CN1745886A - Titanium dioxide nanometer pipe composite separating membrane, its preparation and use thereof - Google Patents
Titanium dioxide nanometer pipe composite separating membrane, its preparation and use thereof Download PDFInfo
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- CN1745886A CN1745886A CN 200510046986 CN200510046986A CN1745886A CN 1745886 A CN1745886 A CN 1745886A CN 200510046986 CN200510046986 CN 200510046986 CN 200510046986 A CN200510046986 A CN 200510046986A CN 1745886 A CN1745886 A CN 1745886A
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Abstract
A composite separating membrane with TiO2 nano-tubes for treating the organic sewage is prepared through providing inorganic Al2O3 membrane, preparing the high-density through nanoholes on it to obtain carrier, washing, baking at 50-100 Deg C., preparing TiO2 sol at 15-20 Deg C., ultrasonic dispersing, immersing said Al2O3 membrane in it, drying, calcining and cooling.
Description
Technical field
The present invention relates to use Al
2O
3As titanium dioxide nanometer pipe composite separating membrane of carrier and template and its production and application, particularly pass through the preparation of this composite separating film, photocatalysis is separated two unit operations that are mutually independent merge into a unit operations with film, make its function, belong to the environmental pollution treatment technology field with photocatalysis-isolation integral.
Background technology
The development of inoranic membrane starts from 1940's, has experienced three phases so far: first stage starts from Manhattan plan in World War II, is mainly used in the separation and concentration of uranium isotope; Second stage starts from the eighties, and inoranic membrane enters industrial application, develops industrial inorganic micro filtering membrane and inorganic milipore filter and assembly thereof in succession, replaces polymeric membrane; Three phases enters the nineties, and the development of inoranic membrane has entered a new stage, and new membrane material, new masking technique are developed day by day.
The inoranic membrane research of China starts from the end of the eighties, under the support of state natural sciences fund and each ministries and commissions, units such as Nanjing University of Chemical Technology, Dalian Chemiclophysics Inst., Chinese Academy of Sciences, China Science ﹠ Technology University, South China Science ﹠ Engineering University have systematically begun the preparation of inorganic application study.
Compare with organic film, inoranic membrane has following character:
(1) high temperature resistant: the serviceability temperature of inoranic membrane can be higher than 400 ℃, even can reach 800 ℃, therefore is particularly suitable for the direct separation of high-temperature operation product or artificially improves temperature, to be used for the separation of high viscosity fluid; Directly high-temperature steam cleaning and sterilization when being used for food and bioengineering field.
(2) chemical stability is good: inoranic membrane energy acid and alkali-resistance, organic solvent-resistant are applicable to the pH scope of broad, so can use in strong corrosive media, and can adopt chemical reagent to clean; Inoranic membrane can be used for the separation of non-aqueous solution system in addition.
(3) mechanical strength height: particularly diffusion barrier is generally with the form preparation of carrier film for inoranic membrane, and therefore its mechanical strength can be used under elevated pressures far above organic film, and membrane module and membrane micropore can not produce distortion and damage; Can also the high pressure recoil regenerate.
(4) anti-microbe ability is strong: generally do not have an effect with microorganism, itself is nontoxic, does not pollute separated system, therefore is used for food, there is special advantages in biochemical field.
(5) inoranic membrane also has advantages such as pore size distribution range is narrower.
The weak point of inoranic membrane is that its cost is higher, and the filling area is less, and operating cost is higher, and film is seriously polluted, only plays the effect of separation etc.
Since the Fujishima of Japan finds TiO
2Monocrystalline electrode light decomposition water has greatly promoted developing rapidly of multiphase photocatalysis research.1976, J.H.Cary reported TiO
2Water suspension can make the Polychlorinated biphenyls dechlorination under the irradiation of black light, thereby has opened up TiO
2Photocatalysis oxidation technique is in the application prospect in environmental protection field.The basic principle of photocatalysis to degrade organic matter be semiconductor catalyst under the irradiation of ultraviolet light, the electronics on its valence band is excited on the conduction band, forms electron-hole pair, thereby has strong redox ability.This electron-hole pair can with organic matter generation redox reaction, also can generate and have highly active hydroxyl radical free radical with on every side oxygen, hydrogen peroxide or water effect (OH, this free radical carries out oxidation reaction with organic matter again, until organic matter by mineralising.Heavy metal ion in some solution also can be reduced recovery by this method.This method treatment effeciency is higher, oxidant utilization ratio height, selectivity is good and do not bring other impurity in processing procedure into.And this method is difficult to industrialized subject matter and is: (1) catalyst granules is easy to run off with treatment fluid, is difficult to recycle; (2) because TiO
2Be wide bandgap semiconductor, energy gap is 3.2eV, needs the illumination of higher-energy to penetrate can to excite to produce photic electronics and hole.Therefore, the efficient of catalyst is generally lower, is still waiting to improve; (3) design of photo catalysis reactor has directly influenced the absorption of photochemical catalyst to photon, and then has influenced the height of photocatalysis efficiency.Therefore, the design of photo catalysis reactor haves much room for improvement.
Based on the pluses and minuses of inoranic membrane and photochemical catalyst, prepare and a kind of the collection separate the inorganic photocatalysis membrana reactor combine with photocatalysis and become possibility.This inoranic membrane may be played the part of important role in film separation in the future, photocatalysis and light compositing reaction.The inoranic membrane catalytic reaction that inoranic membrane is combined with catalytic reaction process and constitute is considered to one of the three great development directions in catalysis subject future.Compare traditional reaction, membrane catalytic reaction improves equilibrium conversion efficient by part or all that remove product with the restriction of breaking chemical reaction equilibrium, perhaps changes the selection that reaction path increases target product by the film diffusion.Diffusion barrier mainly contains following dual mode with combining of light-catalyzed reaction:
(1) film is a resolution element of reaction zone.At this moment film has only separation function, by selectively the some or all of of product being shifted out the restriction of breaking chemical balance from reaction zone, improves the reaction rate of irreversible reaction, and the conversion ratio of reversible reaction is improved.Like this, not only solved the losing issue of catalyst, and catalyst granules (especially ultra-fine grain catalyst) can be suspended in the solution, surface area can be fully used, and reaction time also is easier to control.
(2) to have photocatalytic activity, film itself be that catalyst or film are to handle with catalytic active substance and have catalysis to film.As with semiconductor catalyst (TiO
2) directly as the form existence of film, make it have the performance of separation and catalysis simultaneously, importing light into then in the membrane reactor, the inner tubal wall of film surface and fenestra is the place that reaction takes place.This kind method is fixed up the form of catalyst with film, has solved the problem that runs off, the pollution that has also alleviated film simultaneously.
At present, research to first kind of combination is comparatively general, but this mode is still separated the process that is mutually independent as two with photocatalysis with film, not only improved the operating cost of practical operation, and photochemical catalyst runs off easily and diffusion barrier pollutes easily.To the research of this combination, typical example:
(1) people such as Soo-Ah Lee is at Ind.Eng.Chem.Res.2001, and 40, the article of delivering on the 1712-1719: " use milipore filter to separate the TiO that reclaims in the drinking water treatment
2Photochemical catalyst " (Use of UltrafiltrationMembranes for the Separation of TiO
2Photocatalysts in Drinking Water Treatment) in the literary composition, its:
(1) scheme
Use the P-25 TiO that German Degussa company produces
2Powder photocatalyst, in the photo catalysis reactor of design voluntarily, the organic matter in the photocatalytic degradation drinking water is as humic acid etc.; After reaction finishes, use the cellulose-acetafolic that Britain Millipore company produces, separate, reclaim P-25 TiO
2Powder photocatalyst.
(2) advantage
Photocatalysis, film are separated two kinds of technology combine, be used for the organic matter of Drinking Water, as humic acid etc.
(3) shortcoming of Cun Zaiing
1. photocatalysis separates with film and remains separately independently unit;
2.TiO
2Powder is used for photocatalytic degradation drinking water organic matter, and diffusion barrier is used for TiO as unit independently in addition
2The recovery of powder photocatalyst, in this process, diffusion barrier does not produce effect to organic removal in the drinking water, the effect of only play separation, reclaiming catalyst;
3. because TiO
2Powder is thinner, causes diffusion barrier seriously polluted, and membrane flux descends rapidly;
4.TiO
2Powder photocatalyst runs off easily.
(2) people such as R.Molinari is at Catalysis Today.2000,55, in the article of delivering on the 71-78 " application study of photocatalysis membrana reactor in desalt " (the Study on a photocatalytic membrane reactor forwater purification) literary composition, its:
(1) scheme
Use a series of organic polymer milipore filters, the P-25 TiO that German Degussa company is produced
2Powder photocatalyst by the mode of ultrafiltration, separates, is fixed on the surface of polymer film; At this moment, polymer film plays TiO
2The effect of powder photocatalytic agent carrier is applied to contain in the wastewater treatment of 4-nitrophenols then, and under the condition that constantly blasts purity oxygen, through 5 hours UV-irradiation, the 4-nitrophenols almost completely was degraded.
(2) advantage
Photocatalysis technology and membrane separation technique are combined, handle organic matter in the water.
(3) shortcoming of Cun Zaiing
1. the mode by ultrafiltration is with TiO
2Powder separates, is fixed on the surface of diffusion barrier, is used for photocatalytic degradation water organic matter then, and at this moment, diffusion barrier only plays the effect of catalyst support, and is inoperative to organic removal;
2. by the fixing TiO of such mode
2Powder, surperficial insecure at film runs off easily;
3. use organic separation membrane in the literary composition as TiO
2The supporter of powder, through long-time UV-irradiation, diffusion barrier all has slight damage.
Summary of the invention
Purpose of the present invention and task overcome prior art and exist: (1) powder titanium dioxide is suspended in the pollutant solution as photochemical catalyst, needs the stirring that continues.After reaction was finished, photochemical catalyst reclaimed relatively difficulty, and it is more serious to run off; (2) combination that separates with film of photocatalysis is that two processes mechanically are together in series with separate unit operations form, the deficiency of complex process, and provide a kind of at Al
2O
3Prepare titanium dioxide nanometer pipe composite separating membrane on the inorganic diaphragm carrier, be applied in the separation and photocatalytic degradation of organic pollution, the special technical solution that proposes titanium dioxide nanometer pipe composite separating membrane of the present invention and its production and application.
