Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 Contents lists available at ScienceDirect Colloids and Surfaces B: Biointerfaces journal homepage: www.elsevier.com/locate/colsurfb Immobilization of acid phosphatase on uncalcined and calcined Mg/Al-CO3 layered double hydroxides Jun Zhu a,b , Qiaoyun Huang a,∗ , Massimo Pigna b , Antonio Violante b,∗∗ a b Key Laboratory of Subtropical Agriculture and Environment, Ministry of Agriculture, College of Resources and Environment, Huazhong Agricultural University, Wuhan 430070, China Department of Soil, Plant, Environment and Animal Production Science, Faculty of Agriculture, University of Naples “Federico II”, Via University 100, 80055 Portici (Naples), Italy a r t i c l e i n f o Article history: Received 25 November 2009 Received in revised form 18 December 2009 Accepted 25 January 2010 Available online 4 February 2010 Keywords: Acid phosphatase Layered double hydroxides Immobilization Activity Kinetics Stability a b s t r a c t Acid phosphatase was immobilized on layered double hydroxides of uncalcined- and calcined-Mg/AlCO3 (Unc-LDH-CO3 , C-LDH-CO3 ) by the means of direct adsorption. Optimal pH and temperature for the activity of free and immobilized enzyme were exhibited at pH 5.5 and 37 ◦ C. The Michaelis constant (Km ) for free enzyme was 1.09 mmol mL−1 while that for immobilized enzyme on Unc-LDH-CO3 and C-LDHCO3 was increased to 1.22 and 1.19 mmol mL−1 , respectively, indicating the decreased affinity of substrate for immobilized enzymes. The residual activity of immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 at optimal pH and temperature was 80% and 88%, respectively, suggesting that only little activity was lost during immobilization. The deactivation energy (Ed ) for free and immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 was 65.44, 35.24 and 40.66 kJ mol−1 , respectively, indicating the improving of thermal stability of acid phosphatase after the immobilization on LDH-CO3 especially the uncalcined form. Both chemical assays and isothermal titration calorimetry (ITC) observations implied that hydrolytic stability of acid phosphatase was promoted significantly after the immobilization on LDH-CO3 especially the calcined form. Reusability investigation showed that more than 60% of the initial activity was remained after six reuses of immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 . A half-life (t1/2 ) of 10 days was calculated for free enzyme, 55 and 79 days for the immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 when stored at 4 ◦ C. Therefore, immobilization of acid phosphatase on Unc-LDH-CO3 and C-LDH-CO3 by direct adsorption is an effective means and would have promising potential for the practical application in agricultural production and environmental remediation. © 2010 Elsevier B.V. All rights reserved. 1. Introduction Acid phosphatase, which comes from microorganisms, animals, and plants, catalyzes the hydrolysis of a wide range of phosphomonoesters and phosphoproteins nonspecifically in acidic environments [1,2]. It plays a key role in the transformation of organic phosphorus to orthophosphate, the only type of phosphorus source taken up by crops [3,4]. Acid phosphatase is also used as an indicator enzyme for monitoring the risk of various pollutants in soils [5–7]. Moreover, the enzyme is important in promoting the degradation of organophosphorous pesticides in terrestrial and aqueous environments [8,9]. It has been reported that free enzymes generally have a short-lived activity because of rapid denaturation and degradation [10–12]. Immobilization on ideal support is an effective way ∗ Corresponding author. Tel.: +86 27 87671033; fax: +86 27 87280670. ∗∗ Corresponding author. Tel: +39 081 2539175; fax: +39 081 2539186. E-mail addresses: [email protected] (Q. Huang), [email protected] (A. Violante). 0927-7765/$ – see front matter © 2010 Elsevier B.V. All rights reserved. doi:10.1016/j.colsurfb.2010.01.020 to reuse or for improving their stability [13–16]. Ohmiya et al. [17] have immobilized acid phosphatase on porous glass beads for the dephosphorylation of casein. Kurita et al. [18] have compared the immobilization of acid phosphatase on 2-mercapto- and 6-mercapto-chitin, 6-mercapto-chitin was found to be a better support according to the durability of immobilized enzyme. Chang and Juang [13] have taken composite beads of chitosan and activated clay as support for the immobilization of acid phosphatase, the immobilized enzyme kept 90% of its original activity after 50 times of reuse. The immobilization of acid phosphatase on wet/dried pure chitosan beads, wet/dried chitosan–ZnO2 composite beads has also been observed by Chang and Juang [14], chitosan–ZnO2 composite as wet form was suggested as the most promising support for immobilization application. Moreover, acid phosphatase has been immobilized on montmorillonite and chitosan by Lai and Shin [19] to enhance the content of phosphorus in soils. However, most of these reported carriers are organic or semi-organic matrices and would subject to microbial attack in practical application. In order to find more effective materials as immobilizing agents, we have carried out an investigation on the immobilization of acid phosphatase by a type of inorganic clay, namely, layered double hydroxides (LDHs). J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 LDHs have a general formula of [M1−x 2+ Mx 3+ (OH)2 ]x+ [Ax/n n− ·mH2 O]x− , where M2+ , M3+ and An− are divalent cation, trivalent cation and interlayer anion, respectively, x is defined as M2+ /(M2+ + M3+ ) and varies between 0.20 and 0.33 [20,21]. These so-called anionic clays, which exist in nature or easily and cheaply synthesized under laboratory conditions, consist of positively charged layers and negatively charged interlayer anions [20,22]. The positive charges are developed due to the partial substitution of divalent metal ions by trivalent cations and balanced by interlayer anions [20,23]. By calcination above 450 ◦ C, LDHs would lose their layer structure due to dehydroxylation and decarbonation and form highly active composite metal oxides with larger surface area, higher porosity and greater anion exchange capacity [21,24]. Over the past decades, uncalcined- and calcined-LDHs have been used in many fields such as pharmaceutics and environmental remediation [25,26]. They have also been found to be available as the host material for enzymes due to their charged structure and porous surface. Ren et al. [27] reported that calcined-Mg/Al-CO3 have higher affinity for penicillin G acylase but lower percentage of residual activity than calcined-Zn/Al-CO3 . Alkaline phosphatase (AIP) immobilized within a Mg2 Al-LDH by “soft chemistry” coprecipitation synthesis showed 36–44% of residual activity [28]. The thermal and storage stability of lipase was increased obviously after the immobilization on layered double hydroxide of Zn/AlNO3 , Ni/Al-NO3 , Mg/Al-NO3 and Mg/Al-sodium dodecyl sulphate (SDS) by direct adsorption [15,16], which is a physical method and relatively easier and cheaper compare to chemical method [15]. The objectives of the present study are to investigate the optimal conditions for the immobilization of acid phosphatase by direct adsorption on Unc-LDH-CO3 and C-LDH-CO3 and the kinetic property, thermal, hydrolytic, reusable and storage stability of the immobilized enzyme. The potentials of immobilized acid phosphatase in the regulation of soil fertility and remediation of pesticides pollution might be evaluated. 2. Materials and methods 2.1. Enzyme Acid phosphatase (EC3.1.3.2 Type II, 1.0 units mg−1 from potato) was purchased from Sigma Chemical Company. 2.2. Synthesis and characterization of uncalcined and calcined LDH-CO3 The layered double hydroxide of Unc-LDH-CO3 was synthesized by coprecipitation as described by Violante et al. [29]. Part of UncLDH-CO3 was calcined at 500 ◦ C in an oven for 4 h. Both Unc-LDHCO3 and C-LDH-CO3 were used for the following immobilization studies. The surface area of the sample was determined by high speed automated surface area and pore size analyzer (Quantachrome Autosorb-1, USA), it was 90.5 m2 g−1 for Unc-LDH-CO3 and 176.8 m2 g−1 for C-LDH-CO3 . The point of zero charge (PZC) was 7.9 for Unc-LDH-CO3 and 8.7 for C-LDH-CO3 as measured by Mehlich method [30]. The SEM images of freeze dried LDHs–enzyme complexes were obtained by a JSM-6390 scanning electron microscope (JEOL, Japan) after the gold coating in vacuum by a JFC-1600 sputter coater (JEOL, Japan). The X-ray diffraction (XRD) patterns of LDH-CO3 and LDHs–enzyme complexes were obtained by a Rigaku diffractometer (Rigaku Corporation, Japan) equipped with Cu K␣ radiation. 