CN113797770A - Dopamine-modified molybdenum oxide-molybdenum disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane and preparation method thereof - Google Patents

Dopamine-modified molybdenum oxide-molybdenum disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane and preparation method thereof Download PDF

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CN113797770A
CN113797770A CN202010539613.8A CN202010539613A CN113797770A CN 113797770 A CN113797770 A CN 113797770A CN 202010539613 A CN202010539613 A CN 202010539613A CN 113797770 A CN113797770 A CN 113797770A
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dopamine
oxide
molybdenum disulfide
modified molybdenum
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CN113797770B (en
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陈云强
洪昱斌
方富林
蓝伟光
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Suntar Membrane Technology Xiamen Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/024Oxides
    • 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
    • B01D67/0079Manufacture of membranes comprising organic and inorganic components
    • 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
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10Supported membranes; Membrane supports
    • B01D69/105Support pretreatment
    • 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
    • B01D69/12Composite membranes; Ultra-thin membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/56Polyamides, e.g. polyester-amides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/30Chemical resistance
    • 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

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  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses a dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane and a preparation method thereof. According to the invention, the organic-inorganic piperazine polyamide composite ceramic nanofiltration membrane is prepared on the inorganic ceramic membrane loaded with the cross-linking agent, so that the magnesium sulfate solution has high desalination rate, high pure water flux and good acid and alkali resistance.

