This application is based on Japanese Patent Application No. 2004-114569 filed on Apr. 8, 2004, the disclosure of which is incorporated herein by reference.
This invention relates to a refrigerant evaporator for evaporating the refrigerant in a refrigerating cycle, which can be favorably used, for example, for an air conditioning system for vehicles. The refrigerant evaporator can be further used as an outdoor heat exchanger in a heat pump cycle.
In recent years, study has been forwarded to control the airflow rates independently for the driver's seat and the assistant's seat to meet the requirements of the users of the vehicles. The above requirements have been heretofore been satisfied by controlling the airflow rate through the refrigerant evaporator independently on the right side and on the left side in the direction of core width. When the airflow rate is to be independently controlled on the right side and on the left side of the refrigerant evaporator in which the heat-exchanging tubes are longitudinally arranged, it has been necessary for the refrigerant evaporator to have a structure in which a separator is inserted in a tank to separate the flow of refrigerant in the direction of core width, so that the refrigerant flows through passages that are different depending on the right side and the left side.
This, however, results in an increase in the distance of the refrigerant flow passages and, hence, in an increase in the pressure loss making it difficult to improve performance of the refrigerant evaporator. To cope with this, therefore, the present inventors have proposed a refrigerant evaporator as disclosed in Japanese Patent Application No. 2003-434216 (U.S. patent application Ser. No. 10/827,559). According to this refrigerant evaporator, the refrigerant flowing through a first path on the front surface is folded to a second path on the back surface and, at this moment, the flow is changed over right side left to decrease the pressure loss on the refrigerant side, to improve the temperature distribution and to independently control the airflow rate on the right side and on the left side (hereinafter, this new refrigerant path system is referred to as front-and-rear right-and-left cross path).
The problem, however, has been how to realize the heat exchanger having the front-and-rear right-and-left cross path in a simple constitution that facilitates the mass production.
The present invention was accomplished in view of the problems inherent in the above prior art and its object is to provide a refrigerant evaporator having a simplified tank structure yet constituting the front-and-rear right-and-left cross path and producing less pressure loss on the refrigerant side.
In the refrigerant evaporator of the invention, the flow of the refrigerant constitutes at least a first path portion and a second path portion between a refrigerant inlet portion and a refrigerant outlet portion. The refrigerant evaporator includes a core portion formed by rows of tubes arranged in parallel, refrigerant collecting portions where the refrigerant is collected flowing through the first path portion, and refrigerant distributing portions for distributing the refrigerant to the second path portion. The core portion has a first row of tubes and a second row of tubes on the front and rear sides, respectively, to form the first path portion and the second path portion on the nearly right and left whole regions. The refrigerant collecting portions have a structure for collecting the refrigerant of the first path portion in a manner of being divided to the right and the left, the refrigerant distributing portions are formed by a pair of tank portions disposed front and rear, and has a structure in which the second path portion is formed in a region different from the first path portion in terms of the right-and-left direction, the refrigerant collecting portions and the refrigerant distributing portions being connected together through a pair of communication members.
Namely, the tank portion of the refrigerant evaporator is of a form in which the refrigerant passed through the first path portion on the downstream side in the direction of air flow is introduced into the second path portion on the upstream side in the direction of air flow being switched over right side left of the core portion, the tank portion being constituted by the tank portions having the refrigerant collecting portions which are flow passages having a function for guiding the refrigerant flew through the first path portion to the ends of the tank in the right-and-left direction and the refrigerant distributing portions which are flow passages for guiding the refrigerant to a group of tubes forming the second path portion, and by a header plate having a refrigerant collecting space for the tubes, and wherein the side tanks (communication members) are provided to envelop the open portions at the ends of the tank portion in the right-and-left direction and to spatially connect the above flow passages, and separators (flow-preventing weirs) are provided at portions for accomplishing the spatial blocking thereby to constitute the front-and-rear right-and-left cross path.
According to the present invention, increased sectional areas of the flow passages are obtained at the ends of the tank portion in the right-and-left direction (refrigerant flow corner portions) by simple means making it possible to decrease the pressure loss on the refrigerant side in the tank and to improve performance.