2.3. Immobilization of acid phosphatase In a 10 mL centrifuge tube, ten milligram of LDHs were mixed with 4 mL of 10 mmol L−1 acetate buffer (pH 5.5) containing 200, 167 400, 600, 800, 1000, 1200, 1400, and 1600 g of acid phosphatase. The mixture was shaken at 25 ◦ C and 250 rpm for 2 h and then centrifuged at 10,000 × g for 20 min. The supernatant was collected and the residue was washed twice by 1.5 mL of acetate buffer. After centrifugation again, the washings were collected and the enzyme on the final residue (LDHs–enzyme complex) was the immobilized acid phosphatase. The concentration of acid phosphatase in the first supernatant and the following washings was determined at 280 nm by UV-spectrophotometer using BSA as the standard. The amount of acid phosphatase immobilized was calculated by subtracting the quantity of enzyme in solution from enzyme added initially. The immobilization of acid phosphatase was also investigated as a function of residence time and buffer pH. The immobilized acid phosphatase which was prepared by the immobilization of the enzyme with the initial concentration of 250 g mL−1 in 4 mL acetate buffer on 10 mg LDHs at pH 5.5 and 25 ◦ C was employed for the following activity and stability assays. 2.4. Activity of free and immobilized acid phosphatase The activity of free and immobilized acid phosphatase were determined as follows: The pH-activity profiles were constructed by re-suspending the LDHs–enzyme complex by 2 mL of 10 mmol L−1 buffer at various pHs (acetate buffer for pH 4.5, 5.0, 5.5, 6.0, 6.5 and Tris–HCl buffer for pH 7.0). One hundred microlitres of free acid phosphatase (0.5 mg mL−1 ) or the thoroughly re-suspended LDHs–enzyme complex was then mixed with 900 L of corresponding buffer containing 8 mol -nitrophenyl phosphate (pNPP). After incubation at 37 ◦ C for 1 h, the enzymatic reaction was terminated immediately by the addition of 1 mL of 1 mol L−1 NaOH solution [12]. The concentration of enzymatic product -nitrophenol was determined directly at 405 nm spectrophotometrically. The specific activity of free and immobilized acid phosphatase was defined as mol nitrophenol released by the catalysis of 1 mg acid phosphatase within 1 min. The temperature–activity profiles were constructed by conducting the enzymatic reaction in 10 mmol L−1 of acetate buffer (pH 5.5) with 8 mol pNPP at 15, 25, 37, 45, 55, and 65 ◦ C for 1 h. The catalytic kinetics was analyzed by incubating the enzyme in 10 mmol L−1 of acetate buffer (pH 5.5) containing 1, 2, 4, 6, and 8 mol pNPP at 37 ◦ C for 1 h. 2.5. Stability of free and immobilized acid phosphatase The thermal stability was investigated by incubating 100 L of free enzyme (0.5 mg mL−1 ) or the thoroughly re-suspended LDHs–enzyme complex in the absence of substrate at 50, 60, and 70 ◦ C for 30, 60, 90, 120, and 150 min. The activity was then determined after the further incubation with 900 L of 10 mmol L−1 of acetate buffer (pH 5.5) containing 8 mol pNPP at 37 ◦ C for 1 h. The hydrolytic stability was estimated by mixing 100 L of free enzyme (0.5 mg mL−1 ) or the thoroughly re-suspended LDHs–enzyme complex with 900 L of 10 mmol L−1 of acetate buffer (pH 5.5) containing 25 g of proteinase K. The mixture was thoroughly dispersed and then incubated at 37 ◦ C for 1 h, 2 h and 24 h, respectively. One millilitre of 10 mmol L−1 of acetate buffer (pH 5.5) containing 8 mol pNPP was then added immediately into the tube and the mixture was incubated in succession at 37 ◦ C for 1 h. No proteinase exposure was tested as the control for free and immobilized enzyme. The hydrolytic stability of free and immobilized phosphatase was calculated according to the following expression: hydrolytic stability (%) = (specific activity of acid phosphatase in the presence of proteinase/specific activity of acid phosphatase in the absence of proteinase) × 100. The hydrolytic stability of free and immobilized enzyme was also investigated by 168 J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 Fig. 1. Immobilization of acid phosphatase on LDHs with increasing enzyme concentrations (A), reaction time (B) and buffer pH (C). ITC with an isothermal microcalorimeter TAM III (Thermometric AB, Sweden). Net hydrolytic heat was calculated by deducting the dilution and/or adsorption heat of proteinase (sample without acid phosphatase) from the total heat (sample with acid phosphatase). For reusability, both immobilized enzyme were employed to catalyze the hydrolysis of pNPP repeatedly in a continuous cycles. The storage stability was observed by storing the free and immobilized enzymes in 10 mmol L−1 of acetate buffer (pH 5.5) at 4 ◦ C for 5, 10, 30, 60, and 90 days. The residual activity was determined in time by the method described above. of the enzyme on both supports reached a plateau value at an enzyme concentration of 250 g mL−1 within 2 h. The maximum immobilization was observed at pH 5.5. The percentage of acid phosphatase immobilized at optimal conditions by Unc-LDH-CO3 and C-LDH-CO3 was 59% and 73%, respectively, indicating higher immobilization of acid phosphatase on the latter support than that on the former one. 3. Results The LDHs and/or LDHs–enzyme complexes were characterized by SEM and XRD techniques. A flocky morphology of C-LDH-CO3 and a studded shape of Unc-LDH-CO3 after the immobilization of acid phosphatase were recorded by SEM (Fig. 2). The XRD patterns of Unc-LDH-CO3 in Fig. 3 showed some typical peaks which characterized the widely reported hydrotalcite [29], a basal space of 0.756 nm was calculated from the 003 reflection. For C-LDH-CO3 , 3.1. Immobilization of acid phosphatase on LDHs Figure 1 depicts the amount of acid phosphatase immobilized by Unc-LDH-CO3 and C-LDH-CO3 with increasing enzyme concentrations, reaction time and buffer pH. The immobilization 3.2. Characterization of LDHs and LDHs–acid phosphatase complex Fig. 2. SEM micrographs of Unc-LDH-CO3 (A) and C-LDH-CO3 (B) after enzyme immobilization. J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 169 Table 1 Kinetic parameters of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ) by Michaelis–Menten equation. Enzyme Km (mmol mL−1 ) Vmax (mol mg−1 min−1 ) F-E I-E on Unc-LDH-CO3 I-E on C-LDH-CO3 1.09 1.22 1.19 0.68 0.57 0.62 acid phosphatase immobilized on LDH-CO3 exceeded that of free enzyme at 55 ◦ C. The results indicated that Unc-LDH-CO3 and CLDH-CO3 had an obvious protecting effect for acid phosphatase against excess energy which may destroy the functional group of both enzyme and substrate and then limit the enzymatic reaction rate. Fig. 3. Powder XRD patterns of Unc-LDH-CO3 and C-LDH-CO3 before and after enzyme immobilization. the typical peaks of hydrotalcite disappeared while new broad peaks appeared (Fig. 3), indicating the collapse of layered double structure and the formation of Mg–Al mixed oxides. The XRD patterns of both Unc-LDH-CO3 –enzyme and C-LDH-CO3 –enzyme complex were similar to that of the corresponding pure mineral (Fig. 3), suggesting that acid phosphatase was limited to be intercalated into Unc-LDH-CO3 and the immobilization of the enzyme on the surface of C-LDH-CO3 prevented its structural reconstruction. Therefore, acid phosphatase was immobilized mainly on the external surface of Unc-LDH-CO3 and C-LDH-CO3 . 3.3. Activity of free and immobilized acid phosphatase As revealed by the pH-activity profiles (Fig. 4A), the maximum activity for free and immobilized acid phosphatase were observed at pH 5.5, where the enzyme on Unc-LDH-CO3 and C-LDH-CO3 retained 80 and 88% of the residual activity. These results indicated that the optimal pH for the activity of acid phosphatase did not change after the immobilization. The optimal pH for the activity of acid phosphatase was also reported at pH 5.5 and kept constant after the immobilization on Red soil colloids, kaolinite, goethite and 6-mercapto-chitin [12,18]. However, a shift of optimal pH from 5.2 for free acid phosphatase to 2.9 for the immobilized enzyme on composite beads of chitosan and ZrO2 powders was documented by Chang and Juang [13]. Figure 4B presents the activity of free and immobilized acid phosphatase at temperatures from 15 ◦ C to 60 ◦ C. The activity of free and immobilized enzyme increased with the increase of temperature from 15 ◦ C to 37 ◦ C and reached maximum at 37 ◦ C. Free enzyme lost its activity rapidly above 37 ◦ C, whereas enzymes immobilized on both supports were more stable. The activity of 3.4. Catalytic kinetics of free and immobilized acid phosphatase The effects of substrate concentration on the reaction rate of free and immobilized acid phosphatase were described well (R2 > 0.98, n = 6) by Michaelis–Menten equation: V = (Vmax S)/(Km + S), where S is substrate concentration (mmol L−1 ), V is reaction rate and Vmax is the maximum rate of reaction (mol mg−1 min−1 ), Km is the Michaelis constant (mmol L−1 ). The lower the Km value, the stronger the affinity of substrate for enzyme. The Vmax value for free and immobilized acid phosphatase on Unc-LDH-CO3 and C-LDH-CO3 was 0.68, 0.57 and 0.62 mol mg−1 min−1 , respectively (Table 1). The Michaelis constant (Km ) for free enzyme was 1.09 mmol mL−1 while that for immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 was increased to 1.22 and 1.19 mmol mL−1 , respectively, suggesting the decreased affinity of substrate for immobilized enzymes. The increase of Km value was also reported for acid phosphatase when immobilized on Ca-polygalacturonate and dry bead [4,31]. 3.5. Stability of free and immobilized acid phosphatase 3.5.1. Thermal stability The heat inactivation curves in Fig. 5 showed that free and immobilized acid phosphatase on Unc-LDH-CO3 and C-LDH-CO3 retained 32%, 56% and 46% of their initial activity after 150 min incubation at 50 ◦ C. At 60 ◦ C, the free and immobilized enzymes kept their initial activity to a level of 14%, 42% and 31%, respectively. Free acid phosphatase was nearly fully deactivated after 90 min incubation at 70 ◦ C, while the immobilized enzyme on Unc-LDHCO3 and C-LDH-CO3 preserved 20% and 12% of their initial activity after 150 min incubation at the same temperature. The thermal deactivation of the free and immobilized enzymes was fitted by the first-order kinetic equation to evaluate the deactivation rate: ln(A/A0 ) = −kd t + C1 , where A0 and A are the initial Fig. 4. Activity of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ) at different pH (A) and temperature (B). 170 J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 Fig. 5. Thermal stability of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ) at 50, 60, and 70 ◦ C. activity and the activity after t min incubation, kd is the deactivation rate constant (min−1 ), C1 is a constant. The deactivation energy of free and immobilized acid phosphatase was then calculated according to Arrhenius equation: ln(kd ) = −Ed /(RT) + C2 , where kd is the deactivation rate constant (min−1 ), R is gas constant (8.314 J mol−1 K−1 ), T is absolute temperature, C1 is a constant, and Ed is deactivation energy (J mol−1 ). The lower the Ed value, the less the temperature sensitivity of the enzyme [13]. Good correlation coefficients (R2 > 0.95) were obtained and the parameters are listed in Table 2. The kd value was decreased in the sequence of free enzyme > immobilized enzyme on C-LDHCO3 > immobilized enzyme on Unc-LDH-CO3 . The half-life (t1/2 ) value for free enzyme was 67, 28 and 9 min at 50 ◦ C, 60 ◦ C and 70 ◦ C, respectively. The values were increased to 175, 114 and 44 min for immobilized enzyme on Unc-LDH-CO3 and 132, 81 and 33 min for immobilized enzyme on C-LDH-CO3 . The Ed values for immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 were 35.24 and 40.66 kJ mol−1 , which were significantly lower than that of free enzyme (65.44 kJ mol−1 ). These results suggested that the thermal stability of acid phosphatase was enhanced markedly after the immobilization on LDH-CO3 particularly the uncalcined form. The Ed value for acid phosphatase immobilized on composite beads of chitosan and activated clay was 66.4 kJ mol−1 while that on wet/dried pure chitosan beads, wet/dried chitosan–ZnO2 composite beads ranged from 78 to 142 kJ mol−1 [13,14]. Lower Ed values for the immobilized acid phosphatase in the current study implied the less temperature sensitivity. Fig. 6. Hydrolytic stability of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ). 3.5.2. Hydrolytic stability Free acid phosphatase retained 45%, 30% and 12% of its original activity after the hydrolysis by proteinase for 1 h, 2 h and 24 h, respectively. However, 78%, 73% and 51% of the original activity was kept by immobilized enzyme on Unc-LDH-CO3 and 91%, 85% and 64% was remained by immobilized enzyme on C-LDH-CO3 after the hydrolysis by proteinase for 1 h, 2 h and 24 h, respectively (Fig. 6). These data indicated clearly that acid phosphatase became more resistant to proteolysis after the immobilization on LDH-CO3 especially the calcined form. Similar increase in the hydrolytic stability of acid phosphatase on organo-mineral complex has been reported by Rao et al. [32]. Table 2 Thermal deactivation parameters of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ) at 50, 60, and 70 ◦ C. Enzyme 50 ◦ C 60 ◦ C −1 Kd (min F-E I-E on Unc-LDH-CO3 I-E on C-LDH-CO3 0.0059 0.0047 0.0039 ) 70 ◦ C −1 t1/2 (min) Kd (min 67 175 132 0.0107 0.0063 0.0052 ) Ed (kJ mol−1 ) −1 t1/2 (min) Kd (min 28 115 81 0.0245 0.0114 0.0084 ) t1/2 (min) 9 44 33 65.44 35.24 40.66 J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 171 Fig. 7. ITC spectra for the hydrolysis of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ) by proteinase K. Hydrolytic heat of free and immobilized acid phosphatase by proteinase in 2 h was determined by ITC. The power–time curves for hydrolytic samples (sample with acid phosphatase) and corresponding controls (sample without acid phosphatase) are illustrated in Fig. 7. The net hydrolytic enthalpy (Hhyd ) values are listed in Table 3. With the equal amount of enzyme (45 g mL−1 ), the Hhyd value for free acid phosphatase was −1204.3 J, and that for immobilized enzyme on Unc-LDH-CO3 and C-LDH-CO3 was −528.3 and −453.9 J, respectively. The negative values indicated that the hydrolysis of the enzyme was an exothermic process. The amount of hydrolytic heat is closely related to the hydrolytic stability of the enzyme. The higher the hydrolytic heat, the more the enzyme molecules are hydrolyzed, and thus the lower the hydrolytic stability [33]. The hydrolytic heat released from free enzyme was 2.3 and 2.7 times higher than that from immobilized Table 3 Heat released from the hydrolysis of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on CLDH-CO3 ) (45 g mL−1 ) by proteinase K in 2 h. Enzyme F-E I-E on Unc-LDH-CO3 I-E on C-LDH-CO3 Net H (J) −1204.3 −528.3 −453.9 enzyme on Unc-LDH-CO3 and C-LDH-CO3 , implying that hydrolytic stability of acid phosphatase was improved significantly after the immobilization on LDH-CO3 particularly the calcined form. These findings were in good agreement with the above chemical assays. 3.5.3. Reusability The immobilized acid phosphatase on Unc-LDH-CO3 kept 62% and 10% of the initial activity after 6 and 10 reuses, while 77% and 30% of the initial activity was remained by the immobilized enzyme on C-LDH-CO3 after the same cycles (Fig. 8), indicating good durability of acid phosphatase immobilized on LDH-CO3 especially the calcined form. Higher reusability of acid phosphatase was reported by the immobilization on 6-mercapto-chitin, which retained 80% of its initial activity after 10 runs [18]. The immobilization of penicillin G acylase on calcined-Mg/Al-LDHs (Mg/Al = 2, calcined at 500 ◦ C) also displayed higher activity (36%) even after 15 operational cycles [27]. However, acid phosphatases immobilized on LDH-CO3 in the current study were much more durable than that on 2-mercaptochitin, which showed a sharp reduction in the activity only after 3 runs [18]. 3.5.4. Storage stability Acid phosphatases immobilized on Unc-LDH-CO3 and C-LDHCO3 kept 40% and 48% of their initial activity after 90 days, whereas the free enzyme lost all its activity after 60 days (Fig. 9). The semi- 172 J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 Fig. 8. Reusability of immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ). Fig. 9. Storage stability of free (F-E) and immobilized acid phosphatase on LDHs (I-E on Unc-LDH-CO3 and I-E on C-LDH-CO3 ). log plot of the relative activity against the duration of the days gave a half-life (t1/2 ) of 10 days for free enzyme, 55 and 77 days for the enzyme immobilized on Unc-LDH-CO3 and C-LDH-CO3 , respectively. These observations indicated that the storage stability of acid phosphatase was enhanced by the immobilization on LDH-CO3 particularly the calcined form. In an investigation by Rahman et al. [15], lipase immobilized on Mg/Al-LDHs and their nanocomposites showed storage stability up to 70% at 30 ◦ C for 60 days. 4. Discussions The promotive effects for the thermal stability, hydrolytic stability, reusability and storage stability of acid phosphatase by the immobilization on both Unc-LDH-CO3 and C-LDH-CO3 were shown in the present study. The enzyme immobilized on Unc-LDH-CO3 was more resistant to thermal inactivation than that on C-LDH-CO3 , while the enzyme immobilized on C-LDH-CO3 was more resistant to proteolysis and more durable for reuse and storage than that on Unc-LDH-CO3 . The promotion in thermal stability of enzyme after the immobilization was usually ascribed to the loss of its conformational flexibility [34], the immobilized enzyme therefore became rigid and remained stable even at higher temperature [16]. Moreover, the stability of immobilized enzyme was proportional to the ratio of physical adsorption between the enzyme and the support, which lock the enzyme into the active conformation [16,35]. The iso-electric point (IEP) of acid phosphatase is 5.0 [36], while the value of PZC for Unc-LDH-CO3 and C-LDHCO3 was 7.9 and 8.7, respectively. There is a strong electrostatic attraction between the negatively charged enzyme and positively charged LDHs at the present study (pH 5.5). More rigid structure of immobilized acid phosphatase on both Unc-LDH-CO3 and CLDH-CO3 compared to free enzyme may explain at least in part for the increase of their thermal stability. However, the proportion of physical adsorption on the immobilization of acid phosphatase by C-LDH-CO3 might be more than that by Unc-LDH-CO3 because of the higher PZC and the increase of anion exchange capacity after the calcination of LDHs [24]. Higher thermal stability of acid phosphatase immobilized on Unc-LDH-CO3 than that on C-LDH-CO3 might be due to the decrease of heat capacity after the calcination of LDHs. More heat energy from reaction or extra-environment was absorbed by Unc-LDH-CO3 and thus alleviated the destruction for the immobilized enzyme. The results from XRD indicated that acid phosphatase was immobilized mainly on the external surface of Unc-LDH-CO3 and C-LDH-CO3 . According to SEM images, both supports showed rough surface with three-dimensional pores (Fig. 2), acid phosphatase molecules could penetrate into these pores and become less accessible to proteinase [32,36]. Moreover, flocky morphology of C-LDH-CO3 was more porous than studded shape of Unc-LDH-CO3 . The steric hindrance for the diffusion of proteinase on the surface of LDH-CO3 and the restriction for the penetration of proteinase into the three-dimensional pores of the supports was stronger on C-LDH-CO3 than that on Unc-LDH-CO3 . More acid phosphatase immobilized on C-LDH-CO3 than that on Unc-LDH-CO3 thus was protected from hydrolysis by proteinase. The reusability of the immobilized enzyme was limited by the detachment of enzyme from the supports and the distortion of active site of the enzyme after continuous use [37]. Larger amount of immobilization and higher retention of residual activity might contribute together to the better durability for reuse of immobilized acid phosphatase on C-LDH-CO3 than that on Unc-LDH-CO3 . The dissimilarity in thermal stability and the coincidence in hydrolytic stability suggested that better storage stability of immobilized acid phosphatase on C-LDH-CO3 than that on Unc-LDH-CO3 was ascribed chiefly to the advantage in hydrolytic stability. The affinity of substrate (pNPP) for the immobilized acid phosphatase on LDH-CO3 was decreased compared to that for free enzyme, which was in agreement with the loss of activity after the immobilization. Since the molecular size of pNPP is smaller than proteinase [32], three-dimensional pores which prevented the penetration of proteinase on the surface of LDH-CO3 may have little limitation for the diffusion of substrate to contact with immobilized enzyme. Higher affinity of substrate for the enzyme immobilized on C-LDH-CO3 than that on Unc-LDH-CO3 might be due to the higher proportion of physical adsorption in the enzyme immobilization as discussed above, more enzyme molecules thus kept active conformation. The optimal residual activity in the present study was 80% on Unc-LDH-CO3 and 88% on C-LDH-CO3 . The values were higher than that on most natural or synthesized supports such as red soil colloids (39–72%), montmorillonite (20%), kaolinite (57%), goethite (68%), tannic acid (33%), composite beads of chitosan and activated clay (41–61%), composite beads of chitosan and ZrO2 powders (30–48%) which reported previously [12–14,32,36]. Actually, there are abundant of Al–OH groups presented on the surface of LDH-CO3 [26], the benefit effects of these groups have been documented for the retention of activity of acid phosphatase and urease [32,38]. Consequently, LDH-CO3 , particularly C-LDH-CO3 , is promising immobilization agent for acid phosphatase. 5. Conclusions Layered double hydroxides of uncalcined- and calcined-Mg/AlCO3 were used successfully as supports for the immobilization of acid phosphatase by the means of direct adsorption. Little activ- J. Zhu et al. / Colloids and Surfaces B: Biointerfaces 77 (2010) 166–173 ity loss, excellent thermal stability, hydrolytic stability, reusability and storage stability of the immobilized acid phosphatases revealed their promising potentials for practical application in the fields such as agricultural production and environmental remediation. Acknowledgements The research was financially supported by the National Natural Science Foundation of China (40825002) and the International Foundation for Science (C/2527-2). References [1] [2] [3] [4] [5] [6] [7] [8] [9] [10] [11] [12] [13] J.C. Tarafdar, N. Claassen, Biol. Fertil. Soils 5 (1988) 308. J.C. Tarafdar, R.S. Yadav, S.C. Meena, J. Plant Nutr. Soil Sci. 164 (2001) 279. G.A. Gilbert, J.D. Knight, Plant Cell Environ. 22 (1999) 801. H.K. Pant, P.R. Warman, Biol. Fertil. Soils 30 (2000) 306. L.J. Sikora, D.D. Kaufman, L.C. Horng, Biol. Fertil. Soils 9 (1990) 14. F. Sannino, L. Gianfreda, Chemosphere 45 (2001) 417. P. Bhattacharyya, S. Tripathy, K. Kim, S.H. Kim, Ecotoxicol. Environ. Saf. 71 (2008) 149. L. Gianfreda, M.A. Rao, Enzyme Microb. Technol. 35 (2004) 339. C.F. Hoehamer, C.S. Mazur, N.L. Wolfe, J. Agric. Food. Chem. 53 (2005) 90. J.M. Sarkar, A. Leonowicz, J.M. Bollag, Soil Biol. Biochem. 21 (1989) 183. E. Kandeler, Biol. Fertil. Soils 9 (1990) 199. Q. Huang, W. Liang, P. Cai, Colloids Surf. B 45 (2005) 209. M.Y. Chang, R.S. Juang, Process Biochem. 39 (2004) 1087. 173 [14] M.Y. Chang, R.S. Juang, Int. J. Biol. Macromol. 40 (2007) 224. [15] M.B.A. Rahman, M. Basri, M.Z. Hussein, M.N.H. Idris, R.N.Z.R.A. Rahman, A.B. Salleh, Catal. Today 93–95 (2004) 405. [16] M.B.A. Rahman, U.H. Zaidan, M. Basri, M.Z. Hussein, R.N.Z.R.A. Rahman, A.B. Salleh, J. Mol. Catal. B: Enzyme 50 (2008) 33. [17] K. Ohmiya, S. Sugano, S.E. Yun, S. Shimizu, Agric. Biol. Chem. 47 (1983) 535. [18] K. Kurita, H. Yoshino, S.I. Nishimura, S. Ishii, T. Mori, Y. Nishiyama, Carbohydr. Polym. 32 (1997) 171. [19] C.M. Lai, C.Y. Shin, J. Biomass Energy Soc. China 12 (1993) 31. [20] F. Cavani, F. Trifiroand, A. Vaccari, Catal. Today 11 (1991) 173. [21] S. Miyata, Clays Clay Miner. 23 (1975) 369. [22] S. Miyata, A. Okada, Clays Clay Miner. 25 (1977) 14. [23] S. Miyata, Clays Clay Miner. 28 (1980) 50. [24] L. Châtelet, J.Y. Bottero, J. Yvon, A. Bouchelaghem, Colloids Surf. B 111 (1996) 167. [25] C.D. Hoyo, Appl. Clay Sci. 36 (2007) 103. [26] K.H. Goh, T.T. Lim, Z. Dong, Water Res. 42 (2008) 1343. [27] L. Ren, J. He, D.G. Evans, X. Duan, R. Ma, J. Mol. Catal. B: Enzyme 16 (2001) 65. [28] E. Geraud, V. Prevot, C. Forano, C. Mousty, Chem. Commun. 13 (2008) 1554. [29] A. Violante, M. Pucci, V. Cozzolino, J. Zhu, M. Pigna, J. Colloid Interface Sci. 333 (2009) 63. [30] Y. Xiong, Soil Colloids, vol. 2, Science Press, Beijing, 1985. [31] C. Marzadori, C. Gessa, S. Ciurli, Biol. Fertil. Soils 27 (1998) 97. [32] M.A. Rao, A. Violante, L. Gianfreda, Soil Biol. Biochem. 32 (2000) 1007. [33] M.L. Bianconi, Biophys. Chem. 126 (2007) 59–64. [34] G. Bayramoğlu, E. Yalçin, M.Y. Arıca, Process Biochem. 40 (2005) 3505. [35] J.P. Lenders, P. Germain, R.R. Crichton, Biotechnol. Bioeng. 27 (1985) 572. [36] M.A. Rao, L. Gianfreda, F. Palmiero, A. Violante, Soil Sci. 161 (1996) 751. [37] K.R.C. Reddy, A.M. Kayasha, J. Mol. Catal. B: Enzyme 38 (2006) 104. [38] L. Gianfreda, M.A. Rao, A. Violante, Soil Sci. Soc. Am. J. 59 (1995) 805.
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