The present disclosure relates to a shell-and-plate heat exchanger.
Japanese Unexamined Patent Publication No. 2006-527835 discloses a shell-and-plate heat exchanger (a heat exchanger apparatus) having a plate package including a plurality of heat exchange plates and a tank that houses the plate package. This heat exchanger is a flooded heat exchanger in which a liquid refrigerant is stored in a lower space of the tank. The liquid refrigerant in the tank evaporates when liquid refrigerant exchanges heat with a fluid flowing through the plate package. The evaporated refrigerant flows outside from the top of a shell.
A first aspect of the present disclosure is directed to a shell and plate heat exchanger including a shell forming an internal space, and a plate stack housed in the internal space of the shell. The plate stack includes a plurality of heat transfer plates stacked in a lateral direction and joined together. The shell and plate heat exchanger is configured to allow a refrigerant that has flowed into the internal space of the shell to evaporate. The plate stack forms a plurality of refrigerant channels that communicate with the internal space of the shell and allow a refrigerant to flow through, and a plurality of heating medium channels that are blocked from the internal space of the shell and allow a heating medium to flow through. Each of the refrigerant channels is adjacent to an associated one of the heating medium channels with heat transfer plate interposed therebetween. Each of the heat transfer plates includes a first communication hole that communicates with the heating medium channels to introduce the heating medium into the heating medium channels, a second communication hole formed below the first communication hole that communicates with the heating medium channels to emit the heating medium out of the heating medium channels, and a guide crossing between the first communication hole and the second communication hole to guide the heating medium that has flowed into the heating medium channels from the first communication hole toward side portions of the heat transfer plate.
Embodiments will be described below with reference to the drawings. The following embodiments are merely exemplary ones in nature, and are not intended to limit the scope, applications, or use of the present invention.
A shell-and-plate heat exchanger (10) (will be hereinafter referred to as a “heat exchanger”) of this embodiment is connected to a refrigerant circuit of a refrigeration apparatus (not shown). In this refrigeration apparatus, a refrigerant compressed by a compressor dissipates heat in a condenser (radiator), and is decompressed by a decompression mechanism. The decompressed refrigerant evaporates in a heat exchanger (10) that functions as an evaporator, and is sucked into the compressor. In this manner, a refrigeration cycle is performed in the refrigerant circuit of the refrigeration apparatus.
As illustrated in
The shell (20) is comprised of a horizontally long, cylindrical closed container. The shell (20) has a barrel (20a), a first sidewall (20b), and a second sidewall (20c). The barrel (20a) is formed in a cylindrical shape. The first sidewall (20b) is formed in a circular shape and blocks a left end of the barrel (20a). The second sidewall (20c) is formed in a circular shape and blocks a right end of the barrel (20a). The shell (20) forms the internal space (21) defined by the barrel (20a), the first sidewall (20b), and the second sidewall. The internal space (21) stores the liquid refrigerant.
The barrel (20a) has a refrigerant inlet (32) and a refrigerant outlet (33). The refrigerant inlet (32) is formed at the bottom of the barrel (20a). The refrigerant is introduced into the internal space (21) through the refrigerant inlet (32). The refrigerant outlet (33) is formed at the top of the barrel (20a). The refrigerant evaporated in the internal space (21) is emitted out of the shell (20) through the refrigerant outlet (33). The refrigerant inlet (32) and the refrigerant outlet (33) are connected to the refrigerant circuit via pipes.
The first sidewall (20b) is provided with a heating medium inlet (23) and a heating medium outlet (24). The heating medium inlet (23) and the heating medium outlet (24) are tubular members.
The heating medium inlet (23) penetrates substantially the center of the first sidewall (20b). The heating medium inlet (23) is connected to a heating medium introduction path (43) of the plate stack (40) to supply the heating medium to the plate stack (40).
The heating medium outlet (24) penetrates the first sidewall (20b) at an appropriately intermediate position between the heating medium inlet (23) and a lower end of the first sidewall (20b). The heating medium outlet (24) is connected to a heating medium emission path (44) of the plate stack (40) to emit the heating medium out of the plate stack.
