CN111807477B - Method for removing antibiotic resistance gene based on solar heating film electrolysis - Google Patents

Method for removing antibiotic resistance gene based on solar heating film electrolysis Download PDF

Info

Publication number
CN111807477B
CN111807477B CN202010684763.8A CN202010684763A CN111807477B CN 111807477 B CN111807477 B CN 111807477B CN 202010684763 A CN202010684763 A CN 202010684763A CN 111807477 B CN111807477 B CN 111807477B
Authority
CN
China
Prior art keywords
electrolytic cell
solar heating
film
antibiotic resistance
resistance genes
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010684763.8A
Other languages
Chinese (zh)
Other versions
CN111807477A (en
Inventor
马德方
洪艺博
史伟业
高宝玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong University
Original Assignee
Shandong University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shandong University filed Critical Shandong University
Priority to CN202010684763.8A priority Critical patent/CN111807477B/en
Publication of CN111807477A publication Critical patent/CN111807477A/en
Application granted granted Critical
Publication of CN111807477B publication Critical patent/CN111807477B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/025Thermal hydrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/34Organic compounds containing oxygen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/003Wastewater from hospitals, laboratories and the like, heavily contaminated by pathogenic microorganisms
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/343Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Electrochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention relates to a method for removing antibiotic resistance genes based on solar heating film electrolysis, which comprises an electrolytic cell, wherein the upper part of the electrolytic cell is a platinum wire serving as a cathode, the lower part of the electrolytic cell is a solar heating conductive film serving as an anode, the two electrodes are connected to an external power supply through leads to form a closed loop, the two sides of the upper part of the electrolytic cell are respectively provided with a water inlet and a water outlet, the lower part of the solar heating conductive film is an annular supporting layer, and membrane filter liquid flows out from the annular supporting layer. A sunlight simulator is arranged outside the reactor to simulate sunlight. The invention combines the traditional membrane interception with a chemical electrolytic cell, loads a photo-thermal conversion material on the membrane, and destroys the structure of resistant bacteria and inactivates the resistant genes by utilizing the local high-temperature and acidic environment formed in a reactor, thereby achieving the purpose of removing the resistant genes.