Description

Dopamine-modified molybdenum oxide-molybdenum disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane and preparation method thereof
Technical Field
The invention belongs to the technical field of membrane separation, and particularly relates to a dopamine-modified molybdenum oxide-molybdenum disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane and a preparation method thereof.
Background
The nanofiltration membrane technology is a means for effectively solving the problem of water purification due to simple operation and high efficiency. The nanofiltration membrane operates at lower pressure and higher flux than RO membranes. The nanofiltration membrane technology is used for water purification and has two major problems, namely the problem of flux and interception needs to be balanced, and the problem of pollution resistance of a membrane layer. How to solve the problems becomes a difficult problem of the nanofiltration membrane in the aspect of water purification application.
The research of the nanofiltration membrane in recent years shows that the most widely used organic nanofiltration membrane at present has the advantages of high air permeability, low density, good film forming property, low cost, good flexibility and the like, but loses use value in many fields due to poor high temperature resistance, organic solvent resistance and acid and alkali resistance; the inorganic nanofiltration membrane has the advantages of high mechanical strength, corrosion resistance, solvent resistance, high temperature resistance, stronger pollution resistance than an organic membrane and the like, but has higher preparation cost, large brittleness and difficult processing. Therefore, how to combine the advantages of inorganic materials and organic materials into one, and the preparation of the anti-pollution composite nanofiltration membrane with high flux and high rejection rate becomes a hot focus of attention.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a dopamine modified molybdenum oxide molybdenum disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
The invention also aims to provide a preparation method of the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane.
The technical scheme of the invention is as follows:
a dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane is characterized in that: the organic functional layer is formed by taking a water phase monomer, an organic phase monomer and an acid acceptor as raw materials and performing interfacial polymerization reaction on the porous ceramic membrane support;
the water phase monomer contains dopamine modified molybdenum disulfide oxide and piperazine;
the organic phase monomer is trimesoyl chloride;
the acid acceptor is polyamine;
the amino group on the silane coupling agent reacts with trimesoyl chloride to be connected.
In a preferred embodiment of the invention, the polyamine is diethylamine.
In a preferred embodiment of the present invention, the pore size of the porous ceramic membrane support is 10 to 100 nm.
In a preferred embodiment of the present invention, the material of the porous ceramic membrane support is alumina, titania or zirconia.
In a preferred embodiment of the invention, the mass ratio of the piperazine, the dopamine modified molybdenum oxide disulfide and the polyamine is 0.2-3: 0.01-0.05: 1.
the other technical scheme of the invention is as follows:
the preparation method of the dopamine-modified molybdenum disulfide oxide-doped piperazine polyamide composite ceramic nanofiltration membrane comprises the following steps: preparing molybdenum disulfide oxide by an improved Hummers method, and reacting the molybdenum disulfide oxide with dopamine hydrochloride to prepare dopamine modified molybdenum disulfide oxide; and (2) taking the mixture of the dopamine modified molybdenum disulfide oxide and piperazine as a water phase monomer, taking phthaloyl chloride as an organic monomer, taking polyamine as an acid acceptor, and forming the organic functional layer on the porous ceramic membrane support activated by strong alkali and grafted with the silane coupling agent through interfacial polymerization, wherein amino on the silane coupling agent reacts with trimesoyl chloride to be connected, so that the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane is obtained.
In a preferred embodiment of the present invention, the method comprises the following steps:
(1) preparing a molybdenum disulfide oxide aqueous solution by using an improved Hummers method, adding dopamine hydrochloride, and adjusting the pH to 8.5 by using a Tris-HCl buffer solution to obtain a mixed suspension; magnetically stirring the mixed suspension at 58-62 ℃ for reaction for 11-13h, and then carrying out centrifugal water washing to remove unreacted dopamine hydrochloride completely to obtain a dopamine modified molybdenum disulfide oxide aqueous solution;
(2) fully mixing the dopamine modified molybdenum disulfide oxide aqueous solution, piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution;
(3) after ultrasonic treatment, soaking the ceramic membrane support body in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a silane coupling agent solution, then cleaning with ethanol and water, and drying to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride, carrying out soaking and blow-drying after room temperature reaction, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after room temperature reaction; repeating the step at least 1 time;
(6) and (5) drying the material obtained in the step (5) in the shade, then carrying out heat treatment at 50-80 ℃, and then cooling along with a furnace to obtain the dopamine modified molybdenum oxide and molybdenum disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
Further preferably, in the aqueous phase solution, the concentration of piperazine is 0.2 to 3 wt%, the concentration of the dopamine modified molybdenum oxide disulfide is 0.01 to 0.05 wt%, and the concentration of polyamine is 1 wt%.
Still more preferably, the concentration of the PEG1000 in the aqueous phase solution is 0.8 to 1.2 wt%.
Further preferably, the concentration of the n-hexane solution of trimesoyl chloride is 2-10 wt%.
The invention has the beneficial effects that: according to the invention, the organic-inorganic piperazine polyamide composite ceramic nanofiltration membrane is prepared on the inorganic ceramic membrane loaded with the silane coupling agent, so that the magnesium sulfate solution has high desalination rate, high pure water flux and good acid and alkali resistance.
Detailed Description
The technical solution of the present invention is further illustrated and described by the following detailed description.
The modified Hummers process of the following comparative examples and examples specifically includes:
(1) 1000mL of beaker is taken, cleaned and dried, 3g of molybdenum disulfide is added, and 360mL of concentrated sulfuric acid (98% H) is slowly added under magnetic stirring2SO4) And 40mL concentrated phosphoric acid (95% H)3PO4) Then 18g of potassium permanganate (KMnO) is slowly added in batches4) (ii) a The beaker was transferred to a 50 ℃ oil bath and stirred for 12 h. Taking out the beaker, and naturally cooling to room temperature. The reaction solution was slowly poured into 400mL of dilute hydrogen peroxide (containing 18mL of 30% H)2O2) On ice, the solution turned bright yellow;
(2) performing cross-flow filtration on the solution by using a tubular ceramic membrane with the aperture of 0.05 mu m to remove impurities to obtain a material after impurity removal
(3) And (3) diluting or concentrating the material obtained in the step (2) according to the required concentration to obtain molybdenum oxide disulfide aqueous solutions with different concentrations.
Comparative example 1
(1) Fully mixing a piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution, wherein the content of the piperazine, the PEG1000 and the diethylamine in the aqueous phase solution is 1 wt%, 1 wt% and 1 wt% in sequence;