The plate stack (40) includes a plurality of heat transfer plates (50a, 50b) stacked in the lateral direction and joined together. The plate stack (40) is housed in the internal space (21) of the shell (20) with the stacking direction of the heat transfer plates (50a, 50b) extending in the lateral direction.
As illustrated in
As illustrated in
Each of the first plates (50a) has an inlet protrusion (51a) and an outlet protrusion (53a). Each of the inlet protrusion (51a) and the outlet protrusion (53a) is a circular portion bulging toward the front side of the first plate (50a). Each of the inlet protrusion (51a) and the outlet protrusion (53a) is formed in a widthwise center portion of the first plate (50a). The inlet protrusion (51a) is formed in an upper portion of the first plate (50a). The outlet protrusion (53a) is formed in a lower portion of the first plate (50a). A first inlet hole (52a) is formed in a center portion of the inlet protrusion (51a). The first inlet hole (52a) corresponds to a first communication hole of the first plate (50a). A first outlet hole (54a) is formed in a center portion of the outlet protrusion (53a). Each of the first inlet hole (52a) and the first outlet hole (54a) is a circular hole penetrating the first plate (50a) in a thickness direction.
In the first plate (50a), a first distance d1 between a lower end of the first outlet hole (54a) and a lower end of the first plate (50a) is greater than a second distance d2 between an upper end of the first inlet hole (52a) and an upper end of the first plate (50a). The first distance d1 is greater than a third distance d3 between an upper end of the first outlet hole (54a) and a lower end of the first inlet hole (52a). In this embodiment, the first distance d1 is twice or greater than the third distance d3.
Each of the second plates (50b) has an inlet recess (51b) and an outlet recess (53b). Each of the inlet recess (51b) and the outlet recess (53b) is a circular portion bulging toward the back side of the second plate (50b). Each of the inlet recess (51b) and the outlet recess (53b) is formed in a widthwise center portion of the second plate (50b). The inlet recess (51b) is formed in an upper portion of the second plate (50b). The outlet recess (53b) is formed in a lower portion of the second plate (50b). A second inlet hole (52b) is formed in a center portion of the inlet recess (51b). A second outlet hole (54b) is formed in a center portion of the outlet recess (53b). Each of the second inlet hole (52b) and the second outlet hole (54b) is a circular hole penetrating the second plate (50b) in a thickness direction.
In the second plate (50b), the inlet recess (51b) is formed at a position corresponding to the inlet protrusion (51a) of the first plate (50a), and the outlet recess (53b) is formed at a position corresponding to the outlet protrusion (53a) of the first plate (50a). In the second plate (50b), the second inlet hole (52b) is formed at a position corresponding to the first inlet hole (52a) of the first plate (50a), and the second outlet hole (54b) is formed at a position corresponding to the first outlet hole (54a) of the first plate (50a). The first inlet hole (52a) and the second inlet hole (52b) have a substantially equal diameter. The first outlet hole (54a) and the second outlet hole (54b) have a substantially equal diameter.
Thus, the positions of the second outlet hole (54b) and the second inlet hole (52b) in the second plate (50b) are the same as the positions of the first outlet hole (54a) and the first inlet hole (52a) in the first plate (50a). Strictly speaking, a distance between a lower end of the second outlet hole (54b) of the second plate (50b) and a lower end of the second plate (50b) is the same as the first distance d1. A distance between an upper end of the second inlet hole (52b) and an upper end of the second plate (50b) is the same as the second distance d2.
In the plate stack (40), each first plate (50a) and an adjacent one of the second plates (50b) on the back side of the first plate (50a) are welded together at their peripheral portions along the entire perimeter. In the plate stack (40), the first inlet hole (52a) of each first plate (50a) overlaps the second inlet hole (52b) of an adjacent one of the second plates (50b) on the front side of the first plate (50a), and the rims of the overlapping first inlet hole (52a) and second inlet hole (52b) are welded together along the entire perimeter.
The first inlet hole (52a) and the second inlet hole (52b) overlapping each other correspond to the first communication hole. The first inlet hole (52a) and the second inlet hole (52b) communicate with heating medium channels (42) to introduce the heating medium into the heating medium channels (42).