Description

Method for removing antibiotic resistance gene based on solar heating film electrolysis
Technical Field
The invention relates to a method for removing antibiotic resistance genes based on solar heating film electrolysis, and belongs to the technical field of sewage purification treatment.
Background
Antibiotics exist widely in natural environment, the types of the antibiotics are various, the antibiotic residual quantity is the highest with the waste water of a farm, and the underground water is the lowest. The current situation of antibiotic pollution in domestic environment is more serious than that in foreign countries. The problem of environmental pollution caused by the heavy use of antibiotics and even abuse of antibiotics is becoming more serious, and the ecological environment safety and human health are seriously threatened by the pollution of Antibiotic Resistance Genes (ARGs) generated by microorganisms in animals induced by the selective pressure of antibiotics or microorganisms induced in the environment after entering the environment. The ARGs can carry out horizontal gene transfer in the same or different flora through movable gene elements such as plasmids, integron-gene cassettes, transposons and the like, have persistence and reproducibility in the environment and are considered as a novel environmental pollutant.
Resistance gene pollution exists in water, soil and atmosphere to different degrees, wherein tetracycline ARGs are detected in different environments. At present, resistance genes exist in basically all sewage plants in China, and resistance genes are also detected in natural water, for example, researches of scholars find that sulfonamides ARGs are the resistance genes with the highest occurrence frequency in water samples and sediments of Jiulongjiang, and tetracyclines ARGs and sulfonamides ARGs are detected in sediment samples. Resistance genes have been treated as environmental pollutants.
The existence form of the resistance gene is two types: present in resistant bacteria, free from the environment, and predominantly in the former. At present, the advanced oxidation process and the disinfection process are mainly used for removing the resistance genes. Advanced oxidation can destroy the double helix structure of bacterial DNA through physical or chemical mutagenesis, thereby effectively reducing the content of the resistance gene in effluent, but the practical application of the advanced oxidation has great limitations, firstly, the cost is high, secondly, the treatment effect is not good, and the resistance gene existing in bacteria can not be effectively removed. Sterilization plays an important role in reducing resistance genes in sewage not only because it can reduce the number of live resistant bacteria but also effectively inhibit gene transfer between live resistant bacteria. The effect of reduced resistance to disinfection depends on the degree of penetration of the disinfectant into the body of the resistant bacteria, and the reactivity of various components (e.g., amino acids, fats, carbohydrates, nucleic acids) within the cell. If the disinfectant causes cell inactivation independent of the nucleic acid, the intact resistance gene fragment remains in the cell and may be transferred to other microorganisms, and thus the disinfection cannot effectively remove the resistance gene.
The membrane interception is a common pollutant removal mode in the water treatment process, and has high treatment efficiency and stable water outlet. The amount of the resistance genes and bacteria in the effluent can be greatly reduced by adopting membrane interception, but the resistance genes and bacteria do not disappear, but exist in the concentrated water on one side of the membrane, the concentration is greatly increased compared with the original concentration, and further treatment is needed. Meanwhile, because the membrane has high cost, membrane pollution is easy to occur, the energy consumption in the operation process is high, and the practical application of membrane interception still has a great limit.
Therefore, there is a need to develop an economical and efficient technique for removing antibiotic resistance genes.
The invention content is as follows:
aiming at the defects of the prior art, the invention provides a method for removing antibiotic resistance genes based on solar heat-generating film electrolysis.
The method combines membrane interception with a chemical electrolytic cell, loads a photo-thermal conversion material capable of conducting electricity on the membrane, inactivates resistant bacteria and destroys a resistant gene structure by utilizing local high temperature and acidic conditions formed in a reactor, so as to achieve the aim of removing the resistant gene, and toxic byproducts are not generated in the process. Meanwhile, the external electric field can effectively reduce membrane pollution, prolong the service life of the membrane and have good economic benefit.
In order to achieve the purpose, the invention is realized by the following technical scheme:
a method for removing antibiotic resistance genes based on solar heating film electrolysis is carried out by utilizing a solar heating film electrolysis system, wherein the solar heating film electrolysis system comprises a sewage container, a water pump and an electrolytic cell which are communicated; a water inlet and a water outlet are respectively arranged on two sides of the upper end of the electrolytic cell, and an anode and a cathode are fixed in the electrolytic cell between the water inlet and the water outlet; the anode and the cathode are respectively connected to the anode and the cathode of an external power supply through metal leads to form an electrolytic cell, and the bottom of the electrolytic cell is provided with a filtrate outlet;
the anode is a solar heating conductive film, the solar heating conductive film is arranged on an annular supporting layer at the bottom of the electrolytic cell, the cathode is a platinum electrode, and the solar heating conductive film is obtained by loading a conductive photo-thermal conversion material on a PVDF ultrafiltration membrane;
the method for removing the antibiotic resistance gene is as follows: the method comprises the following steps of enabling sewage containing antibiotic resistance genes to enter an electrolytic cell through a water inlet, turning on a power supply, illuminating at the same time, enabling a solar heating conductive film to absorb solar energy to generate high temperature on the surface of the film, enabling the antibiotic and resistant bacteria structures flowing to the surface of the film along with water to be damaged, releasing the resistance genes, inactivating the resistance genes under the combined action of the high temperature and acidic conditions, filtering through the solar heating conductive film, and discharging from a filtrate outlet to remove the antibiotic resistance genes.
According to the invention, the solar heating conductive film is prepared by the following steps:
(1) placing the PVDF membrane on a dopamine hydrochloride solution, and standing for 10-20min to obtain an ultrafiltration membrane loaded with a polydopamine layer;
(2) dispersing the photo-thermal conductive material into a polyvinyl alcohol (PVA) solution to obtain a photo-thermal conductive material-PVA solution, and carrying out pressure deposition or electrostatic spinning on the photo-thermal conductive material-PVA solution onto the poly dopamine layer-loaded ultrafiltration membrane in the step (1) to form a PVA nanofiber network containing the photo-thermal conductive material, so as to obtain the solar heating conductive film.
Preferably, in step (1), the concentration of the dopamine hydrochloride solution is 1-5mg/mL, and the pH value is 8.5.
Preferably, in the step (2), when the pressure deposition method is adopted, the mass ratio of the photothermal conductive material to the polyvinyl alcohol (PVA) in the photothermal conductive material-polyvinyl alcohol solution is 1: 2 to 6, the pressure during pressure deposition is 0.1MPa, and the deposition time is 1 h.
Preferably, in the step (2), when the electrostatic spinning mode is adopted, the concentration of the photothermal conductive material in the photothermal conductive material-polyvinyl alcohol solution is 3-6wt%, the distance between the injector and the metal plate is 10cm, the injection rate of the injector is 0.5mL/min, the voltage is 10kV, and the spinning time is 3 h.
According to the present invention, preferably, the photothermal conductive material is Carbon Nanotubes (CNTs), carbon black, graphene or doped gold nanoparticles.
Most preferably, the photothermal conductive material is Carbon Nanotubes (CNTs).
According to the present invention, in the method for removing the antibiotic resistance gene, the distance between the solar heat conductive film and the platinum electrode is preferably 3 to 6 cm.
In the method for removing antibiotic resistance gene according to the present invention, the voltage of the power source is 1-3V and the intensity of the light is 1-3kw/m2
According to the preferable method for removing the antibiotic resistance gene, the sewage is secondary effluent of a sewage treatment plant, livestock wastewater, breeding wastewater, pharmaceutical wastewater or medical wastewater.
In the operation process of the method for removing the antibiotic resistance gene, the anode generates oxidation reaction to enrich hydrogen ions to form a local acid environment, and the unwinding and hydrolysis of the resistance gene can be accelerated by combining a high-temperature environment generated on the surface of the solar heating conductive film, so that the harmlessness of the resistance gene is realized.
According to the solar heating conductive film disclosed by the invention, when sunlight irradiates, the CNT absorbs solar energy and converts the solar energy into heat energy, and local high temperature is generated on the surface of the film. In the water treatment process, the resistant bacteria and the resistant genes reach the surface of the membrane along with water flow, the structure of the bacteria is destroyed and the resistant genes are released under the action of local high temperature, the double helix structure of the genes is opened, the resistant genes are released, the resistant genes are inactivated under the combined action of high temperature and acid conditions and no longer have resistance, and the resistant bacteria and the like in the sewage are intercepted on the surface of the membrane, so that the treatment time is prolonged. After a series of treatments, the membrane filtrate basically does not contain resistance genes, and the inlet water exceeding the membrane interception capacity is discharged from the water outlet and flows back to the water inlet.
The invention adopts a commercial PVDF ultrafiltration membrane which can resist high temperature, can intercept bacteria, large gene fragments and other particulate matters, suspended matters and macromolecular organic pollutants in water, and can ensure the quality of the effluent water on one hand; on the other hand, the pollutants are trapped on the surface of the membrane, so that the contact time with high-temperature and acidic environment is prolonged, and the removal effect is enhanced.
The invention has the advantages that:
1. the pollutants and the resistance genes are trapped on the surface of the membrane, so that the effluent quality can be ensured, the treatment time of the resistance genes can be prolonged, and the removal effect is improved.
2. The solar heating conductive film is adopted, and the photo-thermal conversion material is loaded, so that the ultrafiltration membrane can generate local high temperature under the action of solar energy, can sterilize and destroy a DNA double helix structure, is low in energy consumption and high in efficiency, and cannot generate toxic byproducts under the action of high temperature.
3. The membrane electrode is used as an anode, and when the membrane electrode is electrified, a local acidic environment is generated on the surface of the membrane and is coupled with a high-temperature environment, so that the hydrolysis of the secondary structure of the resistance gene can be accelerated, and the removal of the resistance gene is strengthened.
4. The cathode is subjected to reduction reaction to generate hydrogen, so that clean energy can be provided, the electricity of the electrolytic cell can be supplemented, and the energy conservation and environmental protection are realized.
5. The solar heating conductive film and the electrolytic cell are combined and mutually promoted, so that the treatment effect can be effectively improved. The loaded CNT material can endow the film with conductivity while carrying out photo-thermal conversion, and the external electric field can obviously reduce the film pollution, improve the film flux and prolong the service life of the film.
Description of the drawings:
FIG. 1 is a schematic structural view of a solar heating film electrolysis system of the present invention
In the figure: 1. a water inlet; 2. a platinum wire; 3. a water outlet; 4. a solar heating conductive film; 5. a ring-shaped supporting layer; 6. a filtrate outlet; 7. a wire; 8. a power source; 9. a water pump; 10. a sewage container; 11. a solar simulator; 12. an electrolytic cell.
The specific implementation mode is as follows:
the following is further described with reference to the drawings and examples, but is not limited thereto.
Example 1:
the structure of the solar heating film electrolysis system is shown in figure 1, and the solar heating film electrolysis system comprises a water pump and an electrolytic cell 12 which are communicated; the upper end of the electrolytic cell 12 is provided with a water inlet 1 and a water outlet 3 at two sides respectively, and an anode and a cathode are fixed in the electrolytic cell between the water inlet 1 and the water outlet 3; the anode is a solar heating conductive film 4, the solar heating conductive film is arranged on an annular supporting layer 5 at the bottom of the electrolytic cell, the cathode is a platinum electrode 2, the platinum electrode 2 is directly connected with a lead 7 to the cathode of an external power supply 8, two sides of the solar heating conductive film electrode 4 are connected to the anode of the power supply 8 through leads to form the electrolytic cell, and the bottom of the electrolytic cell is provided with a filtrate outlet 6; the secondary effluent of the sewage treatment plant in the sewage container 10 is lifted to the water inlet 1 by the water pump 9, and the sewage exceeding the membrane filtration capacity is discharged from the water outlet 3 and returns to the sewage container 10 again. The reactor is externally provided with a short-arc xenon lamp sunlight simulator 11 for simulating the irradiation of sunlight and providing solar energy.
The method for removing the antibiotic resistance gene is as follows: the sewage containing the antibiotic resistance genes enters the electrolytic cell through the water inlet, the power supply is turned on, meanwhile, illumination is carried out, the solar heating conductive film absorbs solar energy to generate high temperature on the surface of the film, the antibiotic and resistant bacteria structures flowing to the surface of the film along with water are damaged, the resistance genes are released, the resistance genes are inactivated under the combined action of the high temperature and the acidic condition, and the sewage is filtered by the solar heating conductive film and then is discharged from a filtrate outlet to remove the antibiotic resistance genes.
The solar heating conductive film is prepared by the following method:
(1) one side of the PVDF membrane is contacted with 1-5mg/mL dopamine hydrochloride solution with pH of 8.5 for 10-20min, and the polydopamine layer can assist in adhering the hydrophilic photothermal layer on the hydrophobic PVDF membrane.
(2) Fixing the carbon nano tube: the CNTs are dispersed into the PVA solution, pre-treated with polydopamine to ensure adhesion, and the PVA-CNT solution is pressure deposited or electrospun onto the PVDF membrane to form a PVA nanofiber network containing CNTs.
Experimental example 1:
the secondary effluent of a certain sewage treatment plant is treated by using the solar heating membrane electrolytic cell in the embodiment 1, and six genes are selected: sulfanilamide resistance genes sulI and sulI, tetracycline resistance genes tetA and tetW, class I integron integrase genes int I and 16S rRNA, and the initial abundance of the sulfanilamide resistance genes sulI and the tetracycline resistance genes tetA and tetW are respectively 1.93 multiplied by 105~9.95×106copies/mL、2.34×108~4.26×108copies/mL、7.64×107~9.22×107copies/mL、1.37×107~6.19×107copies/mL、4.37×107~9.15×107copies/mL、3.42×108~3.72×109copies/mL were treated with a PVDF film not carrying a photothermal conversion material and a modified solar heat conductive film, respectively, and the concentrations of the six genes after the treatment were measured, and the results are shown in Table 1.
Table 1: removal of resistance genes from PVDF film and solar heat-generating conductive film
Figure DEST_PATH_IMAGE002
Experimental example 2:
the solar heating membrane electrolytic cell in example 1 is used for treating breeding wastewater of a certain pig farm, and six genes are selected: sulfanilamide resistance genes sul I and sul II, tetracycline resistance genes tetM, tet W, tet Q and I type integrase gene int I, and the results are shown in a table 2 by comparing the absolute abundance of the water inlet and outlet resistance genes.
Table 2: removal of resistance gene of solar heating membrane electrolytic cell to breeding wastewater
Figure DEST_PATH_IMAGE004
From the experimental results, the method combines the solar heating conductive film and the electrolytic cell process, and the solar heating conductive film and the electrolytic cell process are mutually promoted, so that the treatment effect can be effectively improved. The loaded CNT material can endow the film with conductivity while carrying out photo-thermal conversion, and the external electric field can obviously reduce the film pollution, improve the film flux and prolong the service life of the film.

Claims (7)

1. A method for removing antibiotic resistance genes based on solar heating film electrolysis is carried out by utilizing a solar heating film electrolysis system, wherein the solar heating film electrolysis system comprises a sewage container, a water pump and an electrolytic cell which are communicated; a water inlet and a water outlet are respectively arranged on two sides of the upper end of the electrolytic cell, and an anode and a cathode are fixed in the electrolytic cell between the water inlet and the water outlet; the anode and the cathode are respectively connected to the anode and the cathode of an external power supply through metal leads to form an electrolytic cell, and the bottom of the electrolytic cell is provided with a filtrate outlet;
the anode is a solar heating conductive film which is arranged on an annular supporting layer at the bottom of the electrolytic cell, and the cathode is a platinum electrode;
the solar heating conductive film is prepared by the following method:
(1) placing the PVDF membrane on dopamine hydrochloride solution, and standing for 10-20min to obtain an ultrafiltration membrane loaded with a polydopamine layer;
(2) dispersing the photo-thermal conductive material into a polyvinyl alcohol solution to obtain a photo-thermal conductive material-polyvinyl alcohol solution, and depositing or electrospinning the photo-thermal conductive material-polyvinyl alcohol solution onto the poly dopamine layer-loaded ultrafiltration membrane in the step (1) through pressure to form a PVA nanofiber network containing the photo-thermal conductive material, so as to obtain the solar heating conductive film; the photo-thermal conductive material is a carbon nano tube;
the method for removing the antibiotic resistance gene is as follows: the sewage containing the antibiotic resistance genes enters the electrolytic cell through the water inlet, the power supply is turned on, meanwhile, illumination is carried out, the solar heating conductive film absorbs solar energy to generate high temperature on the surface of the film, the antibiotic and resistant bacteria structures flowing to the surface of the film along with water are damaged, the resistance genes are released, the resistance genes are inactivated under the combined action of the high temperature and the acidic condition, and the sewage is filtered by the solar heating conductive film and then is discharged from a filtrate outlet to remove the antibiotic resistance genes.
2. The method for removing the antibiotic resistance gene based on the electrolysis of the solar heat-generating film according to claim 1, wherein in the step (1), the concentration of the dopamine hydrochloride solution is 1-5mg/mL, and the pH value is 8.5.
3. The method for removing antibiotic resistance genes based on solar heat generation film electrolysis according to claim 1, wherein in the step (2), when a pressure deposition mode is adopted, the mass ratio of the photothermal conductive material to the polyvinyl alcohol in the photothermal conductive material-polyvinyl alcohol solution is 1: 2 to 6, the pressure during pressure deposition is 0.1MPa, and the deposition time is 1 h.
4. The method for removing antibiotic resistance genes based on solar heat-generating film electrolysis according to claim 1, wherein in the step (2), when the electrospinning method is adopted, the concentration of the photothermal conductive material-the photothermal conductive material in the polyvinyl alcohol solution is 3 to 6wt%, the distance from the injector to the metal plate is 10cm, the injection rate of the injector is 0.5mL/min, the voltage is 10kV, and the spinning time is 3 hours.
5. The method for removing antibiotic resistance genes based on solar heat-generating film electrolysis according to claim 1, wherein the distance between the solar heat-generating conductive film and the platinum electrode is 3-6 cm.
6. The method for removing antibiotic resistance genes based on solar heat-generating film electrolysis according to claim 1, wherein the voltage of the power supply is 1-3V, and the illumination intensity is 1-3kw/m2
7. The method for removing the antibiotic resistance gene based on the electrolysis of the solar heating film according to claim 1, wherein the sewage is secondary effluent of a sewage treatment plant, aquaculture wastewater, pharmaceutical wastewater or medical wastewater.
CN202010684763.8A 2020-07-16 2020-07-16 Method for removing antibiotic resistance gene based on solar heating film electrolysis Active CN111807477B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010684763.8A CN111807477B (en) 2020-07-16 2020-07-16 Method for removing antibiotic resistance gene based on solar heating film electrolysis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010684763.8A CN111807477B (en) 2020-07-16 2020-07-16 Method for removing antibiotic resistance gene based on solar heating film electrolysis

Publications (2)

Publication Number Publication Date
CN111807477A CN111807477A (en) 2020-10-23
CN111807477B true CN111807477B (en) 2022-06-10

Family

ID=72865383

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010684763.8A Active CN111807477B (en) 2020-07-16 2020-07-16 Method for removing antibiotic resistance gene based on solar heating film electrolysis

Country Status (1)

Country Link
CN (1) CN111807477B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115215410B (en) * 2022-07-18 2024-03-08 山东大学 Method for synchronously removing antibiotics and resistance genes by activating sodium hypochlorite through cerium oxide modified carbon nano tube film

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106000130A (en) * 2016-07-09 2016-10-12 大连理工大学 Method for coupling of PVDF/carbon fiber-based MFe2O4 photocatalysis conductive filtering membrane and MBR/MFC
CN106348396A (en) * 2016-10-27 2017-01-25 环境保护部华南环境科学研究所 Method for deep treatment of antibiotics in drinking water based on multiwalled carbon nanotube modified ultrafiltration membrane
CN106660837A (en) * 2014-10-10 2017-05-10 久瑞高科技私人有限公司 An apparatus for conducting an electro-fenton reaction for decomposing organic chemical compounds
CN110498491A (en) * 2019-08-28 2019-11-26 山东大学 A kind for the treatment of process of electrochemical membrane filtering coupled system degradation antibiotic waste water
CN111185104A (en) * 2020-01-09 2020-05-22 东华大学 Composite forward osmosis membrane and preparation method and application thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004012206A2 (en) * 2002-07-29 2004-02-05 The C & M Group, Llc Mediated electrochemical oxidation used for the destruction of organics contaminated with radioactive materials, dissolution of transuranics, and the decontamination of equipment contaminated with mixed waste
US20160101390A1 (en) * 2014-10-08 2016-04-14 The Johns Hopkins University Modification of membranes with polydopamine and silver nanoparticles formed in situ to mitigate biofouling

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106660837A (en) * 2014-10-10 2017-05-10 久瑞高科技私人有限公司 An apparatus for conducting an electro-fenton reaction for decomposing organic chemical compounds
CN106000130A (en) * 2016-07-09 2016-10-12 大连理工大学 Method for coupling of PVDF/carbon fiber-based MFe2O4 photocatalysis conductive filtering membrane and MBR/MFC
CN106348396A (en) * 2016-10-27 2017-01-25 环境保护部华南环境科学研究所 Method for deep treatment of antibiotics in drinking water based on multiwalled carbon nanotube modified ultrafiltration membrane
CN110498491A (en) * 2019-08-28 2019-11-26 山东大学 A kind for the treatment of process of electrochemical membrane filtering coupled system degradation antibiotic waste water
CN111185104A (en) * 2020-01-09 2020-05-22 东华大学 Composite forward osmosis membrane and preparation method and application thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Investigation of the potential of a membrane bioreactor followed by solar fenton oxidation to remove antibiotic-related microcontaminants;P. Karaolia, et al.;《Chemical Engineering Journal》;20160423;第491-502页 *

Also Published As

Publication number Publication date
CN111807477A (en) 2020-10-23

Similar Documents

Publication Publication Date Title
Deng et al. What will happen when microorganisms “meet” photocatalysts and photocatalysis?
CN206720796U (en) A kind of photoelectrocatalysioxidization oxidization rolling membrane reactor device for water process
CN110980895B (en) Method and device for electro-adsorption and degradation removal of antibiotics from water
CN104003580A (en) System for treatment of wetland-produced electricity from domestic sewage and electrochemical disinfection of wetland effluent
CN109502932B (en) Chlorinated hydrocarbon polluted underground water treatment device and remediation method based on microbial degradation coupled electrochemical method
Pi et al. Electroporation-coupled electrochemical oxidation for rapid and efficient water disinfection with Co3O4 nanowire arrays-modified graphite felt electrodes
CN107138028A (en) A kind of flexible plasma gas purifier
CN107162123A (en) Filtering sterilization method and device and application in a kind of electrode
Lu et al. Recent advances on inactivation of waterborne pathogenic microorganisms by (photo) electrochemical oxidation processes: Design and application strategies
CN111807477B (en) Method for removing antibiotic resistance gene based on solar heating film electrolysis
CN108178423B (en) Cylindrical spiral electrode biomembrane organic sewage and wastewater reaction device
CN115159627A (en) Flowing water driven molybdenum disulfide/carbon felt flexible piezoelectric material, preparation method thereof and application of material to degradation of antibiotics
CN109368767A (en) The method of the electro-active persulfate degrading azoic dye waste water of biology
CN107915380B (en) A kind of technique for treating industrial wastewater and its application
CN103302091A (en) Sequencing-batch polluted soil remediation method and device
WO2012146897A1 (en) An anode and cathode for a microbial fuel cell and a microbial fuel cell incorporating the anode or cathode
CN108751381A (en) The method of Zero-valent Iron reduction coupling microbiological fuel cell degrading azoic dye waste water
CN215667273U (en) Medical sewage disinfection system
CN108178286B (en) Device and method for cooperatively treating sewage and wastewater by three-dimensional electrode biomembrane and photoelectric reoxygenation
CN213141505U (en) Device for environment-friendly disinfection and sterilization of epidemic prevention equipment and public space
CN108675504A (en) A kind of circular water treating system for swimming pool
CN209292133U (en) A kind of combination unit for Wastewater from Organic Chemistry Laboratory processing
CN203408616U (en) Device for adsorbing coupling electrocatalytic oxidation treated benzene-contained waste gas by particle swarm electrodes
CN113651492A (en) In-situ recycling treatment device and method for black water in rural household toilet
CN210163254U (en) Purification treatment device for printing and dyeing sewage

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant