CN115368158B - Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane - Google Patents

Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane Download PDF

Info

Publication number
CN115368158B
CN115368158B CN202110561931.9A CN202110561931A CN115368158B CN 115368158 B CN115368158 B CN 115368158B CN 202110561931 A CN202110561931 A CN 202110561931A CN 115368158 B CN115368158 B CN 115368158B
Authority
CN
China
Prior art keywords
titanium oxide
sol
oxide ceramic
nanofiltration membrane
membrane support
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202110561931.9A
Other languages
Chinese (zh)
Other versions
CN115368158A (en
Inventor
陈云强
洪昱斌
方富林
蓝伟光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suntar Membrane Technology Xiamen Co Ltd
Original Assignee
Suntar Membrane Technology Xiamen Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Suntar Membrane Technology Xiamen Co Ltd filed Critical Suntar Membrane Technology Xiamen Co Ltd
Priority to CN202110561931.9A priority Critical patent/CN115368158B/en
Publication of CN115368158A publication Critical patent/CN115368158A/en
Application granted granted Critical
Publication of CN115368158B publication Critical patent/CN115368158B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/027Nanofiltration
    • 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
    • B01D67/0039Inorganic membrane manufacture
    • B01D67/0048Inorganic membrane manufacture by sol-gel transition
    • 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
    • B01D71/02Inorganic material
    • 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
    • B01D71/02Inorganic material
    • B01D71/024Oxides
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/46Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on titanium oxides or titanates
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/62218Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products obtaining ceramic films, e.g. by using temporary supports
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/624Sol-gel processing
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/63Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
    • C04B35/632Organic additives
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/63Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
    • C04B35/632Organic additives
    • C04B35/634Polymers
    • C04B35/63448Polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B35/63488Polyethers, e.g. alkylphenol polyglycolether, polyethylene glycol [PEG], polyethylene oxide [PEO]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Nanotechnology (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses a preparation method of an ultrathin titanium oxide ceramic nanofiltration membrane, which comprises the following steps: (1) Performing sol-gel reaction, adding nitric acid solution for de-gelling, adding sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion; (2) Adding an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10; (3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid; (4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support; (5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 8-12 hours at 175-185 ℃, and then calcined and naturally cooled, so that the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.

Description

Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane
Technical Field
The invention belongs to the technical field of nanofiltration membranes, and particularly relates to a preparation method of an ultrathin titanium oxide ceramic nanofiltration membrane.
Background
Membrane separation is mainly divided into microfiltration, ultrafiltration, nanofiltration and reverse osmosis. The application field of membrane separation technology has been deep into various aspects of life and production of people, such as chemical industry, environmental protection, electronics, textiles, medicine, food, etc. The organic film is limited in separation process requiring special conditions due to poor high temperature resistance, poor chemical corrosion resistance, easy pollution, swelling and shrinkage in solvent, and the like. The inorganic film has the characteristics of good chemical stability, high mechanical strength, high pressure resistance, wear resistance, scouring resistance, high temperature resistance (on-line disinfection can be realized), microbial corrosion resistance, long service life and the like, so that the inorganic film can be applied to the fields with harsh conditions.
In the prior art, the preparation method of the nano particles mainly comprises a chemical precipitation method, a sol-gel method, a hydrothermal method, a microemulsion method and the like. Wherein the sol-gel method is the most main method for preparing the titanium dioxide ceramic ultrafiltration membrane by a liquid phase method. However, when the titanium dioxide nano solution obtained by the sol-gel method is used for preparing the ceramic nanofiltration membrane, multiple coating films are needed due to serious shrinkage in the calcination process, and the stability of the prepared sol has a great influence on the coating film effect, so that the expansion production of the sol-gel method is limited to a certain extent. When preparing the ceramic nanofiltration membrane, firstly preparing film coating liquid, adding polyvinyl alcohol or cellulose thickener to increase the viscosity of the film coating liquid and increase the strength of the film layer and the substrate, but controlling the amount of the thickener to be finer, otherwise, the prepared film layer is easy to crack. In addition, the thickness of the membrane layer of the nanofiltration membrane has a great influence on flux, the thicker the membrane layer is, the lower the flux is, but the thinner the membrane layer is, the defect of the nanofiltration membrane is easily caused, and how to prepare an ultrathin complete membrane layer becomes a research hot spot.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a preparation method of an ultrathin titanium oxide ceramic nanofiltration membrane.
The technical scheme of the invention is as follows:
the preparation method of the ultrathin titanium oxide ceramic nanofiltration membrane comprises the following steps:
(1) Mixing n-butyl titanate with 0.1-0.6mol/L and water in the molar ratio of 1:10-20 for sol-gel reaction, adding nitric acid solution for de-colloid, adding sodium citrate in the concentration of 0.8-1.2wt% to obtain dispersed titania sol;
(2) Adding 0.8-1.2wt% of emulsifying agent into the titanium oxide sol, and uniformly mixing, wherein the emulsifying agent consists of cyclohexane, n-hexanol and OP-10 according to the molar ratio of 7-9:1.5-2.5:0.8-1.2;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 8-12 hours at 175-185 ℃, and then calcined and naturally cooled, so that the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
In a preferred embodiment of the present invention, the concentration of n-butyl titanate in the step (1) is 0.1 to 0.6mol/L.
In a preferred embodiment of the invention, the molar ratio of n-butyl titanate to water in step (1) is 1:10.
In a preferred embodiment of the present invention, the concentration of n-butyl titanate in step (1) is 0.1 to 0.6mol/L and the molar ratio of n-butyl titanate to water is 1:10.
In a preferred embodiment of the invention, the pH of the material after the debonder in step (1) is 3.
In a preferred embodiment of the invention, the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1.
In a preferred embodiment of the present invention, the reaction temperature in step (5) is 180℃and the time is 10 hours.
In a preferred embodiment of the present invention, the calcination in the step (5) is as follows: heating to 350-500 ℃ at the speed of 2-4 ℃/min, and preserving heat and calcining for 2-4h.
Further preferably, the calcining in step (5) is: heating to 350-500 ℃ at the speed of 3 ℃/min, and preserving heat and calcining for 3h.
In a preferred embodiment of the present invention, the reaction temperature in the step (5) is 180 ℃, the time is 10 hours, and the calcination is as follows: heating to 350-500 ℃ at the speed of 3 ℃/min, and preserving heat and calcining for 3h.
The beneficial effects of the invention are as follows:
1. the invention combines a sol-gel method with a microemulsion medium hydrothermal method to prepare a titanium oxide film in situ, and the titanium oxide nanofiltration membrane layer is directly obtained through calcination.
2. According to the invention, the titanium oxide film is prepared by adding a specific emulsifier into titanium oxide sol and performing hydrothermal reaction at a lower temperature in a shorter time, and the titanium oxide nanofiltration membrane with no defects and high quality is prepared by a calcination step, wherein the flux of the ultrathin titanium oxide nanofiltration membrane is improved by 1 time compared with that of the thicker ceramic nanofiltration membrane.
Drawings
FIG. 1 is a scanning electron microscope photograph of the ultra-thin titania ceramic nanofiltration membrane prepared in examples 1 to 5 of the present invention.
FIG. 2 is another SEM photograph of the ultra-thin titania ceramic nanofiltration membranes prepared according to examples 1 to 2 of the present invention.
FIG. 3 is another SEM photograph of the ultra-thin titania ceramic nanofiltration membrane prepared according to examples 3 and 5 of the present invention.
FIG. 4 is another SEM photograph of the ultra-thin titania ceramic nanofiltration membrane prepared according to example 4 of the present invention.
FIG. 5 is a scanning electron micrograph of a comparative film 1 produced in comparative example 1 of the present invention.
FIG. 6 is a scanning electron micrograph of comparative film 2 prepared in comparative example 2 of the present invention.
Detailed Description
The technical scheme of the invention is further illustrated and described below by the specific embodiments in combination with the accompanying drawings.
Example 1
(1) Mixing n-butyl titanate with the concentration of 0.2mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 350 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is shown in figures 1 and 2, the membrane layer is complete, the flux of PEG (molecular weight 2000) for 2g/L is 62LHM, and the rejection rate is 96.5%.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is subjected to acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, and maintaining the retention rate at 95% and 96% respectively for PEG (molecular weight 2000) flux of 2g/L of 65 and 61LHM, respectively.
Example 2
(1) Mixing n-butyl titanate with the concentration of 0.2mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 500 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is shown in figures 1 and 2, the membrane layer is complete, the flux of PEG (molecular weight 2000) for 2g/L is 60LHM, and the rejection rate is 92.1%.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is subjected to acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, and maintaining the retention rate of 91.5% and 90.8% respectively for 2g/L PEG (molecular weight 2000) flux of 62 and 65LHM, respectively.
Example 3
(1) Mixing n-butyl titanate with the concentration of 0.5mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 350 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is shown in figures 1 and 3, the membrane layer is complete, the flux of PEG (molecular weight 2000) for 2g/L is 52LHM, and the rejection rate is 97.1%.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is subjected to acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, respectively 53 and 50LHM for 2g/L PEG (molecular weight 2000), retention rates of 96.5% and 95.8%, respectively, and keeping performance basically unchanged.
Example 4
(1) Mixing n-butyl titanate with the concentration of 0.1mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 350 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is shown in figures 1 and 4, the membrane layer is complete, the flux of PEG (molecular weight 2000) with the concentration of 2g/L is 80LHM, and the rejection rate is 66%.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is subjected to acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, respectively 85 and 83LHM for 2g/L PEG (molecular weight 2000), with retention rates of 62% and 64.2%, respectively, and substantially unchanged performance.
Example 5
(1) Mixing n-butyl titanate with the concentration of 0.6mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support; the method comprises the steps of carrying out a first treatment on the surface of the
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 350 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is shown in figures 1 and 3, the membrane layer is complete, the flux of PEG (molecular weight 2000) with the concentration of 2g/L is 45LHM, and the rejection rate is 96.3%.
The ultrathin titanium oxide ceramic nanofiltration membrane prepared in the embodiment is subjected to acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, respectively, with PEG (molecular weight 2000) flux of 47 and 48LHM for 2g/L, retention rates of 95.6% and 94.8%, respectively, and keeping performance basically unchanged.
Comparative example 1
(1) Mixing n-butyl titanate with the concentration of 0.8mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 500 ℃ at a rate of 3 ℃/min, calcined for 3 hours at a temperature) and naturally cooled to obtain a comparative membrane 1, as shown in figure 5, the membrane layer is thicker and reaches 900-1000nm.
The comparative membrane 1 prepared in this comparative example has a complete membrane layer, a flux of 30LHM for 2g/L PEG (molecular weight 2000), and a rejection of 94.5%.
The comparative film 1 prepared in this comparative example was subjected to an acid and alkali resistance test: soaking in 20% nitric acid solution and 5% sodium hydroxide solution at 100deg.C for 96 hr, and maintaining the retention rate at 93% and 92.8% respectively for 2g/L PEG (molecular weight 2000) flux at 32 and 31.5LHM, respectively.
Comparative example 2
(1) Mixing n-butyl titanate with the concentration of 0.05mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for dispergation, wherein the pH value of the dispergated material is 3, adding 1wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 1wt% of an emulsifier into the titanium oxide sol, and uniformly mixing, wherein the emulsifier consists of cyclohexane, n-hexanol and OP-10 in a molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 10 hours at 180 ℃, calcined (heated to 500 ℃ at the speed of 3 ℃/min, heat-preserved and calcined for 3 hours) and naturally cooled, and the comparative membrane 2 is obtained, wherein the coating layer is too thin and is not completely covered.
As shown in FIG. 6, the comparative membrane 2 prepared in this comparative example has incomplete membrane layer, a flux of 180LHM for 2g/L PEG (molecular weight 2000), and a rejection rate of 9.8%.
The foregoing description is only illustrative of the preferred embodiments of the present invention and is not to be construed as limiting the scope of the invention, i.e., the invention is not to be limited to the details of the invention.

Claims (5)

1. A preparation method of an ultrathin titanium oxide ceramic nanofiltration membrane is characterized by comprising the following steps of: the method comprises the following steps:
(1) Mixing n-butyl titanate with the concentration of 0.1-0.6mol/L and water in the molar ratio of 1:10 for sol-gel reaction, adding nitric acid solution for de-gelling, wherein the pH value of the de-gelled material is 3, adding 0.8-1.2wt% sodium citrate, and uniformly mixing to obtain titanium oxide sol with good dispersion;
(2) Adding 0.8-1.2wt% of emulsifying agent into the titanium oxide sol, and uniformly mixing, wherein the emulsifying agent consists of cyclohexane, n-hexanol and OP-10 according to the molar ratio of 8:2:1;
(3) Carrying out ultrasonic treatment on the material obtained in the step (2) to obtain a coating liquid;
(4) After ultrasonic treatment, soaking the titanium oxide ceramic membrane support in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support;
(5) The coating liquid is dip-coated on an activated ceramic membrane support, reacted for 8-12 hours at 175-185 ℃, and then calcined and naturally cooled, so that the ultrathin titanium oxide ceramic nanofiltration membrane is obtained.
2. The method of manufacturing according to claim 1, wherein: the reaction temperature in the step (5) is 180 ℃ and the time is 10 hours.
3. The method of manufacturing according to claim 1, wherein: the calcination in the step (5) is as follows: heating to 350-500 ℃ at the speed of 2-4 ℃/min, and preserving heat and calcining for 2-4h.
4. A method of preparation as claimed in claim 3, wherein: the calcination in the step (5) is as follows: heating to 350-500 ℃ at the speed of 3 ℃/min, and preserving heat and calcining for 3h.
5. The method of manufacturing according to claim 1, wherein: the reaction temperature in the step (5) is 180 ℃, the time is 10 hours, and the calcination is as follows: heating to 350-500 ℃ at the speed of 3 ℃/min, and preserving heat and calcining for 3h.
CN202110561931.9A 2021-05-21 2021-05-21 Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane Active CN115368158B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110561931.9A CN115368158B (en) 2021-05-21 2021-05-21 Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110561931.9A CN115368158B (en) 2021-05-21 2021-05-21 Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane

Publications (2)

Publication Number Publication Date
CN115368158A CN115368158A (en) 2022-11-22
CN115368158B true CN115368158B (en) 2023-07-07

Family

ID=84059830

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110561931.9A Active CN115368158B (en) 2021-05-21 2021-05-21 Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane

Country Status (1)

Country Link
CN (1) CN115368158B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1800030A (en) * 2005-12-20 2006-07-12 湘潭大学 Process for preparing barium titanate nano-rod
CN102010185A (en) * 2010-09-28 2011-04-13 景德镇博智陶瓷有限公司 Thermostable white nano far-infrared ceramic powder and preparation method thereof
CN103537286A (en) * 2013-10-28 2014-01-29 湛江师范学院 Single-step hydrothermal micro-emulsion method for preparing iron-doped nano titanium dioxide powder
WO2021047205A1 (en) * 2019-09-12 2021-03-18 三达膜科技(厦门)有限公司 Method for preparing ceramic nanofiltration membrane

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10167727A (en) * 1995-10-26 1998-06-23 Matsumoto Seiyaku Kogyo Kk Modified titanium oxide sol, photocatalyst composition and its forming agent
JP5039970B2 (en) * 2007-01-19 2012-10-03 国立大学法人信州大学 Method for producing titania microporous membrane
CN105214521B (en) * 2014-06-25 2017-08-04 天津大学 A kind of polyetherimide amine composite nanofiltration membrane and preparation method
CN110038436B (en) * 2019-04-04 2022-01-04 三达膜科技(厦门)有限公司 Preparation method of titanium dioxide/graphene oxide/polyethylene glycol composite ceramic nanofiltration membrane
CN110743401A (en) * 2019-09-12 2020-02-04 三达膜科技(厦门)有限公司 Preparation method of high-flux ceramic ultrafiltration membrane
CN110801738B (en) * 2019-11-25 2021-06-01 泰州清润环保科技有限公司 Preparation method of high-dispersion titanium dioxide doped polyamide nanofiltration membrane

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1800030A (en) * 2005-12-20 2006-07-12 湘潭大学 Process for preparing barium titanate nano-rod
CN102010185A (en) * 2010-09-28 2011-04-13 景德镇博智陶瓷有限公司 Thermostable white nano far-infrared ceramic powder and preparation method thereof
CN103537286A (en) * 2013-10-28 2014-01-29 湛江师范学院 Single-step hydrothermal micro-emulsion method for preparing iron-doped nano titanium dioxide powder
WO2021047205A1 (en) * 2019-09-12 2021-03-18 三达膜科技(厦门)有限公司 Method for preparing ceramic nanofiltration membrane

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
微乳液法制备纳米TiO_2粒子;益帼;邓瑞红;聂基兰;;有色金属(01);第46-48页 *

Also Published As

Publication number Publication date
CN115368158A (en) 2022-11-22

Similar Documents

Publication Publication Date Title
CN110038437B (en) Preparation method of organic-inorganic piperazine polyamide composite ceramic nanofiltration membrane
CN107029562B (en) MXene-based composite nanofiltration membrane and preparation method thereof
CN106000125B (en) Bionic preparation method of inorganic composite nanofiltration membrane
Rahimpour et al. Structural and performance properties of UV-assisted TiO2 deposited nano-composite PVDF/SPES membranes
CN106807251B (en) Polyethyleneimine-tannic acid/hydrolyzed polyacrylonitrile ultrathin composite membrane and preparation and application thereof
CN110038436B (en) Preparation method of titanium dioxide/graphene oxide/polyethylene glycol composite ceramic nanofiltration membrane
WO2021248896A1 (en) Preparation method for titania ceramic ultrafiltration membrane
CN106178981B (en) A kind of method of low temperature preparation titanium oxide ceramics ultrafiltration membrane
Li et al. Zirconia ultrafiltration membranes on silicon carbide substrate: microstructure and water flux
CN110743385A (en) Preparation method of titanium oxide-silicon oxide composite ceramic ultrafiltration membrane
Kreiter et al. Sol–gel routes for microporous zirconia and titania membranes
CN108283889B (en) Composite membrane, preparation method thereof and application thereof in gas separation and purification
Abadikhah et al. SiO2 nanoparticles modified Si3N4 hollow fiber membrane for efficient oily wastewater microfiltration
CN110743386A (en) Preparation method of zirconia-titanium oxide composite ultrafiltration membrane
CN115368158B (en) Preparation method of ultrathin titanium oxide ceramic nanofiltration membrane
CN209317459U (en) A kind of novel organic ultrafiltration membrane
CN110743401A (en) Preparation method of high-flux ceramic ultrafiltration membrane
CN111420564B (en) Inorganic composite separation membrane containing graphene oxide, and preparation method and application thereof
CN115364689B (en) Preparation method of ultrathin zirconia-titania ceramic composite nanofiltration membrane
Chowdhury et al. Development and comparative study of different nanofiltration membranes for recovery of highly charged large ions
Zhang et al. Sacrificial GO-BD interlayer for high performance ceramic ultrafiltration membrane
CN113230907B (en) Method for preparing LTL type molecular sieve membrane by space-limited steam conversion method
CN113797765B (en) Preparation method of zirconia ceramic ultrafiltration membrane
CN114130219B (en) Titanium dioxide-loaded molybdenum oxide disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane and preparation method thereof
CN116550164B (en) Preparation method of nanofiltration ceramic membrane and product prepared by preparation method

Legal Events

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