In the plate stack (40), the first outlet hole (54a) of each first plate (50a) overlaps the second outlet hole (54b) of an adjacent one of the second plates (50b) on the front side of the first plate (50a), and the rims of the overlapping first outlet hole (54a) and second outlet hole (54b) are welded together along the entire perimeter. The first outlet hole (54a) and the second outlet hole (54b) overlapping each other correspond to a second communication hole. The first outlet hole (54a) and the second outlet hole (54b) are formed below the first communication hole (52a, 52b) and communicate with the heating medium channels (42) to emit the heating medium out of the heating medium channels (42).
In the plate stack (40), the inlet protrusions (51a) and first inlet holes (52a) of the first plates (50a) and the inlet recesses (51b) and second inlet holes (52b) of the second plates (50b) form the heating medium introduction path (43). In the plate stack (40), the outlet protrusions (53a) and first outlet holes (54a) of the first plates (50a) and the outlet recesses (53b) and second outlet holes (54b) of the second plates (50b) form the heating medium emission path (44).
The heating medium introduction path (43) and the heating medium emission path (44) are passages extending in the stacking direction of the heat transfer plates (50a, 50b) in the plate stack (40). The heating medium introduction path (43) is a passage blocked from the internal space (21) of the shell (20), and allows all the heating medium channels (42) to communicate with the heating medium inlet (23). The heating medium emission path (44) is a passage blocked from the internal space (21) of the shell (20), and allows all the heating medium channels (42) to communicate with the heating medium outlet (24).
The plate stack (40) includes the refrigerant channels (41) and the heating medium channels (42), each of the heating medium channels (42) being adjacent to an associated one of the refrigerant channels (41) with the heat transfer plate (50a, 50b) interposed therebetween. The heat transfer plate (50a, 50b) separates the refrigerant channel (41) from the corresponding heating medium channel (42). The first plate (50a) has a first corrugated pattern (62a), and the second plate (50b) has a second corrugated pattern (62b). Each of the first and second corrugated patterns includes repetition of long and narrow ridges and grooves.
As illustrated in
The first corrugated pattern (62a) includes first front-side protrusions (55a) protruding toward the front side of the first plate (50a) and first back-side protrusions (57a) protruding toward the back side of the first plate (50a). The first front-side protrusions and the first back-side protrusions are alternately arranged.
The second corrugated pattern (62b) includes second front-side protrusions (57b) protruding toward the front side of the second plate (50b) and second back-side protrusions (55b) protruding toward the back side of the second plate (50b). The second front-side protrusions and the second back-side protrusions are alternately arranged.
Each of the refrigerant channels (41) is a channel sandwiched between the front surface of the first plate (50a) and the back surface of the second plate (50b). The refrigerant channel (41) is a channel that communicates with the internal space (21) of the shell (20) and allows the refrigerant to flow through. Strictly speaking, the refrigerant channel (41) includes first channels (45) and first spaces (M). Each of the first channels (45) is formed between a front surface of the first back-side protrusion (57a) and a back surface of the second front-side protrusion (57b). Each of the first spaces (M) is formed between the first front-side protrusion (55a) and the second back-side protrusion (55b). The first channels (45) and the first spaces (M) are alternately arranged from the upper end to lower end of the plate stack (40). Upper and lower ends of each first channel (45) communicate with the first spaces (M). The first channels (45) adjacent to each other in the vertical direction communicate with each other through the first space (M). The first channels (45) and the first spaces (M) are open to the internal space (21).
Each of the heating medium channels (42) is a channel sandwiched between the back surface of the first plate (50a) and the front surface of the second plate (50b). The heating medium channel (42) is a channel blocked from the internal space (21) of the shell (20) and allows the heating medium to flow through. Strictly speaking, the heating medium channel (42) includes second channels (46) and second spaces (N). Each of the second channels (46) is formed between a back surface of the first front-side protrusion (55a) and a front surface of the second back-side protrusion (55b). Each of the second spaces (N) is formed between the first back-side protrusion (57a) and the second front-side protrusion (57b). The second channels (46) and the second spaces (N) are alternately arranged from the upper end to lower end of the plate stack (40). Upper and lower ends of each second channel (46) communicate with the second spaces (N). The second channels (46) adjacent to each other in the vertical direction communicate with each other through the second space (N). The second channels (46) and the second spaces (N) are blocked from the internal space of the shell (20).
