to the third embodiment of the present
application comprises micro-channels or flat tubes 5, fins 4 disposed between the
adjacent micro-channels or flat tubes 5, an inlet manifold 3 and an outlet manifold
(not shown) disposed at ends of the micro-channels or flat tubes 5 respectively, and
a refrigerant distributor 1 disposed in the inlet manifold 3 as shown in Figs. 6 and
8. The refrigerant distributor 1 is disposed at a side of the heat exchanger 2 to
distribute refrigerant.
[0025] The distributor 1 comprises a plurality of distributing pipes 9 (three pipes 9 are
shown in Figs. 6-8) having the same diameter and inserted into the inlet manifold
3 as shown in Figs. 6-8. The plurality of distributing pipes 9 have different lengths.
The first one of the plurality of distributing pipes 9 is shortest and is used for
distributing the refrigerant in a range from the inlet 7 to an end 11 of the first
pipe away from the inlet 7. The lengths of the remaining pipes 9 are increased successively
from the second one to the last one, and each of the remaining pipes is used for distributing
the refrigerant in a range from an end 11 of the preceding pipe 9 away from the inlet
7 to its end 11 away from the inlet 7, as shown in Fig. 7.
[0026] Each of the plurality of distributing pipes 9 is responsible for distributing refrigerant
to the same number of the micro-channels or flat tubes 5. In Fig. 7, reference numerals
8' indicate refrigerant flows distributed by the plurality of pipes 9. The pipes 9
shown in Fig. 7 do not contain the portions extending out of the heat exchanger 2
as shown in Fig. 6.
[0027] With the above configuration of the distributor, since each distributor pipe is responsible
for distributing refrigerant to fewer flat tubes, a number of the distributing outlets
is decreased. Therefore, the flow speed of the refrigerant within the distributor
is relative uniform.
[0028] Alternatively, a plurality of distributing pipes 9 are inserted into the inlet manifold
as shown in Fig. 8, but each of the plurality of distributing pipes 9 may be used
to distribute refrigerant to different numbers of flat tubes 5 according to the different
conditions as required, respectively. The flow rate of refrigerant can be distributed
by adjusting the cross-section area of each of the pipes 9 and/or size and number
of the outlets in each of the distributing pipes 9, or different combinations thereof.
When the heat exchanger having the distributor is used for domestic, commercial and
other applications, only the combination of the distributing pipes is adjusted to
improve the distribution of refrigerant conveniently.
[0029] In addition, the distributing pipe 9 may comprise any other number of pipes such
as two, four, and five pipes. The plurality of pipes 9 can be arranged horizontally
(as shown in Fig. 8), vertically (as shown in Fig. 6) or at any appropriate angle
or diagonally.
[0030] Although the above embodiments have been described, but other configuration may be
used to enable fluid to flow at a uniform flow speed within the distributing pipe.
For example, a cone-shape pipe can be used for the distributor.
[0031] In addition, in the above examples not according to the invention, the distributing
pipe 9 and the inlet manifold 3 are made of a cylindrical pipe, but they can be made
of pipe having any appropriate cross-section shape such as a pipe having elliptical
cross-section.
[0032] Furthermore, in the above embodiment, the micro-channel heat exchanger is described
and shown in a state that the micro-channel heat exchanger stands vertically only
for the purpose of convenient description and illustration. The present invention
is not limited to the examples shown in the figures. In addition, the outlet manifold
located on the above side of the micro-channel exchanger is omitted in the figures.
The distributing pipe 9 and the inlet manifold may be disposed on the above side of
the micro-channel exchanger shown in the drawings.
[0033] In addition, although the micro-channel heat exchanger is described in order to explain
the present invention, the principle and concept of the present invention can be applied
to any other appropriate heat exchangers.
[0034] Furthermore, the micro-channel heat exchanger or the heat exchanger according to
the embodiments of the present application can be used as an evaporator and the like.
[0035] Moreover, in the above embodiments, the distributing pipe 9 is inserted from one
end of the inlet manifold, but with regard to the distributing pipe 9 shown in Fig.
5, two distributing pipes 9 may be employed and inserted into the inlet manifold from
both ends of the inlet manifold respectively, and as for the distributor shown in
Fig. 7, two distributors may be employed and inserted into the inlet manifold from
both ends of the inlet manifold, respectively.
1. Kühlmittelverteiler für einen Wärmetauscher, der Folgendes umfasst: ein Rohr mit einem
Einlass, der allgemein an einem Ende des Rohrs angeordnet ist, wobei Kühlmittel durch
den Einlass in das Rohr strömt, wobei ein Querschnitt eines Strömungskanals in dem
Rohr von dem einen Ende zu dem anderen Ende des Rohrs allmählich abnimmt, wobei das
Rohr so konfiguriert ist, dass ein zylindrisches Rohr in mehrere Segmente unterteilt
ist, und dadurch gekennzeichnet, dass das Rohr zumindest teilweise zusammengepresst ist, so dass ein Querschnitt eines
der mehreren Segmente schmaler als der des vorhergehenden der mehreren Segmente von
dem einen Ende zu dem anderen Ende des Rohrs ist, und wobei die Querschnitte des Rohrs
denselben Umfang haben, sich die Querschnittsfläche des Rohrs jedoch in der Kühlmittelströmungsrichtung
allmählich verringert, und wobei das zylindrische Rohr dahingehend zusammengepresst
ist, dass es in der Kühlmittelströmungsrichtung allmählich flacher wird.
2. Wärmetauscher, der Folgendes umfasst: einen Kühlmittelverteiler, der auf einer Seite
des Wärmetauschers zur Verteilung von Kühlmittel angeordnet ist, wobei es sich bei
dem Kühlmittelverteiler um den Verteiler nach Anspruch 1 handelt.
3. Wärmetauscher nach Anspruch 2, wobei es sich bei dem Wärmetauscher um einen Mikrokanalwärmetauscher
handelt.