WO2013093805A1 - Method of reducing contaminants in water - Google Patents
Method of reducing contaminants in water Download PDFInfo
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- WO2013093805A1 WO2013093805A1 PCT/IB2012/057487 IB2012057487W WO2013093805A1 WO 2013093805 A1 WO2013093805 A1 WO 2013093805A1 IB 2012057487 W IB2012057487 W IB 2012057487W WO 2013093805 A1 WO2013093805 A1 WO 2013093805A1
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- WO
- WIPO (PCT)
- Prior art keywords
- preparing
- nanotubular
- composite matrix
- water
- matrix
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 47
- 239000000356 contaminant Substances 0.000 title claims abstract description 37
- 239000011159 matrix material Substances 0.000 claims abstract description 97
- 239000002131 composite material Substances 0.000 claims abstract description 53
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 40
- 230000001699 photocatalysis Effects 0.000 claims abstract description 37
- 239000004599 antimicrobial Substances 0.000 claims abstract description 28
- 239000002904 solvent Substances 0.000 claims abstract description 16
- 238000001354 calcination Methods 0.000 claims abstract description 6
- 230000003213 activating effect Effects 0.000 claims abstract description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 61
- 239000002071 nanotube Substances 0.000 claims description 44
- 239000004408 titanium dioxide Substances 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 18
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 15
- 150000001447 alkali salts Chemical class 0.000 claims description 15
- 239000008367 deionised water Substances 0.000 claims description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 238000011068 loading method Methods 0.000 claims description 6
- 229910002651 NO3 Inorganic materials 0.000 claims description 5
- 229910001867 inorganic solvent Inorganic materials 0.000 claims description 5
- 239000003049 inorganic solvent Substances 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000007873 sieving Methods 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 2
- 239000000920 calcium hydroxide Substances 0.000 claims description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 2
- 230000003028 elevating effect Effects 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- 239000004332 silver Substances 0.000 claims description 2
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 15
- 239000002073 nanorod Substances 0.000 description 10
- 241000588724 Escherichia coli Species 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 229910001961 silver nitrate Inorganic materials 0.000 description 7
- 239000002077 nanosphere Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 230000005855 radiation Effects 0.000 description 5
- 239000003463 adsorbent Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 230000000845 anti-microbial effect Effects 0.000 description 3
- 239000012634 fragment Substances 0.000 description 3
- 229910052736 halogen Inorganic materials 0.000 description 3
- 150000002367 halogens Chemical class 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000003242 anti bacterial agent Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 244000052769 pathogen Species 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 206010012735 Diarrhoea Diseases 0.000 description 1
- 241001646716 Escherichia coli K-12 Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 241000701161 unidentified adenovirus Species 0.000 description 1
- 244000052613 viral pathogen Species 0.000 description 1
- 244000000028 waterborne pathogen Species 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/50—Silver
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/009—Preparation by separation, e.g. by filtration, decantation, screening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/06—Washing
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
- C02F1/505—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/08—Nanoparticles or nanotubes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
Definitions
- the present invention relates to a method and matrix for reducing contaminants in water and to a method for preparing such a matrix.
- halogens such as chlorine (CI) and bromine (Br) are well known and widely used as antibacterial agents, but the direct use of these halogens as antibacterial agents has many disadvantages, because of their high toxicity and high vapour pressure in pure form.
- Another disadvantage associated with the use of halogens is that they may potentially react with other chemical contaminants to form by-products that could be carcinogenic.
- US2712573 One of the disadvantages disclosed in US2712573 is that the method for water purification uses irradiation from an electric light bulb having a specific spectrum of 200 nm to 400 nm. In addition, U32712573 is limited only to the contaminated water exposed to such spectrum of ultraviolet radiation. A further disadvantage is that the method requires a reliable source of electricity and light, without any risk of interruption.
- the intensity may be insufficient to completely inactivate the most UV- resistant microorganisms, such as adenoviruses.
- US20100032353 discloses a liquid dispenser or water purification unit having a housing and a mouthpiece configured for contact with the mouth of a person. At least part of the mouthpiece is provided with an antimicrobial surface coating comprising silver nanoparticles complexed with titanium dioxide.
- a disadvantage associated with US20100032353 is that the filter embedded in the unit lasts only a year, (approximately 700 liters) meaning users must replace the unit annually.
- a further disadvantage is that the antimicrobial surface is not used for water purification, but to ensure that bacteria from one person holding or drinking from the mouthpiece are killed on contact with the antimicrobial, such that a second person using the mouthpiece is not infected by the bacteria.
- a nanotubular composite matrix for reducing contaminants in water comprising a photocatalytic agent in nanotubular form loaded with an antimicrobial agent.
- the photocatalytic agent is a body of titanium dioxide (Ti0 2 ) nanotubes.
- the nanotubes may have a cross- sectional diameter of from 2 nm to 200 nm, preferably 7 nm to 1 1 nm.
- the antimicrobial agent is a body of silver (Ag) particles.
- the particles may have a cross-sectional diameter of from 0.5 nm to 30 nm, preferably 1 nm to 5 nm.
- a method for preparing a nanotubular composite matrix for reducing contaminants in water and on the matrix ' s surface including the steps of:
- the step of preparing the photocatalytic agent in the form of titanium dioxide may include the step of adding the titanium dioxide in an alkali salt to form a mixture, wherein the alkali salt may have a concentration of at least 2 M, preferably from 5 M to 30 M.
- the titanium dioxide in the mixture may be selected in the range of from 2% to 50% (w/v), preferably from 10% to 30% (w/v).
- the alkali salt may be selected from the group consisting of potassium hydroxide, sodium hydroxide, and calcium hydroxide.
- the step of preparing the photocatalytic agent may include the further step of stirring the mixture at an elevated temperature of up to 300 degrees Celsius for up to 24 hours to form titanium dioxide nanotubes. Furthermore, the step of preparing the photocatalytic agent may include the further step of centrifuging the mixture to separate the nanotubes from the alkali salt.
- the step of preparing the photocatalytic agent may include the further step of washing the nanotubes with deionised water to remove excess alkali salt from the nanotubes and to maintain conductivity of the nanotubes constant below 100 pS/cm.
- the step of preparing the photocatalytic agent may include the further step of drying the nanotubes at a temperature up to 200 degrees Celsius for at least 2 hours, preferably at 120 degrees Celsius for 12 hours and subsequently at 25 degrees Celsius for 5 hours.
- the step of preparing the photocatalytic agent may include the further step of sieving the nanotubes having an external diameter of from 2 nm to 200 nm, preferably from 7 nm to 1 1 nm, in accordance with the first aspect of the invention.
- the step of dissolving the antimicrobial agent in the solvent may include the step of selecting the solvent from the group consisting of organic solvents and inorganic solvents, preferably inorganic solvents, further preferably deionised water.
- the step of dissolving the antimicrobial agent in the solvent may further include the antimicrobial agent having a concentration in the range of from 0.1 % to 15% (w/v), preferably 0.5% to 7% (w/v).
- the step of loading the photocatalytic agent with the antimicrobial agent may include the step of mixing the dried nanotubes with the antimicrobial agent in solution to form the matrix.
- the step of removing the excess solvent from the matrix may include the step of incubating the matrix at a temperature up to 250 degrees Celsius for at least 10 hours, preferably at 25 degrees Celsius for 24 hours and subsequently at 120 degrees Celsius for 24 hours.
- the step of calcining the matrix to remove the moiety of the antimicrobial agent may include the step of elevating the temperature up to 1000 degrees Celsius for at least 5 hours, preferably 300 degrees Celsius for 12 hours to form the nanotubular composite matrix of the first aspect of the invention.
- the moiety of the antimicrobial agent is nitrate (N0 3 ).
- a method for reducing contaminants in water including the steps of:
- the light source may be selected from the group consisting light buib or sunlight, preferably sunlight.
- a device for reducing contaminants in water comprising:
- nanotubular composite matrix according to the first aspect of the invention disposed within the container.
- the container is of a translucent material to allow light to pass through the container to activate a photocatalytic agent.
- the container is provided with a light source.
- Figure 1 is a graph depicting the fraction of survivors of Escherichia coli (£. coli) culture incubated with a nanospherical composite matrix at varying concentration when a photocatalytic agent is exposed to ultraviolet radiation from sunlight for 90 minutes;
- Figure 2 is a graph depicting the fraction of survivors of £. coli culture incubated with a nanorod composite matrix at varying concentration when a photocatalytic agent is exposed to ultraviolet radiation from sunlight for 90 minutes; and
- Figure 3 is a graph depicting the fraction of survivors of E. coli culture incubated with a nanotubular composite matrix according to a preferred embodiment of the invention at varying concentration when a photocatalytic agent is exposed to ultraviolet radiation from sunlight for 90 minutes.
- a method for preparing a nanotubular composite matrix for reducing contaminants in water and on the matrix ' s surface includes the steps of:
- - preparing a photocatalytic agent comprising titanium dioxide in nanotubular form to form titanium dioxide nanotubes - dissolving an antimicrobial agent in the form of silver nitrate having a concentration of between 0.1 % to 15% (w/v), preferably 0.5% to 7% (w/v), further preferably 3.4% in an inorganic solvent, such as deionised water;
- ⁇ removing excess solvent from the matrix by incubating the matrix at a temperature of up to 250 degrees Celsius for at least 10 hours, preferably at 25 degrees Celsius for 24 hours and subsequently at 120 degrees Celsius for 24 hours;
- the step of preparing the photocatalytic agent in the form of titanium dioxide includes the step of adding the titanium dioxide in an alkali salt to form a mixture, wherein the alkali salt may have a concentration of at least 2 M, preferably from 5 M to 30 M.
- the step of preparing the photocatalytic agent includes the step of stirring the mixture at an elevated temperature of up to 300 degrees Celsius for at least 12 hours, preferably 150 degrees Celsius for 24 hours to form the titanium dioxide nanotubes.
- the step of preparing the photocatalytic agent includes the further step of centrifuging the mixture to separate the nanotubes from the alkali salt.
- the step of preparing the photocatalytic agent includes the further step of washing the nanotubes with deionised water to remove excess alkali salt from the nanotubes and to maintain conductivity of the nanotubes constant below 100 pS/cm.
- the step of preparing the photocatalytic agent includes the further step of drying the nanotubes at a temperature up to 200 degrees Celsius for at least 2 hours, preferably at 120 degrees Celsius for 12 hours and subsequently at 25 degrees Celsius for 5 hours.
- the step of preparing the photocatalytic agent includes the further step of sieving the nanotubes.
- the nanotubes have a cross- sectional diameter of from 2 nm to 200 nm, preferably 7 nm to 1 1 nm.
- the first step of the method is to prepare the titanium dioxide in a nanotubular form.
- other forms of the titanium dioxide such as nanorod and nanospherical, were also prepared from a commercial P25 Degussa titania to establish which form of titanium dioxide is capable of reducing contaminants in water.
- the titanium dioxide nanotubes about 23 g of the Degussa titania powder is placed in a teflon container together with 150 ml of 18 M potassium hydroxide to form a mixture. The mixture is stirred at a constant rate of 500 rpm in an autoclave at a temperature of 150 degrees Celsius for 24 hours.
- the mixture is stirred at a constant rate of 500 rpm in a microwave reactor for 5-10 minutes.
- the mixture is allowed to cool at room temperature for 24 hours to form titanium dioxide nanotubes.
- the nanotubes are separated from the mixture by centrifugation at a stirring rate of 10 000 rpm for 30 minutes at 4 degrees Celsius.
- the nanotubes are again washed with deionised water to remove excess potassium hydroxide from the nanotubes and to maintain conductivity of the nanotubes constant below 100 pS/cm. It was noted that removal of the alkali salt from the nanotubes could take at least a week.
- the nanotubes are dried in an oven at 120 degrees Celsius for 12 hours and then allowed to cool to room temperature for 5 hours.
- the nanotubes are then sieved to a desired size.
- the nanotubes have a cross-sectional diameter of from 7 nm to 1 1 nm.
- the above method is also followed when preparing the titanium dioxide in a nanorods form but 10 M of potassium hydroxide is used instead.
- the titanium dioxide in a nanospherical form is prepared by using the above commercial P25 Degussa titania powder. Firstly, the powder is modified and then used. The modification is achieved by mixing the powder with water and then compressed into a moist paste. This moist paste is then dried in an oven at 120 degrees Celsius for 48 hours to form the titanium dioxide nanospheres. The nanospheres are cooled and crushed into fragments. The fragments having the desired size of the nanospherical form are sieved out. The larger fragments are recycled and re-sieved while the smaller ones (fine powder formed as a result of crushing) are mixed with water again to from the moist paste.
- the silver nitrate is prepared and loaded to the nanotubes, nanorods or nanospheres.
- About 0.34 g of the silver nitrate is dissolved in 10 ml of deionised water to form a mixture.
- the mixture is then added to a container containing about 4 g of the nanotubes, nanorods or nanospheres to form a matrix. Removing excess solvent from the matrix
- excess water is removed by drying the matrix at room temperature for 24 hours and subsequently in an oven at 120 degrees Celsius for 24 hours. It was observed that the concentration of the loaded silver nitrate differs due to the nature of the ⁇ 2 form used. In all instances, nitrate is used as a precursor, and water is used as a solvent due to excellent solubility of the nitrate in water.
- the matrix is calcined at 300 degrees Celsius for 12 hours to remove the nitrate moiety from the silver nitrate to form a composite matrix (nanotubular, nanorod, or nanospherical).
- each one of the three prepared composite matrix is incubated with a growing culture of E. coli K- 12 strain in order to establish if the matrices could reduce the growth of E. coli within a short period of time when Ti0 2 is exposed to sunlight ( Figures 1 , 2, and 3).
- the nanorod and nanospherical composite matrices were able to reduce the growth of E. coli, but showing insignificant levels of growth reduction ( Figures 1 and 2). It was surprisingly found that the reduction of E. coli is attributed to the form of the composite matrix.
- the nanotubular composite matrix was found to have the largest surface area and thus being more effective in reducing the growth of E. coli when compared with the nanorod and nanospherical composite matrices. Although this specific example pertains to E. coli, the matrix has been found to be highly effective against a broad spectrum of undesirable microorganisms and contaminants.
- a device for reducing contaminants in water, the device comprising a container, with the nanotubu!ar composite matrix as (described above) being disposed within the container.
- the device is made available to communities in remote areas where there are limited resources to reduce contaminants in water.
- the contaminated water is disposed in the container and incubated whilst in contact with the nanotubular composite matrix in the container for 15 minutes thus to reduce the contaminants in the water.
- the nanotubular composite matrix could be an effective way to improve water quality and reduce diarrheal disease from waterborne, bacterial and viral pathogens.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Health & Medical Sciences (AREA)
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Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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ZA2011/09486 | 2011-12-22 | ||
ZA201109486 | 2011-12-22 |
Publications (1)
Publication Number | Publication Date |
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WO2013093805A1 true WO2013093805A1 (en) | 2013-06-27 |
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ID=47714465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/IB2012/057487 WO2013093805A1 (en) | 2011-12-22 | 2012-12-19 | Method of reducing contaminants in water |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020165812A1 (en) | 2019-02-13 | 2020-08-20 | Csir | A composite material and a method to prepare the composite |
CN115231648A (en) * | 2022-08-02 | 2022-10-25 | 内蒙古美赢环保科技有限公司 | Industrial sewage treating agent and preparation method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2712573A (en) | 1951-04-23 | 1955-07-05 | Vilbig Friedrich | Apparatus and method for analyzing, compressing or expanding speech and other sound recordings |
EP1449811A1 (en) * | 2001-10-30 | 2004-08-25 | Catalysts & Chemicals Industries Co., Ltd. | TUBULAR TITANIUM OXIDE PARTICLES, METHOD FOR PREPARING THE SAME, AND USE OF THE SAME |
US20100032353A1 (en) | 2006-12-07 | 2010-02-11 | Mikkel Vestergaard Frandsen | Liquid dispenser or water purification unit with antimicrobial mouthpiece or housing |
WO2010080703A2 (en) * | 2009-01-06 | 2010-07-15 | The Penn State Research Foundation | Titania nanotube arrays, methods of manufactures, and photocatalytic conversion of carbon dioxide using same |
-
2012
- 2012-12-19 WO PCT/IB2012/057487 patent/WO2013093805A1/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2712573A (en) | 1951-04-23 | 1955-07-05 | Vilbig Friedrich | Apparatus and method for analyzing, compressing or expanding speech and other sound recordings |
EP1449811A1 (en) * | 2001-10-30 | 2004-08-25 | Catalysts & Chemicals Industries Co., Ltd. | TUBULAR TITANIUM OXIDE PARTICLES, METHOD FOR PREPARING THE SAME, AND USE OF THE SAME |
US20100032353A1 (en) | 2006-12-07 | 2010-02-11 | Mikkel Vestergaard Frandsen | Liquid dispenser or water purification unit with antimicrobial mouthpiece or housing |
WO2010080703A2 (en) * | 2009-01-06 | 2010-07-15 | The Penn State Research Foundation | Titania nanotube arrays, methods of manufactures, and photocatalytic conversion of carbon dioxide using same |
Non-Patent Citations (1)
Title |
---|
CHANG G ET AL: "Silver Nanoparticles Filling in TiO2 Hollow Nanofibers by Coaxial Electrospinning", ACTA PHYSICO-CHIMICA SINICA, ELSEVIER BV, NETHERLANDS, vol. 24, no. 10, 1 October 2008 (2008-10-01), pages 1790 - 1797, XP025561569, ISSN: 1872-1508, [retrieved on 20081001], DOI: 10.1016/S1872-1508(08)60073-X * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020165812A1 (en) | 2019-02-13 | 2020-08-20 | Csir | A composite material and a method to prepare the composite |
CN115231648A (en) * | 2022-08-02 | 2022-10-25 | 内蒙古美赢环保科技有限公司 | Industrial sewage treating agent and preparation method thereof |
CN115231648B (en) * | 2022-08-02 | 2023-10-24 | 内蒙古美赢环保科技有限公司 | Industrial sewage treatment agent and preparation method thereof |
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