As illustrated in
The guide (70) includes a first linear flat portion (65a) and a second linear flat portion (65b). Strictly speaking, the first linear flat portion is linearly formed on the back surface of the first plate (50a). The first linear flat portion (65a) bulges toward the back side of the first plate (50a), and has a flat bulging top. The second linear flat portion (65b) is linearly formed on the front surface of the second plate (50b). The second linear flat portion (65b) bulges toward the front side of the second plate (50b), and has a flat bulging top.
The second linear flat portion (65b) is formed at a position corresponding to the first linear flat portion (65a) when the first plate (50a) and the second plate (50b) are stacked.
In the plate stack (40), the first linear flat portion (65a) of the first plate (50a) and the second linear flat portion (65b) of the second plate (50b) adjacent to the back surface of the first plate (50a) overlap each other, and the overlapping first linear flat portion (65a) and second linear flat portion (65b) are joined together over the entire length by, for example, brazing. The guide (70) is formed of the first linear flat portion (65a) and the second linear flat portion (65b) joined together.
The guide (70) has a first guide portion (70a) and a second guide portion (70b). The first guide portion (70a) is in the middle of the lower end of the first communication hole (52a, 52b) and the upper end of the second communication hole (54a, 54b), and linearly extends in the width direction of the heat transfer plate (50a, 50b). The second guide portion (70b) linearly extends downward from each end of the first guide portion (70a). The guide (70) is arranged symmetrically with respect to a center line Y of the heat transfer plate (50a, 50b).
The first linear flat portion (65a) of the first guide portion (70a) is in the middle of the first inlet hole (52a) and the first outlet hole (54a) of the first plate (50a), and extends in the width direction of the first plate (50a). The first linear flat portion (65a) of the first guide portion (70a) is located between two first front-side protrusions (55a) adjacent to each other in the vertical direction.
The second linear flat portion (65b) of the first guide portion (70a) is in the middle of the second inlet hole (52b) and the second outlet hole (54b) of the second plate (50b), and extends in the width direction of the second plate (50b). The second linear flat portion (65b) of the first guide portion (70a) is located between two second back-side protrusions (55b) adjacent to each other in the vertical direction. The first guide portion (70a) has a length L1 which is approximately half the length from one end to the other end of the heat transfer plate (50a, 50b).
The first linear flat portion (65a) of the second guide portion (70b) is formed to extend downward from each end of the first linear flat portion (65a) on the back surface of the first plate (50a). The second linear flat portion (65b) of the second guide portion (70b) is formed to extend downward from each end of the first linear flat portion (65a) on the front surface of the second plate (50b). The second guide portion (70b) has a length L2 which is approximately one third of the length L1 of the first guide portion (70a). A lower end of the second guide portion (70b) is located below the upper end of the second communication hole (54a, 54b). Strictly speaking, the lower end of the second guide portion (70b) is located at a position lower than the position of the center (O) of the second communication hole (54a, 54b).
More strictly, the lower end of the second guide portion (70b) is located at a height substantially in the middle of the center (O) of the second communication hole (54a, 54b) and the lower end of the second communication hole (54a. 54b).
How the heating medium and the refrigerant flow in the heat exchanger (10) will be specifically described with reference to
As illustrated in
In this manner, the heating medium flows downward while flowing toward both lateral ends of the heat transfer plate (50a, 50b).
As illustrated in
The heating medium that has passed the lower end of each second guide portion (70b) flows near the lower end of the heat transfer plate (50a, 50b) toward the widthwise center portion of the heat transfer plate (50a, 50b). Around the second communication hole (54a, 54b), flows of the heating medium toward the second communication hole (54a, 54b) from both sides of the second communication hole (54a, 54b) and a flow of the heating medium toward the second communication hole (54a, 54b) from below the second communication hole (54a, 54b) are generated. The heating medium coming from the lateral sides and lower side of the second communication hole (54a, 54b) flows into the second communication hole (54a, 54b).
