CN114191999A - Biological pollution resistance modification method for water treatment membrane material - Google Patents

Biological pollution resistance modification method for water treatment membrane material Download PDF

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CN114191999A
CN114191999A CN202111311590.6A CN202111311590A CN114191999A CN 114191999 A CN114191999 A CN 114191999A CN 202111311590 A CN202111311590 A CN 202111311590A CN 114191999 A CN114191999 A CN 114191999A
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membrane
water treatment
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modification method
membrane material
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韦静
陈新语
侯冰倩
耿茹
吴智仁
周向同
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Jiangsu University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/08Polysaccharides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/08Polysaccharides
    • B01D71/12Cellulose derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/38Polyalkenylalcohols; Polyalkenylesters; Polyalkenylethers; Polyalkenylaldehydes; Polyalkenylketones; Polyalkenylacetals; Polyalkenylketals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/56Polyamides, e.g. polyester-amides
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/14Membrane materials having negatively charged functional groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/36Hydrophilic membranes

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  • Chemical Kinetics & Catalysis (AREA)
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  • Life Sciences & Earth Sciences (AREA)
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  • Water Supply & Treatment (AREA)
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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention belongs to the technical field of membranes, and discloses a biological pollution resistance modification method for a water treatment membrane material. The quorum sensing inhibitor and the film forming agent are utilized to prepare a modified solution, and then the modified solution containing the quorum sensing inhibitor is uniformly coated on the surface of the film; the film forming agent forms a film on the surface of the film in the constant-temperature drying process, so that the quorum sensing inhibitor is fixed on the film. The modified membrane can inhibit the aggregation growth of bacteria on the surface of the membrane and the formation of a biological membrane, simultaneously maintain the water permeability, the hydrophilicity and the surface negative charge of the membrane, reduce biological pollution and improve the water treatment efficiency.

Description

Biological pollution resistance modification method for water treatment membrane material
Technical Field
The invention belongs to the technical field of membranes, and particularly relates to a biological pollution resistance modification method for a water treatment membrane material.
Background
The market share of membrane separation technology in the field of water treatment is rapidly increasing, and the membrane separation technology becomes a strategic technology for solving water pollution and water resource shortage. The membrane pollution is one of the main bottleneck problems restricting the application of the membrane water treatment technology, in particular to the membrane surface deposition and the membrane pore blockage caused by microorganisms and metabolites thereof, so that the water permeability and the separation characteristic of the membrane are irreversibly changed, the water yield and the effluent quality are reduced, the energy consumption is increased, and even the service life of the membrane is shortened. Research and development of anti-pollution membrane materials are the key to controlling membrane pollution. The preparation and modification of membrane materials based on biological methods are the leading directions of membrane material research. During the process of adhering and colonizing free bacteria to the membrane surface, various autoinducers can be generated and secreted extracellularly as signal molecules for the information transmission between species and species. When the density of the bacteria reaches a certain level and the concentration of the signal molecules reaches a threshold value, the bacteria can start the expression of density-dependent specific genes and regulate the physiological characteristics of the population, such as biofilm formation and the like, and the phenomenon is called quorum sensing of the bacteria. Quorum sensing systems have been found in a variety of gram-negative and positive bacteria. Quorum sensing has a significant impact on bacterial colonization, as well as on the maturation, morphology, disintegration, and chemical resistance of biofilms. The technology is a new method for controlling membrane pollution by interfering the quorum sensing path of bacteria and regulating the formation of a biological membrane of the bacteria through the ways of inhibiting the generation and degradation of signal molecules, preventing the combination of the signal molecules and receptor proteins and the like, thereby achieving the purpose of preventing or controlling biological pollution. In recent years, a number of novel quorum sensing inhibitors have been discovered. At present, the quorum sensing inhibitor is mainly applied to membrane biological pollution control by adding a free or carrier immobilized inhibitor into a membrane filtration system, and the long-acting property and the application cost of the regulation and control effect are difficult to control. And the modification of the membrane material based on the quorum sensing inhibitor has great stability and application potential in biological pollution control.
Disclosure of Invention
Aiming at the technical problem of difficult control of biological pollution of a water treatment membrane, the invention provides a method for modifying the pollution resistance of a membrane material.
The present invention achieves the above-described object by the following technical means.
A water treatment membrane material biological pollution resistance modification method comprises the following steps:
(1) adding a certain amount of film forming agent into a solvent, heating and stirring at a constant temperature to prepare a film forming agent solution;
(2) adding the quorum sensing inhibitor into the film forming agent solution according to a certain proportion, heating and stirring at a constant temperature to uniformly disperse the inhibitor in the solution, and preparing to obtain a modified solution;
(3) uniformly coating the modified solution containing the quorum sensing inhibitor on the surface of the membrane;
(4) and (3) drying the film with the coated surface in a constant-temperature heating device, wherein the film forming agent forms a film in the drying process and is adhered to the surface of the film, so that the modifier is fixed on the film.
In the step (1), the film-forming agent is one of sodium alginate, chitosan, polyvinyl alcohol, polydopamine, cellulose derivatives or polyacrylamide, and in the film-forming agent solution, the mass percentage concentration of the film-forming agent is 0.01-10.0%, preferably 0.1-1.0%;
in the step (1), the solvent is one of water, dilute acid solution or dilute alkali solution, and the pH value is 3-11.
In the step (2), the quorum sensing inhibitor is one of curcumin, carvacrol, vanillin, furocoumarin, resveratrol, quercetin, naringenin, or furanone compounds and modified homoserine lactone compounds, and preferably an inhibitor which is non-toxic to human bodies and environments;
in the step (2), the mass percentage concentration of the quorum sensing inhibitor in the modified solution is 0.01-5.0%, and the preferred mass percentage concentration is 0.1-1.0%;
in the step (2), the heating temperature is 30-80 ℃, preferably 30-60 ℃; the heating time is 10min-24h, preferably 10min-6 h.
In the step (3), the membrane comprises one of a microfiltration membrane, an ultrafiltration membrane, a nanofiltration membrane or a reverse osmosis membrane;
in the step (3), the coating thickness of the modification solution is 0.01-5.0mm, and the preferable thickness is 0.05-1.0 mm;
in the step (4), the drying temperature is 30 to 80 ℃, preferably 40 to 60 ℃.
The invention has the beneficial effects that:
the modification method of the membrane material disclosed by the invention enables the water treatment membrane material to have better surface characteristics (such as hydrophilicity, surface negative charge and the like), and the quorum sensing inhibitor can interfere signal transmission among bacteria, regulate and control the expression of quorum density-dependent physiological characteristics such as extracellular polymer synthesis, biofilm formation and the like, so that the bacteria are difficult to attach to the membrane surface, the form and disintegration and diffusion of the biofilm are influenced, the biological pollution resistance of the membrane material is improved, and the reduction of water treatment efficiency caused by biological pollution is reduced. The invention carries out the modification of the membrane material based on quorum sensing, provides a new idea for controlling the membrane biological pollution, and can be used for solving the membrane pollution problem in the field of membrane water treatment. The method has the advantages of simple operation, strong applicability, no adverse effect of the used materials on human bodies, organisms and environment, and the like, and is suitable for industrial production application.
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FIG. 1 is a graph showing bacteriostatic effects of the inhibitors of examples 1 and 2, wherein (a) is LB plate medium; (b) LB plate culture medium for inoculating colibacillus; (c) inoculating escherichia coli, and adding an LB plate culture medium with vanillin of which the mass fraction is 0.1%; (d) inoculating escherichia coli, and adding an LB plate culture medium with vanillin of which the mass fraction is 0.3%; (e) inoculating escherichia coli, and adding an LB plate culture medium with vanillin of which the mass fraction is 0.5%. The medium was incubated at 37 ℃ for 48 hours and then observed.
FIG. 2 is a surface microtopography of the membrane before and after modification in example 1, wherein (a) is an unmodified ultrafiltration membrane; (b) the modified ultrafiltration membrane is obtained.
FIG. 3 is a surface microtopography of the membrane before and after modification in example 2, wherein (a) is an unmodified reverse osmosis membrane; (b) is a modified reverse osmosis membrane.
FIG. 4 is a graph showing membrane separation performance before and after modification in examples 1 and 2, wherein (a) is water permeability of an ultrafiltration membrane before and after modification; (b) the water permeability and salt rejection of the reverse osmosis membrane before and after modification.
FIG. 5 is the E.coli adsorption kinetics of the membrane surface before and after modification in example 1, wherein (a) (c) (e) (g) are surface SEM images of unmodified ultrafiltration membrane after culturing for 4h, 8h, 12h and 24h with E.coli; (b) and (d) (f) (h) are surface SEM pictures of the modified ultrafiltration membrane after being cultured for 4h, 8h, 12h and 24h with Escherichia coli respectively.
FIG. 6 is the E.coli adsorption kinetics before and after modification of the membrane surface in example 2, wherein (a) (c) (e) (g) are surface SEM images of an unmodified reverse osmosis membrane and E.coli after 4h, 8h, 12h and 24h of culture, respectively; (b) and (d) (f) (h) are surface SEM images of the modified reverse osmosis membrane and the Escherichia coli after being cultured for 4h, 8h, 12h and 24h respectively.
FIG. 7 is an SEM image of the membrane surface after the membrane filtration experiment in example 1, wherein (a) is the surface biofouling of the unmodified ultrafiltration membrane; (b) the biological pollution condition on the surface of the modified ultrafiltration membrane is shown.
Detailed Description
The invention will be further described with reference to the following figures and specific examples, but the scope of the invention is not limited thereto.
Example 1
(1) Preparing 0.2 percent (mass fraction) of dilute acetic acid aqueous solution, adding chitosan into the dilute acetic acid solution, heating at constant temperature (30 ℃) and stirring to prepare 0.1 percent of chitosan solution;
(2) adding vanillin into chitosan solution, heating at constant temperature (30 deg.C), stirring, and making into 0.1% vanillin solution;
(3) uniformly coating the vanillin solution on the surface of an ultrafiltration membrane (UF), wherein the thickness of the solution coating is 60 mu m;
(4) and (3) drying the membrane subjected to surface coating in a 40 ℃ oven at constant temperature, wherein a coating layer forms a thin film in the drying process, and a modifier is fixed on the surface of the membrane to prepare the stable modified ultrafiltration membrane (UF-CV 1).
Example 2
(1) Preparing 0.2 percent (mass fraction) of dilute acetic acid aqueous solution, adding chitosan into the dilute acetic acid solution, heating at constant temperature (30 ℃) and stirring to prepare 0.1 percent of chitosan solution;
(2) adding vanillin into chitosan solution, heating at constant temperature (30 deg.C), stirring, and making into 0.1% vanillin solution;
(3) uniformly coating the vanillin solution on the surface of a reverse osmosis membrane (RO), wherein the thickness of the coating of the solution is 60 mu m;
(4) and (3) drying the membrane with the coated surface in a 40 ℃ oven at constant temperature, forming a film by the coating in the drying process, and fixing a modifier on the surface of the membrane to obtain the stable modified reverse osmosis membrane (RO-CV 1).
Analysis of bacteriostatic Properties of modifier
The plate culture method was used to culture escherichia coli cells (OD600 ═ 0.5) in the following ratio of 1: 50, then adding a certain amount of vanillin, uniformly mixing to prepare a culture medium containing 0.1%, 0.3% and 0.5% (mass fraction) of vanillin, pouring the obtained semisolid culture medium into a culture dish, and culturing at constant temperature (37 ℃) for 48 hours, wherein the result is shown in figure 1. As can be seen in fig. 1, a large number of colonies appeared on the medium inoculated with escherichia coli (fig. 1(b)) compared to the blank medium (fig. 1(a)), growth of escherichia coli was inhibited on the medium added with vanillin (fig. 1(c) - (e)), and no colonies of escherichia coli were observed on the plates added with 0.3% and 0.5% of vanillin, indicating that vanillin had a significant inhibitory effect on bacterial growth.
Characterization of film surface characteristics
The micro-morphologies of the surfaces of the ultrafiltration membrane and the reverse osmosis membrane before and after modification in examples 1 and 2 were analyzed, and the SEM observation results are shown in fig. 2 and 3. As can be seen in FIG. 2, the vanillin/chitosan modified coating had no significant effect on the surface roughness of the ultrafiltration membrane UF-CV1, and the pore structure became denser. FIG. 3 shows that the surface appearance of the reverse osmosis membrane (RO-CV1) is smoother after the reverse osmosis membrane is coated by the vanillin/chitosan solution.
The hydrophilicity and surface potential of the unmodified ultrafiltration membrane UF and the modified ultrafiltration membrane UF-CV1 were analyzed, and the results are shown in Table 1. As can be seen from Table 1, the modified membrane surface still has good hydrophilicity, and zeta potential maintains electronegativity, so that microorganisms are difficult to attach to the membrane surface, and the anti-biological pollution capability of the membrane is improved.
TABLE 1 contact angle and surface potential of ultrafiltration membrane before and after modification
Figure BDA0003342130950000041
Analysis of Membrane separation Performance
The separation performance of the ultrafiltration membrane and the reverse osmosis membrane before and after modification in examples 1 and 2 was analyzed. The ultrafiltration membrane of example 1 was tested for water permeability using pure water as feed water at 25 ℃ and a transmembrane pressure difference of 1bar, and the results are shown in FIG. 4 (a). As can be seen from fig. 4(a), the water permeability of the modified ultrafiltration membrane is reduced, but still remains within the applicable range of practical operation. The reverse osmosis membrane related to the embodiment 2 adopts pure water as inlet water, and the water permeability is tested at 25 ℃ and 10bar of transmembrane pressure difference; the salt cut-off was measured at 25 ℃ and a transmembrane pressure difference of 10bar using a NaCl solution as the feed water, and the results are shown in FIG. 4 (b). As can be seen in FIG. 4(b), the reverse osmosis membrane still maintains high water permeability and salt rejection after modification.
Analysis of Membrane for anti-biofouling Performance
The modified membrane materials prepared in examples 1 and 2 were analyzed for their antibacterial adsorption properties. The unmodified and modified membrane samples were placed in well plates, 3ml LB medium and 50. mu.L Escherichia coli liquid were added to each well, and the mixture was cultured in a shaker (37 ℃ C., 100r/min) at constant temperature. After culturing for 4h, 8h, 12h and 24h, the membrane samples were taken out from the well plate, subjected to bacterial immobilization and observed on the surface of the membrane for bacterial adsorption by SEM, and the results are shown in FIGS. 5 and 6. As can be seen from FIGS. 5 and 6, the bacterial adsorption on the surfaces of the ultrafiltration membrane UF-CV1 and the reverse osmosis membrane RO-CV1 after modification is reduced, and the growth of flora is obviously slowed down. Dense biological membranes are quickly formed on the surfaces of the unmodified ultrafiltration membrane UF and the reverse osmosis membrane RO, and the biological membranes on the surfaces of the UF-CV1 and the RO-CV1 are slow in forming and sparse in shape. Examples 1 and 2 the membrane materials prepared by coating with the modified solution containing quorum sensing inhibitor have good antibacterial adsorption performance.
The modified ultrafiltration membrane prepared in example 1 was evaluated for anti-biofouling performance in water treatment applications. The simulated secondary effluent inoculated with escherichia coli was used as influent and membrane filtration experiments were performed at 25 ℃ and 1bar transmembrane pressure differential. After running for 8h, a membrane sample is taken out, and the morphology of the biological membrane on the surface of the membrane is observed by adopting SEM (scanning electron microscope), and the result is shown in FIG. 7. FIG. 7 shows that the unmodified membrane surface is completely covered by accumulated flora and extracellular polymeric substances, and a dense biofilm is formed; the biomass on the surface of the modified membrane is obviously reduced, and the biological membrane is sparse and easy to peel off.
The embodiment of the invention provides a novel water treatment membrane modification method, which adopts a modifier prepared from a quorum sensing inhibitor to inhibit the adsorption growth of bacteria on the membrane surface and the formation of a biological membrane, improves the biological pollution resistance of the membrane material, and provides an environment-friendly new way for reducing the biological pollution in the application of membrane water treatment.
The present invention is not limited to the above-described embodiments, and any obvious improvements, substitutions or modifications can be made by those skilled in the art without departing from the spirit of the present invention.

Claims (10)

1. A modification method for resisting biological pollution of a water treatment membrane material is characterized by comprising the following steps:
(1) adding a certain amount of film forming agent into a solvent, heating and stirring at a constant temperature to prepare a film forming agent solution;
(2) adding the quorum sensing inhibitor into the film forming agent solution according to a certain proportion, heating and stirring at a constant temperature to uniformly disperse the inhibitor in the solution, and preparing to obtain a modified solution;
(3) uniformly coating the modified solution containing the quorum sensing inhibitor on the surface of the membrane;
(4) and (3) drying the film with the coated surface in a constant-temperature heating device, wherein the film forming agent forms a film in the drying process and is adhered to the surface of the film, so that the modifier is fixed on the film.
2. The water treatment membrane material anti-biological pollution modification method as claimed in claim 1, wherein in the step (1), the film forming agent is one of sodium alginate, chitosan, polyvinyl alcohol, polydopamine, cellulose derivative or polyacrylamide; the solvent is one of water, dilute acid solution or dilute alkali solution, and the pH value is 3-11; in the film forming agent solution, the mass percentage concentration of the film forming agent is 0.01-10.0%.
3. The water treatment membrane material anti-biological pollution modification method as claimed in claim 2, wherein the mass percentage concentration of the film forming agent in the film forming agent solution is 0.1-1.0%.
4. The water treatment membrane material anti-biological pollution modification method as claimed in claim 1, wherein in the step (2), the quorum sensing inhibitor is one of curcumin, carvacrol, vanillin, furocoumarin, resveratrol, quercetin, naringenin, or furanone type compound, and modified homoserine lactone type compound, and the quorum sensing inhibitor is present in the modification solution at a concentration of 0.01-5.0% by mass.
5. The water treatment membrane material anti-biological contamination modification method as claimed in claim 4, wherein the mass percentage concentration of the quorum sensing inhibitor in the modification solution is 0.1-1.0%.
6. The water treatment membrane material anti-biological pollution modification method as claimed in claim 1, wherein, in the step (2), the heating temperature is 30-80 ℃; the heating time is 10min-24 h.
7. The water treatment membrane material anti-biological contamination modification method as claimed in claim 1, wherein in the step (3), the membrane comprises one of a microfiltration membrane, an ultrafiltration membrane, a nanofiltration membrane or a reverse osmosis membrane; the coating thickness of the modifying solution is 0.01-5.0 mm.
8. The water treatment membrane material anti-biofouling modification method of claim 7, wherein the modification solution is applied at a thickness of 0.05-1.0 mm.
9. The water treatment membrane material anti-biological contamination modification method as claimed in claim 1, wherein in the step (4), the drying temperature is 30-80 ℃.
10. The water treatment membrane material anti-biological contamination modification method as claimed in claim 9, wherein in the step (4), the drying temperature is 40-60 ℃.
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