[0001] The present invention relates to a refrigeration system comprising a refrigerant
circuit having a first heat exchanger, a compressor, a second heat exchanger, and
a separator connected to an outlet of the first heat exchanger.
[0002] In such a refrigeration circuit a refrigerant is circulated. Gaseous refrigerant
is compressed by the compressor. This leads to an increased temperature. When the
compressed refrigerant gas is guided through a heat exchanger, the so-called condenser,
it is cooled and changes from the gaseous state to a liquid state. The liquid refrigerant
is then supplied to the other heat exchanger, the so-called evaporator. In the evaporator
the refrigerant is evaporated while drawing heat from the ambient air or any other
fluid, so that the ambient air is cooled. The refrigerant leaving the evaporator returns
to the suction side of the compressor.
[0003] The refrigerant leaving the evaporator or first heat exchanger is in many cases not
fully gaseous. It contains as well refrigerant in liquid form. The liquid phase of
the refrigerant may be up to 30 % of the whole refrigerant leaving the evaporator.
This liquid refrigerant must be removed from the refrigerant flow in order to avoid
a situation in which liquid enters the compressor. Liquid entering the compressor
can damage or destroy the compressor. To this end, the separator is used.
[0004] In some applications the space available for the separator is limited. Thus, the
size of the separator is limited as well. This makes it difficult to reliably remove
all liquid from the refrigerant flow.
[0005] The object underlying the invention is to remove liquid from the refrigerant flow
even with limited size of the separator.
[0006] This object is solved with a refrigeration system as described at the outset in that
the separator comprises at least two flow paths arranged in parallel between an inlet
and an outlet.
[0007] Such a design has more than one flow path in the separation zone. The use of two
or more flow paths arranged in parallel has the effect that the velocity of the refrigerant
flow is decreased so that the liquid has more time to "fall" out of the refrigerant
flow. Thus, the length of the flow path can be reduced correspondingly. Furthermore,
when the flow paths have a circular section, the diameter of this section can be reduced
and correspondingly the height of the separator can be kept small while maintaining
the same area of the flow paths.
[0008] In an embodiment of the invention the flow paths are inclined in the same direction
from the inlet to the outlet. In other words, the outlet is arranged in a position
higher than the position of the inlet in the direction of gravity. Thus, liquid refrigerant
removed from the refrigerant flow can flow back in direction towards the inlet under
the action of gravity. Thus, the liquid refrigerant can be removed from the separator.
[0009] In an embodiment of the invention the flow paths have the same angle of inclination.
Such an angle can be rather small, for example 5° or 10°. Liquid removed from the
refrigerant flow has the same conditions in all flow paths to flow back to the input.
[0010] In an embodiment of the invention the flow paths have the same lengths. This is a
simple design to make the flow resistance in all flow paths equal or almost equal.
[0011] In an embodiment of the invention the separator is symmetrical with respect to a
line connecting the inlet and the outlet. In such a construction the flow through
the flow paths can be made the same through all flow paths.
[0012] In an embodiment of the invention each flow path comprises at least one curvature.
Such a curvature provides a benficial flow path for the separation. The creation of
turbulence is avoided or at least reduced helping the separation of the gaseous and
the liquid refrigerant.
[0013] In an embodiment of the invention the number of flow paths is two. Although this
is a rather small number, the area available for the flow is sufficient to pass the
refrigerant flow with a velocity which is low enough to give the refrigerant liquid
enough time to fall out of the flow.
[0014] In an embodiment of the invention the flow paths are arranged in tubes, wherein the
tubes surround a tube free space. The tubes form a kind of "donut", which is a simple
constructional solution.
[0015] In an embodiment of the invention the tubes are arranged in form of a rectangle,
wherein the inlet and the outlet are arranged at opposite sides of the rectangle.
The rectangle will have rounded or squared corners. Such a rectangle form of the separator
can easily be made by using generally available semi-finished products.
[0016] In an embodiment of the invention the first heat exchanger comprises a refrigerant
inlet connected to a connecting pipe and a refrigerant outlet connected to the connecting
pipe, wherein the inlet of the separator is connected to the connecting pipe. Refrigerant
in liquid form can be supplied to the connecting pipe up to a certain level. This
has the effect that the same level of liquid refrigerant is available within the first
heat exchanger. This refrigerant is at least partly evaporated in the first heat exchanger
and escapes at the refrigerant outlet. From there, the refrigerant flow consisting
of a gaseous phase and of a liquid phase enters the separator. Liquid refrigerant
removed from the refrigerant flow in the separator can flow back to the connecting
pipe.
[0017] In an embodiment of the invention the connecting pipe is arranged in parallel to
the direction of gravity. Thus, the connecting pipe is arranged vertically. Liquid
refrigerant removed from the refrigerant flow can directly flow down to the refrigerant
inlet of the first heat exchanger.
[0018] In an embodiment of the invention coalescing means are arranged in a region at the
inlet. Thus, the refrigerant flow is guided through the coalescing means. The coalescing
means have the effect that liquid droplets contained in the refrigerant flow combine
into larger drops or droplets so that it is easier to remove these droplets.
[0019] In an embodiment of the invention the coalescing means comprise a mesh, preferablymade
of metal. Other materials are possible. This is a simple design of coalescing means.
[0020] In addition or alternatively, impingement means are arranged in a region at the inlet.
Impingement means can be formed by a surface which is arranged perpendicular or almost
perpendicular to a flow direction of the refrigerant flow. Thus, drops of liquid refrigerant
hit the surface and can be removed from the surface by gravity.
[0021] The invention is now described in more detail with reference to the drawing, wherein:
- Fig. 1
- shows a schematic illustration of a refrigeration system,
- Fig. 2
- shows a front view of a heat exchanger with separator and
- Fig. 3
- shows a top view of the separator.
[0022] Fig. 1 schematically shows a refrigeration system 1 comprising a refrigerant circuit
having a first heat exchanger 2, a compressor 3, a second heat exchanger 4 and a separator
5.
[0023] Furthermore, in the embodiment shown, the refrigerant circuit comprises an accumulator
6.
[0024] The first heat exchanger 2 is a plate heat exchanger. However, other types of heat
exchangers can be used. The first heat exchanger comprises a refrigerant inlet 7 and
a refrigerant outlet 8. A connecting pipe 9 is connected to the refrigerant inlet
7 and to the refrigerant outlet 8. The connecting pipe 9 comprises an oil drain 10.
Furthermore, the connecting pipe 9 comprises an expansion valve 11 through which refrigerant
in liquid form from the accumulator 6 can be supplied into the connecting pipe 9.
The expansion valve can be of a float type or another type, controlled by a liquid
level measurement.
[0025] The connecting pipe 9 is oriented in vertical direction (corresponding to the direction
of gravity). The liquid level in the connecting pipe 9 is controlled to provide a
driving force to move refrigerant through the heat exchanger.The liquid refrigerant
in the first heat exchanger 2 evaporates. The evaporation needs substance to be cooled,
which could be heat which is withdrawn from another fluid circulating through a secondary
side of the first heat exchanger 2, a product contained in the first heat exchanger
2 or from ambient air around the first heat exchanger 2. The column of liquid refrigerant
within the connecting pipe 9 drives the refrigerant out of the refrigerant outlet
8 to an upper part of the column 9. However, this refrigerant flow is not in all cases
totally gaseous. In most cases it comprises a gaseous phase and a liquid phase. However,
the liquid phase must not arrive at the compressor 3, since the compressor 3 can be
damaged or destroyed, when liquid enters the compressor 3.
[0026] The compressor 3 compresses the gaseous refrigerant. This compression leads to an
elevated temperature and pressure of the gaseous refrigerant. The gaseous refrigerant
with elevated temperature is guided through the second heat exchanger 4, wherein the
heat of the gaseous refrigerant is transferred to a secondary fluid, such as the ambient
air, water or glykol. The temperature of the refrigerant is lowered and the refrigerant
is liquified and guided to the accumulator 6.
[0027] In order to remove the liquid phase from the refrigerant flow before the refrigerant
flow enters the compressor 3, the separator 5 is used.
[0028] The separator 5 comprises an inlet 12 connected to the connecting tube 9 and an outlet
13 connected to the compressor 3.
[0029] As can be seen in Fig. 3, the separator 5 is in form of a donut, i.e. it forms a
rectangle having rounded corners. More precisely, the separator provides two flow
paths 14, 15. The flow path 14 is arranged within a tube 16 and the flow path 15 is
arranged within a tube 17. Both tubes 16, 17 are connected in the region of the inlet
12 and in the region of the outlet 13. Both tubes 16, 17 have the same length and
are inclined upwardly from the inlet 12 towards the outlet 13. The angle of inclination
for both tubes 16, 17 is the same. This angle is in a region from 1° to 20°.
