Evaporator for refrigerating machine and refrigeration apparatus

Information

  • Patent Grant
  • 6655173
  • Patent Number
    6,655,173
  • Date Filed
    Friday, July 19, 2002
    21 years ago
  • Date Issued
    Tuesday, December 2, 2003
    20 years ago
Abstract
An evaporator for a refrigerating system which prevents droplets of refrigerant from blowing upwards, and a refrigeration apparatus using thereof are provided. The evaporator for a refrigerating system includes a container into which the refrigerant is introduced, and heat exchanger tubes disposed in the container through which a cooled object flows. The evaporator further includes a prevention plate disposed above the heat exchanger tubes so that droplets of the refrigerant, which are blown upwards due to a boiling of the refrigerant, hit the prevention plate.
Description




TECHNICAL FIELD




The present invention relates to an evaporator for a refrigerating system which refrigerates an object to be cooled (e.g., water, brine, etc.) by exchanging heat between the object and the refrigerant, and a refrigeration apparatus using the evaporator.




BACKGROUND ART




In a structure of large scale, such as a tall building, cool water, which has been chilled by a refrigerating system, is circulated through a pipe arrangement disposed in the structure so that heat is exchanged between the cool water circulating in the pipe arrangement and air present in the spaces of the structure to decrease the temperature of the spaces.





FIG. 8

is a diagram showing an example of a conventional evaporator which may be provided with a refrigerator. In this evaporator, a plurality of bundles of heat exchanger tubes


2


through which water passes is disposed in a staggered form in a cylindrical container


1


into which a refrigerant is introduced.




The plurality of heat exchanger tubes


2


may be divided into two groups, namely, a group of entering tubes which communicate with a water entrance


3


and a group of exiting tubes which communicate with a water exit


4


. Water enters from the water entrance


3


, passes through heat exchanger tubes


2


of the entering tube group in the container


1


to reach a water chamber (not shown in the figure), and then passes through the heat exchanger tubes


2


of the exiting tube group to exit from the water exit


4


. During this process, water is cooled down by heat exchange with the refrigerant introduced into the container


1


, and the refrigerant which received heat from the water, in turn, boils and vaporizes.




The vaporized refrigerant is then compressed in a compressor, which is not shown in the figure, and transferred to a condenser.




In the above-mentioned type of evaporator, however, when the refrigerant is boiled around the heat exchanger tubes


2


and vapor is generated, droplets of the refrigerant are often blown upwards by the force of the refrigerant vapor. Then, some of these droplets of refrigerant are sometimes drawn into the above-mentioned compressor and cause problems, such as a decrease in the performance of the compressor or damage to an impeller.




Although attempts have been made to create open passages (i.e., spaces among heat exchanger tubes) along the bundle of the heat exchanger tubes in an up-and-down direction as pathways for bubbles generated when the refrigerant boils, the force of the refrigerant vapor blown upwards from the opening of the passages is increased in this case.




Accordingly, one of the objects of the present invention is to provide an evaporator for a refrigerating system, which is capable of preventing blown upwards of droplets of the refrigerant, and a refrigeration apparatus using the evaporator.




DISCLOSURE OF INVENTION




The present invention provides an evaporator for a refrigerating system including a container into which a refrigerant is introduced, and heat exchanger tubes disposed in the container through which an object to be cooled down flows, comprising: a prevention plate disposed above the heat exchanger tubes so that droplets of the refrigerant, which are blown upwards due to boiling of the refrigerant, hit the prevention plate and are prevented from proceeding beyond the prevention plate.




In accordance with another aspect of the invention, the heat exchanger tubes are divided into a plurality of vertically spaced groups so that a space is formed between the groups of the heat exchanger tubes in vertical direction; and the prevention plate is disposed above the space.




In yet another aspect of the invention, the distance between the prevention plate and the heat exchanger tubes at an uppermost level is about 0.5 to 2 times the diameter of a heat exchanger tube which is located at the uppermost level.




In yet another aspect of the invention, the prevention plate has a cross section shaped like an inverted letter “V”, “U”, “W”, etc., and the angle of the prevention plate is designed to be between about 60° and 120°.