Next, how the refrigerant flows will be described below. The refrigerant that has passed through an expansion valve in the refrigerant circuit flows toward the heat exchanger (10). This liquid refrigerant flows into the internal space (21) of the shell (20) through the refrigerant inlet (32). The liquid refrigerant stored in the internal space (21) reaches close to the upper end of the plate stack (40). The plate stack (40) is immersed in the liquid refrigerant. The refrigerant stored in the internal space (21) has a relatively low pressure. The low-pressure refrigerant exchanges heat with the heating medium flowing through the heating medium channels (42). Strictly speaking, the refrigerant channel (41) and the heating medium channel (42) are adjacent to each other with the heat transfer plate (50a, 50b) interposed therebetween. Thus, the liquid refrigerant absorbs heat from the heating medium flowing through the heating medium channel (42) and evaporates. The evaporated refrigerant moves from the refrigerant channel (41) to the upper space (21a) which is an upper portion of the internal space (21). The refrigerant in the upper space (21a) flows into the refrigerant circuit through the refrigerant outlet (33).
The guide (70) crossing between the first communication hole (52a, 52b) and the second communication hole (54a, 54b) is provided for the heating medium channels (42) to guide the heating medium that has flowed into the heating medium channels (42) from the first communication hole (52a, 52b) toward the side portions of the heat transfer plate (50a. 50b).
A known plate stack of a shell-and-plate heat exchanger includes heating medium channels and refrigerant channels, each of the heating medium channels being adjacent to an associated one of the refrigerant channels with a heat transfer plate interposed therebetween. Each heat transfer plate is provided with two holes communicating with the heating medium channels, and the heating medium flows through the heating medium channels from one hole to the other hole. When the heating medium flows from one hole to the other hole in the shortest distance, the heating medium does not easily spread over the entire heat transfer plate. For example, in a portion of the heat transfer plate away from the holes, such as an end portion in the width direction of the heat transfer plate, the heating medium stays still and does not exchange heat with the refrigerant. Thus, the whole heat transfer plate cannot be effectively used for the heat exchange, resulting in only a small amount of heat exchange.
In contrast, according to the feature (1) of this embodiment, the first guide portion (70a) allows the heating medium flowing through the heating medium channels (42) to go toward the side portions of the heat transfer plate (50a, 50b).
Thereafter, the heating medium flows from the ends of the first guide portion (70a) along the second guide portions (70b). The heating medium flowing along the second guide portions (70b) makes contact only with a region of the heat transfer plate (50a, 50b) outside the second guide portions (70b). Thus, the heating medium coming near the lower end of the heat transfer plate (50a. 50b) has a higher temperature than the heating medium flowing in contact with the entire heat transfer plate (50a, 50b) in the width direction. This can keep a temperature difference between the refrigerant and the heating medium in a lower portion of the heat transfer plate (50a, 50b), improving the performance of the heat exchanger (10). The first communication hole (52a, 52b) is formed in the upper portion of the heat transfer plate (50a, 50b). The heating medium that has flowed from the first communication hole (52a, 52b) spreads to the side portions of the heat transfer plate (50a, 50b) along the first guide portion (70a). This accelerates evaporation of the refrigerant in the upper portion of the plate stack (40), and can reduce the amount of liquid refrigerant droplets coming out of the heat exchanger together with the gas refrigerant.
The lower end of the guide (70) is located below the upper end of the second communication hole (54a, 54b).
According to the feature (2), the heating medium flows around the lower ends of the guide (70) and enters the second communication hole (54a. 54b). The heating medium reaches the lower portion of the heat transfer plate (50a, 50b) without decreasing its temperature so much, as compared with the case where no guide (70) is provided. This can maintain the temperature difference between the refrigerant and the heating medium in the lower portion of the heat transfer plate (50a, 50b). As a result, heat exchange efficiency can be kept from decreasing, and the performance of the heat exchanger (10) can be improved.
