Abstract:
A plurality of water passages ( 62 A) allowing flow of water, a plurality of alcohol passages ( 62 A) allowing flow of alcohol and a plurality of high temperature gas passages ( 61 A) heating the water passages ( 62 A) and the alcohol passages ( 62 A), are independently provided in a heat exchanging portion ( 6 ). Liquid alcohol is supplied from a first header ( 1 ) to the alcohol passage ( 62 A) and water is supplied from a second header ( 7 ) to the water passage ( 62 A). The water passage ( 62 A) is preferably adapted to make contact with a high temperature section of the high temperature gas passage ( 61 A) and the alcohol passage ( 62 A) is preferably adapted to make contact with the low temperature section of the high temperature gas passage ( 61 A). By separately vaporizing water and alcohol in this way, the mixing ratio of the water vapor and alcohol vapor can be controlled with high response.

Description:
FIELD OF THE INVENTION  
         [0001]    This invention relates to a heat exchanger applied to a vaporizer of a fuel cell system for example.  
           [0002]    In a fuel cell system using a reformer, alcohol and water are vaporized in a heat exchanger and supplied to a reformer in the form of gaseous mixture in order to generate hydrogen gas which is supplied to the fuel cell system.  
           [0003]    Tokkai Hei 9-79694 published by the Japanese Patent Office in 1997 discloses a heat exchanger which vaporizes a mixture of two types of liquid. In this heat exchanger, a gaseous mixture of ammonia and water is produced from an ammoniacal solution.  
         BACKGROUND OF THE INVENTION  
         [0004]    When vaporizing a mixture of two liquids with a single heat exchanger, the mixing ratio of the liquid mixture must be varied in order to vary the mixing ratio of components in the gaseous mixture. In such a heat exchanger, however, when the mixing ratio of the liquid mixture is varied, the mixing ratio of the gaseous mixture will not coincide with a target ratio until the liquid which remains inside the heat exchanger is completely vaporized. In this type of heat exchanger, response characteristics related to control of the mixing ratio are low.  
           [0005]    Use of a plurality of heat exchangers for independently vaporizing different kinds of fluid and a mixer for mixing the different kinds of vaporized fluid may improve the response characteristics related to control of the mixing ratio. In a fuel cell system for a vehicle, however, it is difficult to obtain a space for accommodating a plurality of heat exchangers.  
           [0006]    It is therefore an object of this invention to increase the control characteristics on the mixing ratio of a plurality of liquids when using a single heat exchanger.  
           [0007]    In order to achieve the above object, this invention provides a heat exchanger which performs heat exchange between a high temperature fluid and a low temperature fluid. The heat exchanger comprises a heat exchanging portion comprising a first fluid passage allowing flow of a first low temperature fluid, and a second fluid passage partitioned from the first fluid passage and allowing flow of a second low temperature fluid. The heat exchanger further comprises a first supply mechanism which supplies the first low temperature fluid to the first fluid passage, and a second supply mechanism which supplies the second low temperature fluid to the second fluid passage.  
           [0008]    This invention also provides a heat changer comprising a heat exchanging portion comprising a water passage allowing flow of water, an alcohol passage allowing flow of alcohol, and a high temperature fluid passage for heating the water passage and the alcohol passage. The high temperature fluid passage comprises a high temperature section having a contact with the water passage, and a low temperature section having a lower temperature than the high temperature section and having a contact with the alcohol passage. The heat exchanger further comprises a water supply mechanism supplying water to the water passage, and an alcohol supply mechanism supplying alcohol to the alcohol passage.  
           [0009]    The details as well as other features and advantages of this invention are set forth in the remainder of the specification and are shown in the accompanying drawings. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0010]    [0010]FIG. 1 is a split perspective view of a heat exchanger according to this invention.  
         [0011]    [0011]FIG. 2 is a longitudinal sectional view of a header according to this invention.  
         [0012]    [0012]FIG. 3 is similar to FIG. 1, but showing a second embodiment of this invention.  
         [0013]    [0013]FIG. 4 is a plan view of a fluid supply member and a comb-shaped plate according to the second embodiment of this invention. 
     
    
     DESCRIPTION OF THE PREFERRED EMBODIMENTS  
       [0014]    Referring to FIG. 1 of the drawings, a heat exchanger according to this invention comprises a first header  1  and a second header  7  mounted on the top of a heat exchanging portion  6 , a first fluid supply member  3  mounted on a lateral face of the first header  1  and a second fluid supply member  9  mounted on the lateral face of the second header  7 . This heat exchanger is used as a vaporizer which vaporizes methanol and water in a fuel cell system by heat exchange with a high temperature gas.  