Basic design of the present invention is that foundation is with porous Al
2O
3Inorganic diaphragm is used sol-gel technique as carrier, by the control dip time, makes the titanium dioxide nanometer pipe composite separating membrane in different apertures.This composite separating film has big specific area and stronger adsorption capacity, helps to improve the photocatalysis performance of titanium dioxide.This titanium dioxide nanometer pipe composite separating membrane can be realized the function that photocatalysis separates with film simultaneously, can solve the loss of photochemical catalyst on the one hand and reclaim difficult problem; On the other hand photocatalysis is separated two unit operations that are mutually independent with film,, merge into a unit operations by titanium dioxide nanometer pipe composite separating membrane; Once more, titanium dioxide and Al
2O
3The composite separating film that inorganic diaphragm constitutes together, contrast organic separation membrane carrier, not fragile in photocatalysis and film separation process, good stability is arranged; At last, composite separating film is applied in the organic pollutant wastewater processing, and not only photocatalysis has the catalytic degradation effect to organic pollution, and the film separation also has certain removal effect to pollutant.
Titanium dioxide nanometer pipe composite separating membrane proposed by the invention, it is characterized in that: titanium dioxide nanometer pipe composite separating membrane is to be 25-47mm with the diameter, thickness is 50-60 μ m, porosity is 25-50%, gathering at its thickness direction of face upper edge is processed with the through hole that the aperture is 20-200nm, and its pitch of holes is the Al of 20-150nm
2O
3Inorganic diaphragm is as carrier; By sol-gel technique, carrier diaphragm [3] is through dipping, dry, roasting, and caliber is 5-130nm in making in the duct of carrier, and pipe range is the titania nanotube of 45-60 μ m, with Al
2O
3Diaphragm constitutes titanium dioxide nanometer pipe composite separating membrane together; This titanium dioxide nanometer pipe composite separating membrane diameter is 25-47mm, and specific area is 20-50m
2/ g, porosity is 20-40%, and aperture [1] is 5-130nm, and the spacing between the Kong Yukong is 20-150nm, and thickness is 50-60 μ m.
The preparation method of titanium dioxide nanometer pipe composite separating membrane is characterized in that, the method step of preparation is as follows:
The first step, the preliminary treatment of carrier
With Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 10-20min, uses acetone, washed with de-ionized water 10-20min again, with after the 50-100 ℃ of following drying, is cooled to room temperature in baking oven, and is standby;
Second step, the preparation of TiO 2 sol
With the volume ratio is V
Butyl titanate: V
Absolute ethyl alcohol=1: 5 ratio is added to butyl titanate in the absolute ethyl alcohol, magnetic agitation 10-30min in ice-water bath, and slowly dripping volume ratio then is V
Ethanol: V
Glacial acetic acid: V
Water=50: the mixed solution of 3: 1 absolute ethyl alcohol, glacial acetic acid and water, its temperature should be controlled at 15-20 ℃, and ultrasonic again dispersion 10-20min obtains transparent TiO
2Colloidal sol.
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses this TiO
2In the colloidal sol, treat to take out behind the 10-50min, at first, at air drying 1-2h, then, the speed with 100 ℃/h in Muffle furnace is warming up to 400 ℃-500 ℃, and insulation 4-6h is last, reduces to room temperature with the speed of 50 ℃/h, and is standby.
Use titanium dioxide nanometer pipe composite separating membrane proposed by the invention to handle the application of organic pollutant wastewater, it is characterized in that:
Organic pollutant wastewater is cycled through composite separating film, at room temperature, when light source irradiation that wavelength and semiconductor band gap are complementary, titanium dioxide is activated, on the basis that produces photohole-duplet, organic matter generation redox reaction continues bubbling air in the course of reaction, make O in the solution on the one hand
2Concentration remains saturation state; Agitating solution makes it even on the other hand; Simultaneously, the pressure reduction that is produced by vavuum pump provides separation process needed driving force, and pressure differential range is 0.02-0.1MPa; Use titanium dioxide nanometer pipe composite separating membrane and handle organic pollutant wastewater, under the acting in conjunction that light source shines with film separates that wavelength and semiconductor band gap are complementary, after 4-6 hour, obtaining has higher removal efficient than simple film separation and simple photocatalysis, can reach 80-96%.
Of the present invention being further characterized in that, titanium dioxide nanometer pipe composite separating membrane is handled the application of organic pollutant wastewater, and its organic pollutant wastewater has: dyestuff, surfactant-based, pesticide, classes of herbicides, hydro carbons, polychlorinated biphenyl, adhesive class; The suitable concentration of handling organic pollutant wastewater should be less than 500mg/L.
The preparation method of titanium dioxide nanometer pipe composite separating membrane provided by the present invention works as Al
2O
3The time that diaphragm floods in TiO 2 sol more in short-term, prepared titanium dioxide nanometer pipe composite separating membrane have bigger aperture and the titania nanotube pipe range that obtained shorter, when handling organic pollution, it is relatively low to obtain rejection; When the time of carrier impregnation was longer, the aperture of the titanium dioxide nanometer pipe composite separating membrane of formation was less, and the nanotube pipe range of acquisition is longer, and therefore, the composite separating film that makes has bigger specific area and photocatalytic activity.
