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·1152·                            精细化工   FINE CHEMICALS                                  第 36 卷

            of  IL-6,  IL-1β  and  TNF-α  were  determined  using   3.2    Adsorption kinetics
            ELISA kits as per the manufacturer’s instructions.   The  adsorption  kinetics  curves  for  FMTs  on  AB-8
            2.10    Statistical analysis                       resin were obtained at 25 ℃  and are shown in Fig.2A.
               All  the  data  are  presented  as  the  mean  ±  standard   The FMTs adsorption capacities rapidly increased with
            deviation (SD). One-way analysis of variance (ANOVA)
            and  Student’s-test  were  performed  to  evaluate  the
            significant  differences.  Statistical  significance  was
            considered when the P value was less than 0.05 (P<
            0.05). All statistical analyses were performed by using
            SPSS 18.0 software.

            3. Results and Discussion

            3.1    Selection  of  macroporous  resins  suitable  for
                 the separation of FMTs
               Macroporous resins can be used for the adsorption
            of  organic  constituents  due  to  their  hydrophobic
            properties.  The  adsorption  capacity  of  macroporous
            resins  correlates  not  only  with  the  physical  and
            chemical properties of the adsorbent but also with the
            size and chemical features of the adsorbed substance.
            To effectively enrich flavonoids, the optimum type of
            macroporous resin was screened. First, the properties
            of  twelve  resins  were  compared  in  terms  of  their
            adsorption  and  desorption  capacities.  As  shown  in
            Fig.1,  among  the  selected  resins,  the  adsorption
            capacity of AB-8 resin to FMTs was 105.89 mg/g and
            the desorption ratio of AB-8 resin was 86.31%. All of
            the  above  indicators  were  higher  than  those  of  the
            others, and NKA-9 resin showed the lowest adsorption
            capacity,  which  indicated  that  differences  existed  in
            the  adsorption  capacities  for different resins. This
            result  indicated  that  an  appropriate  surface  area  and
            resin  size  were  both  crucial  for  total  purification.
            Taking  the  adsorption  and  desorption  ratios  into
            account,  AB-8  resin  was  considered  the  most
            appropriate  resin  for  FMTs  purification  among  the
            tested resins.
















                                                               Fig. 2    Adsorption kinetics curves for FMTs on AB-8 resin
                                                                     at 25 ℃  (A); adsorption isotherms for FMTs on AB-8

                                                                     resin  at  different  temperatures  (25 ℃,  35 ℃ and
            Fig.  1    Static  adsorption  and  desorption  results  based  on   45 ℃) (B); effects of the initial concentration of the
                   the  phloridzin  content  in  different  types  of   sample  solution  on  the  adsorption  capacities  and
                   macroporous resins. The results were expressed as   adsorption ratios of FMTs on AB-8 resin (C); effects
                   mean  ±  S.D.  (n = 3). The  mean values  were    of the pH value on FMTs adsorption capacities of the
                   considered significantly different when P<0.05.   AB-8 resin (D).
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