The invention is further concerned with a refrigerant evaporator for exchanging the heat between a fluid to be cooled flowing through the outer portion and a refrigerant flowing through the inner portion, wherein the flow of the refrigerant has at least a first path portion and a second path portion between a refrigerant inlet portion and a refrigerant outlet portion, and a core portion formed by rows of tubes arranged in parallel, refrigerant collecting portions where the refrigerant is collected flowing through the first path portion, refrigerant distributing portions for distributing the refrigerant to the second path portion, and a pair of tank portions for communicating the refrigerant collecting portions with the refrigerant distributing portions, wherein the core portion has a first row of tubes and a second row of tubes to form the first path portion and the second path portion on nearly the right and left whole regions; the refrigerant collecting portions and the refrigerant distributing portions are divided to the right and left, respectively; and the pair of tank portions communicate the refrigerant collecting portions with the refrigerant distributing portions of separate regions in the right-and-left direction, respectively.
The tank portions for changing over the flow of the refrigerant constitutes the front-and-rear right-and-left cross path by laminating a header plate and a tank header plate which form the tank portions as two flow passages in a vertical direction at right angles with the direction of the air flow or with the direction in which the tubes are arranged in parallel, a space-forming plate forming a refrigerant collecting/distributing space for the tubes, and a distributing plate having a separator function for guiding the refrigerant from the space-forming plate to two flow passages ahead and another separator function for separating the two flow passages.
According to the present invention, further, the flow of the refrigerant has decreased corner portions and a short flow passage in the tanks, making it possible to decrease the pressure loss on the refrigerant side in the tanks and to improve performance.
An embodiment of the invention will now be described in detail with reference to the drawings.
This embodiment is applied to the front-and-rear U-turn evaporator of the constitution in which the path stretches in the direction of whole width, and the description deals with a case where the refrigerant evaporator 1 of the invention is applied to the supercritical refrigerating cycle that operates when the refrigerant pressure of the high-pressure side becomes greater than a critical pressure by using a carbon dioxide refrigerant (hereinafter, CO2 refrigerant). The CO2 refrigerant of which the pressure is decreased by an expansion valve (not shown) on the upstream side of the refrigerant, flows in to exchange the heat with the air through the evaporator 1, and the vaporized refrigerant flows out to the downstream side.
The evaporator is of the multi-flow (MF) type in which a front row of tubes (first row of tubes) 1L that serves as a front core portion (first path portion) 1P and a rear row of tubes (second row of tubes) 2L that serves as a rear core portion (second path portion) 2P are arranged between the upper tank portion (refrigerant collecting/distributing portion) 2A and the lower tank portion (refrigerant inlet/outlet portion) 3. The refrigerant introduced through the refrigerant inlet portion 6a of the connector 6 flows (guided) into the core portion from the side of the front lower tank portion 8A, flows out (guided) from the lower tank portion 8B, and is drained from the refrigerant outlet portion 6b of the connector 6. Both ends of the front and rear lower tank portions 8A and 8B are sealed with caps 9.
The core portions 1P and 2P are such that heat-absorbing fins (corrugated fins) 5 are arranged as shown in the drawings among the gaps formed by the tubes 4, front row of the tubes 1L and rear row of the tubes 2L.
The connector 6 may be arranged on the upper side so that the first path 1P creates the descending stream. Further, the first path 1P may be realized by the rear core portion (second row of the tubes) 2P. In the front-and-rear U-turn evaporator, the refrigerant that has flown through a path is changed over in the direction of width of the core. The following description deals with a case where the tubes 4 are all changed over in the direction of width of the core. The invention, however, exhibits its effect even when the tubes are partly changed over.
The tank portion 2A of this embodiment is formed by stacking a header plate 7, a distribution plate 10, a tank header plate 11 and side tanks (communication members) 12 roughly on the core portion. The tank header plate 11 is obtained by press-forming a plate member so as to form three tank portions 11a to 11c (one wide tank and two narrow tanks) in the front-and-rear direction. The tank portion 11a works as a refrigerant collecting portion, and the tank portions 11b and 11c work as refrigerant distributing portions.
The distributing plate 10 is obtained by perforating in a plate, by press work, a group of communication holes 10a over the full length of the refrigerant collecting portion corresponding to the tank portion 11a on the front side, a group of communication holes 10b in the refrigerant distributing portion corresponding to the tank portion 11b on the left half portion on the rear side and a group of communication holes 10c in the refrigerant distributing portion corresponding to the tank portion 11c on the right half portion on the rear side. The group of communication holes 10a of the front side is corresponded to the upper open ends of the tubes 4 of the front core portion (front row of the tubes) 1P, the group of communication holes 10b of the rear side is corresponded to the upper open ends of the tubes 4 of the left half 2P(L) of the rear core portion (rear row of the tubes) 2P, and the group of communication holes 10c of the rear side are corresponded to the upper open ends of the tubes 4 of the right half 2P(R) of the rear core portion (rear row of the tubes) 2P.
The header plate 7 is for connecting the tubes 4 and is obtained by forming in a plate, by presswork, tubular holes (not shown) corresponding to the tubes 4 and refrigerant collecting spatial portions 7a. The side tanks 12 which are major portions of the invention are for spatially connecting the flow passages formed by the tank portions 11a to 11c enveloping the open end portions of the tank portions 11a to 11c in the right-and-left direction. The side tanks 12 are obtained by pressing a plate member forming openings 12a to 12c so as to be corresponded to the tank portions 11a to 11c.
Side caps 13 which are the sealing members are arranged at both ends of the side tank 12 in the axial direction. Further, separators 9a are arranged in the tank portion 11a to divide the flow passage into the right and the left, and separators (flow-preventing weirs) 9b are arranged at places where the flow passages are shut off between the tank portions 11b, 11c and the side tanks 12. The separators 9 may not be to completely block the flow of the refrigerant. These parts are all made of aluminum, and are stacked and are joined integrally together by brazing.
Next, described below is the flow of the refrigerant in the refrigerant evaporator 1 of the above structure.
In the tank header plate 11 shown in
On the other hand, the refrigerant collected in the tank portion 11a(L) from the left row of the tubes of the front core portion 1P which is the left first path 1P(L) through the group of communication holes 10a(L), flows into the tank portion 11c through the left side tank 12(L), flows into the right row of the tubes of the rear core portion 2P through the group of communication holes 10c of the right side and is changed over to the right second path 2P(R) (see a thick solid line LT).
Next, described below are the feature and the effect of the embodiment. First, the refrigerant evaporator exchanges the heat between the air flowing through the outer portion and the refrigerant flowing through the inner portion. The flow of the refrigerant has at least the first path portion 1P and the second path portion 2P between the refrigerant inlet portion 6a and the refrigerant outlet portion 6b. The refrigerant evaporator includes a core portion formed by a row of the tubes 4 arranged in parallel, refrigerant collecting portions 10a, 11a where the refrigerant is collected flowing through the first path portion 1P, and refrigerant distributing portions 10b, 10c, 11b, 11c for distributing the refrigerant to the second path portion 2R The core portion has a first row 1L of the tubes and a second row 2L of the tubes on the front and rear sides, respectively, to form the first path portion 1P and the second path portion 2P on the right and left whole regions. The refrigerant collecting portions 10a, 11a have a structure for collecting the refrigerant of the first path portion 1P in a manner of being divided to the right and the left. The refrigerant distributing portions 10b, 10c, 11b, 11c are formed by a pair of tank portions 11b, 11c disposed front and rear, and has a structure for distribution in which the second path portion 2P is formed in a separate region from the first path portion 1P in terms of the right-and-left direction. The refrigerant collecting portions 10a, 11a and the refrigerant distributing portions 10b, 10c, 11b, 11c are connected together through the pair of side tanks 12.
Namely, the tank portion 2A of the refrigerant evaporator (heat exchanger) is of a form in which the refrigerant passed through the first path portion 1P on the downstream side in the direction of air flow is introduced into the second path portion 2P on the upstream side in the direction of air flow being switched over right side left of the core portion, the tank portion 2A being constituted by the tank portions having the refrigerant collecting portions 10a, 11a which are flow passages having a function for guiding the refrigerant flew through the first path portion 1P to the ends of the tank in the right-and-left direction and the refrigerant distributing portions 10b, 10c, 11b, 11c which are flow passages for guiding the refrigerant to a group of tubes 4 forming the second path portion 2P, and by a header plate 7 having a refrigerant collecting space for the tubes 4, and wherein the side tanks 12 are provided to envelop the open portions at the ends of the tank portion in the right-and-left direction and to spatially connect the above flow passages, and separators 9 are provided at portions for accomplishing the spatial interruption thereby to constitute the front-and-rear right-and-left cross path.
According to the above constitution, an increased sectional area of the flow passage is obtained at the ends of the tank portion in the right-and-left direction (refrigerant flow corner portions) by simple means making it possible to decrease the pressure loss on the refrigerant side in the tank and to improve performance. Further, the refrigerant collecting portions 10a, 11a and the refrigerant distributing portions 10b, 10c, 11b, 11c are formed by laminating a header plate 7 for connecting the tubes 4, a tank header plate 11 forming the tank portions 11a to 11c integrally together, and a distributing plate 10 arranged therebetween and having communication holes 10a to 10c for communicating the tubes 4 with the tank portions 11a to 11c.