The application technology of titanium dioxide nanometer pipe composite separating membrane provided by the present invention, when organic pollution concentration is higher, use the titanium dioxide nanometer pipe composite separating membrane that long-time dipping obtains, under certain pressure reduction, separate and photocatalytic degradation by film, can obtain higher organic pollutant removal efficient; On the other hand, separate by film, the small-molecule substance that photocatalytic degradation is produced enters into filtered solution, thereby has broken the balance of original chemical reaction, and light-catalyzed reaction is had facilitation.
Titanium dioxide nanometer pipe composite separating membrane provided by the present invention, in organic pollutant wastewater is handled, can carry out the function that photocatalysis or film separate individually, but, by the composite separating film of sol-gel technology preparing, in preparation process, by the control dip time, we can obtain different apertures, porosity, the titanium dioxide nanometer pipe composite separating membrane of specific area and pitch of holes; Except the control dip time, because some objective factors and artificial factor make to rely on Al
2O
3The interior caliber of the titania nanotube that the duct of inorganic diaphragm forms, pipe ranges etc. are not uniform; According to the difference of used carrier size, thickness, can obtain the composite separating film of different-diameter and thickness; In the preparation process, Al
2O
3The cleaning of carrier, the length of drying time can influence the quality of composite separating film, TiO
2The temperature of the mixing time of colloidal sol, ultrasonic jitter time and preparation has directly determined the character of colloidal sol and the quality of composite separating film, the drying time of composite separating film, sintering temperature and temperature retention time have significant effects to the formation of composite separating film inside titania nanotube; Composite separating film is in application, and different pressure reduction can influence its separating effect to organic pollution in the waste water.In view of above experiment conditions, objective factor and artificial factor, therefore, some parameters of titanium dioxide nanometer pipe composite separating membrane provided by the present invention and preparation thereof and application are the value range that statistical mathematics is calculated.
Titanium dioxide nanometer pipe composite separating membrane provided by the present invention should be noted that when organic pollutant wastewater handle to be used because the thickness of composite separating film is less, intensity a little less than, in corresponding membrane module, must increase the supporter of composite separating film; In addition, when operation pressure reduction surpasses 1.0MPa, can destroy the structure of composite separating film, during application, operation pressure reduction should be less than 1.0MPa.
Major advantage of the present invention is:
(1), realized that on same unit photocatalysis separates two kinds of operations with film by the preparation of titanium dioxide nanometer pipe composite separating membrane; This composite separating film not only has the effect that film separates, and has light-catalysed ability; Can alleviate the pollution of film itself by photocatalytic process; The film separation process of carrying out has simultaneously also promoted light-catalyzed reaction to carry out;
(2) technology simply, does not need expensive equipment, both can be used for experimental implementation, again can industrial large-scale production, and preparation process only needs carrier impregnation is taken out behind the certain hour in the TiO 2 sol, gets final product after dry then, the calcining;
(3), can prepare the titanium dioxide nanometer pipe composite separating membrane of respective aperture according to the size of handled organic pollutant molecule size.This composite separating film specific area is big, and high adsorption capacity has the function of photocatalysis-isolation integral.Simultaneously, the loss and the difficult problem of recovery of titanium dioxide optical catalyst have been solved.
The subordinate list explanation
The present invention is provided with 6 subordinate lists altogether, now is respectively described below:
Table 1 is that titanium dioxide nanometer pipe composite separating membrane is used to handle and contains each parameter values table that Polychlorinated biphenyls waste water is adopted
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 1 is 20mg/L, and wastewater flow rate is the Polychlorinated biphenyls solution of 1L, and after 4 hours, its treatment effeciency reaches 96%, exceeds independent separation and independent photocatalysis 28-15%.
Table 2 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that agricultural chemicals waste water adopts
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 3 is 50mg/L, and wastewater flow rate is the agricultural chemicals Atrazine of 1L, and after 5 hours, its treatment effeciency reaches 95%, exceeds independent separation and independent photocatalysis 32-15%.
Table 3 is that titanium dioxide nanometer pipe composite separating membrane is used for each parameter values table that surfactant waste water adopts
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 4 is 50mg/L, and wastewater flow rate is the neopelex of 1L, reacts after 4 hours, and its treatment effeciency reaches 89%, exceeds independent separation and independent photocatalysis 28-13%.
Table 4 is that titanium dioxide nanometer pipe composite separating membrane is used for each parameter values table that dye wastewater treatment using adopts
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 3 is 500mg/L, and wastewater flow rate is that the dyestuff of 1L directly deceives 168, reacts after 5 hours, and its treatment effeciency reaches 80%, exceeds independent separation and independent photocatalysis 16-13%.
Table 5 is that titanium dioxide nanometer pipe composite separating membrane is used for each parameter values table that dye wastewater treatment using adopts
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 3 is 300mg/L, and wastewater flow rate is that the dyestuff of 1L directly deceives 168, reacts after 5 hours, and its treatment effeciency reaches 85%, exceeds independent separation and independent photocatalysis 20-12%.
Table 6 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that dyestuff Acid Orange II waste water is adopted
Titanium dioxide nanometer pipe composite separating membrane concentration of treatment in the Application Example 3 is 100mg/L, and wastewater flow rate is the dyestuff Acid Orange II of 1L, reacts after 4 hours, and its treatment effeciency reaches 86%, exceeds independent separation and independent photocatalysis 29-14%.
Description of drawings
The present invention is provided with 3 width of cloth accompanying drawings altogether, now is respectively described below:
Fig. 1 is the ESEM front view (SEM) of titanium dioxide nanometer pipe composite separating membrane
The sem photograph of titanium dioxide nanometer pipe composite separating membrane of the present invention is to adopt the JSM-5600LV ESEM, is 12kV at accelerating potential, and under the condition that multiplication factor is 10000 times, vertical composite separating film direction is taken.As seen from the figure, titanium dioxide nanometer pipe composite separating membrane has cellular aperture [1] to be arranged, and the aperture is 50-100nm.Because the titania nanotube that generates is perpendicular to diaphragm, so can only see the aperture [1] (stain place) of titanium dioxide nanometer pipe composite separating membrane among the figure, and cannot see the pipe range of titania nanotube, but can see hole wall [2] termination (netted in vain) of titanium dioxide nanometer pipe composite separating membrane.A-A is a section symbols.
Fig. 2 is that the A-A profile scanning Electronic Speculum of Fig. 1 is faced structural representation (SEM)
This A-A cross-sectional view adopts the JSM-5600LV ESEM, is 12kV at accelerating potential, and under the condition that multiplication factor is 40000 times, vertical view 1A-A profile direction is taken.As seen from the figure, the aperture of titanium dioxide nanometer pipe composite separating membrane [1] (secret note shape), the duct all perpendicular to the face direction, is evenly distributed, and discrete orderly, the aperture is 50-100nm.By carrier diaphragm [3] Al that can also clearly see composite separating film among the figure
2O
3(informal voucher shape).
Fig. 3 is the transmission electron microscope picture (TEM) of single titania nanotube
In order to observe the inner formed TiO of composite separating film
2Nano tube structure at first, dissolves the Al that removes in the composite separating film with 6mol/LNaOH solution under 50 ± 5 ℃ of temperature
2O
3Diaphragm then, is used 0.1mol/LHCl, deionized water rinse 10min, and ultrasonic again dispersion 10min, last, characterize TiO after the drying
2Nano tube structure.The transmission electron microscope picture of titania nanotube of the present invention is to adopt TECNAI G
220 type transmission electron microscopes are 200kV at accelerating potential, and multiplication factor is under 50000 times the condition, single titania nanotube transmission electron microscope picture.As seen from the figure, the titania nanotube outer tube diameter that obtains is approximately 200nm, and interior caliber is approximately 100nm, and pipe thickness is approximately 50nm.By the interior caliber that can clearly see titania nanotube among the figure is the aperture [1] (part between the secret note shape up and down) of composite separating film, and the tube wall of single titania nanotube [4] (secret note shape part), the shot-like particle that seems more coarse on the nanotube is for constituting the TiO 2 particles [5] (white point shape) of titania nanotube tube wall.
The specific embodiment
Below by specific embodiment, further specify the details of titanium dioxide nanometer pipe composite separating membrane and its production and application.
Embodiment 1:
Molecular dimension is less for handling, the organic pollutant wastewater that wastewater flow rate is little is as agricultural chemicals etc., when requiring the composite separating film permeation flux little, can use the titanium dioxide nanometer pipe composite separating membrane for preparing under the following condition, this composite separating film can satisfy the laboratory research needs.
With the aperture is 20nm, and diameter is 25mm, and thickness is 50 μ m, and pitch of holes is 40-80nm, and porosity is 30% Al
2O
3Inorganic diaphragm is as carrier, and the preparation aperture is the titanium dioxide nanometer pipe composite separating membrane of 5-10nm, and step is:
The first step, the preliminary treatment of carrier
Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 20min, uses acetone, washed with de-ionized water 10min again, with after 50 ℃ of following dryings, is cooled to room temperature in baking oven, and is standby.
Second step, the preparation of TiO 2 sol
The 5ml butyl titanate is added in the 25ml absolute ethyl alcohol, and magnetic agitation 10min in ice-water bath slowly drips the mixed solution of 25ml absolute ethyl alcohol, 0.5ml water and 1.5ml glacial acetic acid then, and ultrasonic again 10min obtains transparent TiO
2Colloidal sol.The preparation temperature of colloidal sol is 15 ℃.
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses in this colloidal sol, treats to take out behind the 10min, and at first, at air drying 1h, then, the speed with 100 ℃/h in Muffle furnace is warming up to 500 ℃, and insulation 5h is last, reduces to room temperature with the speed of 50 ℃/h.In order to observe the inner TiO of composite separating film
2Nano tube structure dissolves the Al that removes in the composite separating film with 6mol/L NaOH solution under 50 ± 5 ℃ of temperature
2O
3Diaphragm is used 0.1mol/L HCl again, and deionized water rinse 10min characterizes TiO after the drying
2Nano tube structure.
Testing result: the titanium dioxide nanometer pipe composite separating membrane aperture is 5-10nm, the titania nanotube structure of composite separating film inside, and interior caliber 5-10nm, about outer tube diameter 20nm, pipe range 45-50 μ m.Titania nanotube is discrete in order, all perpendicular to the diaphragm direction.
Embodiment 2:
For handling the bigger organic pollutant wastewater of molecular dimension, as dyestuff, Polychlorinated biphenyls etc. can be used the titanium dioxide nanometer pipe composite separating membrane for preparing under the following condition, and this composite separating film can satisfy the needs of laboratory research and a small amount of actual waste water processing.
With the aperture is 100nm, and diameter is 47mm, and thickness is 60 μ m, and pitch of holes is 30-60nm, and porosity is 40% Al
2O
3Inorganic diaphragm is as carrier, and the preparation aperture is the titanium dioxide nanometer pipe composite separating membrane of 40-50nm, and step is:
The first step, the preliminary treatment of carrier
Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 15min, uses acetone, washed with de-ionized water 10min again, with after 100 ℃ of following dryings, is cooled to room temperature in baking oven, and is standby.
Second step, the preparation of TiO 2 sol
The 5ml butyl titanate is added in the 25ml absolute ethyl alcohol, and magnetic agitation 10min in ice-water bath slowly drips the mixed solution of 25ml absolute ethyl alcohol, 0.5ml water and 1.5ml glacial acetic acid then, and ultrasonic again 15min obtains transparent TiO
2Colloidal sol.The preparation temperature of colloidal sol is 20 ℃.
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses in this colloidal sol, treats to take out behind the 30min, and at first, at air drying 2h, then, the speed with 100 ℃/h in Muffle furnace is warming up to 500 ℃, and insulation 5h is last, reduces to room temperature with the speed of 50 ℃/h.In order to observe the inner TiO of composite separating film
2Nano tube structure dissolves the Al that removes in the composite separating film with 6mol/L NaOH solution under 50 ± 5 ℃ of temperature
2O
3Diaphragm is used 0.1mol/L HCl again, and deionized water rinse 10min characterizes TiO after the drying
2Nano tube structure.
Testing result: the titanium dioxide nanometer pipe composite separating membrane aperture is 40-50nm, the titania nanotube structure of composite separating film inside, and interior caliber 40-50nm, about outer tube diameter 100nm, pipe range 60 μ m.Titania nanotube is discrete in order, all perpendicular to the diaphragm direction.
Embodiment 3:
For handling the bigger organic pollutant wastewater of molecular dimension, as dyestuff, surface active agent wastewaters etc. can be used the titanium dioxide nanometer pipe composite separating membrane for preparing under the following condition, and this composite separating film can satisfy the needs of laboratory research and a small amount of actual waste water processing.
With the aperture is 200nm, and diameter is 47mm, and thickness is 60 μ m, and pitch of holes is 20-50nm, and porosity is 50% Al
2O
3Inorganic diaphragm is as carrier, and the preparation aperture is the titanium dioxide nanometer pipe composite separating membrane of 50-80nm, and step is:
The first step, the preliminary treatment of carrier
Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 20min, uses acetone, washed with de-ionized water 20min again, with after 50 ℃ of following dryings, is cooled to room temperature in baking oven, and is standby.
Second step, the preparation of TiO 2 sol
The 5ml butyl titanate is added in the 25ml absolute ethyl alcohol, and magnetic agitation 20min in ice-water bath slowly drips the mixed solution of 25ml absolute ethyl alcohol, 0.5ml water and 1.5ml glacial acetic acid then, and ultrasonic again 10min obtains transparent TiO
2Colloidal sol.The preparation temperature of colloidal sol is 20 ℃.
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses in this colloidal sol, treats to take out behind the 30min, and at first, at air drying 1h, then, the speed with 100 ℃/h in Muffle furnace is warming up to 400 ℃, and insulation 6h is last, reduces to room temperature with the speed of 50 ℃/h.In order to observe the inner TiO of composite separating film
2Nano tube structure dissolves the Al that removes in the composite separating film with 6mol/L NaOH solution under 50 ± 5 ℃ of temperature
2O
3Diaphragm is used 0.1mol/L HCl again, and deionized water rinse 10min characterizes TiO after the drying
2Nano tube structure.
Testing result: the titanium dioxide nanometer pipe composite separating membrane aperture is 50-80nm, the titania nanotube structure of composite separating film inside, and interior caliber 50-80nm, about outer tube diameter 200nm, pipe range 50-60 μ m.Titania nanotube is discrete in order, all perpendicular to the diaphragm direction.
Embodiment 4:
For handling the bigger organic pollutant wastewater of molecular dimension, as dyestuff, surface active agent wastewater etc., when the permeation flux that requires composite separating film is big, can use the titanium dioxide nanometer pipe composite separating membrane for preparing under the following condition, this composite separating film can satisfy the needs of laboratory research and a large amount of actual waste water processing.
With the aperture is 200nm, and diameter is 25mm, and thickness is 50 μ m, and pitch of holes is 60-100nm, and porosity is 25% Al
2O
3Inorganic diaphragm is as carrier, and the preparation aperture is the titanium dioxide nanometer pipe composite separating membrane of 100-130nm, and step is:
The first step, the preliminary treatment of carrier
Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 15min, uses acetone, washed with de-ionized water 15min again, with after 50 ℃ of following dryings, is cooled to room temperature in baking oven, and is standby.
Second step, the preparation of TiO 2 sol
The 5ml butyl titanate is added in the 25ml absolute ethyl alcohol, and magnetic agitation 10min in ice-water bath slowly drips the mixed solution of 25ml absolute ethyl alcohol, 0.5ml water and 1.5ml glacial acetic acid then, and ultrasonic again 10min obtains transparent TiO
2Colloidal sol.The preparation temperature of colloidal sol is 20 ℃.
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses in this colloidal sol, treats to take out behind the 10min, and at first, at air drying 1h, then, the speed with 100 ℃/h in Muffle furnace is warming up to 450 ℃, and insulation 4h is last, reduces to room temperature with the speed of 50 ℃/h.In order to observe the inner TiO of composite separating film
2Nano tube structure dissolves the Al that removes in the composite separating film with 6mol/L NaOH solution under 50 ± 5 ℃ of temperature
2O
3Diaphragm is used 0.1mol/L HCl again, and deionized water rinse 10min characterizes TiO after the drying
2Nano tube structure.
Testing result: the titanium dioxide nanometer pipe composite separating membrane aperture is 100-130nm, the titania nanotube structure of composite separating film inside, and interior caliber 100-130nm, about outer tube diameter 180-200nm, pipe range 45-50 μ m.Titania nanotube is discrete in order, all perpendicular to the diaphragm direction.
Embodiment 5: titanium dioxide nanometer pipe composite separating membrane is used for processing and contains Polychlorinated biphenyls waste water
Waste water quality: Polychlorinated biphenyls is 20mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 1 is handled and is contained Polychlorinated biphenyls waste water.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make Polychlorinated biphenyls solution by the diffusion barrier unit, flow velocity is 12.7L/h.At pressure reduction is 0.05MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.After 4 hours, its treatment effeciency reaches 96%.
Embodiment 6: titanium dioxide nanometer pipe composite separating membrane is used to handle agricultural chemicals waste water
Waste water quality: the Atrazine initial concentration is 50mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 3 is handled the agricultural chemicals Atrazine.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make pesticidal solutions pass through the diffusion barrier unit, flow velocity is 12.7L/h.At pressure reduction is 0.05MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.After 5 hours, its treatment effeciency reaches 95%.
Embodiment 7: titanium dioxide nanometer pipe composite separating membrane is used for surfactant waste water
Waste water quality: surfactant neopelex initial concentration is 50mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 4 is handled neopelex.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make surfactant solution pass through film unit, flow velocity is 12.7L/h.At pressure reduction is 0.08MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.React after 4 hours, its treatment effeciency reaches 89%.
Embodiment 8: titanium dioxide nanometer pipe composite separating membrane is used for dye wastewater treatment using
Waste water quality: directly black 168 initial concentrations of dyestuff are 500mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 3 is handled dyestuff and is directly deceived 168.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make dye solution pass through film unit, flow velocity is 7.0L/h.At pressure reduction is 0.02MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.React after 5 hours, its treatment effeciency reaches 80%.
Embodiment 9: titanium dioxide nanometer pipe composite separating membrane is used for dye wastewater treatment using
Waste water quality: directly black 168 initial concentrations of dyestuff are 300mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 3 is handled dyestuff and is directly deceived 168.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make dye solution pass through film unit, flow velocity is 7.0L/h.At pressure reduction is 0.05MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.React after 5 hours, its treatment effeciency reaches 85%.
Embodiment 10: titanium dioxide nanometer pipe composite separating membrane is used to handle dyestuff Acid Orange II waste water
Waste water quality: dyestuff Acid Orange II initial concentration is 100mg/L, and the water yield is 1.0L.
Titanium dioxide nanometer pipe composite separating membrane in the Application Example 3 is handled the dyestuff Acid Orange II.Under the room temperature condition, in the experimental rig of design voluntarily, by pump, make dye solution pass through film unit, flow velocity is 7.0L/h.At pressure reduction is 0.05MPa, and film separates when participating in, and adopts the surface of uviol lamp or near ultraviolet light irradiation titanium dioxide nanometer pipe composite separating membrane, and bubbling air continues to stir in the course of reaction.React after 4 hours, its treatment effeciency reaches 86%.
Subordinate list
Table 1 is that titanium dioxide nanometer pipe composite separating membrane is used to handle and contains each parameter values table that Polychlorinated biphenyls waste water is adopted
Table 2 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that agricultural chemicals waste water adopts
Table 3 is that titanium dioxide nanometer pipe composite separating membrane is used for each parameter values table that surfactant waste water adopts
Table 4 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that directly black 168 waste water of dyestuff are adopted
Table 5 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that directly black 168 waste water of dyestuff are adopted
Table 6 is that titanium dioxide nanometer pipe composite separating membrane is used to handle each parameter values table that dyestuff Acid Orange II waste water is adopted
Claims (5)
1. titanium dioxide nanometer pipe composite separating membrane, it is characterized in that: titanium dioxide nanometer pipe composite separating membrane is to be 25-47mm with the diameter, thickness is 50-60 μ m, porosity is 25-50%, gathering at its thickness direction of face upper edge is processed with the through hole that the aperture is 20-200nm, and its pitch of holes is the Al of 20-150nm
2O
3Inorganic diaphragm is as carrier; By sol-gel technique, carrier diaphragm [3] is through dipping, dry, roasting, and caliber is 5-130nm in making in the duct of carrier, and pipe range is the titania nanotube of 45-60 μ m, with Al
2O
3Diaphragm constitutes titanium dioxide nanometer pipe composite separating membrane together; This titanium dioxide nanometer pipe composite separating membrane diameter is 25-47mm, and specific area is 20-50m
2/ g, porosity is 20-40%, and aperture [1] is 5-130nm, and the spacing between the Kong Yukong is 20-150nm, and thickness is 50-60 μ m.
2. prepare the method for titanium dioxide nanometer pipe composite separating membrane as claimed in claim 1, it is characterized in that, preparation process is as follows:
The first step, the preliminary treatment of carrier
With Al
2O
3Inorganic diaphragm spends ionized water ultrasonic cleaning 10-20min, uses acetone, washed with de-ionized water 10-20min more respectively, with after the 50-100 ℃ of following drying, is cooled to room temperature in baking oven, and is standby;
Second step, the preparation of TiO 2 sol
With the volume ratio is V
Butyl titanate: V
Absolute ethyl alcohol=1: 5 ratio is added to butyl titanate in the absolute ethyl alcohol, magnetic agitation 10-30min in ice-water bath, and slowly dripping its volume ratio then is V
Ethanol: V
Glacial acetic acid: V
Water=50: the mixed solution of 3: 1 absolute ethyl alcohol, glacial acetic acid and water, its temperature should be controlled at 15-20 ℃, and ultrasonic again dispersion 10-20min obtains transparent TiO
2Colloidal sol;
The 3rd step, the preparation of titanium dioxide nanometer pipe composite separating membrane
With Al
2O
3Inorganic diaphragm immerses this TiO
2In the colloidal sol, treat to take out behind the 10-50min, at first, at air drying 1-2h; Then, the speed with 100 ℃/h in Muffle furnace is warming up to 400 ℃-500 ℃, insulation 4-6h; At last, reduce to room temperature with the speed of 50 ℃/h, standby.
3. use titanium dioxide nanometer pipe composite separating membrane as claimed in claim 1 to handle the application of organic pollutant wastewater, it is characterized in that:
Organic pollutant wastewater is cycled through composite separating film, at room temperature, when light source irradiation that wavelength and semiconductor band gap are complementary, titanium dioxide is activated, on the basis that produces photohole-duplet, organic matter generation redox reaction continues bubbling air in the course of reaction, make O in the solution on the one hand
2Concentration remains saturation state; Agitating solution makes it even on the other hand; Simultaneously, the pressure reduction that is produced by vavuum pump provides separation process needed driving force, and pressure differential range is 0.02-0.1MPa; Use titanium dioxide nanometer pipe composite separating membrane and handle organic pollutant wastewater, under the acting in conjunction that light source shines with film separates that wavelength and semiconductor band gap are complementary, after 4-6 hour, obtaining has higher removal efficient than simple film separation and simple photocatalysis, can reach 80-96%.
4. titanium dioxide nanometer pipe composite separating membrane according to claim 3 is handled the application of organic pollutant wastewater, it is characterized in that organic pollutant wastewater has: dyestuff, and surfactant-based, pesticide, classes of herbicides, hydro carbons, polychlorinated biphenyl, adhesive class.
5. according to the application of claim 3 or 4 described titanium dioxide nanometer pipe composite separating membranes processing organic pollutant wastewaters, it is characterized in that: the suitable concentration of handling organic pollutant wastewater should be less than 500mg/L.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN100428984C (en) * | 2006-11-17 | 2008-10-29 | 大连理工大学 | Composite separating membrane of Si-doped TiO2 nanotube and its preparing method and application |
| CN100563819C (en) * | 2006-06-27 | 2009-12-02 | 中国科学院合肥物质科学研究院 | Has diffusion barrier of photocatalysis performance and preparation method thereof |
| CN106315756A (en) * | 2016-10-18 | 2017-01-11 | 南昌航空大学 | Device for advanced treatment of organic wastewater through coordination of photocatalysis and fenton oxidation |
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| US6464881B2 (en) * | 1996-10-21 | 2002-10-15 | Orelis | Inorganic nanofiltration membrane and its application in the sugar industry |
| JP2002066278A (en) * | 2000-08-31 | 2002-03-05 | Japan Science & Technology Corp | Titanium dioxide porous film, and method and apparatus for treating water using the same |
| EP1468737A4 (en) * | 2002-01-21 | 2005-09-21 | Sumitomo Titanium Corp | Photocatalytic composite material and method for preparation thereof |
| CN1150980C (en) * | 2002-08-14 | 2004-05-26 | 清华大学 | Process for preparing photocatalytic TiO2 film used to clean water and air |
| CN1206015C (en) * | 2003-03-11 | 2005-06-15 | 武汉理工大学 | Method for preparing porous ceramic material with titanium dioxide optical catalytic nano-coating for purifying air and water |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN100563819C (en) * | 2006-06-27 | 2009-12-02 | 中国科学院合肥物质科学研究院 | Has diffusion barrier of photocatalysis performance and preparation method thereof |
| CN100428984C (en) * | 2006-11-17 | 2008-10-29 | 大连理工大学 | Composite separating membrane of Si-doped TiO2 nanotube and its preparing method and application |
| CN106315756A (en) * | 2016-10-18 | 2017-01-11 | 南昌航空大学 | Device for advanced treatment of organic wastewater through coordination of photocatalysis and fenton oxidation |
| CN110898679A (en) * | 2019-11-29 | 2020-03-24 | 珠海大横琴科技发展有限公司 | Filter membrane preparation method and filter membrane |
| CN111068525A (en) * | 2019-12-11 | 2020-04-28 | 天津科技大学 | Composite membrane with titanium dioxide nanorod array on surface, and preparation method and application thereof |
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