In yet another aspect of the invention, an end portion of the prevention plate covers at least a part, preferably, half or all, of a heat exchanger tube which is located at the uppermost level of the heat exchanger tubes and is adjacent to the prevention plate.




In yet another aspect of the invention, a group of the heat exchanger tubes facing an inner surface of the container is disposed so that a space is formed between the group of the heat exchanger tubes and the container along the inner surface of the container; and a prevention plate is disposed above the space.




The present invention also provides a refrigeration apparatus, comprising: a compressor for compressing a refrigerant; a condenser for condensing and liquefying the refrigerant which is compressed in the compressor; a throttling mechanism for reducing the pressure of the liquefied refrigerant; and an evaporator for cooling down an object to be cooled by exchanging heat between the object to be cooled and a resultant condensed and pressure-reduced liquefied refrigerant, and evaporating and vaporizing the liquefied refrigerant, wherein the evaporator is one of the above-mentioned evaporators.











BRIEF DESCRIPTION OF DRAWINGS





FIG. 1

is a diagram showing a schematic structure of a refrigerating system to which an evaporator according to an embodiment of the present invention may be applied.





FIG. 2

is a diagram showing a cross-sectional view of the refrigerating system shown in

FIG. 1

cut along the II—II line.





FIG. 3

is a diagram showing a partial enlarged cross-sectional view of the arrangement of a prevention plate having a cross section substantially shaped as an inverted letter “V”.





FIG. 4

is a diagram showing a partial enlarged cross-sectional view of the arrangement of a flat prevention plate.





FIG. 5

is a diagram showing a partial enlarged cross-sectional view of the arrangement of a plurality of the prevention plates.





FIG. 6

is a perspective view to explain the structure and construction of an evaporator in a refrigeration apparatus according to an embodiment of the present invention.





FIG. 7

is a schematic piping diagram to explain the configuration of the evaporator in the refrigeration apparatus according to an embodiment of the present invention.





FIG. 8

is a diagram showing an example of a conventional evaporator which may be provided with a refrigerator.











BEST MODE FOR CARRYING OUT THE INVENTION




The evaporator for a refrigerating system according to embodiments of the present invention will be described with reference to the accompanying drawings.





FIG. 1

is a diagram showing a schematic structure of a refrigerating system according to an embodiment of the present invention. The refrigerating system includes a condenser


10


, an expansion valve (throttle valve)


11


, an evaporator


12


, and a compressor


13


. The condenser


10


condenses and liquefies a refrigerant by exchanging heat between cooling water (the cooled object) and the refrigerant which may be in a vapor phase. The expansion valve


11


decreases the pressure of the condensed refrigerant. The evaporator


12


refrigerates the cooling water by exchanging heat between the cooling water and the condensed refrigerant. The compressor


13


compresses the refrigerant, which has been evaporated and vaporized in the evaporator


12


, and supplies it to the above-mentioned condenser


10


. The cooling water refrigerated in the evaporator


12


may be utilized, for instance, for air-conditioning in a building.





FIG. 2

is a diagram showing a cross-sectional view of the refrigerating system shown in

FIG. 1

cut along the II—II line indicated by arrows. As shown in

FIG. 2

, the evaporator


12


includes a cylindrical container


14


into which a refrigerant is introduced, and a plurality of bundles of heat exchanger tubes


15


disposed in the container


14


.




The plurality of heat exchanger tubes


15


is disposed in the longitudinal direction (i.e., a vertical direction with respect to the sheet surface of

FIG. 2

) of the container


14


and function as pathways for cooling water, which is the cooled object. The heat exchanger tubes


15


are divided into groups, namely, a group of entering tubes which communicate with a cooling water entrance


16




a


and a group of exiting tubes which communicate with a cooling water exit


16




b


shown in FIG.


1


. The direction of the flow of cooling water in the heat exchanger tubes


15


communicating with the cooling water entrance


16




a


is different from the direction of the flow of cooling water in the heat exchanger tubes


15


communicating with the cooling water exit


16




b.






The plurality of heat exchanger tubes


15


may be divided into a plurality of groups, for instance, four, (i.e., groups of tubes A-D as shown in

FIG. 2

) in the lower half of the container


14


. A space


17


is formed between each of the groups A-D of the heat exchanger tubes


15


in a vertical direction, and a space


18


is formed between the group A and the container


14


along the inner surface of the container


14


, and between the group D and the container


14


along the inner surface of the container


14


. Note that the above-mentioned spaces


17


and


18


are hereinafter referred to as passages


17


and


18


since it may be regarded that they are formed by extracting the corresponding heat exchanger tubes


15


which may be present there originally.




A prevention plate


19


having an inverted “V” cross sectional shape is disposed above each of the passage


17


. Also, a blow-up prevention plate


20


, which may have a flat shape, is disposed above each of the passage


18


. The shape of the prevention plates


19


and


20


is not particularly limited, and any suitable shape, such as inverted “U” and “W”, can be used.




As shown in the enlarged view of

FIG. 3

, the vertical angle θ of the prevention plate


19


in this embodiment is designed to be between about 60° and 120°. The prevention plate


19


is disposed at a position above the passage


17


so that the right and left portions, respectively, of the prevention plate


19


cover at least a part, preferably, half or all, of the corresponding adjacent heat exchanger tube


15


at the uppermost level, and that the distance between the right and left edge portions, respectively, of the prevention plate


19


and the corresponding heat exchanger tube


15


be 0.5 to 2 times the diameter D of the heat exchanger tube


15


.




On the other hand, as shown in the enlarged view of

FIG. 4

, the prevention plate


20


is disposed above the heat exchanger tube


15


so that the edge portion thereof covers at least a part of the corresponding adjacent heat exchanger tube


15


at the uppermost level, and that the distance between the edge portion of the prevention plate


19


and the corresponding heat exchanger tube


15


be 0.5 to 2 times the diameter D of the heat exchanger tube


15


.




Note that although the end portion of the prevention plate


20


is downwardly bent in order to stop the upward flow from the passage


18


in the above embodiment, the prevention plate


20


may have a flat shape and no problems would be caused by the use of such a prevention plate


20


.




The number of the heat exchanger tubes


15


contained in the groups A-D in the above embodiment may be chosen to be, for instance, five hundreds. Also, the heat exchanger tubes


15


in each of the groups A-D may be arranged in a staggered manner. That is, the heat exchanger tubes


15


at an upper level are shifted by about half of the distance, i.e., ½ offset, between each other in the transverse direction with respect to the heat exchanger tubes


15


at the next lower level.




In the evaporator


12


having the above-mentioned configuration, the refrigerant is introduced into the container


14


via a lower portion thereof. Since the refrigerant boils when heat is exchanged between cooling water flowing through the heat exchanger tubes


15


and itself, vapor of the refrigerant is generated around the heat exchanger tubes


15


, which are mainly located at a lower portion of each of the groups A-D, and rises to the surface through the passages


17


or


18


.




Although the vapor and droplets of refrigerant bubbles up vigorously from the opening of the passages


17


, the ascent rate thereof is significantly reduced when the vapor and droplets hit the above-mentioned prevention plates


19


and


20


.




As a result, only the vapor of the evaporated refrigerant exits the container


14


via the demister


21


. That is, it becomes possible to prevent the droplets of refrigerant from being supplied to the compressor


13


shown in FIG.


1


. Note that the above-mentioned vapor of the refrigerant is supplied to the compressor


13


and is compressed.




As mentioned above, according to the evaporator of this embodiment of the present invention, since the prevention plates


19


and


20


prevent the droplets of refrigerant being blown upwards beyond the plates


19


and


20


in the container


14


, the droplets of refrigerant are not drawn into the compressor


13


. Accordingly, it becomes possible to avoid problems, such as a decrease in the performance of the compressor or damage to an impeller.




Note that although the prevention plates


19


and


20


are disposed only above the passages


17


and


18


in the above-mentioned embodiments, droplets of refrigerant may sometimes be blown upwards by bubbles of the refrigerant which ascend between the heat exchanger tubes


15


in each of the groups A-D. Accordingly, the prevention plates


19


may be disposed so as to cover all of the heat exchanger tubes


15


of the groups A-D as shown in FIG.


5


. In this manner, it becomes possible to assuredly prevent the droplets of refrigerant from entering the compressor


13


.




In this embodiment, although each of the prevention plates


19


is disposed so as to be vertically shifted relative to each other and to overlap, when viewed from the above, with adjacent prevention plates


19


, it is possible to arrange the prevention plates


19


in a different manner.




Also, although the passages


17


and


18


are provided in order to decrease the amount of bubbles in each of the tube groups A-D in the evaporator


12


according the above-mentioned embodiments, the present invention, which can prevent the droplets of refrigerant from blowing upwards, may also be effectively and suitably applied to an evaporator having no passages


17


and


18


.




The heat exchanger tubes


15


are arranged in the staggered manner in each of the groups A-D in the above-mentioned embodiments to enhance the contact between the refrigerant and the heat exchanger tubes


15


and to improve the heat transfer rate between them.




Next, the overall structure of a refrigeration apparatus including the above-mentioned evaporator according to an embodiment of the present invention will be explained with reference to

FIGS. 6 and 7

.




The refrigeration apparatus shown in the figures includes the above-mentioned evaporator


12


; a compressor


13


for compressing the refrigerant vaporized in the evaporator


12


; a condenser


10


for condensing and liquefying the refrigerant compressed in the compressor


13


; an expansion valve (throttle valve)


11


for reducing the pressure of the refrigerant liquefied in the condenser


10


; an intermediate cooler


25


for temporarily storing and cooling the refrigerant liquefied in the condenser


10


; and an oil cooler


26


for cooling the lubricating oil for the compressor


13


by utilizing a portion of the refrigerant cooled in the condenser


13


.




Also, a motor (a driving mechanism)


27


is connected to the compressor


13


for operating the compressor


13


.




The condenser


10


, the throttle valve


11


, the evaporator


12


, the compressor


13


, and the intermediate cooler


25


are connected via primary piping


28


to constitute a closed system in which the refrigerant is circulated.




The compressor


13


in this embodiment is based on a 2-stage (multistage) centrifugal compressor, a so-called turbo compressor, and this turbo compressor


13


is provided with a plurality of impellers


29


. The refrigerant is compressed in a first stage impeller


29




a


situated in the upstream side of the impeller


29


, and the compressed refrigerant is led into the second stage impeller


29




b


to be compressed further and then sent to the condenser


10


.




The condenser


10


includes a main condenser


10




a


and a sub-cooler


10




b


which is an auxiliary compressor, and the refrigerant is introduced first into the main condenser


10




a


and then to the sub-cooler


10




b


. However, a portion of the refrigerant cooled in the main condenser


10




a


is introduced into the oil cooler


26


, without passing through the sub-cooler


10




b


, to cool the lubricating oil.




Also, apart from the above process, a portion of the refrigerant cooled in the main condenser


10




a


is introduced into the casing


31


of the motor


27


, which will be explained later, without passing through the sub-cooler


10




b


, and cools stators and coils which are not shown in the diagram.




The throttle valve


11


is disposed between the condenser


10


and the intermediate cooler


25


, and between the intermediate cooler


25


and the evaporator


12


, and they are used for stepwise reduction of the pressure of the refrigerant liquefied in the condenser


10


.




The structure of the intermediate cooler


25


is equivalent to a hollow vessel, and the refrigerant which has been cooled in the main condenser


10




a


and the sub-cooler


10




b


and reduced in pressure in the throttle valve


11


, is temporarily stored therein and is subjected to further cooling. Here, the vapor phase components in the intermediate cooler


25


are introduced into the second stage impeller


29




b


of the compressor


13


through the bypass piping


23


, without passing through the evaporator


12


.




INDUSTRIAL APPLICABILITY




According to the evaporator of the present invention, since the prevention plates are disposed above the heat exchanger tubes so that droplets of refrigerant, which are blown upwards when the refrigerant is boiled, hit the prevention plates, the droplets of refrigerant are not drawn into the compressor. Accordingly, it becomes possible to avoid problems caused by the droplets, such as a decrease in the performance of the compressor or damage to an impeller.



Claims
  • 1. An evaporator for a refrigerating system including a container into which a refrigerant is introduced, and heat exchanger tubes disposed in the container through which an object to be cooled down flows, comprising:a prevention plate disposed above said heat exchanger tubes so that droplets of the refrigerant, which are blown upwards due to boiling of the refrigerant, hit said prevention plate.
  • 2. An evaporator for a refrigerating system according to claim 1, whereinsaid heat exchanger tubes are divided into a plurality of vertically spaced groups so that a space is formed between the groups of said heat exchanger tubes in a vertical direction; and said prevention plate is disposed above the space.
  • 3. An evaporator for a refrigerating system according to claim 1, whereinthe distance between said prevention plate and said heat exchanger tubes at an uppermost level is about 0.5 to 2 times the diameter of a heat exchanger tube which is located at the uppermost level.
  • 4. An evaporator for a refrigerating system according to claim 1, whereinsaid prevention plate has a cross section substantially shaped as an inverted letter “V”, and a vertical angle of said prevention plate is designed to be between 60° and 120°.
  • 5. An evaporator for a refrigerating system according to claim 1, whereinan end portion of said prevention plate covers at least a part of a heat exchanger tube which is located at the uppermost level of said heat exchanger tubes and is adjacent to said prevention plate.
  • 6. An evaporator for a refrigerating system according to claim 1, whereina group of said heat exchanger tubes facing an inner surface of said container is disposed so that a space is formed between the group of said heat exchanger tubes and said container along the inner surface of said container; and said prevention plate is disposed above said space.
  • 7. A refrigeration apparatus, comprising:a compressor for compressing a refrigerant; a condenser for condensing and liquefying the refrigerant which is compressed in said compressor; a throttling mechanism for the pressure of the liquefied refrigerant; and an evaporator for cooling down an object to be cooled by exchanging heat between the object to be cooled and a resultant condensed and pressure-reduced liquefied refrigerant, and evaporating and vaporizing the liquefied refrigerant, wherein said evaporator comprises: a container into which the refrigerant is introduced; heat exchanger tubes disposed in the container through which the object to be cooled down flows; and a prevention plate disposed above said heat exchanger tubes so that droplets of the refrigerant, which are blown upwards due to boiling of the refrigerant, hit said prevention plate.
  • 8. A refrigeration apparatus according to claim 7, whereinsaid heat exchanger tubes are divided into a plurality of vertically spaced groups so that a space is formed between the groups of said heat exchanger tubes in a vertical direction, and said prevention plate is disposed above the space.
  • 9. A refrigeration apparatus according to claim 7, whereinthe distance between said prevention plate and said heat exchanger tubes at an uppermost level is about 0.5 to 2 times the diameter of a heat exchanger tube which is located at the uppermost level.
  • 10. A refrigeration apparatus according to claim 7, whereinsaid prevention plate has a cross section substantially shaped as an inverted letter “V”, and a vertical angle of said prevention plate is designed to be between 60° and 120°.
  • 11. A refrigeration apparatus according to claim 7, whereinan end portion of said prevention plate covers at least a part of a heat exchanger tube which is located at the uppermost level of said heat exchanger tubes and is adjacent to said prevention plate.
  • 12. A refrigeration apparatus according to claim 7, whereina group of said heat exchanger tubes facing an inner surface of said container is disposed so that a space is formed between the group of said heat exchanger tubes and said container along the inner surface of said container; and said prevention plate is disposed above said space.
Priority Claims (1)
Number Date Country Kind
P2000-357022 Nov 2000 JP
PCT Information
Filing Document Filing Date Country Kind
PCT/JP01/07686 WO 00
Publishing Document Publishing Date Country Kind
WO02/42696 5/30/2002 WO A
US Referenced Citations (6)
Number Name Date Kind
3744264 Ware Jul 1973 A
4354551 Kristoffersson et al. Oct 1982 A
4365487 Dobney Dec 1982 A
4823561 Medlock Apr 1989 A
5435155 Paradis Jul 1995 A
6516627 Ring et al. Feb 2003 B2
Foreign Referenced Citations (2)
Number Date Country
8-189726 Jul 1996 JP
8-233407 Sep 1996 JP