HYBRID MATERIAL COMPRISING A PROTEIN MATRIX AND COPPER NANOPARTICLES THEREIN, PROCESS FOR PREPARING THE SAME AND USE THEREOF
20220258143 · 2022-08-18
Inventors
- Jose Miguel PALOMO CARMONA (Madrid, ES)
- Noelia LOSADA GARCÍA (Madrid, ES)
- Alba RODRÍGUEZ OTERO (Madrid, ES)
Cpc classification
C12N9/20
CHEMISTRY; METALLURGY
B01J37/009
PERFORMING OPERATIONS; TRANSPORTING
B01J27/055
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J31/00
PERFORMING OPERATIONS; TRANSPORTING
B01J27/055
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates a hybrid material comprising: a protein matrix comprising the lipase B from Candida antarctica and nanoparticles of copper species selected from: Cu (0), Cu.sub.2O Cu.sub.3(PO.sub.4).sub.2 or any combination thereof, having their larger dimension between 3 and 15 nm. The material was prepared by the use of an enzyme in a buffer solution and a copper salt at room temperature. The material shows excellent catalase-like activity, excellent catalytic capacity in the degradation of organic pollutants, like Bisphenol A, and in the reduction of 4-nitrophenol to 4-aminophenol.
Claims
1. A hybrid material comprising: a protein matrix comprising lipase B from Candida Antarctica and nanoparticles of copper species selected from: Cu (0), Cu.sub.2O Cu.sub.3(PO.sub.4).sub.2 or any combination thereof, wherein the nanoparticles have an average diameter between 3 and 15 nm and are homogeneously distributed within the matrix.
2. The hybrid material according to claim 1, wherein the protein matrix consists of lipase B from Candida antarctica.
3. The hybrid material according to claim 1, wherein the hybrid material has between 22 and 94% by weight in Cu.
4. A process for preparing the hybrid material described in claim 1, the process comprises the next steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution, wherein the pH of the buffer solution ranges between 6 and 10 b) addition of a copper salt to the solution obtained in step a) at a temperature between 20 and 25° C., c) incubation of the solution obtained in step b) for a time between 16 h and 3 days, d) collecting, washing and drying the hybrid material obtained in the previous step.
5. The process according to claim 4, wherein the collected hybrid material is washed with water and/or drying by lyophilization in step d).
6. The process according to claim 4, wherein the process includes an additional step c)′, after step c) and before step d), which is: a reduction step comprising the addition of a reducing agent to the mixture obtained in step c) or an oxidation step comprising the addition of an oxidant agent, to the mixture obtained in step c).
7. The process according to claim 4, wherein the buffer solution of step a) is either a sodium phosphate buffer or a sodium bicarbonate buffer.
8. The process according to claim 4, wherein between 0.3 to 3 mg of lipase B from Candida antarctica is added per ml of buffer solution in step a).
9. The process according to claim 4, wherein the copper salt is Cu.sub.2SO.sub.4.5H.sub.2O.
10. The process according to claim 4, wherein 10 mg of copper salt is added in step b) per ml of buffer solution.
11. The process according to claim 4, wherein the incubation time in step c) ranges from 16 h to 24 h.
12. The process according to claim 4, wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium bicarbonate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for 16 h, c′) addition of sodium borohydride to a final concentration thereof of 0.12 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
13. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for 16 h, c′) addition of sodium borohydride to a final concentration thereof of 0.12 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
14. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium bicarbonate 0.1 M, wherein the protein is added in a proportion of 0.6 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for 16 h, c′) addition of sodium borohydride to a final concentration thereof of 0.12 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
15. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.6 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for 16 h, c′) addition of sodium borohydride to a final concentration thereof of 0.12 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
16. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for a 16 h. d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
17. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for a 16 h, c′) addition of H.sub.2O.sub.2 to a final concentration thereof of 0.1 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
18. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica, to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for a 16 h, c′) addition of NaOH to a final concentration thereof of 0.5 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
19. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica, to a buffer solution of sodium phosphate 0.1 M, wherein the protein is added in a proportion of 0.3 mg per ml of buffer solution, b) addition of the Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for a 16 h, c′) addition of sodium borohydride to a final concentration thereof of 0.012 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
20. The process according to claim 4 wherein the process comprises the following steps: a) addition under stirring of the lipase B from Candida antarctica to a buffer solution of sodium phosphate 0.1 M (pH 7), wherein the protein is added in a proportion of 3 mg per ml of buffer solution, b) addition of Cu.sub.2SO.sub.4.5H.sub.2O to the solution obtained in step at 20-25° C., wherein the Cu.sub.2SO.sub.4.5H.sub.2O is added in a proportion of 10 mg per ml of buffer solution, c) incubation of the solution obtained in step b) for 3 days, c′) optionally addition of sodium borohydride to a final concentration thereof of 0.12 M, d) collecting, washing with water and drying by lyophilization the hybrid material obtained on the previous step.
21. A catalyst characterized in that it comprises the hybrid material described in claim 1.
22-24. (canceled)
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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EXAMPLES
[0087] Some examples carried out by the inventors are provided below in order to illustrate the present invention:
Experimental Section
[0088] General
[0089] Lipase B from Candida antarctica (CAL-B) solution (Lipozyme®CALB) (10 mg/mL) was purchased from Novozymes (Copenhagen, Denmark). Copper (II) sulfate pentahydrate [Cu.sub.2SO.sub.4×5H.sub.2O] and hydrogen peroxide (33%) were from Panreac (Barcelona, Spain). P-nitrophenol, p-nitrophenyl propionate, sodium bicarbonate, sodium phosphate, sodium borohydride and Bisphenol A (BPA) were purchased from Sigma-Aldrich (St. Louis, Mo., USA). HPLC grade acetonitrile was purchased from Scharlab (Barcelona, Spain). Inductively coupled plasma-optical emission spectrometry) (ICP-OES) was performed on a OPTIMA 2100 DV instrument (PerkinElmer, Waltham, Mass., USA). X-Ray diffraction (XRD) patterns were obtained using a Texture Analysis D8 Advance Diffractometer (Bruker, Billerica, Mass., USA) with Cu Kα radiation. Transmission electron microscopy (TEM) and high resolution TEM microscopy (HRTEM) images were obtained on a 2100F microscope (JEOL, Tokyo, Japan) equipped with an EDX detector INCA x-sight (Oxford Instruments, Abingdon, UK). Interplanar spacing in the nanostructures was calculated by using the inversed Fourier transform with the GATAN digital micrograph program (Corporate Headquarters, Pleasanton, Calif., USA). Scanning electron microscopy (SEM) imaging was performed on a TM-1000 microscope (Hitachi, Tokyo, Japan). To recover the biohybrids, a Biocen 22 R (Orto-Alresa, Ajalvir, Spain) refrigerated centrifuge was used. Spectrophotometric analyses were run on a V-730 spectrophotometer (JASCO, Tokyo, Japan). A spectrum P100 HPLC system (Thermo Scientifics, Waltham, Mass., USA) was used. Analyses were run at 25° C. using an L-7300 column oven (Hitachi, Tokyo, Japan) and a UV6000LP detector (Thermo Scientifics, Waltham, Mass., USA).
Example 1: General Synthesis of Cu-CALB-BIC and Cu-CALB-PHOS Bionanohybrids
[0090] 1.8 mL (18 mg protein) of commercial Candida antarctica lipase solution was added to 60 mL buffer 0.1M (sodium bicarbonate pH=10 or sodium phosphate pH 7) in a 250 mL glass bottle containing a small magnetic bar stirrer. Then, 600 mg of Cu.sub.2SO.sub.4×5H.sub.2O (10 mg/ml) was added to the protein solution and it was maintained for 16 hours. After the first 30 min incubation, the solution turned cloudy (turquoise) and the pH solution was measured indicating a decrease from 8 or 6 depending on the buffer used. After 16 h, 6 mL of NaBH.sub.4 (300 mg) aqueous solution (1.2 M) was added to the cloudy solution (in two times of 3 mL) obtaining a final concentration of 0.12 M of sodium borohydride in the mixture. The solution turned rapidly black and, the mixture was reduced during 30 min. After the incubation, in all cases, the mixture was centrifuged at 8000 rpm for 5 min, (10 mL per falcon type tube). The generated pellet was re-suspended in 15 mL of water. The pH of the supernatant solution was measured to be approximately 7 or 9. It was centrifuged again at 8000 r.p.m for 5 min and the supernatant removed. The pH of the supernatant solution was measured again, given a pH value of 7. The process was repeated twice more. Finally, the supernatant was removed and the pellet of each falcon was re-suspended in 2 mL of water, collected all solutions in a round-bottom flask, frozen with liquid nitrogen and lyophilized for 16 hours. After that 150 mg of the so called Cu-CALB-BIC and Cu-CALB-PHOS respectively were obtained.
[0091] Different modifications of the protocol were made to obtain different species. Initially, a catalyst was prepared using double amount of enzyme (3.6 mL CALB solution instead of 1.8 mL), obtaining Cu-CALB-PHOS-2 and Cu-CALB-BIC-2.
[0092] Another variation of the protocol was used, in which the reduction step was not performed, obtaining Cu-CALB-PHOS-NR. In addition to the last variation, an oxidation step was also performed instead of reduction step by the addition of either 6 ml of a 500 mM solution of sodium hydroxide (NaOH) for 30 min or 6 ml of a 0.1 M solution of hydrogen peroxide (H.sub.2O.sub.2) for 30 min (60 μL of the H.sub.2O.sub.2 stock solution in 6 mL of distillate water), obtaining Cu-CALB-PHOS-NRNaOH and Cu-CALB-PHOS-NRH.sub.2O.sub.2 respectively. Another one of the variations was reduction of sodium borohydride at 10%, adding 6 mL of water containing NaBH.sub.4 (30 mg), obtaining Cu-CAL-B-PHOS10% R.
[0093] The last variation was referred both to the enzyme amount as well as the incubation time, increasing them from 1.8 mL to 18 mL in enzyme volume and from 16 h to 72 h; the obtained catalysts were Cu-CALB-PHOS-10 and Cu-CALB-PHOS-NR-10.
[0094] Characterization of the different Cu bionanohybrids was performed by XRD, ICP-OES, TEM and SEM analysis.
Example 2: Catalytic Reduction of 4-Nitrophenol (pNP) to 4-Aminophenol (pAP)
[0095] To an aqueous solution of p-nitrophenol (pNP) (1 mM; 2 mL), solid NaBH.sub.4 (3 mg) was added to reach a final concentration of 0.04 M (The typical catalytic reaction was performed by adding an excess of NaBH.sub.4 (0.04 M) to ensure its constant concentration throughout the reaction and, therefore, to apply a pseudo-first-order kinetic with respect to the pNP to an aqueous solution of the substrate in the presence of catalysts). In these conditions, upon the addiction of NaBH.sub.4, the initial absorbance band of the solution of pNP undergoes to an immediate shift from 317 to 400 nm due to the formation of 4-nitrophenolate ions. Immediately after that, 3 mg of the different Cu-CALB bionanohybrids were added under gentle stirring at 25° C. in an orbital shaker. The reaction progress was monitored by taking out an aliquot of the solution (0.1 mL) at different times, diluting it with distilled water (2 mL) and measuring the absorption spectrum between 500 and 300 nm in a PMMA cuvette (Table 1).
TABLE-US-00001 TABLE 1 Degradation of pNP by all bionanohybrids.
Example 3: Catalytic Degradation of Bisphenol-A (BPA)
[0096] A solution of 10 mM of BPA in pure acetonitrile was prepared. 0.2 ml of this solution were dissolved in 10 mL of either 100 mM or 5 mM sodium phosphate buffer pH 6, pH 7 or pH 8 to achieve a 0.2 mM concentration of BPA. The solution pH was adjusted using HCl or NaOH 1 M. Hydrogen peroxide was added to this BPA solution to obtain different concentrations (12, 25, 50, 100 or 150 mM). To initialize the reaction, 3 mg of the nanohybrid was added to 2 mL of this solution (BPA and H.sub.2O.sub.2) in a 7 mL glass flask. Gentle stirring was provided at room temperature by a roller. Samples (30 μl) at different times were taken and the reaction was followed by HPLC. The samples were diluted 5 times in a mixture of distilled water/acetonitrile 50/50 before injection. The HPLC column was C8 Kromasil 150×4.6 mm AV-2059. The HPLC conditions used were: an isocratic mixture of 50% acetonitrile and 50% bi-distilled water, UV detection at 225 nm using a Diode array detector, and a flow rate of 1 mL/min. Under these conditions, the retention time of BPA was 4.90 min, and for H.sub.2O.sub.2 was 1.57 min.
Example 4: Reuse of Cu-CALB-PHOS2 Nanohybrid in the Degradation of Bisphenol-A (BPA)
[0097] The Cu-CALB-PHOS2 nanohybrid was reused in five cycles for the degradation of BPA using the conditions described above. The catalyst was washed with water several times and centrifuged before the next reaction.
Example 5: Catalase-Like Activity of Cu Nanohybrids
[0098] A substrate solution was prepared adding 52 μL of hydrogen peroxide to 9.8 mL of 100 mM or 5 mM phosphate buffer (pH 6, pH 7 and pH 8) or distilled water in order to obtaining a final concentration of 50 mM. The solution pH was adjusted using HCl or NaOH 1 M. To start the reaction, 4.5 mg of the Cu nanohybrid or 50 μL of Catazyme® 25 L (1 mg/mL in distilled water) was added to a 3 mL of the previous solution at room temperature. The reaction was followed by measuring the degradation of hydrogen peroxide recording the decrease of absorbance by spectrophotometrically at 240 nm in quartz cuvettes of 1 cm path length, adding 2 mL of this solution at different times. After each measurement the volume added was again recovered and poured to the reaction solution.
[0099] In order to determine the catalase activity for each catalyst, the ΔAbs/min value was calculated using the linear portion of the curve (ΔAbs.sub.s).
[0100] The specific activity (U/mg) was calculated using the following equation:
where the molar extinction coefficient (ε) used was 43.6 M.sup.−1cm.sup.−1
Results and Discussion:
[0101] 1) Preparation and Characterization of Different Bionanohybrids Comprising the Protein Lipase B from Candida antarctica (CAL-B) and NPs of Different Cu Species:
[0102] The synthesis of these bionanohybrids containing copper nanoparticles have been performed in aqueous media by adding the commercial lipase B from Candida antarctica (CAL-B, 33 kDa, monomeric enzyme, supplied by Novozymes) to an aqueous solution of fully water-soluble copper salt at room temperature and under gentle stirring (
[0103] After 16 h incubation, the solid was reduced by using sodium borohydride, washed several times with distilled water, centrifuged and lyophilized overnight to obtaining the two heterogeneous biohybrids Cu-CALB-BIC and Cu-CALB-PHOS respectively. Both catalysts were characterized by different analysis techniques such as XRD, ICP-OES, TEM and SEM. Different species were obtained depending on the buffer used in the synthesis.
[0104] XRD analysis demonstrated that the main copper species in Cu-CALB-BIC hybrid was Cu(0), containing around 20% by weight of Cu(I) in form of Cu.sub.2O (
[0105] In the case of Cu-CALB-PHOS hybrid, XRD showed than the main Cu species was Cu(I) in form of Cu.sub.2O around 70% and also containing around 30% of Cu (0) (
[0106] One modification on the previous protocols was adding the double amount of enzyme in the preparation maintaining the rest steps the same. This modification did not affect to the copper species in method using carbonate as buffer, where XRD pattern of the so-called nanohybrid Cu-CALB-BIC2 showed the characteristic peaks of Cu (0) and one minority at 37° of the Cu.sub.2O (thus was slightly lower than in Cu-CALB-BIC) (
[0107] In the case of using phosphate as buffer, differences in Cu species and nanoparticles size were observed. In this case, XRD pattern determined that Cu-CALB-PHOS2 biohybrid showed peaks exclusively corresponding to Cu.sub.2O species, without traces of Cu (0) (
[0108] Therefore, by using this last methodology, a novel Cu bionanohybrid of controlled morphology, size and metal species was synthesized. This could be explained by the concept of larger amount of protein influence controlling the reduction of the cooper oxide species and also influenced in the coalescence step, controlling the nanoparticle growth.
[0109] Furthermore, selecting the methodology using phosphate buffer, other types of Cu bionanohybrids were synthesized avoiding the reducing step (Cu-CALB-NR) or changing it by incubation in the presence of hydrogen peroxide (oxidative step) (Cu-CALB-NRH.sub.2O.sub.2) or NaOH (Cu-CALB-NRNaOH) in the methodology. In the three cases, a light blue solid was obtained instead of the typical black color for the other biohybrids. XRD showed that in this case the copper species were Cu.sub.3(PO.sub.4).sub.2 in all cases (
[0110] TEM analysis revealed the slightly differences on the diameter size of the nanoparticles. In all cases crystalline spherical nanoparticles were formed, from 3-5 nm in Cu-CALB-NR (
[0111] Finally, a decrease in the amount of sodium borohydride used in the reduction step was performed. 10% (w/v) of NaBH.sub.4 used in the previous method was added in this case maintaining the intact the rest of synthetic steps in the method of synthesis of Cu-CALB-PHOS, in this case the biohybrid called Cu-CALB-PHOS10% R.
[0112] At these synthetic conditions, a biohybrid constitutes of extremely crystalline Cu.sub.3(PO.sub.4).sub.2 nanoparticles (diameter size approx. 10 nm) was obtained (
[0113] A final test using 10 times more amount of protein and increasing the incubation time from 1 day to 3 days was performed. These variations were used in two protocols, using phosphate buffer and with or without reduction step, being the Cu-CALB-PHOS-10 and Cu-CALB-PHOS-NR-10 bionanohybrids respectively. In this case SEM analysis revealed the formation of well-formed nanoflowers in both cases (
[0114] In all cases, the bionanohybrids were synthesized by a very effective, simple and sustainable way at multimilligram scale, easily scalable to grams.
2) Determination of Catalytic Activity pNP Reduction
[0115] In order to evaluate the metallic activity of the novel bionanohybrids prepared in example 1, the activity of them in the reduction of p-nitrophenol (pNP) to p-aminophenol (pAP) in aqueous media and room temperature (r.t.) was performed (Table 1). The differences in the rate of degradation of pNP that exist between the different catalysts was due to the Cu species obtained.
[0116] Cu-CALB-BIC and Cu-CALB-BIC2 (mainly Cu (0)) were the faster nanocatalysts with a complete transformation of pNP to pAP (150 ppm) in 30 seconds. However, Cu nanohybrids containing Cu(I) species showed lower catalytic efficiency, Cu-CALB-PHOS2 was more active than Cu-CALB-PHOS which needs double of time to complete transformation, 3 min instead 1.5 min (Table 1).
[0117] The catalyst prepared without reduction steps or with very high amount of proteins showed lower catalytic activities, being necessary between 3 to 15 min for full degradation (Table 1).
3) Bisphenol A Degradation by Bionanohybrids
[0118] The catalytic capacity of the bionanohybrids prepared in example 1 was evaluated in the degradation of Bisphenol A (BPA) in aqueous media at room temperature. The experimental conditions selected were 100 mM buffer phosphate in range pH 6-8 and the amount of BPA was 46 ppm using H.sub.2O.sub.2 as oxidant. All the Cu nanocatalysts were initially tested using 100 mM of H.sub.2O.sub.2 in 100 mM phosphate buffer at pH 8. From them the results obtained for the best four ones are represented in
[0119] The reaction was also tested with these two excellent catalysts at different pHs (from 6 to 8) (
[0120] The amount of H.sub.2O.sub.2 also was evaluated. The reaction was performed using Cu-CALB-PHOS2 as catalyst at 100 mM phosphate pH 8 in the presence of different concentrations of H.sub.2O.sub.2 from 12 to 150 mM (
[0121] Once optimal conditions were obtained, a recycling experiment was performed using the best Cu bionanohybrid, Cu-CALB-PHOS2 (
[0122] Considering the very fast degradation process by this catalyst and in order to elucidate a possible mechanism of degradation of BPA, the reaction was performed reducing the ratio mg catalyst/mL reaction volume from 1.5 (the previous result) to 0.3. At these conditions the catalyst still worked well, degrading more than 95% BPA in 60 min (
4) Catalase-Like Activity of Cu-Nanoparticles Biohybrids
[0123] The catalase activity (degradation of H.sub.2O.sub.2) of the different synthesized Cu bionanohybrids in water, 5 mM buffer and 100 mM buffer at different pHs was evaluated (Table 2). Interesting differences were found between the different Cu bionanohybrids and specially in comparison with the native catalase from Novozymes (Catazyme).
TABLE-US-00002 TABLE 2 Catalase activities of the different Cu bionanohybrids (catalysts). Specific activity (U/mg) pH not Catalyst Reaction solution adjusted pH 6 pH 7 pH 8 Cu-CAL- Distilled water 0.43 0.92 0.37 0.37 B-PHOS 5 mM phosphate 0.23 0.43 1.29 buffer 100 mM phosphate 0.32 0.14 0.57 buffer Cu-CAL- Distilled water 2.49 2.11 0.65 1.46 B-PHOS2 5 mM phosphate 0.08 0.46 0.19 buffer 100 mM phosphate 0.38 0.35 0.08 buffer Cu-CAL- Distilled water 1.19 0.36 1.02 0.20 B-BIC 5 mM phosphate 0.08 0.50 0.28 buffer 100 mM phosphate 0.17 0.19 0.06 buffer Cu-CAL- Distilled water 0.65 0.65 0.79 0.79 B-BIC2 5 mM phosphate 0.10 0.57 0.17 buffer 100 mM phosphate 0.02 0.17 0.10 buffer Catazyme Distilled water 2.79 11.16 6.98 46.05 5 mM phosphate 58.60 103.26 78.14 buffer 100 mM phosphate 26.51 36.28 9.77 buffer
[0124] The Cu-CALB-PHOS2 biohybrid exhibited the highest catalytic activity in the degradation of hydrogen peroxide, showing 2.49 U/mg of specific activity in distilled water and 2.11 U/mg in water adjusted at pH 6. At this latter condition this catalyst showed 6-fold higher activity compared with Cu-CALB-BIC, 4-fold more than Cu-CALB-BIC2 and 2-fold than Cu-CALB-PHOS (Table 2). In simply distilled water, Cu-CALB-PHOS2 showed almost six times more activity than Cu-CALB-PHOS, 2 times than Cu-CALB-BIC and 4 times than Cu-CALB-BIC2.
[0125] In particular, for Cu-CALB-PHOS2, the evaluation of the catalase activity was measured in distilled water at a range of pH from 4 to 9 (
[0126] In the case of the others Cu bionanohybrids, for example Cu-CALB-PHOS showed the highest activity value in distilled water adjusted at pH 6 whereas the best catalytic activity at higher pHs was achieved in the presence of 5 mM buffer (Table 2).
[0127] For Cu-CALB-BIC, the best results were obtained in distilled water, also adjusted at pH 6 and 7 whereas for Cu-CALB-BIC2 were in distilled water at pH 7 and 8.
[0128] In comparison with the natural catalase, the very interesting results was found in the conditions of distilled water (without pH adjust) where the Cu-CALB-PHOS2 showed similar activity than the natural enzyme.
Conclusions of the Examples
[0129] Novel Cu nanoparticles biohybrids have been synthesized, where the control of the Cu species, size, crystallinity and morphology of the nanoparticles was possible depending on the methodology used, for example being possible to obtain bionanohybrids containing very small size Cu (0) NPs, exclusively Cu.sub.2O NPs or crystalline Cu.sub.3(PO.sub.4).sub.2 NPs.
[0130] Cu bionanohybrids showed excellent catalytic activity in reduction of p-nitrophenol. These novel catalysts showed excellent catalytic performance in the degradation of a toxic and pollutant compound as BPA, where the best one, the Cu-CALB-PHOS2 biohybrid, was able to eliminate more than 95% of BPA (46 ppm) in 20 min in the presence of hydrogen peroxide at pH 8 using 1.5 g/L of catalyst.
[0131] Furthermore, here it has been demonstrated for the first time that these novel Cu bionanohybrids showed catalase activity, even in one case similar values of specific activity to the natural Catalase (Catazyme from Novozymes) in distilled water, which demonstrate that they are stable artificial metalloenzymes with possible interesting applications. This also can be extended to comparison with other catalases from different sources or even pseudocatalases.