Abstract:
The present invention relates to a method for conducting deracemization using Taylor flow and a device for conducting the same. With respect to the deracemization of a racemate, it may be efficiently conducted with improved rapidity when a racemate-containing fluid is placed under Taylor flow.

Description:
TECHNICAL FIELD 
       [0001]    The present invention relates to a method for conducting deracemization using Taylor flow and a device for the same. 
       BACKGROUND ART 
       [0002]    Among organic and inorganic materials, there exist materials in which structures of atoms are arranged identically but as mirror images of each other according to a chiral center. These are known as enantiomers. For example, for the amino acids constituting the body, two mirror images can exist with the carbon atom as the chiral center, to which carboxyl and amine groups are attached, and these are respectively called the L- and D-forms. 
         [0003]    On the other hand, when the non-chiral compound NaClO 4  is stirred, it may crystallize while spontaneously forming a structure of a pure L- or D-form. Additionally, all amino acids existing in organisms are composed of the L-form, and further, when D-amino acids enter the body, it is known that the amino acids may be inactive or cause side effects even if the atomic structure thereof corresponds to that of the L-form. In contrast, all saccharides in the body are known to have the D-form, and therefore, preparing an organic material and/or inorganic material of a single enantiomer is of the utmost importance in producing highly efficient medicines with reduced side effects in the pharmaceutical field. Generally, when synthesizing an organic material and/or inorganic material, both enantiomers are made almost identically, and a mixture with the same amount of each enantiomer is called as a racemic mixture (hereinafter, racemate). The reaction in which a prepared material in a racemic state is converted into one enantiomer is called deracemization. 
         [0004]    A conventional deracemization process uses a method of slowly increasing the enantiomeric excess (ee) of one side by increasing and decreasing the temperature of a well-mixed batch reactor (Science 1990, 16, 975; Phys. Rev. Lett. 2005, 94, 065504; Crys. Growth. Deg. 2007, 7, 553; Crys. Growth. Deg. 2009, 9, 4802; Crys. Growth. Deg. 2013, 13, 3498). At this time, when the initial percentage of each enantiomer is formed, one enantiomer is produced slightly more than the other, such that the ratio therebetween is slowly converted from 51:49 to 99:1, and this is called the deracemization phenomenon. However, in this case, there is a disadvantage in that the reaction time requires at least 150 hours. 
       DISCLOSURE 
     Technical Problem 
       [0005]    An object of the present invention is to provide an efficient deracemization method with improved rapidity, and a device for conducting the same. 
       Technical Solution 
       [0006]    An aspect of the present invention provides a method of deracemization of a racemate, including: a first step for supplying a racemate-containing fluid to a reaction zone of a reactor, which is equipped with an inner cylinder having a surface with a first temperature (T 1 ), an outer cylinder having a surface with a second temperature (T 2 ), and a reaction zone between the inner cylinder and the outer cylinder; and a second step for stirring the racemate-containing fluid under Taylor flow by rotating the inner cylinder while immobilizing the outer cylinder. 
         [0007]    A second aspect of the present invention provides a device for deracemization of a racemate including an inner cylinder having a surface with a first temperature (T 1 ), an outer cylinder having a surface with a second temperature (T 2 ), a reaction zone between the inner cylinder and the outer cylinder, and an inlet for providing a racemate-containing fluid within the reaction zone, wherein the racemate is deracemized by stirring the racemate-containing fluid in the reaction zone under Taylor flow by rotating the inner cylinder while immobilizing the outer cylinder. 
         [0008]    Hereinafter, the present invention will be described in more detail. 
         [0009]    In the present invention, for deracemization of a racemate, it has been found that it is efficiently carried out with improved rapidity when a racemate-containing fluid is placed under Taylor flow. Additionally, in the present invention, it also has been found that the deracemization is further accelerated when the temperature of the surfaces of the inner and outer cylinders producing such Taylor flow is different. The present invention is based on these findings. 
         [0010]    When a fluid is flowed between two concentric cylinders, the inner cylinder is rotated. Further, the fluid near the inner cylinder are accelerated to direct toward the outer cylinder by centrifugal force, and thus the fluid becomes unstable and forms a vortex having a pair of rings that are regularly rotated in opposite directions along with the rotation axis of the inner cylinder. This vortex is called “Taylor flow”. 
         [0011]    In the device generating the Taylor flow, a fluid is flowed between two cylinders having the same axis, and the inner cylinder is rotated about the axis in order to generate the flow. This driving force of the rotation causes the flow of the fluid, and the flow varies according to rotational speed. Laminar flow is generated at low rotational speed, but the speed distribution deviates from the laminar flow with increased rotational speed. This flow exhibits instability, generates a recurrent vortex surrounding the inner cylinder, and further generates various types of flow with increased rotational speed. 
         [0012]    In such Taylor flow, a feature of the flow is determined based on the Taylor Number, a dimensionless quantity. The Taylor Number (Ta) is defined in Equation 1 below 
         [0000]    
       
         
           
             
               
                 
                   Ta 
                   ≡ 
                   
                     
                       Centrifugal 
                        
                       
                           
                       
                        
                       Force 
                     
                     
                       Viscous 
                        
                       
                           
                       
                        
                       Force 
                     
                   
                   ≡ 
                   
                     
                       
                         Ω 
                         2 
                       
                        
                       
                         
                           
                             R 
                             1 
                           
                            
                           
                             ( 
                             
                               
                                 R 
                                 2 
                               
                               - 
                               
                                 R 
                                 1 
                               
                             
                             ) 
                           
                         
                         3 
                       
                     
                     
                       v 
                       2 
                     
                   
                 
               
               
                 
                   [ 
                   
                     Equation 
                      
                     
                         
                     
                      
                     1 
                   
                   ] 
                 
               
             
           
         
       
     
         [0013]    In Equation 1 above, Ω (rad/s) refers to a rotational speed of the inner cylinder, R 1  refers to a radius of the inner cylinder, R 2  refers to an internal radius of the external cylinder, and v refers to a dynamic viscosity of a fluid (m 2 /s). The Taylor Number indicates a ratio of centrifugal and viscous forces of a fluid, and is used for determining a form of a flow of the Tylor flow. 
         [0014]    When a flow of a fluid between two cylinders having the same axis is changed by the rotation of the inner cylinder, a laminar flow is formed at the low rotational speed of the inner cylinder, and a flow of a radial direction occurs about the axis in a certain rotational speed when the speed of the inner cylinder is increased. That is, the flow changes from the stable laminar flow into a continuous donut-shaped reflux. Such flow is due to the increase in the centrifugal force of the fluid, which was in the laminar flow, according to the growing rotational speed of the inner cylinder, such that it exceeds the viscous force of the fluid, thereby forming the donut-shaped reflux. The Taylor Number at which the donut-shaped reflux is formed due to the unstable fluid in the laminar Couette flow is called as the critical Taylor Number (Ta c ≈1708), and a periodic donut-shaped flow (Taylor flow) is generated when the Taylor Number becomes greater than the critical Taylor Number. Although the vortex is formed by the instability of the flow, the flow thereof stably covers the inner cylinder. It exhibits an aspect wherein the fluid is well mixed according to the flow generated inside of each periodic vortex, but the fluid is not connected with the vortex. 
         [0015]    Flows of various structures are observed when the rotational speed of the inner cylinder is gradually increased. According to the rotation speed of the inner cylinder, flows of various structures, such as a periodic donut-shaped laminar Taylor-vortex flow surrounding the inner cylinder (1&lt;Ta/Ta c &lt;3), a wavy-vortex flow wherein the parts of the formed donut-shaped flow which are dissipated and produced are recurrently flowed (3&lt;Ta/Ta c &lt;13.3), a quasi-periodic wavy-vortex flow (13.3&lt;Ta/Ta c &lt;18), a weak turbulent-vortex flow (18&lt;Ta/Ta c &lt;33), a turbulent Taylor-vortex flow (33&lt;Ta/Ta c &lt;160), and a turbulent flow (Ta/Ta c &gt;160), are consecutively formed in the above order from a laminar Couette flow, in which only a flow of an angular direction from the inner cylinder to the outer cylinder is present (Ta/Ta c &lt;1). 
         [0016]    As illustrated above, the deracemization method of a racemate according to the present invention includes a first step for supplying a racemate-containing fluid to a reaction zone of a reactor, which is equipped with the inner cylinder having the surface with a first temperature (T 1 ), the outer cylinder having the surface with a second temperature (T 2 ), and a reaction zone between the inner and outer cylinders; and a second step for stirring the racemate-containing fluid under Taylor flow by rotating the inner cylinder while immobilizing the outer cylinder. 
         [0017]    The above first step is a step for supplying the racemate-containing fluid to the reaction zone capable of generating the Taylor flow. The fluid can be supplied as a batch type or a continuous type. 
         [0018]    As used herein, the term “racemate” may refer to a mixture in which the same amounts of two mirror-image isomers are mixed. In the present invention, a racemate may refer to one having an enantiomeric excess (ee) value less than or equal to 1. 
         [0019]    A racemate capable of being deracemized according to the method in the present invention is not particularly limited, and it may include an inorganic substance or an organic substance. Specifically, examples of the racemate may be NaClO 4 , clopidogrel, fructose, threonine, carvone, thalidomide, ethambutol, naproxen, penicillin, propranolol, carvedilol, or 1-(4-chlorophenyl)-4,4-dimethyl-2-(1H-1,2,4-triazole-1-yl)pentan-3-one. 
         [0020]    In the present invention, a racemate is placed under Taylor flow upon containing the racemate in a fluid. Specifically, the racemate-containing fluid may be an aqueous solution containing a racemate, but is not limited thereto. 
         [0021]    In the present invention, when the racemate-containing fluid is supplied as a continuous type, an average retention time of the fluid remaining in a reaction zone may be several minutes to several hours, preferably 1 minute to 10 hours. At this time, the rate of supplying a fluid can be calculated by dividing the volume of the reaction zone by the average retention time. For example, the rate of supplying a fluid may be 300 mL/minute to 0.5 mL/minute when the volume of the reaction zone is 300 mL. 
         [0022]    In the present invention, T 1  may be equal to T 2  (T 1 =T 2 ) or T 1  may not be equal to T 2  (T 1 ≠T 2 ). That is, the racemate-containing fluid may be placed under isothermal Taylor flow or non-isothermal Taylor flow. Preferably, it is advantageous to apply the non-isothermal Taylor flow for rapid deracemization. 
         [0023]    In the present invention, when T 1  is not equal to T 2  (T 1 ≠T 2 ), the temperature difference may be 1° C. to 50° C., preferably 1° C. to 10° C. or 2° C. to 5° C., or more preferably 3° C. If the temperature difference between T 1  and T 2  is below 1° C., an advantageous effect of applying the non-isothermal Taylor flow may not sufficiently be exhibited. Additionally, if such difference is more than 10° C., a process may be inefficiently conducted due to the energy consumption. 
         [0024]    The second step is a step of inducing deracemization by placing a racemate-containing fluid under Taylor flow. 
         [0025]    In the present invention, in order to apply the Taylor flow, the rotational speed of the inner cylinder may be adjusted to meet the condition of 1&lt;Ta/Ta c &lt;160, wherein Ta is a Taylor Number under an applied condition in the second step and Ta c  is a critical Taylor Number. 
         [0026]    As described above, at least 50% of the enantiomeric excess (ee) value may be obtained within 24 hours through the deracemization using the Taylor flow according to the present invention. 
         [0027]    In an exemplary embodiment of the present invention, it was observed that at least 80% of the enantiomeric excess (ee) value is obtained within 24 hours when the deracemization reaction is carried out under the isothermal Taylor flow using an aqueous NaClO 4  solution (Example 1). 
         [0028]    Additionally, at least 50% of the enantiomeric excess (ee) value can be obtained within 12 hours if the non-isothermal Taylor flow, i.e., T 1 ≠T 2 , is used. 
         [0029]    In an exemplary embodiment of the present invention, it was observed that at least 99% of the enantiomeric excess (ee) value is obtained within 12 hours when the deracemization reaction is carried out under the non-isothermal Taylor flow using an aqueous NaClO 4  solution (Example 2). 
         [0030]    Additionally, the deracemization device according to the present invention, as described above, is equipped with the inner cylinder having the surface of a first temperature T 1 , the outer cylinder having the surface of a second temperature T 2 , a reaction zone between the inner cylinder and outer cylinder, and an inlet for providing the racemate-containing fluid within the reaction zone. 
         [0031]    The deracemization device according to the present invention can deracemize a racemate by stirring the racemate-containing fluid in the reaction zone under the Taylor flow by rotating the inner cylinder while immobilizing the outer cylinder. The deracemization device may be a batch type or a continuous type. 
         [0032]    The deracemization device according to the present invention may use a non-isothermal flow or an isothermal flow. That is, the deracemization device according to the present invention may be T 1 =T 2  or T 1 ≠T 2 . 
         [0033]    In the deracemization device according to the present invention, the temperature in the inner and outer cylinders may be adjusted by a heat exchanger for heat generation or that for heat absorption, and thereby isothermal or non-isothermal Taylor flow may be generated within a reaction zone. 
         [0034]    In the present invention, the inner cylinder itself may be a heat exchanger for heat absorption or heat generation, or a heat exchanger for the same may be separately equipped within the inner cylinder. Additionally, the outer cylinder itself may be a heat exchanger for heat absorption or heat generation, or a heat exchanger for heat generation or heat absorption may be separately equipped in the outside of the outer cylinder. 
         [0035]    In the deracemization device, a heat exchanger for the heat generation may be located in the inner cylinder, when T 1 &gt;T 2 . 
         [0036]    In the deracemization device, a heat exchanger for the heat absorption may be located in the inner cylinder, when T 1 &lt;T 2 . 
         [0037]    The first temperature (T 1 ) and second temperature (T 2 ) can be adequately adjusted depending on a type of starting materials to be used or that of products prepared therefrom. 
         [0038]    Final produced materials of the deracemization may be discharged to the outside through an outlet port arranged in the immobilized outer cylinder. 
       Advantageous Effects 
       [0039]    With respect to deracemization of a racemate, the present invention efficiently conducts the deracemization with improved rapidity when a racemate-containing fluid is placed under Taylor flow. In particular, it is advantageous in that the deracemization can be conducted with further improved rapidity when a difference between the surface temperatures of the inner and outer cylinders producing such Taylor flow is created. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0040]      FIG. 1  schematically shows a reactor for the deracemization reaction according to an exemplary embodiment of the present invention. 
           [0041]      FIG. 2  shows a variation of an enantiomeric excess (cc) according to time when the deracemization reaction using the isothermal Taylor flow is carried out according to the present invention. 
           [0042]      FIG. 3  is an outline of the deracemization reaction which uses the non-isothermal Taylor flow according to the present invention. 
           [0043]      FIG. 4  shows a variation in temperatures of the cold surface (outer cylinder) and hot surface (inner cylinder), and an average temperature of a solution within a reaction zone, according to time, when using the non-isothermal Couette-Taylor reactor according to an exemplary embodiment of the present invention. 
           [0044]      FIG. 5  shows a result of the deracemization reaction using the non-isothermal Couette-Taylor reactor. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0045]    Hereinbelow, the present invention will be described in detail with accompanying exemplary embodiments. However, the exemplary embodiments disclosed herein are only for illustrative purposes and should not be construed as limiting the scope of the present invention. 
       Example 1 
     Deracemization Reaction Using Isothermal Taylor Flow 
       [0046]    As shown in  FIG. 1 , a reactor for the deracemization reaction according to an exemplary embodiment was prepared. 
         [0047]    The deracemization reaction was carried out using the prepared reactor for the deracemization reaction, and the result thereof was investigated. The process for carrying out the deracemization reaction will be described in more detail. 
         [0048]    First, NaClO 4  (100 g) was dissolved in water (100 mL) to prepare a NaClO 4  solution. Additionally, the NaClO 4  solution having the initial temperature of 33° C. was placed in the reactor for the deracemization reaction, and was then cooled to finally reach 20° C. at each different cooling rate, as shown in Table 1 below. Induction time, the time taken to obtain the first crystal from the time-point of initiating the cooling, was measured, and an enantiomeric excess (ee) value was then measured at the time-point above, thereby indicating such value as the initial enantiomeric excess (ee) value. 
         [0049]    Thereafter, the deracemization was induced by rotating the inner cylinder in the reactor at a different rotational speed, calculated respectively according to the range of Ta/Ta c , as shown in Table 1 below. 
         [0000]    
       
         
               
               
               
             
           
               
                 TABLE 1 
               
               
                   
               
               
                   
                   
                 Presented rotation 
               
               
                   
                   
                 speed [rpm] 
               
               
                   
                   
                 (applied 
               
               
                 range 
                 Flow regime 
                 Ta/Ta c  value) 
               
               
                   
               
             
             
               
                 Ta/Ta c  &lt; 1 
                 Laminar Couette flow 
                 10 (0.9)  
               
               
                   1 &lt; Ta/Ta c  &lt; 3 
                 Laminar Taylor vortex flow 
                 30 (2.7)  
               
               
                   3 &lt; Ta/Ta c  &lt; 13.3 
                 Wavy vortex flow 
                 100 (8.99)  
               
               
                 13.3 &lt; Ta/Ta c  &lt; 18 
                 Quasy-periodic wavy wortec 
                 180 (16.20) 
               
               
                   
                 flow 
               
               
                   18 &lt; Ta/Ta c  &lt; 33 
                 Weakly turbulent vortex flow 
                 300 (27.00) 
               
               
                   33 &lt; Ta/Ta c  &lt; 160 
                 Turbulent Taylor vortex flow 
                 500 (44.99) 
               
               
                   
               
             
          
         
       
     
         [0050]    The enantiomeric excess (ee) values were measured in each bath time by differing the bath time in the reactor and the result thereof is shown in Table 2 below. 
         [0000]    
       
         
               
               
               
               
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
               
             
           
               
                   
                 TABLE 2 
               
               
                   
                   
               
               
                   
                 Solution 
                 Initial 
                 Setting 
                 Cooling 
                 Rotation 
                 Induction 
                 Ini. 
                 Bath 
                   
               
               
                   
                 Concent 
                 Temp. 
                 Temp. 
                 rate 
                 speed 
                 time 
                 ee 
                 time 
                 Final ee 
               
               
                   
                 [g/100 ml] 
                 [° C.] 
                 [° C.] 
                 [° C./min] 
                 [rpm] 
                 [min] 
                 [%] 
                 [h] 
                 [%] 
               
               
                   
                   
               
             
             
               
                   
               
             
          
           
               
                 1 
                 100 
                 33 
                 20 
                 0.12 
                 500 
                 90 
                 0.81 (L) 
                 10 
                  81.25 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 91 
                 0.769 (L) 
                 10 
                  84.28 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 87 
                 0.629 (D) 
                 10 
                  81.82 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 85 
                 0.412 (D) 
                 1 
                  29.79 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 89 
                 0.6211 (D) 
                 1 
                  31.43 (D) 
               
               
                 2 
                 100 
                 33 
                 20 
                 0.37 
                 500 
                 24 
                 0.569 (D) 
                 10 
                  63.13 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 26 
                 0.56 (L) 
                 10 
                  67.36 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.402 (L) 
                 10 
                  66.22 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 26 
                 0.226 (D) 
                 1 
                  10.07 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 24 
                 0.157 (L) 
                 1 
                  9.79 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 25 
                 0.213 (L) 
                 1 
                  8.16 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 25 
                 0.207 (D) 
                 1 
                  6.422 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 26 
                 0.272 (L) 
                 1 
                  6.782 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 27 
                   
                 24 
                 100 (D) 
               
               
                 3 
                 100 
                 33 
                 20 
                 0.57 
                 500 
                 16 
                 0.12 (D) 
                 10 
                  50.82 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 14 
                 0.22 (L) 
                 10 
                  51.50 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 14 
                 0.36 (L) 
                 10 
                  54.51 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 15 
                 0.42 (L) 
                 1 
                  8.35 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 13 
                 0.212 (D) 
                 1 
                  7.47 (D) 
               
               
                 4 
                 100 
                 33 
                 20 
                 0.68 
                 500 
                 12 
                 0.152 (D) 
                 10 
                  40.12 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 12 
                 0.493 (D) 
                 1 
                  5.73 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 10 
                 0.22 (L) 
                 1 
                  8.15 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 11 
                 0.513 (L) 
                 1 
                  6.631 (L) 
               
               
                 5 
                 100 
                 33 
                 20 
                 0.37 
                 300 
                 27 
                 0.22 (L) 
                 10 
                  49.64 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.319 (L) 
                 1 
                  5.938 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 28 
                 0.426 (D) 
                 1 
                  3.136 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 28 
                 0.24 (L) 
                 1 
                  2.296 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 28 
                 0.182 (D) 
                 1 
                  7.134 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 27 
                 0.388 (D) 
                 1 
                  3.006 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 27 
                 0.339 (L) 
                 1 
                  2.778 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 27 
                 0.215 (L) 
                 1 
                  4.425 (L) 
               
               
                 6 
                 100 
                 33 
                 20 
                 0.37 
                 180 
                 29 
                 0.389 (D) 
                 1 
                  3.018 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 28 
                 0.306 (L) 
                 1 
                  4.478 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.437 (L) 
                 1 
                  3.208 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 30 
                 0.322 (L) 
                 1 
                  4.784 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 28 
                 0.465 (L) 
                 1 
                  5.603 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.358 (D) 
                 1 
                  6.273 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.524 (D) 
                 10 
                  35.87 (D) 
               
               
                 7 
                 100 
                 33 
                 20 
                 0.37 
                 100 
                 29 
                 0.495 (D) 
                 1 
                  1.288 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 29 
                 0.4651 (D) 
                 1 
                  2.351 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 30 
                 0.352 (L) 
                 1 
                  2.301 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 30 
                 0.372 (D) 
                 1 
                  5.975 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.197 (L) 
                 1 
                  6.369 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.408 (L) 
                 1 
                  3.338 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 30 
                 0.126 (D) 
                 1 
                  4.109 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.433 (L) 
                 1 
                  6.796 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.369 (L) 
                 10 
                  24.42 (L) 
               
               
                 8 
                 100 
                 33 
                 20 
                 0.37 
                 30 
                 31 
                 0.264 (L) 
                 1 
                  2.627 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 32 
                 0.324 (D) 
                 1 
                  2.866 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 30 
                 0.258 (D) 
                 1 
                  1.493 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 32 
                 0.469 (D) 
                 1 
                  2.644 (D) 
               
               
                   
                   
                   
                   
                   
                 20 
                 32 
                 0.210 (D) 
                 1 
                  1.639 (D) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.127 (L) 
                 1 
                  1.259 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 33 
                 0.154 (L) 
                 1 
                  3.571 (L) 
               
               
                   
                   
                   
                   
                   
                   
                 31 
                 0.302 (D) 
                 1 
                  2.692 (D) 
               
               
                 9 
                 100 
                 33 
                 20 
                 0.37 
                 800 
                 23 
                 0.79 (L) 
                 10 
                  79.73 (L) 
               
               
                 10 
                 100 
                 33 
                 20 
                 0.37 
                 1100 
                 16 
                 0.86 (L) 
                 10 
                  91.49 (L) 
               
               
                   
               
             
          
         
       
     
         [0051]    The result of Table 2 shows that the ee value was less than 1% during the initial stage, but an ee value of at least 20% was obtained within 10 hours when the deracemization reaction using the isothermal Taylor flow according to the present invention was conducted. 
         [0052]    Additionally, an ee value of at least 99% was obtained within 20 hours when the deracemization reaction using the isothermal Taylor flow according to the present invention was conducted. Specifically, it was confirmed that an ee value of at least 99% was shown within 20 hours from the result of the deracemization reaction on the sample (         ), in which the initial ee value was 0.569% (D) when the cooling rate (0.37° C./min) was applied, and the sample (         ), in which the initial ee value was 0.81% (L) when the cooling rate (0.12° C./min) was applied, among samples in Table 2 above ( FIG. 2 ). 
       Example 2 
     Deracemization Reaction Using Non-Isothermal Taylor Flow 
       [0053]    The deracemization reaction was conducted using the reactor and conditions corresponding to Example 1, except the temperature swing was possible during the deracemization in the inside of the Taylor reactor by differing the temperature of the inner Couette-Taylor reactor from that of the outer Couette-Taylor reactor as shown in  FIG. 3 . 
         [0054]    Specifically, the surface of the outer cylinder was the cold surface while the surface of the inner cylinder was the hot surface.  FIG. 4  shows a variation in temperatures of the cold surface (outer cylinder) and hot surface (inner cylinder), and an average temperature of a solution within a reaction zone, according to time, when using the non-isothermal Couette-Taylor reactor according to an exemplary embodiment of the present invention. 
         [0055]    As a result, it was confirmed that an ee value of at least 99% was obtained when using the non-isothermal Couette-Taylor reactor, in which the temperature difference of the inside and outside is 3° C., thereby carrying out the efficient deracemization process compared to the isothermal Couette-Taylor reactor ( FIG. 5 ).