In the drawings illustrating the embodiment, the tank portion 11a is drawn in a large size and the tank portions 11b, 11c are drawn in a small size. However, they may have an equal size and no limitation is imposed on the size of the flow passages. If the tank portions 11a to 11c are uniformly arranged, the side tank 12 can be used for either the right side or the left side, and there is no difference in the size of the separators 9.
For this purpose, a cut-away portion k1 is formed in the tank portion 11b at an end in the longitudinal direction, and the side tank 12 is not provided with an opening 12b but has a shape 12b′ corresponding to the cut-away portion k1. The outer side surface of the side tank 12 is brought into contact with the end that is cut away in the longitudinal direction to block the communication. This makes it possible to omit the separators 9b which are the constituent parts and, hence, to suppress the cost. Further, the cut-away portion k can be used for positioning the side tank 12 in the direction of width of the core portion.
This also makes it possible to omit the separators 9b which are the constituent parts and, hence, to suppress the cost. Further, the cut portions k3 work to more reliably position the side tank 12 in the direction of width of the core portion, and can be machined more easily than the cut-away portion k1 of the embodiment 1.
This also makes it possible to omit the separators 9b which are the constituent parts and, hence, to suppress the cost. Further, the ends of the tanks can be used for positioning the side tank 12 in the direction of width of the core portion and, besides, the holes h1, h2 can be easily perforated from the upper side by machining.
The tank portion 2B of this embodiment is obtained by stacking, roughly on the core portion, a header plate 14, a space-forming plate 15, an intersecting plate 16, a space-forming plate 15 and a tank header plate 17. The tank header plate 17 is obtained by press-forming a plate member in a manner to form a line of tank portion 17a at the center. Header plate 14, space-forming plate 15 and intersecting plate 16 may constitute a double-sided clad member having brazing material 14c, 15c and 16c, respectively, clad onto their surfaces to facilitate brazing.
Similarly, the header plate 14, too, is obtained by press-forming a plate member in a manner to form a line of tank portion 14a at the center. Here, what makes the header plate 14 different from the tank header plate 17 is that tube holes 14b are perforated at the corresponding positions so that the tubes 4 can be connected thereto. The tank portions 14a and 17a constitute a pair of communication portions for communicating the first path portion 1P and the second path portion 2P with each other.
The space-forming plate 15 exhibits the refrigerant collecting/distributing space function, and is obtained by perforating, by presswork, space holes 15a in a plate member at positions corresponding to the tubes 4. The intersecting plate 16 forms flow passages by using the pair of communication portions 14a and 17a in a manner that the flow of the refrigerant passed through the first path portion 1P is changed over right side left as it is folded into the second path portion 2P. The communication holes 16a are perforated in the plate member at positions corresponding to the tubes 4, and erected portions that become the communication-blocking potions Ta to Td (see
Upon stacking them, there are formed the refrigerant collecting portions and the refrigerant distributing portions by using the space holes 15a, communication holes 16a and communication portions 14a, 17a. Caps 9 are arranged at both ends of the tank portions 14a, 17a. These parts are all formed by using aluminum and are integrally joined together by brazing.
Next described below is the flow of the refrigerant in the refrigerant evaporator 1 having the structure as described above.
On the other hand, the refrigerant (dotted line arrows in
Next, described below are the feature and the effect of the embodiment. First, the refrigerant evaporator exchanges the heat between the air flowing through the outer portion and the refrigerant flowing through the inner portion. The flow of the refrigerant has at least the first path portion 1P and the second path portion 2P between the refrigerant inlet portion 6a and the refrigerant outlet portion 6b. The refrigerant evaporator includes a core portion formed by a row of the tubes 4 arranged in parallel, refrigerant collecting portions 15a, 16a where the refrigerant is collected flowing through the first path portion 1P, refrigerant distributing portions 15a, 16a for distributing the refrigerant to the second path portion 2P, and a pair of tank portions 14a, 17a for communicating the refrigerant collecting portions 15a, 16a with the refrigerant distributing portions 15a, 16a. The core portion has a first row 1L of the tubes and a second row 2L of the tubes on the front and rear sides, respectively, to form the first path portion 1P and the second path portion 2P on the right and left whole regions. The refrigerant collecting portions 15a, 16a and the refrigerant distributing portions 15a, 16a are divided to the right and the left, respectively, and the pair of tank portions 14a and 17a work to communicate the refrigerant collecting portions 15a, 16a with the refrigerant distributing portions 15a, 16a formed in separate regions from each other in terms of the right-and-left direction.
Namely, the tank portion 2B for changing over the flow of the refrigerant is constituted as the front-and-rear right-and-left cross path by laminating the header plate 14 and the tank header plate 17 forming the tank portions 14a, 17a as two flow passages in the vertical direction at right angles with the direction of air flow or with the direction in which the tubes are arranged in parallel, the space-forming plate 15 that forms the refrigerant collecting/distributing space for the tubes 4, and the distributing plate 16 having a separator function for guiding the refrigerant from the space-forming plate 15 to the two flow passages (tank portions 14a, 17a) ahead and a separator function for separating the two flow passages (tank portions 14a, 17a).
According to the above constitution, the number of the refrigerant flow corner portions is smaller than that in the refrigerant evaporator 1 of the first embodiment, and the lengths of the flow passages are short in the tank portions making it possible to decrease the pressure loss on the refrigerant side in the tanks and to improve performance.
Further, the refrigerant collecting portions 15a, 16a, the refrigerant distributing portions 15a, 16a, and the pair of tank portions 14a, 17a, are formed by laminating a header plate 14 for connecting the tubes 4 and having the tank portion 14a, the space-forming plate 15 exhibiting the refrigerant collecting/distributing space function, the intersecting plate 16 having communication-blocking portions Ta to Td for communicating the refrigerant collecting portions 15a, 16a with the refrigerant distributing portions 15a, 16a in a crossing manner, respectively, in the separate regions in the right-and-left direction, the space-forming plate 15, and the tank header plate 17 having the tank portion 17a. There is, thus, obtained a simple constitution that can be easily mass-produced.
The tank header plate 17 illustrated in
So far, there existed a problem in that the tank portion has a curvature which is so large that the fins 5 come in surface contact with the surface of the tank causing the fins 5 to be melted. There further existed a problem in that the brazing material at the roots of the tubes 4 was pulled and a defective brazing was caused. So far, therefore, it was attempted to provide space between the tank surface and the fins 5. However, airflow resistance is small in space, and the air leaked from the space poses another problem of deteriorated heat-exchanging efficiency.
According to this embodiment, however, the tank protuberance has a small curvature, and there takes place a linear contact even if the fins 5 are brought into contact with the tank surface, and the fins are seldom melted. Besides, a distance is maintained from the roots of the tubes 4, and there occurs no defect at the roots. Further, no space exists between the tank surface and the fins 5, enhanced performance is obtained due to an increased heat-conducting area, and no air leaks from the above space suppressing a drop in the heat-exchanging efficiency. This further suppresses the generation of white mist which is a white vapor-like gas generated when the air that is not cooled comes in contact with the condensed water.
According to this constitution, the portion of required performance only can be selected as the front-and-back right-and-left cross path to optimize the temperature distribution, and the tank structure, too, can be partly simplified. The effect increases with an increase in the number of the front-and-rear right-and-left cross paths.
For example, when the constituent parts are to be assembled in the tank portion of the heat exchanger, it is a general practice to form the pawls for caulking on the parts to effect the bonding by caulking. In the heat exchanger that uses a carbon dioxide (CO2) refrigerant of a high pressure, however, it is a tendency to design the parts constituting the tanks to possess an increased thickness for ensuring the resistance to pressure as compared to those used for the heat exchanger that uses a conventional freon (R134a) refrigerant. Due to the thick plate, therefore, only limited space for caulking is maintained as compared to the prior art. According to the present invention, therefore, the caulking pawls are folded in a direction at right angles with the direction of the plate thickness t though it is in the direction of the plate thickness t in the prior art.
This permits the pawls 12d to be deformed requiring a decreased working force and, further, makes it possible to maintain space for caulking. Further, the plate thickness t is utilized for the caulking width to easily obtain strength necessary for the bonding by caulking.
The invention is not limited to the above embodiments only but can be variously applied within the scope set forth in claims. The above embodiments have dealt with the case of a supercritical refrigerating cycle by using the CO2 refrigerant. The invention, however, is not to limit the kinds of the refrigerants or the refrigerant pressure, and may, further, be applied to the refrigerating cycle by using, for example, a freon refrigerant. Though the above embodiments have dealt with the refrigerant evaporator, the invention can be, further, applied to the case of heating a fluid that is to be heated by using a heat medium other than the refrigerant. In this case, the constitution becomes as described below.
A heat exchanger for exchanging the heat between a fluid of which the temperature to be controlled flowing through the outer portion and a heat medium flowing through the inner portion, wherein the flow of the heat medium includes:
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