Abstract:
A processing device and processing method that can perform processing of a starting material fluid while favorably controlling the processing temperature of same. The processing device includes: a processing member that leads in the starting material fluid and processes same therewithin; and a processing tank that houses the processing member and retains the processed processing products. The processing member includes: a minute duct provided therewithin and causes the flow-through of the starting material fluid; and a heat medium duct that causes the flow-through of a heat medium having a different temperature from that of the starting material fluid flowing through the minute duct. The minute duct and the heat medium duct are separated from each other so that heat exchange is possible between the starting material fluid and heat medium flowing through.

Description:
This application is the U.S. National Phase of PCT Application No. PCT/JP2014/002040, now WO 2014/174781, filed Apr. 9, 2014, which claims priority to Japanese Application No. JP2013-089305, filed Apr. 22, 2013, the disclosure of which are incorporated in their entirety by reference herein. 
     TECHNICAL FIELD 
     The present invention relates to a processing device and a processing method in which a material fluid can be subjected to a chemical process such as extraction, separation, and reaction while finely adjusting a processing temperature. 
     BACKGROUND ART 
     For example, as in a case where synthesis of organic compounds or the like is performed, there is sometimes a case where a material fluid supplied into a processing bath is subjected to a chemical process such as extraction, separation, and reaction while finely adjusting a processing temperature. This process requires provision of a temperature regulation mechanism inside the processing bath and strict control of the processing temperature (reaction temperature). As the temperature regulation mechanism, for example, a coil shape heat exchanger, a temperature-regulating jacket, and the like are used. 
     The heat exchanger is used while being immersed in the material fluid stored in the processing bath. The heat exchanger has a spiral shape pipe made of metal excellent in thermal conductivity. (For example, refer to  FIG. 5B ). A heated or cooled heat medium is circulated inside this spiral shape pipe, and by performing heat exchange between this heat medium and the material fluid through a pipe wall of the pipe, the temperature of the material fluid can be adjusted to be a desired processing temperature. 
     The temperature-regulating jacket is a hollow member arranged so as to surround the processing bath, and a heat medium can be accumulated inside the temperature-regulating jacket. Therefore, as well as the above heat exchanger, by supplying a heat medium at a desired temperature into the temperature-regulating jacket, heat exchange can be performed between the heat medium and the material fluid via a bath wall of the processing bath. Thereby, the temperature of the material fluid can be adjusted to be a target processing temperature. 
     In a case of the temperature regulation mechanism in which the heat exchanger or the temperature-regulating jacket is used, a surface of the heat exchanger or an inner wall surface of the processing bath where the temperature-regulating jacket is attached is heated or cooled much more than other places. Thus, great temperature variation easily occurs inside the processing bath. Therefore, in a case where the temperature regulation mechanism described above is used, in general, an agitating means as shown in Non-patent Document 1 is provided inside the processing bath so as to agitate the material fluid in the processing bath, and the process is performed while equalizing the temperature of the material fluid inside the processing bath as far as possible. 
     However, even when the material fluid is agitated in the reaction bath by the agitating blade or the like, a lot of time is required for heating and cooling in a case of a large heat capacity of the processing bath. In particular, with the heat exchanger and the temperature-regulating jacket described above, a heat transmission area to be ensured on a surface of the coil and the jacket is limited. Thus, speed-up of heating and cooling is also limited. 
     As a matter of course, the speed-up of heating and cooling by strengthening of agitation by the agitating blade or an increase in a temperature difference between the material fluid and the heat medium can be expected. However, depending on the type of the material fluid, excessively strong agitation invites segmentation of the material fluid, and there is sometimes a case where it takes a rather long time for separating the segmentalized material fluid into the original simple material fluid. There is also a fear that an excessive increase in the temperature difference between the material fluid and the heat medium invites thermal decomposition of the material fluid. Thus, there is sometimes a case where it becomes difficult to adopt the increase. 
     Therefore, in the conventional processing device and the processing method, even when agitation is performed by the agitating blade, it is actually difficult to adjust the temperature of the material fluid for a short time or to precisely control the temperature. 
     CITATION LIST 
     Patent Document 
     
         
         Non-patent Document 1: Iizumi Shingo, Oct. 25, 1978. Chemical engineering handbook 4th ed. Maruzen Co., Ltd. P. 1322-1323 (second impression: Dec. 25, 1980) 
       
    
     SUMMARY OF THE INVENTION 
     An object of the present invention is to provide a processing device and a processing method in which a material fluid can be subjected to a process while favorably controlling a processing temperature of the material fluid. 
     The present invention is to provide a processing device for subjecting a material fluid to a process while controlling a processing temperature of the material fluid. This processing device includes a processing member into which the material fluid is guided and subjected to the process inside, and a processing bath that accommodates the processing member and stores a processing product provided by the process in the processing member. The processing member has at least one minute flow passage provided inside the processing member, the minute flow passage inside which the material fluid is circulated, and at least one heat medium flow passage provided inside the processing member, the heat medium flow passage inside which a heat medium having a temperature different from the temperature of the material fluid circulated in the at least one minute flow passage is circulated, and the at least one minute flow passage and the at least one heat medium flow passage are isolated from each other in such a manner that heat exchange is capable of being performed between the material fluid flowing through the minute flow passage and the heat medium flowing through the heat medium flow passage. 
     The present invention is also to provide a processing method for subjecting a material fluid to a process while controlling a processing temperature of the material fluid. This processing method includes the steps of preparing a processing device which includes a processing member having minute and heat medium flow passages isolated from each other, the processing member into which the material fluid is guided and subjected to the process inside, and a processing bath that accommodates the processing member and stores a processing product provided by the process in the processing member, and adjusting the processing temperature of the material fluid in the minute flow passage by circulating the material fluid in the minute flow passage of the processing member, circulating a heat medium having a temperature different from the temperature of the material fluid circulated in the minute flow passage in the heat medium flow passage, and performing heat exchange between the material fluid and the heat medium inside the processing member. 
    
    
     
       BRIEF DESCRIPTION OF DRAWINGS 
         FIG. 1A  is a flowsheet showing a flow of fluids at the start of a process in a processing device of a first embodiment of the present invention. 
         FIG. 1B  is a flowsheet showing a flow of the fluids at the end of the process in the processing device of the first embodiment. 
         FIG. 2A  is a flowsheet showing a flow of fluids at the start of a process in a processing device of a second embodiment of the present invention. 
         FIG. 2B  is a flowsheet showing a flow of the fluids at the end of the process in the processing device of the second embodiment. 
         FIG. 3  is a flowsheet showing a processing device of a third embodiment of the present invention. 
         FIG. 4  is a perspective view showing a plurality of single plate members forming a processing member in the processing device. 
         FIG. 5A  is a view showing temperature distribution of a material fluid inside a processing bath in the processing device shown in  FIGS. 1A and 1B . 
         FIG. 5B  is a view showing temperature distribution of a material fluid inside a processing bath in a conventional processing device. 
     
    
    
     DESCRIPTION OF EMBODIMENTS 
     Hereinafter, embodiments of the present invention will be described based on the drawings. 
       FIGS. 1A and 1B  show a reaction device  1  according to a first embodiment serving as one example of a processing device according to the present invention. In the processing device according to the present invention, by using at least one type of material fluid, a chemical operation (chemical process) such as extraction, separation, and reaction is performed while adjusting a temperature of the material fluid to a predetermined processing temperature. This chemical operation includes the following operations. 
     For example, the processing device according to the present invention can be applied to a device in which the “reaction” is performed as the above chemical operation like the reaction device  1 , specifically, a device in which a reaction product is obtained by mixing two or more types of material fluids and chemically reacting the material fluids with each other at a predetermined processing temperature. The reaction device to which the present invention can be applied includes a device into which only one type of material fluid is introduced, in other words, a device in which no mixing is performed and chemical reaction of the material fluid is performed by heating the material fluid to a predetermined processing temperature or the like. 
     The processing device according to the present invention can also be applied to a device in which the “extraction” is performed as the above chemical operation. Specifically, the processing device can also be applied to a liquid-liquid extraction device in which immiscible first and second material fluids, for example, a heavy solution such as water and a light solution having smaller specific gravity than the heavy solution such as oil are brought into contact with each other in a flow passage, a substance to be extracted contained in the light solution (oil) is moved to the heavy solution (water), and the substance to be extracted is taken out as a water solution. 
     Any of the following first to third embodiments relates to the reaction device  1  in which two or more types of material fluids are mixed and chemically reacted with each other at a predetermined temperature. 
     As shown in  FIGS. 1A and 1B , in the reaction device  1  of the first embodiment, a first material fluid  31  and a second material fluid  32  are reacted with each other while being mixed, so as to produce a reaction product  33 , that is, a processing product. This reaction device  1  includes a processing member  2  into which the first material fluid  31  and the second material fluid  32  are guided and reacted with each other while being mixed inside, a reaction bath  3  serving as a processing bath that stores the reaction product  33  obtained by the reaction in this processing member  2 , a material bath  4 , and a plurality of processing pipes  5 . Inside the processing member  2 , a plurality of minute flow passages  10  and a plurality of heat medium flow passages  11  are formed as described in detail later. 
     The material bath  4  is provided outside the reaction bath  3  so as to store the first material fluid  31 . The second material fluid  32  serving as the other material fluid is preliminarily stored inside the reaction bath  3 . The processing member  2  is immersed in the second material fluid  32  inside the reaction bath  3 . The plurality of processing pipes  5  is arranged between the material bath  4  and the reaction bath  3  and around the reaction bath  3  so as to allow movement of the first material fluid  31  in the material bath  4  and the second material fluid  32  in the reaction bath  3  between the baths  3 ,  4 . 
     Next, details of the reaction bath  3 , the material bath  4 , and the plurality of processing pipes  5  arranged between these baths  3 ,  4  and around the reaction bath  3  will be described. 
     The reaction bath  3  serving as the processing bath is a cylindrical bottomed container having an opening toward the upper side, and is capable of storing the first and second material fluids  31 ,  32  and the reaction product  33  obtained by the reaction of these material fluids inside. The upper opening of this reaction bath  3  is closed by a lid (not shown) or the like if necessary. Inside the reaction bath  3 , the above processing member  2  can be accommodated in a state where the processing member is immersed in the material fluid or the reaction product  33 . 
     The fluid to be accommodated in the reaction bath  3  is changed depending on a progress state of the reaction. That is, the type of the fluid accommodated in the reaction bath  3  is different between the start of processing and the end of processing. Specifically, before the reaction is started as shown in  FIG. 1A , the fluid accommodated in the reaction bath  3  is only the second material fluid  32 . However, once the reaction is started, the reaction product  33  is produced inside the processing member  2  and successively stored in the reaction bath  3 . Thus, the fluid accommodated in the reaction bath  3  becomes a mixture of the second material fluid  32  and the reaction product  33 . Then, when almost all the material fluids  31 ,  32  are reacted and changed as shown in  FIG. 1B , the fluid accommodated in the reaction bath  3  becomes only the reaction product  33 . This change in the material fluid to be accommodated in the reaction bath  3  will be described in detail later. 
     As shown in  FIGS. 1A and 1B , the plurality of processing pipes  5  includes a first pipe  6 , a second pipe  7 , and a third pipe  8 . 
     The first pipe  6  has an inlet side end connected to the material bath  4 , and an outlet side end connected to the processing member  2  in the reaction bath  3 . Through this first pipe  6 , the first material fluid  31  is supplied from the material bath  3  toward the processing member  2 . 
     A first pump  51  and a switching valve  9  are provided in the middle of the first pipe  6 . The first pump  51  pressure-feeds the first material fluid  41  from the material bath  4  toward the reaction bath  3 . The switching valve  9  switches a point to which an inlet of the pump  51  is connected between the material bath  4  storing the first material fluid  31  and the third pipe  8 . In a case where the first material fluid  31  remains in the material bath  4  as shown in  FIG. 1A , this switching valve  9  switches the flow passage in such a manner that the material bath  4  storing the first material fluid  31  is connected to the pump  51 . Meanwhile, when all the first material fluid  31  in the material bath  4  is gone as shown in  FIG. 1B , the switching valve switches the flow passage in such a manner that the reaction product  33  is fed to the pump  51  while merging the fluid in the reaction bath  3  (mixture of the reaction product  33  and the unreacted second material fluid  32 ) into the first material fluid  31  in the first pipe  6  via the third pipe  8  to be described in detail later. 
     The second pipe  7  has an inlet side end provided inside the reaction bath  3 , and an outlet side end coupled to the processing member  2 , and is arranged so as to suction and supply the second material fluid  32  preliminarily stored in the reaction bath  3  and the reaction product  33  into the processing member  2  again. The inlet side end of this second pipe  7  is attached at a low position inside the reaction bath  3 , the position where the second pipe can suction the second material fluid  32  preliminarily stored in the reaction bath  3  at the start of processing. In the middle of the second pipe  7 , a pump  52  that pressure-feeds the second material fluid  32  or the reaction product  33  through this second pipe  7  is arranged. 
     Specifically, this second pipe  7  is arranged along a route of once extending toward the outside of the reaction bath  3  from the inlet side end provided inside the reaction bath  3 , going via the second pump  52  provided outside the reaction bath  3 , and then returning into the processing member  2  again. That is, in a case where the fluid stored in the reaction bath  3  is almost the second material fluid  32  as shown in  FIG. 1A , this second material fluid  32  is circulated in the second pipe  7 . However, when the reaction product  33  is also stored in the reaction bath  3  in addition to the second material fluid  32  as shown in  FIG. 1B , the mixture of the second material fluid  32  and the reaction product  33  is circulated in the second pipe  7 . Therefore, the second pipe  7  can also be called as a pipe in which the second material fluid  32  is reacted while being circulated between the processing member  2  and the reaction bath  3 . 
     The third pipe  8  is used for supplying the unreacted first material fluid  31  stored in the reaction bath  3  into the processing member  2  again after feeding almost all the first material fluid  31  in the material bath  4  to the processing member  2  through the first pipe  6  and reacting, so as to enhance a reaction rate. This third pipe  8  has an inlet side end and an outlet side end, and the outlet side end is connected to the switching valve  9 . The inlet side end, that is, the end on the suction side of the third pipe  3  is attached to a relatively high position inside the reaction bath  3 . This position is set to be a position where the third pipe can suction the second material fluid  32  and the reaction product  33  only after the reaction progresses to some extent, a large amount of the reaction product  33  is stored in the reaction bath  3 , and a liquid level in the reaction bath  3  becomes higher than predetermined height. 
     The processing member  2  is accommodated inside the above reaction bath  3  (processing bath), and the material fluids are guided inside and chemical reaction of the material fluids is performed inside. Specifically, this processing member  2  has the plurality of minute flow passages  10  formed inside the processing member  2  so as to allow circulation of the material fluids. The first and second material fluids  31 ,  32  are supplied into and mixed inside the minute flow passages  10  and thereby reacted with each other so as to produce the reaction product  33 . Similarly, inside the processing member  2 , the plurality of heat medium flow passages  11  in which a heat medium having a temperature different from the temperature of the material fluid circulated in the minute flow passages  10  can be circulated is formed. The minute flow passages  10  and the heat medium flow passages  11  are formed so as to be isolated from each other in such a manner that heat exchange can be performed between the material fluid flowing through the minute flow passages  10  and the heat medium flowing through the heat medium flow passages  11  inside the processing member  2 . 
     Next, details of the processing member  2  and the plurality of minute flow passages  10  and the plurality of heat medium flow passages  11  formed in this processing member  2  will be described. 
     In the processing member  2 , the first material fluid  31  supplied through the first pipe  6  and the second material fluid  32  supplied through the second pipe  7  are brought into contact and reacted with each other in the minute flow passages  10 , so that the consequently-obtained reaction product  33  can be taken out. 
     This processing member  4  has a plate shape main body  12  elongated along the up and down direction as shown in  FIG. 4 . This main body  12  is made of metal, synthetic resin, ceramics, or the like having corrosion resistance and heat resistance with respect to the first and second material fluids  31 ,  32  and the reaction product  33 , and has an outer appearance of a thick plate shape (square shape) with relatively great thickness in the plate thickness direction. The plurality of minute flow passages  10  is formed inside the main body  12  so as to pass through the main body  12  in the up and down direction or the horizontal direction, and plural rows of the minute flow passages are formed so as to line up in the plate thickness direction. The first and second material fluids  31 ,  32  can be brought into contact and reacted with each other, that is, subjected to a process inside the respective minute flow passages  10 . The minute flow passages  10  favorably have width of for example about 0.1 mm to 5.0 mm. 
     Each of the plurality of heat medium flow passages  11  is formed between the minute flow passages  10  adjacent to each other in the plate thickness direction inside the processing member  2 , and allows circulation of the heat medium for adjusting the temperatures of the material fluids  31 ,  32  and the reaction product  33  circulated in the minute flow passages  10 . Plural rows of the heat medium flow passages  11  are provided so as to pass through the main body  12  of the processing member  2  in the up and down direction or the horizontal direction in correspondence with the minute flow passages  10 . That is, inside the processing member  2 , the minute flow passages  10  and the heat medium flow passages  11  are spaced from each other in the plate thickness direction and arranged so as to alternately line up in the plate thickness direction. 
     Specifically, the plurality of minute flow passages  10  respectively includes reaction flow passages  13  passing through the main body  12  of the processing member  2  in the up and down direction, and merging flow passages  14  extending in the horizontal direction in the main body  12 . 
     As shown in  FIG. 4 , in each of the reaction flow passages  13 , by reacting the first material fluid  31  supplied through the first pipe  6  in the reaction flow passage  13  while guiding the first material fluid along the reaction flow passage  13 , the reaction product  33  is produced. Since this reaction flow passage  13  passes through the inside of the main body  12  in the up and down direction as described above, the reaction flow passage has a first intake port  15  opened on a bottom surface of the main body  12 . The above first pipe  6  is connected to this first intake port  15 , and the first material fluid  31  taken in (suctioned) from the material bath  4  is guided to the upper side through the inside of the main body  12 . The reaction flow passage  13  also has a take-out port  16  opened on an upper surface of the main body  12 , and the already-reacted reaction product  33  is taken out through this take-out port  16 . In such a way, the reaction product  33  taken out from the take-out port  16  is fed to the reaction bath  3  and stored. 
     In each of the merging flow passages  14 , the second material fluid  32  supplied through the second pipe  7  is merged into the first material fluid  31  flowing through the reaction flow passage  13 . The merging flow passage  14  extends in the main body  12  of the processing member  2  along the direction orthogonal to the reaction flow passage  13 , that is, the horizontal direction. An outer end of the merging flow passage  14  forms a second intake port  17  opened on a side surface of the main body  12  of the processing member  2 . That is, the merging flow passage  14  is formed so as to extend from the second intake port  17  in the horizontal direction in the main body  12 . The above second pipe  7  is connected to the second intake port  17 , and the second material fluid  32  fed via this second pipe  7  can be supplied into the merging flow passage  14 . An inner end of the merging flow passage  14  forms a merging port  18  connected to an up-down intermediate part of the reaction flow passage  13  corresponding to this merging flow passage, and allows the second material fluid  32  flowing through the merging flow passage  14  to be merged into the fluid flowing in the reaction flow passage  13  from the merging port  18 . 
     The heat medium flow passages  11  allow the circulation of the heat medium for adjusting the temperatures of the material fluids flowing through the minute flow passages  10  which include the above reaction flow passages  13  and the merging flow passages  14  respectively, and are respectively formed at positions away from the minute flow passages  10  by a predetermined distance along the plate thickness direction inside the main body  12  of the processing member  2 . The heat medium flow passages  11  are arranged so as to be parallel to the minute flow passages  10 , that is, not to cross the minute flow passages  10 . 
     That is, the minute flow passage  10  and the heat medium flow passage  11  corresponding to this are arranged so as to be adjacent to each other through a thin partition wall in the plate thickness direction. Therefore, heat exchange can be performed between the heat medium circulated in the heat medium flow passage  11 , the heat medium having the temperature different from the temperature of the material fluid flowing through the minute flow passage  10 , and the material fluid flowing through the minute flow passage  10 . Therefore, by adjusting the temperature of the heat medium flowing through the heat medium flow passage  11  adjacent to the minute flow passage  10 , the temperature of the fluid flowing through the minute flow passage  10  can be precisely adjusted. 
     In order to form the above plurality of minute flow passages  10  and the plurality of heat medium flow passages  11  inside the processing member  2 , for example the following method can be adopted. 
     Firstly, as shown in  FIG. 4 , a plurality of single plate members  20  and a plurality of isolation plates  21  formed in rectangles in which height serving as size in the up and down direction is greater than width serving as size in the horizontal direction are prepared. The single plate members  20  and the isolation plates  21  are alternately laminated in such as manner that along the plate thickness direction, the isolation plate  21  is arranged next to one of the single plate members  20 , and another one of the single plate members  20  is arranged next to this isolation plate  21 . Thereby, the above plurality of minute flow passages  10  and the plurality of heat medium flow passages  11  are formed inside the processing member  2 . 
     Each of the single plate members  20  is a plate shape member having the same height and width as those of each of the isolation plates  21  but having thickness greater than thickness of the isolation plate  21 . The plurality of single plate members  20  includes a plurality of first single plate members  22  for forming the above minute flow passages  10 , and a plurality of second single plate members  23  for forming the heat medium flow passages  11 . The first single plate members  22  and the second single plate members  23  are arranged so as to alternately line up in the plate thickness direction respectively via the isolation plates  21 . 
     Each of the first single plate members  22  has a front surface and a back surface. On the front surface among the surfaces, a plurality of first grooves  24  for forming the reaction flow passages  13  is formed. The first grooves  24  line up in the up and down direction and also line up so as to be spaced from each other by a predetermined gap in the horizontal direction. Each of the first grooves  24  is formed by denting the front surface to have for example a semi-circular section, and formed so as to guide the first material fluid  41  along the up and down direction. 
     A plurality of second grooves  25  for forming the merging flow passages  14  is formed on the back surface of the first single plate member  22 . The second grooves  25  extend in the horizontal direction so as to orthogonal to the first grooves  24 , and are formed so as to line up so as to be spaced from each other by a predetermined distance in the up and down direction. Each of the second grooves  25  is also formed by denting the back surface in a recessed shape to have a predetermined section, and formed so as to guide the second material fluid  32  along the horizontal direction along this dented part. 
     Among the plurality of second grooves  25 , the second groove placed on the upper side is longer than the second groove placed on the lower side. Therefore, in the second groove  25  placed on the upper side, the second material fluid  32  can be merged into the first material fluid  31  flowing through the reaction flow passage  13  placed at a position more distant from the second intake port  17  than in the second groove  25  placed on the lower side. 
     Inside the first single plate member  22 , a plurality of through holes  26  respectively connecting the first grooves  24  on the front surface and the second grooves  25  on the back surface is formed. Each of the through holes  26  is formed at a position where the first groove  24  on the front surface and the second groove  25  on the back surface cross each other along the plate thickness direction. In such a way, the through holes  26  allow the second material fluid  42  flowing through the second grooves  25  to be merged into the first material fluid  41  flowing through the first grooves  24  through the through holes  26 . That is, openings of the through holes  26  in the first grooves  24  correspond to the above “merging ports  18  of the merging flow passages  14  with respect to the reaction flow passages  13 .” 
     Meanwhile, each of the second single plate members  23  has a front surface and a back surface as well as the first single plate member  22 , and a plurality of third grooves  27  for forming the heat medium flow passages  11  is formed on both the surfaces. The third grooves  27  extend along the up and down direction or the horizontal direction. Regarding the forming direction of the third grooves  27 , the third grooves may be formed along the up and down direction or may be formed along the left and right direction on both the front and back surfaces. It should be noted that in the example shown in  FIG. 4 , the third grooves  27  formed on the front surface of the second single plate member  23  extend along the up and down direction, and the third grooves  27  formed on the back surface of the second single plate member  23  are formed along the horizontal direction. However, all the third grooves  27  formed on the front and back surfaces may extend in the up and down direction, or all the third grooves  27  formed on the front and back surfaces may extend in the horizontal direction. Alternatively, all the third grooves may extend in the oblique direction. As well as the first groove  24  and the second groove  25 , each of the third grooves  27  is formed by denting so as to have a section in a predetermined shape such as a semi-circular section, and formed so as to guide the heat medium along the up and down direction or the horizontal direction. 
     Each of the isolation plates  21  has a front surface and a back surface but serves as a flat plate in which no grooves are formed on these surfaces. By being laminated between the first single plate member  22  and the second single plate member  23 , the isolation plate closes the first to third grooves  24 ,  25 ,  27  in the plate thickness direction so as to form the above reaction flow passages  13 , the merging flow passages  14 , and the heat medium flow passages  11 . Specifically, by being laminated on the front surface of the first single plate member  22 , the isolation plate  21  closes the first grooves  24  in the plate thickness direction so that the first grooves  24  can be utilized as the reaction flow passages  13 . By being laminated on the back surface of the first single plate member  22 , the isolation plate  21  closes the second grooves  25  in the plate thickness direction so that the second grooves  25  can be utilized as the merging flow passages  14 . Further, by being laminated respectively on the front surface and the back surface of the second single plate member  23 , the isolation plate  21  closes the third grooves  27  in the plate thickness direction so that the third grooves  27  can be utilized as the heat medium flow passages  11 . 
     Therefore, by laminating the first single plate members  22 , the second single plate members  23 , and the isolation plates  21  in the order of the first single plate member  22 , the isolation plate  21 , the second single plate member  23 , the isolation plate  21  which is different from the above isolation plate  21 , and the first single plate member  22  which is different from the above first single plate member  22  along the plate thickness direction, the processing member  2  in which the plurality of reaction flow passages  13 , the plurality of merging flow passages  14 , and the plurality of heat medium flow passages  11  are respectively formed in attachment parts between the plate members adjacent to each other can be easily formed. 
     Next, a method of performing a reaction operation by using the reaction device  1  serving as the above processing device, in other words, a reaction method serving as one example of a processing method according to the present invention will be described. The following description relates to a case where the second material fluid  32  is stored in a lower part of the reaction bath  3  of the reaction device  1 , the first material fluid  31  is stored in the material liquid bath  4 , and the reaction product  33  is produced by reaction between the first material fluid  31  and the second material fluid  32  and taken out. 
     As shown in  FIG. 1A , firstly, the first material fluid  31  stored inside the material liquid bath  4  is suctioned into the first pipe  6  by the first pump  51 , and pressured-fed to the processing member  2  accommodated inside the reaction bath  3  through this first pipe  6 . The inlet side end of this first pipe  6  is connected to the material bath  4  in which the first material fluid  31  is stored, and the outlet side end is connected to the minute flow passages  10  formed inside the processing member  2 , accurately to the first intake ports  15  of the reaction flow passages  13 . Thus, by using the first pump  51  and the first pipe  6 , the first material fluid  31  of the material bath  4  taken into the first pipe  6  can be supplied to the reaction flow passages  13 . 
     Meanwhile, the second material fluid  32  preliminarily stored inside the reaction bath  3  is suctioned out by the second pump  52  and pressure-fed to the processing member  2  accommodated in the reaction bath  3  through the second pipe  7 . The inlet side end of the second pipe  7  is placed in the lower part of the reaction bath  3  in which the second material fluid  32  is stored, and the outlet side end of the second pipe  7  is connected to the minute flow passages  10  formed inside the processing member  2 , accurately to the second intake ports  17  of the merging flow passages  14 . Thus, by using the second pump  52  and the second pipe  7 , the second material fluid  32  taken from the reaction bath  3  into the second pipe  7  can be supplied to the merging flow passages  14 . 
     In such a way, the first material fluid  31  supplied to the reaction flow passages  13  and the second material fluid  32  supplied to the merging flow passages  14  are mixed and reacted in the reaction flow passages  13  placed on the upper side (downstream side) of the merging ports  18 , so that the reaction product  33  is produced by the reaction. 
     Meanwhile, inside the processing member  2 , the heat medium flow passages  11  are formed at a position isolated from the minute flow passages  10  by a distance in the plate thickness direction. Thus, by supplying and circulating the heat medium having the temperature adjusted to be a predetermined reaction temperature in these heat medium flow passages  11 , the temperatures of the material fluids  31 ,  32  flowing through the minute flow passages  10  can be adjusted to be a predetermined reaction temperature. 
     Specifically, the heat medium flow passages  11  are formed at the position isolated from the reaction flow passages  13  of the minute flow passages  10  by a thickness amount of the isolation plate  21 . Thus, by using heat supplied from the heat medium which is circulated in the heat medium flow passages  11 , the first material fluid  31  flowing through the reaction flow passages  13  can be heated or cooled to have a predetermined reaction temperature. 
     On the opposite side of the reaction flow passages  13 , the heat medium flow passages  11  are also formed at a position isolated from the merging flow passages  14  of the minute flow passages  10  by the thickness amount of the isolation plate  21 . Thus, by using heat supplied from the heat medium which is circulated in the heat medium flow passages  11 , the second material fluid  32  flowing through the merging flow passages  14  can be heated or cooled to a predetermined reaction temperature. 
     Therefore, when the heat medium is supplied to the heat medium flow passages  11 , the heat is transmitted from the heat medium to the first and second material fluids  31 ,  32  in the minute flow passages  10  respectively adjacent to the heat medium flow passages  11 . Thereby, while accurately maintaining the temperatures of the first and second material fluids  32  to a preliminarily fixed reaction temperature, the first and second material fluids  31 ,  32  can be surely reacted with each other. 
     In such a way, the reaction product  33  produced by the reaction inside the reaction flow passages  13  is taken out to the outside of the processing member  2  through the take-out ports  16  formed by upper ends of the minute flow passages  10  and stored in the reaction bath  3 . Therefore, when the reaction progresses as shown in  FIG. 1B , all the first material fluid  31  originally placed in the material bath  4  is moved to the reaction bath  3  and used for the reaction inside the minute flow passages  10 . Thereby, the already-reacted material fluid is stored in the reaction bath  3 . 
     It should be noted that in a case where the reaction is not completed only with one-time circulation in the minute flow passages  10 , in other words, in a case where the unreacted material fluid remains in the reaction bath  3  after the one-time circulation, by supplying the reaction product  33  stored in the reaction bath  3  and the unreacted first and second material fluids  31 ,  32  into the processing member  2  again through the second pipe  7  and the third pipe  8 , a reaction rate of the first and second material fluids  31 ,  32  can also be enhanced. 
     When the above reaction device  1  is used, the first material fluid  31  in the material bath  4  and the second material fluid  32  of the reaction bath  3  are finely distributed into the minute flow passages  10  and then reacted in the minute flow passages  10 . Thus, even when agitation is not performed by using an agitation blade or the like, the first and second material fluids  31 ,  32  can be surely mixed and reacted inside the minute flow passages  10 . Therefore, unlike a case where the agitation blade is used, a disadvantage of segmentation of the material fluids is not added. 
     Inside the processing member  2 , the heat medium flow passages  11  in which the heat medium capable of heating or cooling the material fluids flowing through the minute flow passages  10  is circulated are formed at positions adjacent to the minute flow passages  10 . In the minute flow passages  10  and the heat medium flow passages  11 , heat exchange can be performed between the material fluids  31 ,  32  and the heat medium while ensuring a very large heat exchange area. All the minute flow passages  10  and the heat medium flow passages  11  are provided inside the processing member  2  and hence unsusceptible to a temperature of an exterior. Therefore, by the circulation of the heat medium in the heat medium flow passages  11 , the temperatures of the material fluids flowing through the minute flow passages  10  can be selectively and precisely adjusted to be a target reaction temperature for a short time. It does not take a long time for adjustment of the temperature of the reaction bath  4 . 
     For example, as in a processing device shown in  FIG. 5B , in a processing device including a reaction bath  103  and a coil shape metal pipe  111  accommodated in this reaction bath, in which a temperature is adjusted by supplying a heat medium into the pipe  111 , when agitation is performed by using an agitation blade  114  shown in  FIG. 5B  for example, a great temperature gradient (indicated as a temperature difference dT 1  between a bath wall and a bath center in  FIG. 5B ) remains inside the reaction bath  103 . That is, in the example shown in  FIG. 5B , a temperature in the vicinity of an inner wall surface of the reaction bath  103  where the temperature-regulating pipe  111  is provided is high. However, a temperature on the center side of the reaction bath  103  away from the pipe  111  is largely influenced by an external air temperature and conversely low. Thus, the temperature difference in the bath is very large, so that it becomes difficult to perform a process such as reaction under a uniform temperature condition. 
     However, as shown in  FIG. 5A , in temperature regulation by using the above processing member  2 , a temperature gradient (indicated as a temperature difference dT 2  between a bath wall and a bath center in  FIG. 5A ) inside the reaction bath  3  is small, and the reaction is performed in a state unsusceptible to the external air temperature. Thus, the process such as reaction can be performed while substantially uniformly maintaining the temperatures of the material fluids. 
     From the above description, when the reaction device  1  of the first embodiment is used, and even in a case where the reaction bath  3  serving as the processing bath has a large heat capacity, a chemical operation such as extraction, separation, and reaction can be performed for a short time while strictly controlling the processing temperature with high precision. 
     Next, with using  FIGS. 2A and 2B , the reaction device  1  of the second embodiment will be described. 
     As shown in  FIGS. 2A and 2B , the reaction device  1  of the second embodiment includes the reaction bath  3  as well as the first embodiment. However, the material fluid  32  is not preliminarily stored in the reaction bath  3  but stored in the material bath as well as the first material fluid  31 . Specifically, this reaction device  1  of the second embodiment includes a second material bath  42  that stores the second material fluid  32  in addition to a first material bath  41  that stores the first material fluid  31 . Both the first material bath  41  and the second material bath  42  are provided outside the reaction bath  3  as separate baths from the reaction bath  3 . The first material fluid  31  and the second material fluid  32  are supplied from the first and second material baths  41 ,  42  respectively and individually to the processing member  2  accommodated in the reaction bath  3 . 
     As well as the reaction device  1  of the first embodiment, the reaction device  1  of the second embodiment includes the first pipe  6  and a second pipe  72 . However, the second pipe  72  among the pipes is arranged between the second material bath  42  and the second intake ports  17  of the merging flow passages  14  in the processing member  2  (refer to  FIG. 4 ) unlike the second pipe  7  according to the first embodiment. In the middle of this second pipe  72 , the second pump  52  and a switching valve  92  are provided as well as the first pump  51  and the switching valve  9  in the first pipe  6 , and a fourth pipe  82  similar to the third pipe  8  is provided between the switching valve  92  in the second pipe  7  and the reaction bath  3 . The second pump  52  feeds the second material fluid  32  stored in the second material bath  31  to the second intake ports  17  of the merging flow passages  14  through the second pipe  72 , and with the fourth pipe  82 , the material fluid in the reaction bath  3  can be merged into the second material fluid  32  flowing through the pipe  7 B. 
     In this reaction device  1  of the second embodiment, as shown in  FIG. 2A , the reaction product  33  and the material fluids  31 ,  32  are not at all stored in the reaction bath  3  at the start of reaction. After that, by driving the first and second pumps  51 ,  52 , the first pump  51  pressure-feeds the first material fluid  31  to the processing member  2  (in detail, the first intake ports  15  of the reaction flow passages  13  shown in  FIG. 4 ) through the first pipe  6 , and the second pump  52  pressure-feeds the second material fluid  32  to the processing member  2  (in detail, the second intake ports  17  of the merging flow passages  14  shown in  FIG. 4 ) through the second pipe  7 B. Then, the first material fluid  31  flowing into the reaction flow passages  13  from the first intake ports  15  and the second material fluid  32  flowing into the merging flow passages  14  from the second intake ports  17  are mixed and reacted with each other inside the reaction flow passages  13  placed on the upper side of the merging ports  18  shown in  FIG. 4 . The reaction product  33  produced by this reaction is taken out to in the reaction bath  3  through the take-out ports  16  and stored. 
     By continuing the above operation, as shown in  FIG. 2B , the first material fluid  31  stored in the first material bath  41  and the second material fluid  32  stored in the second material bath  42  are both gone, whereas the reaction product  33  obtained by reacting the first material fluid  31  and the second material fluid  32  fills the reaction bath  3 . 
     At this time, in a case where the reaction of the first and second material fluids  31 ,  32  is not completely finished, in other words, at least one of the first material fluid  31  and the second material fluid  32  remains inside the reaction bath  3  in an unreacted state, as well as the first embodiment, in order to complete the reaction of the first and second material fluids  31 ,  32 , the material fluid of the reaction bath  3  is returned to the processing member  2  again through the first pipe  6 , the second pipes  7 ,  7 B, and the third pipes  8 ,  8 B and supplied for further reaction inside the processing member  2 . 
     The above reaction device  1  of the second embodiment is favorable for such reaction of the material fluids that the total amount of the first material fluid  31  or the second material fluid  32  is firstly reacted at a predetermined reaction temperature, and after the reaction of the total amount, the reaction is desirably completed while circulating the material fluid. In a case where the second material fluid  32  is a highly volatile liquid, the second material fluid  32  is volatilized and gasified in the reaction bath  3  in the reaction device of the first embodiment. Thus, there is a fear that the material fluid  32  becomes inappropriate to be supplied into the processing member  2 . However, even in such a case, the reaction device of the second embodiment can be favorably used. 
     Next, with using  FIG. 3 , the reaction device  1  of the third embodiment will be described. 
     As shown in  FIG. 3 , the reaction device  1  of the third embodiment includes the processing member  2  and the reaction bath  3 , and inside thereof, immiscible first and second material fluids  31 ,  32  having different specific gravities from each other are respectively divided and stored into an upper layer and a lower layer. The processing member  2  has the plurality of minute flow passages  10  as well as the first embodiment, and the minute flow passages  10  include the reaction flow passages  13  in which the first material fluid  31  in the upper layer taken in from an upper part of the reaction bath  3  is reacted while circulating the first material fluid, and the merging flow passages  14  in which the second material fluid  32  in the lower layer taken in from a lower part of the reaction bath  3  is merged into the first material fluid  31  in the reaction flow passages  13  through the merging ports  18  in the middle of the reaction flow passages  13  (refer to  FIG. 4 ). 
     When the reaction is performed by using such a processing member  2 , inside a part of the reaction flow passages  13  on the upper side of the merging ports  18 , the first material fluid  31  in the upper layer and the second material fluid  32  in the lower layer are brought into contact and reacted with each other in a two-phase flow state, and the reaction product  33  produced by the reaction can be taken out in a state where the reaction product is solved in either the first material fluid  31  or the second material fluid  32 . 
     This reaction device  1  of the third embodiment can be effectively used in a case where the first and second material fluids  31 ,  32  are immiscible with each other as in water and oil, and in a case where the reaction product  33  needs to be taken out in a state where the reaction product  33  is solved in a liquid or the like. 
     As exemplified in the above embodiments, according to the processing device of the present invention (reaction device  1  in the above embodiments) and the processing method (reaction method in the above embodiments), even in a case where the processing bath (reaction bath  3  in the above embodiments) has a large heat capacity, the chemical operation such as extraction, separation, and reaction can be surely performed while strictly controlling the processing temperature (reaction temperature in the above embodiments) with high precision. 
     It should be noted that the embodiments disclosed herein are thought to be not a limitation but an example in all respects. In particular, regarding matters not explicitly disclosed in the embodiments disclosed herein such as an operation condition, a production condition, various parameters, size of constituent parts, weight, and volume, values not departing from a range that those skilled in the art generally implement, the values easily anticipated by those skilled in the art in general are adopted. 
     For example, the processing member  2  in the above first to third embodiments includes the plurality of minute flow passages  10 . However, the processing member according to the present invention may be a processing member having a single minute flow passage and a single heat medium flow passage corresponding to this, that is, a single flow passage member. 
     As described above, according to the present invention, the processing device and the processing method in which the material fluid can be subjected to the process while favorably controlling the processing temperature of the material fluid are provided. 
     The present invention is to provide a processing device for subjecting a material fluid to a process while controlling a processing temperature of the material fluid. This processing device includes a processing member into which the material fluid is guided and subjected to the process inside, and a processing bath that accommodates this processing member and stores a processing product provided by the process in the processing member. The processing member has at least one minute flow passage provided inside the processing member, the minute flow passage inside which the material fluid is circulated, and at least one heat medium flow passage provided inside the processing member, the heat medium flow passage inside which a heat medium having a temperature different from the temperature of the material fluid circulated in the at least one minute flow passage is circulated. The at least one minute flow passage and the at least one heat medium flow passage are isolated from each other in such a manner that heat exchange is capable of being performed between the material fluid flowing through the minute flow passage and the heat medium flowing through the heat medium flow passage. 
     The present invention is also to provide a processing method for subjecting a material fluid to a process while controlling a processing temperature of the material fluid. This processing method includes the steps of preparing a processing device which includes a processing member having minute and heat medium flow passages isolated from each other, the processing member into which the material fluid is guided and subjected to the process inside, and a processing bath that accommodates this processing member and stores a processing product provided by the process in the processing member, and adjusting the processing temperature of the material fluid in the minute flow passage by circulating the material fluid in the minute flow passage of the processing member, circulating a heat medium having a temperature different from the temperature of the material fluid circulated in the minute flow passage in the heat medium flow passage, and performing heat exchange between the material fluid and the heat medium inside the processing member. 
     According to the processing device and the processing method, even in a case where the processing bath has a large heat capacity, the material fluid can be subjected to the process while favorably controlling the processing temperature. 
     Preferably, in the processing member, the at least one minute flow passage may include a plurality of minute flow passages, and the at least one heat medium flow passage may include a plurality of heat medium flow passages. With this processing member, the material fluid can be subjected to the process more efficiently by circulating the material fluid through the plurality of minute flow passages, and the processing temperature of the material fluid can be more precisely controlled by circulating the heat medium through the plurality of heat medium flow passages. 
     Preferably, the at least one minute flow passage of the processing member may include a reaction flow passage in which by performing heat exchange between the material fluid and the heat medium circulated in the heat medium flow passage, reaction of the material fluid is performed while adjusting the temperature of the material fluid. 
     Plural types of material fluids may be circulated in the at least one minute flow passage as the material fluid. 
     In this case, favorably, the reaction bath stores a first material fluid and a second material fluid as the plural types of material fluids in a state where the immiscible first and second material fluids having different densities from each other are respectively divided into an upper layer and a lower layer, and the at least one minute flow passage of the processing member includes a reaction flow passage in which the second material fluid in the lower layer taken from a lower part of the reaction bath is reacted while circulating the second material fluid, and a merging flow passage in which the first material fluid in the upper layer taken from an upper part of the reaction bath is merged into the second material fluid in the reaction flow passage in the middle of the reaction flow passage.