CN114561293A - Method for purifying cefradine wastewater based on microalgae culture - Google Patents
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- C12N1/12—Unicellular algae; Culture media therefor
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Abstract
The invention belongs to the field of wastewater treatment, and particularly relates to a method for purifying cefradine wastewater based on microalgae culture, which comprises the following steps: 1) pre-culturing functional microalgae to reach logarithmic growth phase; 2) and inoculating the functional microalgae in the logarithmic growth phase in the step 1) into the wastewater containing the cefradine antibiotic to purify the antibiotic wastewater. The invention purifies the high-concentration antibiotic wastewater by utilizing the microalgae, does not need to add nutrient salt, and purifies pollutants by utilizing the photosynthesis of the microalgae to obtain the biomass of the microalgae and the cytochrome.
Description
Technical Field
The invention belongs to the field of wastewater treatment, and particularly relates to a method for purifying cefradine wastewater based on microalgae culture.
Background
The cephalosporin has high efficiency, low toxicity and wide clinical application, has the advantages of wide antibacterial spectrum, strong antibacterial effect, penicillinase resistance, rare allergic reaction compared with penicillins and the like, can not only destroy the cell wall of bacteria, but also sterilize in the propagation period of the bacteria, and has almost no toxicity to organisms, thereby being widely applied clinically.
The waste water from the production of cephalosporin antibiotics often contains a large amount of organic substances and components of cephalosporin antibiotics. Since cephalosporin antibiotics are broad-spectrum antibiotics, they destroy the cell wall of bacteria, rendering the bacteria inactive. High-concentration cephalosporin antibiotic wastewater is difficult to effectively treat by using a traditional activated sludge method, because bacteria are target cells of the antibiotics, the growth of the bacteria can be influenced by the existence of the antibiotics, and the effect of purifying the wastewater by the bacteria is influenced. In addition, the proliferation of the microorganism under the condition of high antibiotic concentration can be induced to generate antibiotic resistance genes, and the microorganism carrying the genes can reduce the antibiotic effect and generate great harm if entering the environment.
Disclosure of Invention
The invention aims to overcome the defects in the prior art and provides a method for purifying cefradine wastewater based on microalgae culture.
In order to achieve the purpose, the invention adopts the technical scheme that:
a method for purifying cefradine wastewater based on microalgae culture comprises the following steps:
1) pre-culturing functional microalgae to reach logarithmic growth phase;
2) and inoculating the functional microalgae in the logarithmic growth phase in the step 1) into the wastewater containing the cefradine antibiotic to purify the antibiotic wastewater.
The functional microalgae is Scenedesmus quadricauda or Chlorella L166.
The concentration of the cefradine in the step 2) is 25-100 mg/L.
The conditions of the pre-culture were set as: illumination all day long, illumination intensity 4800-2And N2Mixed gas of (2), CO2The occupied volume fraction is 5%.
Compared with the prior art, the invention has the beneficial effects that:
1) the invention utilizes microalgae culture to purify artificial simulation high-concentration antibiotic wastewater, and the degradation rate of Scenedesmus quadricauda to antibiotics is more than 95% after 8 days of culture. Meanwhile, the biomass concentration of Scenedesmus quadricaudatus after 8 days can reach 111.85 +/-1.26 mg/L, the chlorophyll content reaches 20.00 +/-1.58 mg/g, and the carotenoid content reaches 7.36 +/-0.26 mg/g. After 8 days of culture, the degradation rate of chlorella L166 to antibiotics is above 85%. Meanwhile, the biomass concentration of the chlorella L1668 days can reach 138.19 +/-0.37 mg/L, the chlorophyll content reaches 18.78 +/-0.38 mg/g, and the carotenoid content reaches 6.80 +/-0.03 mg/g.
2) The invention purifies the high-concentration antibiotic wastewater by utilizing the microalgae, does not need to add nutrient salt, and purifies pollutants by utilizing the photosynthesis of the microalgae to obtain the biomass of the microalgae and the cytochrome.
3) Carotenoids produced by the microalgae can eliminate active oxygen such as triplet chlorophyll and singlet oxygen produced by the microalgae under the stress of antibiotics, and are beneficial to purification of the antibiotics. In the method, the carotenoid content produced by the microalgae under the stress of the antibiotics is obviously higher than that produced by the microalgae without the stress of the antibiotics. It is shown that this alga is very suitable for the elimination of antibiotics and can achieve a very high purification efficacy.
Drawings
FIG. 1 is a graph showing the results of the degradation rate of Scenedesmus quadricauda in example 1 to different concentrations of cephradine;
FIG. 2 is a graph showing the change in biomass concentration of Scenedesmus quadricaudatus at different concentrations of cephradine in example 1;
FIG. 3 is a graph showing the change in chlorophyll content of Scenedesmus quadricauda at different concentrations of cephradine in example 1;
FIG. 4 is a graph showing the change in carotenoid content of Scenedesmus quadricaudatus at different concentrations of cefradine in example 1.
FIG. 5 is a graph showing the results of the degradation rate of the chlorella L166 to cephradine in different concentrations in example 2;
FIG. 6 is a graph showing the change in biomass concentration of Chlorella L166 under different concentrations of cephradine in example 2;
FIG. 7 is a graph showing the change in chlorophyll content of Chlorella L166 under different concentrations of cephradine in example 2;
FIG. 8 is a graph showing the change in carotenoid content of Chlorella L166 under different concentrations of cephradine in example 2.
FIG. 9 is a graph showing the results of the degradation rates of comparative examples Chlorella L166(a) and Scenedesmus quadricaudatus (b) for Sulfadimethoxine (SDM) at different concentrations;
FIG. 10 is a graph of the biomass concentration of the comparative examples Chlorella L166(a) and Scenedesmus quadricauda (b) against different concentrations of Sulfadimethoxine (SDM);
FIG. 11 is a graph showing the change in chlorophyll content of comparative examples Chlorella L166(a) and Scenedesmus quadricaudatus (b) against Sulfadimethoxine (SDM) at different concentrations;
FIG. 12 is a graph showing the carotenoid content changes of comparative examples Chlorella L166(a) and Scenedesmus quadricaudatus (b) for different concentrations of Sulfadimethoxine (SDM).
Detailed Description
In order to make the technical solutions of the present invention better understood by those skilled in the art, the present invention will be further described in detail with reference to the accompanying drawings and preferred embodiments.
Example 1: a method for strengthening microalgae purification of wastewater containing high-concentration antibiotics by utilizing ultraviolet strengthening comprises the following steps:
1) inoculating Scenedesmus quadratus FACHB-44 into 200mL of sterilized BG-11 culture medium, placing the culture medium into a biochemical incubator for pre-culture to enable Scenedesmus quadratus to reach a logarithmic growth phase, and then taking the Scenedesmus quadratus as a working algae solution;
the conditions of the pre-culture were set as: illumination all day long, illumination intensity 4800-2And N2Mixed gas of (2), CO2The occupied volume fraction is 5%.
2) And washing and centrifuging the algae liquid obtained in the step 1) by deionized water for 3 times, inoculating the algae liquid into artificial simulated high-concentration antibiotic wastewater with different concentrations, and culturing the wastewater on a microalgae culture rack. Ensuring that the absorbance of the initially inoculated microalgae is 0.1 at the wavelength of 680nm, illuminating all day by 4800-. The preparation method of the artificial simulated high-concentration antibiotic wastewater is that a certain amount of 4g/L cephradine mother liquor is added into 200mL BG-11 culture medium to obtain the artificial simulated high-concentration antibiotic wastewater containing 25, 50 and 100mg/L cephradine.
3) Periodically collecting the algae liquid cultured in the step 2), measuring the absorbance of the algae liquid at the wavelength of 680nm, and converting the algae liquid into the dry weight of cells according to a standard curve of the dry weight and the absorbance of the scenedesmus tetracaudatum, wherein the standard curve of the dry weight and the absorbance of the scenedesmus tetracaudatum is as follows: scenedesmus tetracaudatus dry cell weight (g/L) ═ 0.446 XOD680-0.006,R2=0.999。
4) Periodically collecting the algae solution cultured in the step 2), centrifuging and removing the supernatant to obtain algae mud, re-suspending the harvested algae mud in methanol-water solution with the same volume, storing at 4 ℃ for 16-24h, centrifuging to determine the absorbance of the supernatant at multiple wavelengths, determining the concentration of intracellular photosynthetic pigment, and comparing the concentration with the cell dry weight to obtain the normalized intracellular photosynthetic pigment content.
FIG. 1 shows that after 8 days of culture, the microalgae have purification rates of 96.89 + -0.14%, 98.32 + -0.40% and 94.45 + -0.12% for cephradine in 25, 50 and 100mg/L artificial simulated wastewater.
FIG. 2 shows that after 8 days of culture, the biomass of microalgae purified from 25, 50 and 100mg/L artificial simulated wastewater containing cephradine is 122.32 + -0.32 mg/L, 117.86 + -0.32 mg/L and 111.847 + -1.26 mg/L, respectively.
After 8 days of culture, the chlorophyll contents of the microalgae in the processes of purifying cephradine from 25mg/L, 50 mg/L and 100mg/L artificial simulated wastewater are respectively 20.00 +/-1.58 mg/g, 21.83 +/-0.45 mg/g and 22.00 +/-0.78 mg/g, which are respectively increased by 47.09%, 60.54% and 61.78% compared with a control group.
FIG. 4 shows that after 8 days of culture, the carotenoids of microalgae in the process of purifying cephradine from artificial simulated wastewater of 25mg/L, 50 mg/L and 100mg/L are respectively 7.36 + -0.26 mg/g, 7.69 + -0.20 mg/g and 7.69 + -0.50 mg/g, which are respectively improved by 22.25%, 27.68% and 27.59% compared with the control group.
BG-11 is a control group, which differs from the examples in that the medium does not require the addition of antibiotics.
Example 2: embodiment 2 is different from embodiment 1 only in that chlorella L166 is used instead of scenedesmus tetracaudatus.
FIG. 5 shows that the purification rate of chlorella L166 to cefradine waste water of 25, 50 and 100mg/L is 96.95 + -1.19%, 95.74 + -0.52% and 86.32 + -0.04% after 8 days of culture.
FIG. 6 shows that the biomass of chlorella L166 in purified waste water of 25, 50 and 100mg/L cephradine after 8 days of culture is 134.32 + -2.55 mg/L, 138.19 + -0.37 mg/L and 127.23 + -0.91 mg/L respectively.
FIG. 7 shows that after 8 days of culture, the chlorophyll contents of Chlorella L166 in purified cefradine wastewater of 25mg/g, 50mg/g and 100mg/L are respectively 18.78 + -0.38 mg/g, 18.97 + -0.24 mg/g and 18.06 + -0.03 mg/g, which are respectively increased by 15.86%, 17.07% and 11.44% compared with the control group.
FIG. 8 shows that after 8 days of culture, the carotenoids of chlorella L166 in the process of purifying cefradine wastewater of 25mg/L, 50 mg/L and 100mg/L are respectively 6.68 + -0.01 mg/g, 6.80 + -0.03 mg/g and 6.52 + -0.14 mg/g, which are respectively improved by 14.39%, 16.50% and 11.60% compared with the control group.
Comparative example: the comparative example only differs from the examples in that Sulfadimethoxine (SDM) is used instead of cefradine.
Chlorella L166(a) and Scenedesmus quadricauda (b) showed removal of Sulfadimethoxine (SDM) at different concentrations as shown in FIG. 9. As can be seen from the figure, after 12 days of culture, the maximum removal rate of 25mg/L sulfadimethoxine by the chlorella L166 is 13.96%, and the maximum removal rate of 100mg/L sulfadimethoxine is 13.44%. At day 6 of culture, Scenedesmus quadricauda reached the maximum removal of SDM at low (25mg/L) and high (100 mg/L) concentrations, 11.43% and 4.01%, respectively.
The growth of chlorella cells exposed to different concentrations of SDM is shown in figure 10. On day 12, exposure to 25, 50, 100mg/L SDM reduced the dry weight of Chlorella L166 by 2.02%, 7.90% and 16.94% compared to the control. After 12 days, exposure to 25, 50, 100mg/L SDM reduced the dry weight of Scenedesmus quadricaudatus 17.28%, 40.03%, 53.42% compared to the control (136.35mg/L)
The photosynthetic pigment content of the two algae varied with SDM concentration is shown in fig. 11. On day 12, when exposed to SDM at 25, 50, 100mg/L, the total chlorophyll content of Chlorella L166 is 23.33 + -1.56 mg/g, 23.87 + -1.27 mg/g, 22.15 + -1.03 mg/g. SDM decreased only 4.80% at 100 mg/L. The chlorophyll content of Scenedesmus quadricaudatus on day 12, when exposed to SDM of 25, 50, 100mg/L, was 5.54 + -0.15 mg/g, 4.66 + -0.51 mg/g, 6.26 + -1.21 mg/g, which were respectively reduced by 49.01%, 57.11%, 42.42%
FIG. 12 shows the change in carotene content of algae exposed to different concentrations of SDM as the culture time was extended. Chlorella L166 carotenoid content was 6.49 + -0.25 mg/g, 6.58 + -0.15 mg/g, 6.23 + -0.32 mg/g, respectively, with a significant 4.80% decrease in SDM at 100mg/L only, when exposed to 25, 50, 100mg/L SDM, compared to the control group (6.53mg/g) on day 12. At day 12, scenedesmus tetracaudatus carotenoid content decreased by 19.88%, 25.22%, 38.22% respectively when exposed to 25, 50, 100mg/L SDM compared to the control group (6.883mg/g), 5.51 + -0.61 mg/g, 5.14 + -0.13 mg/g, 4.25 + -1.08 mg/g respectively.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, various modifications and decorations can be made without departing from the principle of the present invention, and these modifications and decorations should also be regarded as the protection scope of the present invention.
Claims (4)
1. A method for purifying cefradine wastewater based on microalgae culture is characterized by comprising the following steps: 1) pre-culturing functional microalgae to reach logarithmic growth phase;
2) and inoculating the functional microalgae in the logarithmic growth phase in the step 1) into the wastewater containing the cefradine antibiotic to purify the antibiotic wastewater.
2. The method for purifying cephradine wastewater based on microalgae cultivation as claimed in claim 1, wherein the functional microalgae is Scenedesmus quadricauda or Chlorella L166.
3. The method for purifying cephradine-containing wastewater based on microalgae cultivation according to claim 1, wherein the concentration of cephradine in step 2) is 25-100 mg/L.
4. The method for purifying cephradine wastewater based on microalgae cultivation as claimed in claim 1, wherein the pre-cultivation conditions are set as follows: illumination all day long, illumination intensity 4800-2And N2Mixed gas of (2), CO2The occupied volume fraction is 5%.
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KE YANGA ET AL.: "An integrated view of the intimate coupling UV irradiation and algal treatment on antibiotic: Compatibility, efficiency and microbic impact assessment", JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, vol. 5, pages 4262 - 4268 * |
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