         [0015]    The first header  1  comprises a top plate  1 A, a bottom plate  1 B and a comb-shaped plate  2 .  
         [0016]    Referring to FIG. 2, the top plate  1 A and the bottom plate  1 B are fixed to each other by soldering or welding with the comb-shaped plate  2  vertically sandwiched therebetween.  
         [0017]    Referring again to FIG. 1, the comb-shaped plate  2  comprises a plurality of arms  2 B disposed in parallel at equal intervals and a connecting member  2 A connecting an end of each arm  2 B. The first fluid supply member  3  seals the opening on the lateral face of the header  1  which is positioned to face another end of each arm  2 B. The length of the arms  2 B is set so that a fluid distribution space Sb is formed between the first fluid supply member  3  and the end of the arms  2 B. The thickness of the comb-shaped plate  2  is approximately one millimeter.  
         [0018]    The space between adjacent arms  2 B forms a conducting passage  5  which extends at right angles to the cross-section of the header  1  shown FIG. 2. The upper end of the conducting passage  5  is delimited by the top plate  1 A and the bottom end is delimited by the bottom plate  1 B. Each conducting passage  5  is connected to the fluid distribution space Sb. It is preferred that the width of the conducting passage  5  is set to the minimum value which satisfies a liquid methanol supply amount from the header  1  to the heat exchanging portion  6 . The width of the arms  2 B is determined based on this condition.  
         [0019]    Two fluid outlets  3 A which open towards the fluid distribution space Sb are formed in the first fluid supply member  3 . The fluid outlets  3 A are connected to a water supply pump via two supply pipes  3 B which project from the fluid supply member  3  in an opposite direction to the fluid outlet  3 A.  
         [0020]    Through holes  4  are formed at equal intervals on the bottom plate  1 B at positions facing each conducting passage  5 . The second header  7  comprises a top plate  7 A, a bottom plate  7 B and a comb-shaped plate  8 . The comb-shaped plate  8  comprises a plurality of parallel arms  8 B and a connecting member  8 A. The fluid supply passage  9  is provided with only a single fluid outlet  9 A which is connected to a water supply pump via a connecting pipe  9 B.  
         [0021]    The basic structure of the second header  7  is the same as the first header  1 . A fluid distribution space Sc is formed between the arms  8 B and the second fluid supply member  9  and a conducting passage  50  is formed between adjacent arms  8 B. Through holes  40  are formed on the bottom plate  7 B at equal intervals at positions facing each conducting passage  50 .  
         [0022]    The first header  1  and the second header  7  are disposed adjacent to each other on the top of the heat exchanger  6 . However the two headers  1  and  7  are disposed so that the direction of flow in the conducting passage  50  of the second header  7  and the direction of supply of fluid from the second fluid supply member  9  to the second header  7  are respectively orthogonal to the direction of flow in the conducting passage  5  of the first header  1  and the direction of supply of fluid from the second fluid supply member  3  to the first header  1 .  
         [0023]    The heat exchanging portion  6  is formed by alternately laminating a high temperature fluid layer  61  which allows flow of high temperature fluid and a low temperature fluid layer  62  which allows flow of a low temperature fluid in a vertical direction. These layers are laminated perpendicular to one another. The high temperature layer  61  and the low temperature layer  62  are insulated by a partition. A plurality of passages  61 A which pass horizontally through the layers are formed in the high temperature layers  61 . A plurality of passages  62 A which pass vertically through the layers are formed in the low temperature layers  62 .  
         [0024]    Each passage  61 A has an opening on a lateral face of the high temperature fluid layer  62 . High temperature gas is supplied in the direction of an arrow in FIG. 1 in each passage  61 A. The high temperature gas passes horizontally through each passage  61 A and is discharged from the opposite end of the heat exchanging portion  6 .  
         [0025]    Each passage  62 A has an opening on the top end of the low temperature fluid layer  62 .  
         [0026]    The through hole  4  in the bottom plate  1 B of the first header  1  and the through hole  40  in the bottom plate  7 B of the second header  7  are disposed so that both are directly above the passage  62 A.  
         [0027]    In this heat exchanger, liquid methanol is supplied to the first header  1  through the first fluid supply member  3  and water is supplied to the second header  9  through the second fluid supply member  9 .  
         [0028]    The second header  7  is disposed upstream of the first header  1  with respect to the flow of high temperature gas in the passage  61 A. The boiling point of the water supplied to the second header  7  is higher than the boiling point of methanol supplied to the first header  1 . In order to effectively vaporize two different kinds of liquids, a header handling liquid with a higher boiling point should therefore be disposed at a position nearer to the inlet of the passage  61 A than a header handling a liquid with a lower boiling point.  
         [0029]    In the first header  1 , liquid methanol is supplied to each conducting passage  5  from the fluid distribution space Sb and drips in equal amounts from the through holes  4  to the passage  62 A of the low temperature fluid layer  62 . However, of the passages  62 A in the low temperature fluid layer  62 , liquid methanol only drips into the passages  62 A positioned below the first header  1 . Liquid methanol does not drip into the passages  62 A positioned below the second header  7 .  
         [0030]    In the second header  7 , water is supplied to each conducting passage  8 B from the fluid distribution space Sc and drips from the through hole  40  down into the passage  62 A of the low temperature fluid layer  62 . However, of the passages  62 A in the low temperature fluid layer  62 , water only drips into the passages  62 A positioned below the second header  7 . Water does not drip into the passages  62 A positioned below the first header  1 .  
         [0031]    Thus the liquid methanol and water dripping down into the low temperature fluid layer  62  do not mix and are respectively heated and vaporized by heat exchange with the high temperature gas of the high temperature fluid layer  61 . The methanol vapor and water vapor are separately discharged from the lower end of the low temperature fluid layer  62 . The fuel cell system may mix discharged fuel vapor and water vapor before supplying them to a reformer, or alternatively, they may separately be supplied to the reformer.  
         [0032]    Thus water and methanol are not mixed at all in the heat exchanger and are vaporized in separate passages. Therefore when varying the mixing ratio of methanol vapor and water vapor, varying the supply amount of water or liquid methanol to the heat exchanger makes it possible to vary the mixing ratio of methanol vapor and water vapor discharged from the heat exchanger with high response characteristics.  
         [0033]    In this embodiment, the high temperature gas corresponds to a high temperature fluid, methanol corresponds to a first low temperature fluid and water corresponds to a second low temperature fluid.  
         [0034]    The top plate  1 A corresponds to a first top plate and the top plate  7 A corresponds to the second top plate. The bottom plate  1 B corresponds to a first bottom plate and the bottom plate  7 B corresponds to a second bottom plate. The passage  62 A positioned below the first header  1  corresponds to a first fluid passage or alcohol passage and the passage  62 A positioned below the second header  7  corresponds to a second fluid passage or water passage. The passage  61 A corresponds to a high temperature fluid passage. The first header  1  and the first fluid supply member  3  correspond to a first supply mechanism or an alcohol supply mechanism. The second header  7  and the second fluid supply member  9  correspond to a second supply mechanism or a water supply mechanism. The holes  4  correspond to a first group of holes and the holes  40  correspond to a second group of holes. The fluid distribution space Sb corresponds to a first fluid distribution space and the fluid distribution space Sc corresponds to a second fluid distribution space. The conducting passage  5  corresponds to a first conducting passage and the conducting passage  50  corresponds to a second conducting passage.  
         [0035]    A second embodiment of this invention will now be described with reference to FIGS. 3 and 4.  
         [0036]    In this embodiment, a single header  21  is used instead of the first header  1  and the second header  7 . A water passage and a liquid methanol passage are separately formed in the header  21 .  
         [0037]    Referring to FIG. 3, the header  21  comprises a top plate  21 A, a bottom plate  21 B and a comb-shaped plate  22 .  
         [0038]    The top plate  21 A and the bottom plate  21 B are fixed to each other by welding or soldering with the comb-shaped plate  22  vertically sandwiched therebetween.  
         [0039]    A fluid supply member  23  is mounted on the lateral face of the header  21 . Three fluid outlets  23 A- 23 C are formed in the fluid supply member  23  and open towards the interior of the header  21 . The fluid outlets  23 A and  23 C are disposed on both sides of the fluid outlet  23 B and are respectively connected to a methanol supply pump via two connecting pipes  23 D,  23 F which project from the fluid supply member  23  in an opposite direction to the fluid outlets  23 A,  23 C. The central fluid outlet  23 B is connected to a water supply pump via a supply pipe  23 E which projects from the fluid supply member  23  in a direction opposite to the fluid outlet  23 B.  
         [0040]    Referring to FIG. 4, the comb-shaped plate  22  is provided with a long arm  22 B and a short arm  22 C which are disposed alternately at equal intervals. An end of the respective arms  22 B and  22 C are connected to a connecting member  22 A. Another end of the long arm  22 B reaches the fluid supply member  23  and in this manner partitions the fluid distribution spaces Sb 1 -Sb 3  which independently face the fluid outlets  23 A- 23 C. A conducting passage  25 A ( 25 B,  25 C) is formed between adjacent arms  22 B and  22 C. The conducting passages  25 A are connected to the fluid distribution spaces Sb 1 , the conducting passages  25 B are connected to the fluid distribution spaces Sb 2 , and the conducting passages  25 C are connected to the fluid distribution spaces Sb 3 .  
         [0041]    Referring again to FIG. 3, holes  41  are formed at equal intervals in the bottom plate  21 B corresponding to each conducting passage  25 A- 25 C in a manner similar to the holes  4  formed in the bottom plate  1 B of the first embodiment.  
         [0042]    The structure of the heat exchanger  6  is the same as that described with reference to the first embodiment.  
         [0043]    In this heat exchanger, liquid methanol is only supplied to the conducting passage  25 A connected to the fluid distribution space Sb 1  and the conducting passage  25 C which is connected to the fluid distribution space Sb 2 . Thus liquid methanol only drips into the passages  62 A of the low temperature fluid layer  62  which are positioned below the conducting passages  25 A and  25 C.  
         [0044]    On the other hand, only water is supplied to the conducting passage  25 C which is connected to the fluid distribution space Sb 2 . Thus water only drips into the passages  62 A of the low temperature fluid layer  62  which are placed below the conducting passage  25 B. High temperature gas is supplied to the high temperature fluid layer  61  of the heat exchanging portion  6  in the same manner as the first embodiment. At this time, the high temperature fluid layers  61  located at the center of the heat exchanging portion  6  tend to have a higher temperature than the high temperature fluid layers  61  located near to both lateral faces of the heat exchanging portion  6 .  
         [0045]    According to this embodiment, water which has a higher boiling point drips into the high temperature fluid layers  61  located at the center of the heat exchanging portion  6 . Liquid methanol which has a lower boiling point drips into the high temperature fluid layers  61  located near to both lateral faces of the heat exchanging portion  6 . Thus it is possible to perform highly efficient vaporization of the liquid methanol and water in the same manner as the first embodiment. The heat exchanger according to this embodiment makes it possible to process two types of fluid separately using a single header  21 . This allows the structure to be simplified and manufacturing costs to be reduced in comparison to the heat exchanger according to the first embodiment.  
         [0046]    In each of the embodiments above, fluid is supplied from the top of the heat exchanging portion  6 . However it is possible to mount a structural member equivalent to the first header  1  and the second header  7  or the header  21  on the lower face of the heat exchanging portion  6  and to discharge fluid vapor to the top of the heat exchanging portion  6 . Furthermore it is possible to form the passages  61 A of the high temperature fluid layer  61  vertically, to form the passages  62 A of the low temperature fluid layer  62  horizontally and to mount a structural member equivalent to the header on the lateral face of the heat exchanging portion  6 .  
         [0047]    In each of the above embodiments, the fluid distribution spaces Sb, Sc, Sb 1 , Sb 2 , Sb 3  and the conducting passages  5 ,  50 ,  25 A- 25 C are partitioned by the comb-shaped plates  2 ,  8 ,  22  inside the header  1 ,  7 , or  21 .  
         [0048]    However it is possible to partition a plurality of spaces having a waveform cross section by press forming any of the top plates  1 A,  7 A,  21 A or the bottom plates  1 B,  7 B,  21 B. Furthermore it is possible to assign the fluid distribution spaces Sb, Sc, Sb 1 , Sb 2 , Sb 3  and the conducting passages  5 ,  50 ,  25 A- 25 C to these spaces. In this manner, the comb-shaped plate becomes unnecessary which reduces the cost of manufacturing the header and improves the rigidity thereof.  
         [0049]    In this embodiment, the fluid distribution spaces Sb 1  and Sb 2  correspond to a first fluid distribution space and the fluid distribution space Sb 2  corresponds to the second fluid distribution space. The conducting passages  25 A and  25 C correspond to a first conducting passage and the conducting passage  25 B corresponds to a second conducting passage. The fluid outlets  23 A and  23 C correspond to a first outlet and the fluid outlet  23 B corresponds to a second outlet.  
         [0050]    The contents of Tokugan 2001-60089 with a filing date of Mar. 5, 2001 in Japan, are hereby by reference. Although the invention has been described above by reference to certain embodiments of the invention, the invention is not limited to the embodiments described above. Modifications and variations of the embodiments described above will occur to those skilled in the art, in light of the above teachings.  
         [0051]    The embodiments of this invention in which an exclusive property or privilege is claimed are defined as follows: