CN109422352B - Method for treating antibiotic wastewater by using immobilized laccase - Google Patents

Method for treating antibiotic wastewater by using immobilized laccase Download PDF

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CN109422352B
CN109422352B CN201710757563.9A CN201710757563A CN109422352B CN 109422352 B CN109422352 B CN 109422352B CN 201710757563 A CN201710757563 A CN 201710757563A CN 109422352 B CN109422352 B CN 109422352B
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bentonite
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文晓凤
杜春艳
曾光明
黄丹莲
赖萃
张辰
万佳
许飘
尹令实
谭诗扬
王荣忠
薛文静
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    • C12N9/0057—Oxidoreductases (1.) acting on diphenols and related substances as donors (1.10) with oxygen as acceptor (1.10.3)
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    • C12Y110/03—Oxidoreductases acting on diphenols and related substances as donors (1.10) with an oxygen as acceptor (1.10.3)
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Abstract

The invention discloses a method for treating antibiotic wastewater by using immobilized laccase, which comprises the following steps: mixing the immobilized laccase, a mediator substance and antibiotic wastewater for degradation treatment, and completing the degradation treatment of the antibiotic in the wastewater, wherein the immobilized laccase takes mesoporous bentonite as a carrier, the mesoporous bentonite is immobilized with the laccase, and the mesoporous bentonite is prepared by taking the bentonite as a raw material and performing acid-base etching. The method can quickly and efficiently degrade the antibiotics in the wastewater when the immobilized laccase is used for treating the antibiotic wastewater, and meanwhile, the immobilized laccase has better adaptability to the environment, so that the immobilized laccase has wider application environment compared with free laccase, has the advantages of simplicity, quickness, high efficiency, low cost, no secondary pollution and the like, and has good application prospect in the catalytic oxidation degradation of the antibiotics.

Description

Method for treating antibiotic wastewater by using immobilized laccase
Technical Field
The invention belongs to the field of treatment of antibiotic wastewater, relates to a method for treating antibiotic wastewater by using immobilized laccase, and particularly relates to a method for treating antibiotic wastewater by using immobilized laccase with mesoporous bentonite as a carrier.
Background
In recent years, a large amount of research and data of actual measurement show that the antibiotic pollution range in the natural environment is very wide, and meanwhile, the antibiotic exists in the environment for a long time and at low concentration, so that bacteria in the environment generate certain drug resistance, the potential harm to ecology is great, and the problem of antibiotic environmental pollution is attracted a great deal of attention. The traditional water treatment process has a great problem in the removal of antibiotics, and the antibiotics in the sewage cannot be effectively and thoroughly removed.
The biological enzyme is a protein biocatalyst secreted by organisms and having high efficiency and specificity (stereo, regional and chemical specificity). In the whole human history, the origin of the application of the enzyme is very early, along with the development of science and technology, the application range of the enzyme is increasingly wide and deep, the enzyme has application in the aspects of industrial and agricultural processing production, medical treatment, analysis and assay and the like, the enzyme has application in the aspects of environmental energy sources, including biosensors, biofuel cells, wastewater treatment and the like, the application in the fields has good prospects, and the enzyme occupies a very important position in basic scientific research. Therefore, the biological enzyme catalysis technology with high efficiency and high selectivity provides a new solution for solving the problems of energy, resources and environmental protection all over the world.
Laccase in biological enzyme is a protein found and extracted from lac lacquer tree secretion, is a copper-containing polyphenol oxidase, comprises 4 copper ions, and is one of copper blue oxidase proteins. Laccase has a good effect in catalytic oxidation degradation of organic pollutants, and is widely researched. The laccase has the advantages of wide oxidation substrates, low energy consumption, high efficiency and the like, so that the laccase has more and more attention. In recent years, researchers research the performance of the antibiotics in wastewater degradation, and find that the antibiotics can be efficiently and rapidly removed from sulfonamides, tetracyclines and the like in the presence of natural mediators, so that another effective way is provided for the treatment of the antibiotics.
In the existing method for treating antibiotics by adopting a bio-enzyme catalysis technology, all immobilized carriers of the used immobilized laccase are ordered mesoporous materials, however, the ordered mesoporous materials have high dependence on a preparation process, and meanwhile, the preparation process of the ordered mesoporous materials has the defects of high cost, large potential harm to the environment, high energy consumption, relatively long production period, more toxic and harmful reagents and the like. Therefore, the prior art for treating antibiotics by adopting immobilized laccase also has a series of problems of high preparation cost, high energy consumption, more toxic and harmful reagents and the like. Although the existing process for preparing the disordered mesoporous material by using the ceramic material and the natural mineral kaolin as the raw materials can reduce the cost and reduce the potential harm to the environment, the mesoporous material prepared by using the ceramic material and the natural mineral kaolin as the raw materials still has the defects, for example, in the separation step of the preparation process by using the kaolin as the raw material, because the particles are fine, easy to agglomerate and difficult to separate, the kaolin cannot be stably dispersed in an aqueous solution in the preparation process, the etching mesoporous efficiency can be influenced, the uniformity of the pore size distribution cannot be ensured, the application range of the prepared mesoporous material as a carrier is relatively small, and the immobilization performance is not ideal; similarly, when a mesoporous material prepared from a ceramic material is used as a support, there is a problem that the immobilization performance is not satisfactory. Therefore, the problems of high cost, high secondary pollution risk, complicated treatment process, poor treatment effect and the like still exist in the conventional antibiotic treatment technology. Therefore, how to comprehensively improve the problems and the defects in the prior art and obtain a mesoporous material with wide application, simple and convenient preparation method, excellent performance and low cost as a carrier for immobilizing laccase to prepare an immobilized laccase with good operation stability, good thermal stability, large enzyme adsorption amount, strong enzyme activity and environmental friendliness is of great significance for providing a method for treating antibiotic wastewater by using the immobilized laccase, which is simple, rapid, efficient, low in cost and free of secondary pollution.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide a simple, quick and efficient method for treating antibiotic wastewater by using immobilized laccase, which is low in cost and free of secondary pollution.
In order to solve the technical problems, the invention adopts the technical scheme that:
a method for treating antibiotic wastewater by using immobilized laccase comprises the following steps: mixing the immobilized laccase, the mediator substance and the antibiotic wastewater for degradation treatment to complete the degradation treatment of the antibiotic in the wastewater; the immobilized laccase is characterized in that mesoporous bentonite is used as a carrier, and laccase is immobilized on the mesoporous bentonite; the mesoporous bentonite is prepared by taking bentonite as a raw material and performing acid-base etching.
In the above method, preferably, the mesoporous bentonite includes silicon oxide, aluminum oxide, magnesium oxide; the mesoporous bentonite is a layered clay mineral; the particle size of the mesoporous bentonite is 1-20 μm; the average pore diameter of the mesoporous bentonite is 2 nm-10 nm; the mesoporous bentonite has a specific surface area of 244.622m2/g。
In the above method, preferably, the immobilized amount of the laccase in the immobilized laccase is 16.073 mg/g; the size of the laccase is 6.5nm multiplied by 5.5nm multiplied by 4.5 nm.
In the above method, preferably, the preparation method of the immobilized laccase comprises the following steps: mixing mesoporous bentonite and laccase solution, performing oscillation adsorption, and centrifuging to obtain immobilized laccase; the mass-volume ratio of the mesoporous bentonite to the laccase solution is 400 mg: 100 mL.
In the method, preferably, the laccase solution is prepared by dissolving laccase powder in a buffer solution with a pH value of 3-7; the initial concentration of the laccase solution is 0.1 mg/mL-4 mg/mL; the buffer solution is a citric acid buffer solution or a phosphate buffer solution; the phosphate buffer solution is prepared by mixing a disodium hydrogen phosphate solution and a sodium dihydrogen phosphate solution; the citric acid buffer solution is prepared by mixing a citric acid solution and a sodium citrate solution.
In the above method, preferably, the method for preparing mesoporous bentonite comprises the following steps:
s1, mixing bentonite with an alkali solution, carrying out alkali etching at a rotating speed of 5 r/min-60 r/min and a temperature of 50-120 ℃, washing to neutrality, and drying at a temperature of 80-120 ℃ to obtain alkali-etched bentonite;
s2, mixing the alkali etching bentonite with an acid solution, performing acid etching at the rotation speed of 5 r/min-60 r/min and the temperature of 50-100 ℃, washing to be neutral, drying at the temperature of 80-120 ℃, grinding, and sieving with a 100-200-mesh sieve to obtain the mesoporous bentonite.
In the above method, preferably, in step S1: the mass volume ratio of the bentonite to the alkali solution is 4 g-10 g: 100 mL; the alkali solution is NaOH solution; the concentration of the alkali solution is 5M-10M; the time of the alkali etching is 5-12 h; the drying time is 5-12 h;
and/or, in the step S2: the mass volume ratio of the alkali etching bentonite to the acid solution is 4 g-10 g: 100 mL; the acid solution is an HCl solution; the concentration of the acid solution is 2M-8M; the acid etching time is 5-10 h; the drying time is 5-12 h.
In the above method, preferably, the rotation speed of the oscillating adsorption is 150r/min to 300 r/min; the temperature of the oscillation adsorption is 20-40 ℃; the oscillating adsorption time is 5 min-120 min;
and/or the rotating speed of the centrifugation is 4000 r/min-10000 r/min; the centrifugation time is 5-15 min.
In the above method, preferably, the amount of the immobilized laccase added is 0.5mg to 10mg per ml of the antibiotic wastewater;
and/or the mediator substance is 1-hydroxybenzotriazole or syringaldehyde; the concentration of the mediator substance in the reaction system is 0.5 mmol/L;
and/or the degradation treatment is carried out under stirring conditions; the stirring speed is 150 r/min-300 r/min; the temperature of the degradation treatment is 20-40 ℃; the time of the degradation treatment is 5min to 120 min;
and/or, a buffer solution is adopted to adjust the pH value of the reaction system in the degradation treatment process; the pH value of the reaction system is 5-7; the buffer solution is citric acid buffer solution or PBS buffer solution.
In the above method, preferably, the antibiotic wastewater is tetracycline hydrochloride wastewater or sulfonamide antibiotic wastewater; the concentration of the antibiotic wastewater is 10 mg/L.
In the invention, the method for measuring the laccase immobilization amount comprises the following steps:
the amount of laccase immobilized is the difference between the amount of enzyme added before immobilization minus the amount of enzyme remaining in the supernatant after immobilization. And (2) after the laccase and the mesoporous bentonite are subjected to oscillation adsorption, performing centrifugal separation, taking supernatant obtained by centrifugation, measuring the absorbance of the supernatant at 275nm by using an ultraviolet spectrophotometer to obtain the concentration of the residual laccase in the supernatant, and calculating the fixed amount of the laccase on the mesoporous bentonite under different conditions according to the formula (1).
Figure BDA0001392523350000031
In formula (1): q. q.st-adsorbed amount of laccase, (mg/g);
C0initial concentration of laccase, (mg/mL);
Ctresidual laccase concentration in the supernatant after immobilization, (mg/mL);
v-total volume of immobilization system, (mL);
m represents the mass of the mesoporous bentonite as a carrier, (g).
In the invention, the method for measuring the activity of the immobilized laccase and the free laccase comprises the following steps:
(1) immobilized laccase: adding 1mg of immobilized laccase into a mixed solution of 2mL of PBS buffer solution with pH of 7 and 0.9mL of 1mmol/L ABTS solution, reacting for 5min at 25 ℃, stopping the reaction in an ice bath, centrifuging, taking supernatant obtained by centrifugation, and measuring the change value of absorbance of the supernatant at 420 nm. A mixed solution of 2mL of a pH 7 PBS buffer solution and 0.9mL of distilled water was used as a background solution. The activity of the immobilized laccase is expressed by an enzyme activity unit (U/g) per gram of carrier, and the enzyme activity is calculated by a formula (2).
(2) Free laccase: adding 0.1mL of free laccase into a mixed solution of 2mL of PBS buffer solution with pH value of 7 and 0.9mL of 1mmol/L ABTS solution, reacting for 5min at 25 ℃, stopping the reaction in an ice bath, centrifuging, taking supernatant obtained by centrifugation, and measuring the change value of absorbance of the supernatant at 420 nm. A mixed solution of 2mL of a pH 7 PBS buffer solution and 0.9mL of distilled water was used as a background solution. The activity of free laccase is expressed by enzyme activity unit (U/L), and the enzyme activity is calculated by formula (2).
(3) The calculation formula of enzyme activity is as follows:
Figure BDA0001392523350000041
in formula (2): v is the volume (mL) of the reaction system and the molar extinction coefficient (cm)2·mol-1) V (m) is the amount of liquid (solid) sample (mL/mg), L is the cuvette optical path (cm), Δ A is the absorbance change, 106To convert mol to μmol,. DELTA.t is reaction time (min).
The innovation points of the invention are as follows:
according to the invention, when the immobilized laccase is used for treating the antibiotic wastewater, the antibiotic in the wastewater can be degraded quickly and efficiently, and meanwhile, the immobilized laccase has better adaptability to the environment, so that the immobilized laccase has wider application environment compared with free laccase, and the method has the advantages of simplicity, quickness, high efficiency, low cost, no secondary pollution and the like, and has good application prospect in catalytic oxidation degradation of the antibiotic. The carrier of the immobilized laccase is mesoporous bentonite, the carrier takes bentonite as a raw material, and the characteristics of pore channels (micropores, mesopores and macropores), structure, good dispersibility, expansibility, cation exchange performance and the like of the bentonite are utilized to modify the carrier by an acid-base etching method, so that the mesoporous pore channels in the bentonite are increased by a simple method, and the environment-friendly mesoporous bentonite with high specific surface area, high pore volume, more uniform pore size distribution is prepared, and is a mesoporous material with wide application, simple and convenient preparation method, excellent performance and low cost. According to the invention, the laccase is immobilized on the mesoporous bentonite (specifically, the laccase is immobilized on the surface of the mesoporous bentonite and in pore channels of the mesoporous bentonite), so that the immobilized laccase which is good in operation stability, good in thermal stability, large in enzyme adsorption capacity, strong in enzyme activity and environment-friendly is obtained.
Compared with the prior art, the invention has the advantages that:
1. the invention provides a method for treating antibiotic wastewater by using immobilized laccase, which is characterized in that the immobilized laccase and the antibiotic wastewater are mixed for oscillation treatment to complete the treatment of the antibiotic wastewater. According to the invention, the immobilized laccase takes mesoporous bentonite as a carrier, the mesoporous bentonite has a pore size which is adaptive to the molecular size of the laccase, so that the immobilized laccase has better operation stability, the mesoporous bentonite has high heat resistance, so that the immobilized laccase has better thermal stability, and the mesoporous bentonite has high specific surface area, so that the immobilized laccase contains more laccase. Therefore, when the immobilized laccase with the advantages of good operation stability, good thermal stability, large enzyme adsorption capacity, strong enzyme activity, cleanness, no pollution, no toxic or side effect on the environment and the like is used for treating antibiotic wastewater, the antibiotic in the wastewater can be rapidly and efficiently degraded, and meanwhile, the immobilized laccase has better adaptability to the environment, so that the immobilized laccase has wider application environment relative to free laccase and has good application prospect in catalytic oxidation degradation of the antibiotic.
2. In the method, the immobilized laccase is successfully prepared by mixing the mesoporous bentonite and the laccase solution and immobilizing the mixture by physical adsorption, and the method has the advantages of simple and convenient operation, easy control, low preparation cost, good laccase immobilization effect, difficult inactivation of laccase, suitability for large-scale preparation and the like. In the invention, the mesoporous bentonite has the advantages of wide raw material source, low price, economy, simple preparation process, no harm to the environment and the like.
3. In the method, the mesoporous bentonite is prepared by etching bentonite serving as a raw material with acid and alkali. According to the invention, the bentonite is etched by adopting alkali treatment and acid treatment, so that the mesoporous of the bentonite is realized, the pore size of the bentonite is reduced, the specific surface area of the bentonite is greatly increased, and the environment-friendly mesoporous bentonite material with high specific surface area, high pore volume, more uniform pore size distribution is obtained; meanwhile, compared with other clay mineral materials, the mesoporous bentonite can be well and uniformly dispersed in a solution, so that laccase immobilization can be easily realized, the laccase immobilization efficiency can be remarkably improved, and a new carrier and a new path are provided for laccase immobilization.
4. In the method, the bentonite is used as a raw material to prepare the mesoporous bentonite, wherein the bentonite is an environment-friendly and cheap environmental mineral material, has wide sources and low cost, is clean and pollution-free, has no toxic or side effect on the environment, and has the advantages of high specific surface area, porosity, fine particles and the like. Compared with other clay materials, the bentonite adopted in the invention can be stably dispersed in water, the etching mesoporous efficiency is improved by better dispersion in the solution, and the mesoporous bentonite material with high specific surface area and high porosity is finally obtained.
5. In the method, the mesoporous bentonite is prepared by adopting an acid-base etching method, the used reagent is easy to obtain and can be repeatedly used, and the method has the advantage of low preparation cost.
Drawings
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention.
Fig. 1 is SEM images of mesoporous bentonite prepared in example 1 of the present invention and non-mesoporous bentonite prepared in comparative example 1, wherein (a) is non-mesoporous bentonite and (b) is mesoporous bentonite.
Fig. 2 is EDS graphs of the mesoporous bentonite prepared in example 1 of the present invention and the non-mesoporous bentonite prepared in comparative example 1, wherein (a) is the non-mesoporous bentonite and (b) is the mesoporous bentonite.
FIG. 3 is an SEM image of mesoporous bentonite and immobilized laccase prepared in example 1 of the present invention, wherein (a) is mesoporous bentonite and (b) is immobilized laccase.
FIG. 4 is an EDS chart of mesoporous bentonite and immobilized laccase prepared in example 1 of the present invention, wherein (a) is mesoporous bentonite and (b) is immobilized laccase.
FIG. 5 is a graph showing the effect of different amounts of immobilized laccase on the degradation of tetracycline hydrochloride in example 1 of the present invention.
FIG. 6 is a SEM comparison of before and after degradation of the antibiotic by the immobilized laccase of example 1 of the present invention, wherein (a) is the immobilized laccase before degradation, and (b) is the immobilized laccase after degradation.
FIG. 7 is a comparison of EDS before and after degradation of the antibiotic by the immobilized laccase of example 1 of the present invention, wherein (a) is the immobilized laccase before degradation and (b) is the immobilized laccase after degradation.
FIG. 8 is a graph showing the effect of immobilized laccase on tetracycline hydrochloride degradation at different treatment times in example 2 of the present invention.
FIG. 9 is a graph showing the effect of different immobilization times on immobilized laccase in example 3 of the present invention.
FIG. 10 is a graph showing the effect of laccase solutions of different initial concentrations on immobilized laccase in example 4 of the invention.
FIG. 11 is a graph showing the effect of laccase solutions of different pH values on immobilized laccase in example 5 of the present invention.
FIG. 12 is a graph showing the effect of the operation stability of the immobilized laccase of example 6 of the present invention.
FIG. 13 is a graph comparing the thermal stability of immobilized laccase and free laccase at different temperatures in example 7 of the present invention.
FIG. 14 is a graph showing the comparison of the immobilization effect of different mesoporous materials on laccase in example 8 of the present invention.
Detailed Description
The invention is further described below with reference to the drawings and specific preferred embodiments of the description, without thereby limiting the scope of protection of the invention.
The materials and equipment used in the following examples are commercially available. In the following examples, unless otherwise specified, the data obtained are the average of three or more replicates.
Example 1
A method for treating antibiotic wastewater by using immobilized laccase comprises the following steps:
mixing the immobilized laccase with tetracycline hydrochloride wastewater with initial concentration of 10mg/L according to the addition amount of 0.5mg/mL, 1mg/mL, 2mg/mL, 4mg/mL, 6mg/mL and 10mg/mL (namely, 0.5mg, 1mg, 2mg, 4mg, 6mg and 10mg of immobilized laccase is respectively added into tetracycline hydrochloride wastewater per milliliter), simultaneously adding a mediator substance (the mediator substance is 1-hydroxybenzotriazole, HBT for short, and is used as a reaction mediator to play an oxidative coupling role), the concentration of the mediator substance in the reaction system is 0.5mmol/L, and a citric acid buffer solution (the mediator substance is used for providing a reaction environment with constant pH, specifically, the pH value in the reaction system is 5 by adding the citric acid buffer solution), uniformly mixing, and rotating at the speed of 200r/min, And (3) degrading for 30min at the temperature of 30 ℃ to finish the degradation treatment of the tetracycline hydrochloride in the wastewater.
A placebo control group was set with antibiotic alone.
In this embodiment, the immobilized laccase is obtained by using mesoporous bentonite as a carrier, and laccase is immobilized on the mesoporous bentonite (specifically, laccase is immobilized on the surface of the mesoporous bentonite and in the mesoporous bentonite), wherein the mesoporous bentonite is obtained by using bentonite as a raw material and performing acid-base etching. Wherein the mesoporous bentonite comprises silicon oxide, aluminum oxide and magnesium oxide, is a layered clay mineral with particle diameter of 1-20 μm, average pore diameter of 5.531nm, and specific surface area of 244.622m2(ii) in terms of/g. The immobilized amount of laccase in the immobilized laccase was 16.073 mg/g. Laccase is a biological enzyme with the size of 6.5nm multiplied by 5.5nm multiplied by 4.5nm, and is an oxidase which is easy to obtain and has excellent characteristics.
A preparation method of the immobilized laccase in the embodiment comprises the following steps:
taking mesoporous bentonite as a carrier, adding the mesoporous bentonite into laccase solution with the initial concentration of 2mg/mL according to the solid-liquid ratio of 400 mg: 100mL (namely the mass-volume ratio of the carrier to the laccase solution is 400 mg: 100mL), adopting a physical adsorption method, oscillating and adsorbing for 30min by using a shaker at the rotation speed of 200r/min and the temperature of 30 ℃, then centrifugally separating the mixed solution after oscillating and adsorbing for 5min at the rotation speed of 8000r/min to obtain a precipitate, namely immobilized laccase, washing the precipitate for several times by using a buffer solution, then freeze-drying for 24h at-100 ℃, and storing at 4 ℃. Tests show that the enzyme activity of the immobilized laccase prepared by the invention under the optimal conditions is 33 kU/g.
The mesoporous bentonite is prepared by the following method: taking bentonite as a raw material, adding the bentonite into 6M NaOH solution according to the solid-liquid ratio of 5g/100mL (namely the mass-volume ratio of the bentonite to the NaOH solution is 5 g: 100mL), and carrying out alkali etching for 6h at the rotating speed of 30r/min and the temperature of 100 ℃; and after etching, filtering, washing the solid substance obtained by filtering to be neutral by using ultrapure water, and drying for 12h (the drying time can be implemented for 5 h-12 h) at 110 ℃ (the drying temperature can be 80 ℃ -120 ℃) to obtain the alkali etching bentonite. Adding the alkali etching bentonite into a 5M HCl solution according to the solid-liquid ratio of 5g/100mL (namely the mass-volume ratio of the alkali etching bentonite to the HCl solution is 5 g: 100mL), and carrying out acid etching for 6h under the conditions that the rotating speed is 30r/min and the temperature is 80 ℃; and after etching, filtering, washing the solid substance obtained by filtering to be neutral by using ultrapure water, drying for 12h (drying time can be implemented for 5 h-12 h) at 110 ℃ (the drying temperature can be 80 ℃ -120 ℃), grinding, and sieving by using a 100-mesh sieve to obtain the mesoporous bentonite.
The laccase solution is prepared by the following method: mixing a citric acid solution with the concentration of 0.1M and a sodium citrate solution with the concentration of 0.1M according to the volume ratio of 8.2: 11.8 to prepare a citric acid buffer solution with the pH value of 5.0. Weighing 200mg of laccase powder, dissolving the laccase powder in a citric acid buffer solution with the pH value of 5.0, and performing constant volume by using a 100mL volumetric flask to obtain a laccase solution with the concentration of 2 mg/mL.
Comparative example 1
A preparation method of non-mesoporous bentonite comprises the following steps: and (3) placing the bentonite in a ceramic crucible, and drying at 110 ℃ for 12h until the weight is constant, thereby obtaining the non-mesoporous bentonite.
SEM examination and analysis were performed on the mesoporous bentonite prepared in example 1 of the present invention and the non-mesoporous bentonite prepared in comparative example 1, and the results are shown in fig. 1. Fig. 1 is SEM images of mesoporous bentonite prepared in example 1 of the present invention and non-mesoporous bentonite prepared in comparative example 1, wherein (a) is non-mesoporous bentonite and (b) is mesoporous bentonite. As can be seen from FIG. 1, in the present invention, the mesoporous bentonite obtained by alkali etching and acid etching of bentonite is a layered clay mineral, the particle size of which is 1 μm to 20 μm, and more pores are generated and have higher porosity. Namely, the apparent structure of the bentonite after mesoporous treatment is greatly changed, so that the porosity of the mesoporous bentonite is greatly improved in appearance.
EDS detection analysis was performed on the mesoporous bentonite prepared in example 1 of the present invention and the non-mesoporous bentonite prepared in comparative example 1, and the results are shown in fig. 2. Fig. 2 is EDS graphs of the mesoporous bentonite prepared in example 1 of the present invention and the non-mesoporous bentonite prepared in comparative example 1, wherein (a) is the non-mesoporous bentonite and (b) is the mesoporous bentonite. As is clear from fig. 2, the mesoporous bentonite obtained by modifying bentonite by alkali etching and acid etching contains elements such as Al, Mg, Na, Ti, Si, O, and the like, that is, the mesoporous bentonite contains substances such as silicon oxide, aluminum oxide, magnesium oxide, and the like. In addition, the modification of the bentonite by acid-base etching does not change the element composition in the bentonite, which shows that the acid-base etching has no great influence on the components in the mesoporous bentonite, and the method is a relatively stable modification method.
SEM detection and analysis are carried out on the mesoporous bentonite and the immobilized laccase prepared in the embodiment 1 of the invention, and the result is shown in figure 3. FIG. 3 is an SEM image of mesoporous bentonite and immobilized laccase prepared in example 1 of the present invention, wherein (a) is mesoporous bentonite and (b) is immobilized laccase. As can be seen from FIG. 3, the immobilized laccase of the invention uses mesoporous bentonite as a carrier, the laccase is immobilized on and in the mesoporous bentonite, and the apparent structure of the immobilized laccase obtained after the laccase is immobilized has no change, which indicates that the appearance of the immobilized laccase has no change, the high specific surface area and the high porosity are still maintained, and the treatment of pollutants is facilitated.
EDS detection analysis is performed on the mesoporous bentonite and the immobilized laccase prepared in the embodiment 1 of the invention, and the result is shown in FIG. 4. FIG. 4 is an EDS chart of mesoporous bentonite and immobilized laccase prepared in example 1 of the present invention, wherein (a) is mesoporous bentonite and (b) is immobilized laccase. As can be seen from FIG. 4, the element composition of the immobilized laccase obtained after the laccase is immobilized on the mesoporous bentonite is not changed greatly, but C element appears, and the laccase contains C as protein, i.e., the C element in the immobilized laccase is derived from laccase, which also indicates that the laccase has been successfully immobilized on the mesoporous bentonite and in the mesoporous bentonite.
Table 1 is comparative data of the mesoporous bentonite prepared in example 1 of the present invention with the non-mesoporous bentonite prepared in comparative example 1 in terms of specific surface area, pore volume, average pore diameter and most probable pore diameter. As can be seen from Table 1, the alkali etching and acid etching of the bentonite significantly increase the specific surface area and pore volume of the material, and simultaneously reduce the average pore diameter of the material, wherein the specific surface area is 3.297m2The/g is increased to 244.622m2(iv)/g, increased by 74 fold; the pore volume is 0.02246cm3The/g is increased to 0.33830cm3(iv)/g, increased by 15 fold; the average pore diameter is reduced from 27.26nm to 5.531nm and is distributed between 2nm and 10 nm; the pore diameter of the most probable pore is increased from 4.074nm to 4.770nm and is distributed between 2nm and 10 nm. Therefore, after acid and alkali etching, the mesoporous bentonite has higher specific surface area, higher porosity and higher pore volume, and the pore size distribution is more uniform, and most probable pore size distribution is between 2nm and 10 nm.
TABLE 1 comparative data of the mesoporous bentonite prepared in example 1 of the present invention with the non-mesoporous bentonite prepared in comparative example 1 in terms of specific surface area, pore volume, average pore diameter and most probable pore diameter
Figure BDA0001392523350000091
FIG. 5 is a graph showing the effect of different amounts of immobilized laccase on the degradation of tetracycline hydrochloride in example 1 of the present invention. As can be seen from FIG. 5, when the addition amount is 4mg/mL, the degradation rate of the immobilized laccase of the invention to tetracycline hydrochloride reaches the maximum, which is 50.81%. In addition, when the addition amount is 2mg/mL, the unit degradation amount of the immobilized laccase to tetracycline hydrochloride reaches the maximum, and is 1.82 mg/g. Therefore, the immobilized laccase of the invention has better treatment capacity on antibiotic wastewater.
SEM detection and analysis of the immobilized laccase obtained after degradation of tetracycline hydrochloride in example 1 (i.e., the immobilized laccase in an amount of 2 mg/mL) are shown in FIG. 6. FIG. 6 is a SEM comparison of before and after degradation of the antibiotic by the immobilized laccase of example 1 of the present invention, wherein (a) is the immobilized laccase before degradation, and (b) is the immobilized laccase after degradation. As can be seen from FIG. 6, the immobilized laccase of the present invention has no structural change before and after degradation of tetracycline hydrochloride, which indicates that the immobilized laccase of the present invention has better environmental adaptability and very good practical application potential.
EDS detection analysis is carried out on the immobilized laccase obtained after degrading tetracycline hydrochloride in example 1 (namely, the immobilized laccase with the addition amount of 2 mg/mL), and the result is shown in FIG. 7. FIG. 7 is a comparison of EDS before and after degradation of the antibiotic by the immobilized laccase of example 1 of the present invention, wherein (a) is the immobilized laccase before degradation and (b) is the immobilized laccase after degradation. As can be seen from FIG. 7, the immobilized laccase of the present invention has no change in composition before and after degradation of tetracycline hydrochloride, which also indicates that the immobilized laccase of the present invention has better environmental suitability.
Example 2
A method for treating antibiotic wastewater by using immobilized laccase comprises the following steps:
the immobilized laccase obtained in example 1 is mixed with tetracycline hydrochloride waste water with the initial concentration of 10mg/L according to the addition of 2mg/mL, simultaneously adding a mediator substance (the mediator substance is 1-hydroxybenzotriazole solution, HBT for short) which is used as a reaction mediator and plays an oxidation coupling role, the concentration of the mediator substance in a reaction system is 0.5mmol/L) and a citric acid buffer solution (the function of the mediator substance is to provide a reaction environment with a fixed pH value, specifically, the pH value in the reaction system is 5 by adding the citric acid buffer solution), uniformly mixing, carrying out degradation treatment at the rotation speed of 200r/min and the temperature of 30 ℃, sampling and measuring the degradation rate of the immobilized laccase to the tetracycline hydrochloride when the reaction time is 0, 20min, 40min, 60min, 120min and 180min, and finishing the treatment of the tetracycline hydrochloride wastewater.
One control group of inactivated immobilized enzyme was set up and one blank with antibiotic only.
FIG. 8 is a graph showing the effect of immobilized laccase on tetracycline hydrochloride degradation at different treatment times in example 2 of the present invention. As can be seen from FIG. 8, the removal of tetracycline hydrochloride by the immobilized laccase and the inactivated immobilized laccase was gradually increased with the increase of time, and the maximum removal was reached after 180min of degradation treatment, wherein the removal of tetracycline hydrochloride by the immobilized laccase was 4.05mg/g, and the removal of tetracycline hydrochloride by the inactivated immobilized laccase was 1.74 mg/g. Meanwhile, as can be seen from FIG. 8, the degradation rate of the immobilized laccase to tetracycline hydrochloride reaches 62.57% at 180min, while the degradation rate of the inactivated immobilized laccase to tetracycline hydrochloride can only reach 30.37% at most, which is relatively lower by about half.
Example 3
The optimal immobilization time in the immobilization process of the immobilized laccase is considered, and the method comprises the following steps:
taking the mesoporous bentonite obtained in the example 1 as a carrier, adding the mesoporous bentonite into laccase solution with the initial concentration of 1mg/mL according to the solid-liquid ratio of 400 mg: 100mL (namely the mass-volume ratio of the carrier to the laccase solution is 400 mg: 100mL), and carrying out oscillatory adsorption by using a physical adsorption method and a shaking table at the rotation speed of 200rpm and the temperature of 30 ℃; and when the oscillating adsorption time is 15min, 30min, 60min, 120min and 180min, taking the mixed solution after oscillating adsorption, centrifugally separating for 5min at the rotating speed of 4000r/min to obtain a precipitate and a supernatant, wherein the precipitate obtained by centrifugation is the immobilized laccase, washing the immobilized laccase for a plurality of times by using a buffer solution, freeze-drying the immobilized laccase for 24h at the temperature of-100 ℃, and storing the immobilized laccase at the temperature of 4 ℃. And (3) taking the supernatant obtained by centrifugation, and measuring the content and the enzyme activity of the residual enzyme by using an ultraviolet spectrophotometer to obtain the enzyme activity and the relative activity of the immobilized laccase, wherein the result is shown in figure 9.
The laccase solution is prepared by the following method: weighing 100mg of laccase powder, dissolving the laccase powder in citric acid buffer solution with the concentration of 0.1M, pH and the value of 5.0, and fixing the volume by using a 100mL volumetric flask to obtain laccase solution with the concentration of 1 mg/mL.
FIG. 9 is a graph showing the effect of different immobilization times on immobilized laccase in example 3 of the present invention. As can be seen from FIG. 9, the activity and relative activity of the immobilized laccase reached maximum values substantially when the immobilization time reached 30min, wherein the activity and relative activity of the immobilized laccase were 794.44U/g and 100%, respectively. The immobilization time is 30-120 min, and the immobilization amount of the mesoporous bentonite to the laccase reaches a saturation state. The activity and relative activity of the immobilized laccase begin to be reduced after 120min, and the possible reason is that the structure of the carrier is changed to a certain extent due to long-time oscillation adsorption, so that the laccase falls off, the loss of the laccase is increased, and the activity and relative activity of the immobilized laccase are reduced. Therefore, when the immobilization time is 30-120 min, the immobilization amount and activity of the immobilized laccase reach the optimal state, namely, the immobilized laccase with better activity and relative activity can be prepared in the optimal immobilization time.
Example 4
The method for investigating the optimal initial concentration of the laccase solution in the immobilization process of the immobilized laccase comprises the following steps:
taking the mesoporous bentonite obtained in the example 1 as a carrier, adding six parts of mesoporous bentonite into laccase solutions with initial concentrations of 0.1mg/mL, 0.5mg/mL, 0.8mg/mL, 1.0mg/mL, 2.0mg/mL and 4.0mg/mL according to a solid-liquid ratio of 400 mg: 100mL (namely the mass-volume ratio of the carrier to the laccase solution is 400 mg: 100mL), respectively, adopting a physical adsorption method, carrying out oscillatory adsorption for 30min by using a shaking table under the conditions of a rotating speed of 200rpm and a temperature of 30 ℃, taking a mixed solution after the oscillatory adsorption, carrying out centrifugal separation for 5min at the rotating speed of 8000r/min, obtaining a precipitate which is immobilized laccase, washing the precipitate for several times by using a buffer solution, carrying out freeze drying for 24h at-100 ℃, and storing the precipitate at 4 ℃. The relative activity of the immobilized laccase (with the optimal enzyme activity value being 100%) was determined for each initial concentration of laccase, and the results are shown in FIG. 10.
The laccase solution is prepared by the following method: weighing 400mg of laccase powder, dissolving the laccase powder in citric acid buffer solution with the concentration of 0.1M, pH and the value of 5, performing constant volume by using a 100mL volumetric flask to obtain laccase solution with the initial concentration of 4.0mg/mL, and then diluting by corresponding times to obtain laccase solutions of 0.1mg/mL, 0.5mg/mL, 0.8mg/mL, 1.0mg/mL and 2.0 mg/mL.
FIG. 10 is a graph showing the effect of laccase solutions of different initial concentrations on immobilized laccase in example 4 of the invention. As can be seen from FIG. 10, the relative activity of the immobilized laccase increased with increasing initial concentration of the laccase solution; when the initial concentration of laccase solution is increased to 2mg/mL, the relative activity of the immobilized laccase reaches the maximum of 100%.
Example 5
The method for investigating the optimal pH value of the laccase solution in the immobilization process of the immobilized laccase comprises the following steps:
taking the mesoporous bentonite prepared in the example 1 as a carrier, adding six parts of the mesoporous bentonite into laccase solutions with pH values of 3.0, 4.0, 5.0, 6.0, 7.0 and 8.0 (the initial concentration of the laccase solution is 2.0mg/mL) according to a solid-liquid ratio of 400 mg: 100mL (namely the mass-volume ratio of the carrier to the laccase solution is 400 mg: 100mL), adopting a physical adsorption method, performing oscillatory adsorption for 30min by using a shaking table under the conditions of a rotating speed of 200rpm and a temperature of 30 ℃, centrifuging and separating the mixed solution subjected to the oscillatory adsorption for 5min at a rotating speed of 8000r/min, obtaining precipitates which are immobilized laccase, washing the precipitates by using a buffer solution for a plurality of times, then performing freeze drying at-100 ℃ for 24h, and storing the precipitates at 4 ℃. The relative activity of the immobilized laccase was determined by measuring the change in absorbance at 420nm of the solution obtained after the immobilized laccase was oxidized to 2, 2-azino-bis (3-ethylthia-6-sulfonic acid, ABTS) with an ultraviolet spectrophotometer, the results are shown in FIG. 11.
The laccase solution is prepared by the following method: weighing three parts of laccase powder, each 200mg, respectively dissolving in citric acid buffer solution (with concentration of 0.1M) with pH values of 3.0, 4.0 and 5.0, and diluting to constant volume with 100mL volumetric flask to obtain laccase solutions with pH values of 3.0, 4.0 and 5.0.
Weighing three parts of laccase powder, each 200mg of laccase powder is respectively dissolved in phosphate buffer solution (with the concentration of 0.1M) with the pH values of 6.0, 7.0 and 8.0, and the volumes are respectively determined by using 100mL volumetric flasks to respectively obtain laccase solutions with the pH values of 6.0, 7.0 and 8.0.
Meanwhile, the effect of different pH values on the activity of free laccase was determined by using free laccase as a control group, and the results are shown in FIG. 11.
FIG. 11 is a graph showing the effect of laccase solutions of different pH values on immobilized laccase in example 5 of the present invention. As can be seen from FIG. 11, the relative activity of the free laccase is maximal at pH 4 and that of the immobilized laccase is maximal at 100% at pH 5.
As can be seen from FIGS. 9, 10 and 11, in the preparation process of the immobilized laccase of the invention, the immobilization time, the initial concentration of the laccase solution and the pH of the laccase solution all affect the immobilization effect of the laccase, wherein the immobilization time is 30min, the initial concentration of the laccase solution is 2mg/mL, and the pH of the laccase solution is 5, so that the most ideal immobilized laccase can be prepared, and therefore, the optimal conditions for preparing the immobilized laccase of the invention are that the immobilization time is 30min, the initial concentration of the laccase solution is 2mg/mL, and the pH of the laccase solution is 5.
Example 6
The operation stability of the immobilized laccase is inspected, and the operation stability test is carried out by using the immobilized laccase prepared in the example 1, wherein the specific operation process is as follows:
reacting the immobilized laccase with 0.5mM ABTS at 30 ℃, washing with a citric acid buffer solution (the concentration is 0.1M, pH, the value is 5) for three times, performing centrifugal separation to obtain the immobilized laccase after reaction, and determining the enzyme activity of the immobilized laccase; the above procedure was repeated 10 times to determine the stability of the immobilized laccase, the results of which are shown in FIG. 12.
FIG. 12 is a graph showing the effect of the operation stability of the immobilized laccase of example 6 of the present invention. As can be seen from FIG. 12, after the 5 th operation, the enzyme activity is relatively greatly reduced, which may be because the laccase partially immobilized on the mesoporous material is greatly eluted during the washing process with the buffer solution, resulting in a large decrease in the enzyme activity, and then remains substantially unchanged, which may be because the laccase is immobilized inside the material and is not easily eluted. After 10 times of repeated operations, the relative activity of the immobilized laccase can still reach 27.34044%. Therefore, the immobilized laccase of the invention has better operation stability.
Example 7
The thermal stability of the immobilized laccase was investigated, and the immobilized laccase prepared in example 1 was used for the thermal stability test, the specific procedures were as follows:
the immobilized laccase is placed in a citric acid buffer solution with the concentration of 0.1M, pH value of 5.0 at 30 ℃, 40 ℃, 50 ℃, 60 ℃, 70 ℃ and 80 ℃ for heat treatment for 1h, and then is placed at room temperature for 1h to determine the activity of the immobilized laccase, so as to measure whether the enzyme has reversibility after heat treatment inactivation, study whether the immobilization has influence on the reversibility, detect the activity of the enzyme in oxidizing ABTS, and obtain the relative activity of the immobilized laccase at different temperatures (taking the immobilized laccase as 100% at the beginning), and the result is shown in FIG. 13.
Meanwhile, the relative activity of the free laccase was measured at different temperatures (starting with the free enzyme activity of 100%) using the free laccase as a control, and the results are shown in FIG. 13.
FIG. 13 is a graph comparing the thermal stability of immobilized laccase and free laccase at different temperatures in example 7 of the present invention. As can be seen from FIG. 13, the activity of the immobilized laccase is not changed basically with the increase of temperature, and the relative activity of the immobilized laccase is still 96.61272% when the temperature reaches 80 ℃; free laccase is highly susceptible to temperature, and as the temperature rises to 60 ℃ (i.e., above 50 ℃), the relative activity of free laccase decreases from 99.76527% to 75.51794%, and particularly, as the temperature reaches 70 ℃ and above, the free laccase substantially loses activity (the relative activity decreases to 0.53686%). Therefore, the immobilized laccase has high thermal stability and small irreversible damage to the immobilized laccase due to temperature, probably because the mesoporous bentonite prepared by the invention has high thermal tolerance, and meanwhile, the laccase is effectively immobilized on the mesoporous bentonite, so that the laccase is less influenced by the temperature.
The results in fig. 9, 10, 11, 12 and 13 show that the immobilized laccase of the present invention has a good immobilization effect, and has better operation stability and thermal stability compared with free laccase, high recycling rate and strong environmental adaptability. Therefore, when the immobilized laccase is used for treating antibiotic wastewater, the invention can rapidly and efficiently degrade antibiotics in the wastewater, and the immobilized laccase has better adaptability to the environment, so that the immobilized laccase has wider application environment compared with free laccase, and has good application prospect in catalytic oxidation degradation of organic pollutants.
Example 8
Investigating the immobilization effect of different mesoporous materials on laccase, specifically comprising the following steps:
(1) preparation of mesoporous material:
(1.1) preparation of mesoporous bentonite B1: same as in example 1.
(1.2) preparation of mesoporous bentonite B2: weighing 40g of NaOH into a beaker, adding a proper amount of ultrapure water to dissolve and transfer the NaOH into a 500mL volumetric flask, using the ultrapure water to perform constant volume until a scale mark is formed, and shaking up to obtain a 2M NaOH solution. Calcining the bentonite at 1000 ℃ for 2h, and taking out after naturally cooling to room temperature to obtain the calcined bentonite. Adding calcined bentonite into 2M NaOH solution at a solid-liquid ratio of 5g/100mL (namely the mass-volume ratio of calcined bentonite to NaOH solution is 5 g: 100mL), carrying out alkali etching at a rotation speed of 30r/min and a temperature of 80 ℃ for 6h, filtering after etching is finished, washing a solid substance obtained by filtering to be neutral by using ultrapure water, and drying at a temperature of 110 ℃ to obtain mesoporous bentonite with the number of B2.
(1.3) preparation of mesoporous kaolin K1: weighing 40g of NaOH into a beaker, adding a proper amount of ultrapure water to dissolve and transfer the NaOH into a 500mL volumetric flask, using the ultrapure water to perform constant volume until a scale mark is formed, and shaking up to obtain a 2M NaOH solution. And calcining the kaolin at 1000 ℃ for 2h, and taking out the kaolin after the kaolin is naturally cooled to room temperature to obtain the calcined kaolin. Adding calcined kaolin into NaOH solution with the concentration of 2M according to the solid-liquid ratio of 5g/100mL (namely the mass-volume ratio of the calcined kaolin to the NaOH solution is 5 g: 100mL), carrying out alkali etching for 6h at the rotation speed of 30r/min and the temperature of 80 ℃, filtering after etching, washing the solid matter obtained by filtering to be neutral by using ultrapure water, and drying at the temperature of 110 ℃ to obtain the mesoporous kaolin with the serial number of K1.
(1.4) preparation of mesoporous kaolin K2: adding kaolin into 6mol/L NaOH solution at a solid-to-liquid ratio of 5g/100ml for reaction at 100 ℃ for 6h, washing ultrapure water after the reaction is finished, and drying at 110 ℃. And (3) adding the kaolin subjected to alkali treatment into 5mol/L HCl solution at a solid-to-liquid ratio of 5g/100ml for reaction, wherein the reaction temperature is 80 ℃, the reaction time is 6 hours, after the reaction is finished, washing with ultrapure water, and drying at 110 ℃ to obtain the mesoporous material with the number of K2.
(2) Preparing a solution:
(2.1) preparation of Phosphate Buffer Solution (PBS) pH 7.0: 35.814g of disodium hydrogen phosphate (Na) were weighed2HPO4·12H2And O), dissolving the mixture by using deionized water, and then transferring the dissolved mixture into a 500ml volumetric flask to fix the volume for standby use to obtain a disodium hydrogen phosphate solution with the concentration of 0.2M. 15.601g of sodium dihydrogen phosphate (NaH) were weighed out2PO4·2H2O), dissolving the sodium dihydrogen phosphate by using deionized water, and transferring the solution into a 500ml volumetric flask to fix the volume for standby use to obtain a sodium dihydrogen phosphate solution with the concentration of 0.2M. And mixing the disodium hydrogen phosphate solution and the sodium dihydrogen phosphate solution according to a certain ratio until the pH of the mixed solution is 7.0 to obtain a phosphate buffer solution, and storing at 4 ℃ for later use.
(2.2) preparing a laccase solution: weighing 10mg of laccase powder, dissolving the laccase powder in PBS solution with the pH value of 7.0, and metering the volume by using a 100mL volumetric flask to obtain laccase solution with the concentration of 0.1 mg/mL.
(3) Immobilization of laccase
And (2) taking mesoporous bentonite (B1), mesoporous bentonite (B2), mesoporous kaolin (K1) and mesoporous kaolin (K2) as carriers, respectively adding the carriers into the laccase solution in the step (2) according to a solid-liquid ratio of 400 mg: 100mL (namely the mass-volume ratio of the carriers to the laccase solution is 400 mg: 100mL), adopting a physical adsorption method, carrying out vibration adsorption for 30min by using a shaking table at the rotation speed of 200r/min and the temperature of 30 ℃, then carrying out centrifugal separation on the mixed solution after vibration adsorption for 8min at the rotation speed of 5000r/min, and obtaining precipitates which are immobilized laccase, washing the precipitates for several times by using buffer solution, freezing and drying the precipitates for 24h at the temperature of 100 ℃ and storing the precipitates at the temperature of 4 ℃.
FIG. 14 is a graph showing the comparison of the immobilization effect of different mesoporous materials on laccase in example 8 of the present invention. As can be seen from FIG. 14, the mesoporous bentonite (B1) of the invention is used as a carrier, so that the immobilization effect on laccase is the best, the immobilization effect on free laccase is basically the best after oscillation for 30min, the enzyme activity of the immobilized laccase reaches 780.56U/g, and the enzyme activity begins to decrease until 120min later, namely oscillation for 30min-120min realizes effective immobilization on laccase. The immobilized laccase using mesoporous bentonite (B2) as a carrier has the largest enzyme activity of 447.12U/g after oscillation for 30min, and then has an inflection point on the immobilization effect of laccase, so that the enzyme activity is obviously reduced, namely the immobilized stabilization effect of the laccase using mesoporous bentonite (B2) as a carrier in the comparison document 2 is poor. The enzyme activity of the immobilized laccase taking the mesoporous kaolin (K1) as the carrier is increased along with the increase of oscillation time, the enzyme activity reaches the maximum value of 552.37U/g when the immobilized laccase is oscillated for 120min, then an inflection point appears on the immobilization effect of the laccase, and the enzyme activity is obviously reduced, namely the immobilization effect of the laccase taking the mesoporous kaolin (K1) as the carrier is poorer. In addition, the enzyme activity of the immobilized laccase taking the mesoporous kaolin (K2) as the carrier is increased along with the increase of oscillation time, the enzyme activity reaches the maximum value of 237.64U/g when the immobilized laccase is oscillated for 60min, then an inflection point appears after the immobilization effect on the laccase is 120min, the enzyme activity is obviously reduced, and the immobilization effect on the laccase by taking the mesoporous kaolin (K2) as the carrier is also poor. The reason for the above phenomena may be that the mesoporous bentonite (B2) and the mesoporous kaolin (K1) are respectively prepared by calcining bentonite and kaolin and performing alkali etching, and the mesoporous kaolin (K2) is prepared by performing alkali etching and acid etching on kaolin, and after the three materials are subjected to high-temperature calcination and acid-alkali etching, the porosity, the pore diameter and the specific surface area of the material are reduced, and the original structure of the material, which is beneficial to immobilized laccase, is damaged. Therefore, the mesoporous bentonite is used as a carrier, so that laccase can be immobilized more easily, and a better immobilization effect is achieved.
The above examples are merely preferred embodiments of the present invention, and the scope of the present invention is not limited to the above examples. All technical schemes belonging to the idea of the invention belong to the protection scope of the invention. It should be noted that modifications and embellishments within the scope of the invention may be made by those skilled in the art without departing from the principle of the invention, and such modifications and embellishments should also be considered as within the scope of the invention.

Claims (8)

1. A method for treating antibiotic wastewater by using immobilized laccase is characterized by comprising the following steps: mixing the immobilized laccase, the mediator substance and the antibiotic wastewater for degradation treatment to complete the degradation treatment of the antibiotic in the wastewater; the immobilized laccase is characterized in that mesoporous bentonite is used as a carrier, and laccase is immobilized on the mesoporous bentonite; the mesoporous bentonite is prepared by taking bentonite as a raw material and performing acid-base etching; the mesoporous bentonite comprises silicon oxide, aluminum oxide and magnesium oxide; the mesoporous bentonite is a layered clay mineral; the particle size of the mesoporous bentonite is 1-20 μm; the mesoporous bentonite has an average pore diameter of 5.531 nm; the mesoporous bentonite has a specific surface area of 244.622m2(ii)/g; the meso-porous bentonite has a most probable pore size of 4.770 nm;
the preparation method of the mesoporous bentonite comprises the following steps:
s1, mixing bentonite with an alkali solution, carrying out alkali etching at a rotating speed of 5 r/min-60 r/min and a temperature of 50-120 ℃, washing to neutrality, and drying at a temperature of 80-120 ℃ to obtain alkali-etched bentonite; the mass volume ratio of the bentonite to the alkali solution is 4 g-10 g: 100 mL; the alkali solution is NaOH solution; the concentration of the alkali solution is 5M-10M; the time of the alkali etching is 5-12 h;
s2, mixing the alkali etching bentonite with an acid solution, performing acid etching at the rotation speed of 5 r/min-60 r/min and the temperature of 50-100 ℃, washing to be neutral, drying at the temperature of 80-120 ℃, grinding, and sieving with a 100-200-mesh sieve to obtain the mesoporous bentonite; the mass volume ratio of the alkali etching bentonite to the acid solution is 4 g-10 g: 100 mL; the acid solution is an HCl solution; the concentration of the acid solution is 2M-8M; the acid etching time is 5-10 h.
2. The method of claim 1, wherein the immobilized amount of the laccase in the immobilized laccase is 16.073 mg/g; the size of the laccase is 6.5nm multiplied by 5.5nm multiplied by 4.5 nm.
3. The method according to claim 1 or 2, wherein the preparation method of the immobilized laccase comprises the following steps: mixing mesoporous bentonite and laccase solution, performing oscillation adsorption, and centrifuging to obtain immobilized laccase; the mass-volume ratio of the mesoporous bentonite to the laccase solution is 400 mg: 100 mL.
4. The method as claimed in claim 3, wherein the laccase solution is prepared by dissolving laccase powder in a buffer solution with a pH value of 3-7; the initial concentration of the laccase solution is 0.1 mg/mL-4 mg/mL; the buffer solution is a citric acid buffer solution or a phosphate buffer solution; the phosphate buffer solution is prepared by mixing a disodium hydrogen phosphate solution and a sodium dihydrogen phosphate solution; the citric acid buffer solution is prepared by mixing a citric acid solution and a sodium citrate solution.
5. The method according to claim 1, wherein in step S1: the drying time is 5-12 h;
and/or, in the step S2: the drying time is 5-12 h.
6. The method according to claim 3, wherein the rotation speed of the oscillating adsorption is 150r/min to 300 r/min; the temperature of the oscillation adsorption is 20-40 ℃; the oscillating adsorption time is 5 min-120 min;
and/or the rotating speed of the centrifugation is 4000 r/min-10000 r/min; the centrifugation time is 5-15 min.
7. The method according to claim 1 or 2, wherein the amount of the immobilized laccase added is 0.5-10 mg per ml of the antibiotic wastewater;
and/or the mediator substance is 1-hydroxybenzotriazole or syringaldehyde; the concentration of the mediator substance in the reaction system is 0.5 mmol/L;
and/or the degradation treatment is carried out under stirring conditions; the stirring speed is 150 r/min-300 r/min; the temperature of the degradation treatment is 20-40 ℃; the time of the degradation treatment is 5min to 120 min;
and/or, a buffer solution is adopted to adjust the pH value of the reaction system in the degradation treatment process; the pH value of the reaction system is 5-7; the buffer solution is citric acid buffer solution or PBS buffer solution.
8. The method according to claim 7, wherein the antibiotic wastewater is tetracycline hydrochloride wastewater or sulfonamide antibiotic wastewater; the concentration of the antibiotic wastewater is 10 mg/L.
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