In the heat exchanger of this embodiment, the distance between the lower end of the second communication hole (54a, 54b) and the lower end of the heat transfer plate (50a, 50b) is greater than the distance between the upper end of the first communication hole (52a, 52b) and the upper end of the heat transfer plate (50a, 50b).
According to the feature (3), the second communication hole (54a, 54b) is at some distance from the lower end of the heat transfer plate (50a, 50b). The heating medium passing through the heating medium channels (42) flows around the lower ends of the second guide portions (70b), and then goes upward to the second communication hole (54a, 54b). Thus, the heating medium flowing near the lower end of the heat transfer plate (50a, 50b) has a higher temperature than the heating medium flowing into the second communication hole (54a, 54b).
This can keep the temperature of the heating medium from decreasing at the lower end of the heat transfer plate (50a, 50b), and can keep the heat exchange efficiency of the heat exchanger (10) from decreasing.
In the heat exchanger of this embodiment, the center of the second communication hole (54a, 54b) is located at a position higher than the position of the lower end of the guide (70).
According to the feature (4), the heating medium flows into the second communication hole (54a, 54b) from below the second communication hole (54a, 54b). Thus, the ratio of the heating medium flowing into the second communication hole (50a, 50b) without passing near the lower end of the heat transfer plate (54a, 54b) decreases. i.e., the ratio of the heating medium flowing near the lower end of the heat transfer plate (50a. 50b) increases. The heating medium passing near the lower end of the heat transfer plate has a relatively high temperature. This can improve the heat exchange efficiency between the refrigerant and the heating medium at the lower end of the heat transfer plate (50a, 50b).
The guide (70) is formed of the protrusion (57a, 57b) or the recess (56a. 56b) formed in the heat transfer plate (50a, 50b).
According to this feature (5), the guide (70) can be formed integrally with the heat transfer plate by pressing, for example. This allows easy manufacture of the heat transfer plate (50a, 50b), and makes the manufacturing process of the plate stack (40) less complicated.
The heat exchanger (10) of the embodiment may be modified into the following variations. The following variations may be combined or replaced without deteriorating the functions of the heat exchanger (10).
As illustrated in
The first guide portion (70a) of the guide (70) of the first variation is located at a position in the middle of the lower end of the first communication hole (52a, 52b) and the upper end of the second communication hole (54a, 54b). The length L1 of the first guide portion (70a) is approximately equal to the radius of the heat transfer plate (50a, 50b). The second guide portion (70b) is formed to extend from each of the ends of the first guide portion (70a) to the lower portion of the heat transfer plate (50a, 50b). Strictly speaking, a distance between the position of the lower end of the second guide portion (70b) and the position of the lower end of the second communication hole (54a. 54b) is greater than a distance between the position of the lower end of the second guide portion (70b) and the position of the lower end of the heat transfer plate (50a, 50b). The length L2 of the second guide portion (70b) is greater than the length L1 of the first guide portion (70a).
According to the first variation, the heating medium flows laterally along the first guide portion (70a) from the first communication hole (52a, 52b), and then flows along the second guide portions to the lower portion of the heat transfer plate (50a, 50b). The heating medium flows upward from the lower ends of the second guide portions (70b) to the second communication hole (54a, 54b). This can maintain a sufficient distance from the first communication hole (52a, 52b) to the second communication hole (54a, 54b), keeping the heat exchange efficiency between the heating medium and the refrigerant from decreasing. The distance that the heating medium flows upward from the lower ends of the second guide portions (70b) to the second communication hole (54a, 54b) is relatively long. This can keep a sufficient temperature difference between the heating medium at the lower end of the heat transfer plate (50a, 50b) and the heating medium in the second communication hole (54a. 54b). Thus, the temperature of the heating medium at the lower end of the heat transfer plate (50a, 50b) is relatively high, accelerating the heat exchange between the refrigerant and the heating medium in the lower portion of the heat transfer plate (50a. 50b). Moreover, the second communication hole (54a, 54b) located at a relatively high position allows storage of a relatively large amount of liquid refrigerant.
As illustrated in
The second communication hole (54a, 54b) is formed immediately below the first communication hole (52a, 52b) and near the center of the heat transfer plate (50a, 50b). The length L1 of the first guide portion (70a) is substantially equal to half of the major axis of the heat transfer plate (50a, 50b). The second guide portion (70b) is formed to extend from each of the ends of the first guide portion (70a) to a lower portion of the heat transfer plate (50a, 50b).
Strictly speaking, the lower end of the second guide portion (70b) is located at a relatively great distance from the lower end of the second communication hole (54a, 54b).
The length L2 of the second guide portion (70b) is equal to or greater than the length L1 of the first guide portion (70a).
According to the second variation, the heating medium flows laterally along the first guide portion (70a) from the first communication hole (52a, 52b), and then flows along the second guide portions to the lower portion of the heat transfer plate (50a, 50b). The heating medium flows upward from the lower ends of the second guide portions (70b) to the second communication hole (54a, 54b). This can maintain a sufficient distance from the first communication hole (52a, 52b) to the second communication hole (54a, 54b), keeping the heat exchange efficiency between the heating medium and the refrigerant from decreasing. The distance that the heating medium flows upward from the lower ends of the second guide portions (70b) to the second communication hole (54a, 54b) is relatively long. This can keep a sufficient temperature difference between the heating medium at the lower end of the heat transfer plate (50a, 50b) and the heating medium in the second communication hole (54a, 54b). Thus, the temperature of the heating medium at the lower end of the heat transfer plate (50a, 50b) is relatively high, accelerating the heat exchange between the refrigerant and the heating medium in the lower portion of the heat transfer plate (50a. 50b). A space is formed above the plate stack in the internal space (21) of the shell (20). The liquid refrigerant that failed to evaporate in this space falls onto the plate stack (40). This can keep the liquid refrigerant from flowing out of the refrigerant outlet, which can avoid the carry-over.
As illustrated in
As illustrated in
The eliminator (15) is housed in the internal space (21) of the shell (20). The eliminator (15) is placed to traverse the internal space (21) of the shell (20) above the plate stack (40). The gas refrigerant passed through the eliminator (15) flows out of the shell (20) through the refrigerant outlet (33). The liquid refrigerant captured by the eliminator (15) falls down in the form of relatively large droplets.
As illustrated in
The first angle α1 of the first corrugated pattern (62a) may be the same as the second angle α2 of the second corrugated pattern (62b). For example, both the first angle α1 of the first corrugated pattern (62a) and the second angle α2 of the second corrugated pattern (62b) may be zero degrees, i.e., the first corrugated pattern (62a) and the second corrugated pattern (62b) may extend in the horizontal direction.
The heat exchanger (10) of the embodiment may be a falling film type shell-and-plate heat exchanger. Strictly speaking, the heat exchanger (10) may include a sprayer arranged above the plate stack (40) in the shell (20) to spray the liquid refrigerant onto the plate stack (40). Alternatively, the heat exchanger (10) may include a plate stack having a structure that sprays the liquid refrigerant.
While the embodiments and variations thereof have been described above, it will be understood that various changes in form and details may be made without departing from the spirit and scope of the claims. The embodiments and the variations thereof may be combined and replaced with each other without deteriorating intended functions of the present disclosure. The ordinal numbers such as “first,” “second,” “third,” . . . , described above are used to distinguish the terms to which these expressions are given, and do not limit the number and order of the terms.
As can be seen from the foregoing description, the present disclosure is useful for a shell-and-plate heat exchanger.
Number | Date | Country | Kind |
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2020-003837 | Jan 2020 | JP | national |
This is a continuation of International Application No. PCT/JP2021/001000 filed on Jan. 14, 2021, which claims priority to Japanese Patent Application No. 2020-003837, filed on Jan. 14, 2020. The entire disclosures of these applications are incorporated by reference herein.
Number | Date | Country | |
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Parent | PCT/JP2021/001000 | Jan 2021 | US |
Child | 17857893 | US |