[0030] The separator 5 is symmetrical with respect to a line 18 connecting the inlet 12
and the outlet 13. This means that both flow paths 14, 15 have the same flow resistance.
[0031] As mentioned above, the separator 5 is in form of a rectangle. The inlet 12 and the
outlet 13 are arranged at opposite sides of the rectangle. The rectangle has rounded
corners, so that each flow path comprises two curvatures 19, 20 (for flow path 14)
and 21, 22 (for flow path 15). A space 23 within the rectangle is kept free from tubes.
[0032] The inlet 12 is arranged in vertical direction at the upper end of the connecting
tube 9. Since the inlet 12 is arranged in the axis of symmetry of the separator 5,
the separator 5 is symmetric with respect to a plane intersecting the connecting tube
9.
[0033] Coalescing means 24 and/or impingement means 25 are arranged in a region at the inlet.
Other locations are possible.
[0034] When the refrigeration system 1 is operated, refrigerant comes out of the refrigerant
outlet 8 of the first heat exchanger 2 or evaporator. The flow of refrigerant having
a liquid phase and a gaseous phase is guided through the separator 5. In the separator
5 the refrigerant flow flows along the two flow paths 14, 15. Due to the fact that
two flow paths 14, 15 are arranged in parallel, the velocity of the refrigerant flow
is reduced so that liquid refrigerant can separate from the gaseous refrigerant. This
is supported by the coalescing means 24 and/or the impingement means 25.
[0035] Liquid refrigerant removed from the refrigerant flow comes to the bottom of the tubes
16, 17. Since the tubes 16, 17 are inclined, the liquid refrigerant flows back to
the input 12 and from there to the connecting tube 9, so that it can directly enter
the first heat exchanger 2.
[0036] If this is not desired, it is of course possible to use additional piping to connect
a liquid drain of the separator 5 with a position in the refrigerant system downstream
the compressor 3.
1. Refrigeration system (1) comprising a refrigerant circuit having a first heat exchanger
(2), a compressor (3), a second heat exchanger (4), and a separator (5) connected
to a refrigerant outlet (8) of the first heat exchanger (2), characterized in that the separator (5) comprises at least two flow paths (14, 15) arranged in parallel
between an inlet (12) and an outlet (13).
2. Refrigeration system according to claim 1, characterized in that the flow paths (14, 15) are inclined in the same direction from the inlet (12) to
the outlet (13).
3. Refrigeration system according to claim 2, characterized in that the flow paths (14, 15) have the same angle of inclination.
4. Refrigeration system according to any of claims 1 to 3, characterized in that the flow paths (14, 15) have the same length.
5. Refrigeration system according to any of claims 1 to 4, characterized in that the separator (5) is symmetrical with respect to a line (18) connecting the inlet
(12) and the outlet (13).
6. Refrigeration system according to any of claims 1 to 5. characterized in that each flow path (14, 15) comprises at least one curvature (19-22).
7. Refrigeration system according to any of claims 1 to 6, characterized in that the number of flow paths (14, 15) is two.
8. Refrigeration system according to claim 7, characterized in that the flow paths (14, 15) are arranged in tubes (16, 17), wherein the tubes (16, 17)
surround a tube free space (23).
9. Refrigeration system according to claim 8, characterized in that the tubes (16, 17) are arranged in form of a rectangle, wherein the inlet (12) and
the outlet (13) are arranged at opposite sides of the rectangle.
10. Refrigeration system according to any of claims 1 to 9, characterized in that the first heat exchanger (2) comprises a refrigerant inlet (7) connected to a connecting
pipe (9) and the refrigerant outlet (8) is connected to the connecting pipe (9), wherein
the inlet (12) of the separator (5) is connected to the connecting pipe (9).
11. Refrigeration system according to claim 10, characterized in that the connecting pipe (9) is arranged in parallel to the direction of gravity.
12. Refrigeration system according to any of claims 1 to 11, characterized in that coalescing means (24) are arranged in a region at the inlet (12).
13. Refrigeration system according to claim 12, characterized in that the coalescing means (24) comprise a mesh made of metal.
14. Refrigeration system according to any of claims 1 to 13, characterized in that impingement means (25) are arranged in a region at the inlet.