(2) ultrasonically treating an alumina ceramic membrane tube with the aperture of about 50cm after cutting for 5 hours, soaking the alumina ceramic membrane tube with the aperture of 100nm for 24 hours by using 2mol/L sodium hydroxide, drying the tube for 10 hours at the temperature of 100 ℃, washing the ceramic membrane tube by using cellulose after cooling, then washing the ceramic membrane tube by using ethanol and deionized water for a plurality of times in sequence, drying the tube for 12 hours at the temperature set value of 100 ℃ in a drying oven, and cooling the tube along with the oven to obtain an activated ceramic membrane support body;
(3) soaking the activated ceramic membrane support body in a 2 mmol/L3-aminopropyltriethoxysilane ethanol solution, reacting for 12 hours at room temperature, washing with ethanol and deionized water for several times, drying for 12 hours in a drying oven at a set temperature of 150 ℃, and cooling with the oven to obtain a grafted ceramic membrane support body;
(4) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride with the concentration of 2 wt%, carrying out soaking and blow-drying after reacting for 10min at room temperature, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after reacting for 10min at room temperature; repeating the step for 1 time;
(5) and (5) placing the material obtained in the step (4) in a shade place for air drying, then placing the material in a 50 ℃ oven for heat treatment for 15min, and then cooling along with the oven to obtain the contrast film.
Testing the performance of the membrane tube: the comparative film obtained in this comparative example was tested at room temperature and a pressure of 0.69MPa, and had a pure water flux of 40LHM and a rejection of 94% for a 0.2 wt% solution of magnesium sulfate.
And (3) acid and alkali resistance test: after the comparative membrane prepared in the comparative example is respectively soaked in a nitric acid solution with the pH value of 2 and a sodium hydroxide solution with the pH value of 12 for 168 hours at the temperature of 85 ℃, the pure water flux is respectively 39 LHM and 38LHM, the retention rates are respectively 93.7 percent and 93.3 percent, and the performance is basically kept unchanged.
Comparative example 2
(1) Preparing a molybdenum disulfide oxide aqueous solution with the concentration of 3mg/mL by using a modified Hummers method;
(2) fully mixing the molybdenum disulfide oxide aqueous solution, the piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution, wherein the contents of the molybdenum disulfide oxide, the piperazine, the PEG1000 and the diethylamine in the aqueous phase solution are 0.02 wt%, 1 wt% and 1 wt% in sequence;
(3) ultrasonically treating an alumina ceramic membrane tube with the aperture of about 50cm after cutting for 5 hours, soaking the alumina ceramic membrane tube with the aperture of 100nm for 24 hours by using 2mol/L sodium hydroxide, drying the tube for 10 hours at the temperature of 100 ℃, washing the ceramic membrane tube by using cellulose after cooling, then washing the ceramic membrane tube by using ethanol and deionized water for a plurality of times in sequence, drying the tube for 12 hours at the temperature set value of 100 ℃ in a drying oven, and cooling the tube along with the oven to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a 2 mmol/L3-aminopropyltriethoxysilane ethanol solution, reacting for 12 hours at room temperature, washing with ethanol and deionized water for several times, drying for 12 hours in a drying oven at a set temperature of 150 ℃, and cooling with the oven to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride with the concentration of 2 wt%, carrying out soaking and blow-drying after reacting for 10min at room temperature, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after reacting for 10min at room temperature; repeating the step for 1 time;
(6) and (5) placing the material obtained in the step (5) in a shade place for air drying, then placing the material in a 50 ℃ oven for heat treatment for 15min, and then cooling along with the oven to obtain the contrast film.
Testing the performance of the membrane tube: the comparative film obtained in this comparative example was tested at room temperature and a pressure of 0.69MPa, and had a pure water flux of 65LHM and a rejection of 95% for a 0.2 wt% solution of magnesium sulfate.
And (3) acid and alkali resistance test: after the comparative membrane prepared in the comparative example is respectively soaked in a nitric acid solution with the pH value of 2 and a sodium hydroxide solution with the pH value of 12 for 168 hours at the temperature of 85 ℃, the pure water flux is respectively 64 LHM and 63.8LHM, the retention rates are respectively 94.2 percent and 94.6 percent, and the performance is basically kept unchanged.
Example 1
(1) Preparing a molybdenum disulfide oxide aqueous solution with the concentration of 3mg/mL by using an improved Hummers method, adding dopamine hydrochloride, and adjusting the pH value to 8.5 by using a Tris-HCl buffer solution to obtain a mixed suspension; magnetically stirring the mixed suspension at 60 ℃ to react for 12 hours, and then carrying out centrifugal water washing to remove unreacted dopamine hydrochloride completely to obtain a dopamine modified molybdenum disulfide oxide aqueous solution;
(2) fully mixing the dopamine modified molybdenum oxide disulfide aqueous solution, piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution, wherein the content of the dopamine modified molybdenum oxide disulfide, piperazine, PEG1000 and diethylamine in the aqueous phase solution is 0.02 wt%, 1 wt% and 1 wt% in sequence;
(3) ultrasonically treating an alumina ceramic membrane tube with the aperture of about 50cm after cutting for 5 hours, soaking the alumina ceramic membrane tube with the aperture of 100nm for 24 hours by using 2mol/L sodium hydroxide, drying the tube for 10 hours at the temperature of 100 ℃, washing the ceramic membrane tube by using cellulose after cooling, then washing the ceramic membrane tube by using ethanol and deionized water for a plurality of times in sequence, drying the tube for 12 hours at the temperature set value of 100 ℃ in a drying oven, and cooling the tube along with the oven to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a 2 mmol/L3-aminopropyltriethoxysilane ethanol solution, reacting for 12 hours at room temperature, washing with ethanol and deionized water for several times, drying for 12 hours in a drying oven at a set temperature of 150 ℃, and cooling with the oven to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride with the concentration of 2 wt%, carrying out soaking and blow-drying after reacting for 10min at room temperature, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after reacting for 10min at room temperature; repeating the step for 1 time;
(6) and (5) placing the material obtained in the step (5) in a shade place for air drying, then placing the material in a 50 ℃ oven for heat treatment for 15min, and then cooling along with the oven to obtain the dopamine modified molybdenum oxide disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
Testing the performance of the membrane tube: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is tested under the conditions of room temperature and pressure of 0.69MPa, the pure water flux is 82LHM, and the rejection rate of 0.2 wt% magnesium sulfate solution is 98%.
And (3) acid and alkali resistance test: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is respectively placed in a nitric acid solution with the pH value of 2 and a sodium hydroxide solution with the pH value of 12, after the membrane is soaked for 168 hours at the temperature of 85 ℃, pure water flux is respectively 80LHM and 79LHM, retention rates are respectively 96.7% and 97.4%, and performances are basically kept unchanged.
Example 2
(1) Preparing a dopamine modified molybdenum disulfide oxide aqueous solution with the concentration of 1mg/mL by using an improved Hummers method, adding dopamine hydrochloride, and adjusting the pH value to 8.5 by using a Tris-HCl buffer solution to obtain a mixed suspension; magnetically stirring the mixed suspension at 60 ℃ to react for 12 hours, and then carrying out centrifugal water washing to remove unreacted dopamine hydrochloride completely to obtain a dopamine modified molybdenum disulfide oxide aqueous solution;
(2) fully mixing the dopamine modified molybdenum oxide disulfide aqueous solution, piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution, wherein the content of the dopamine modified molybdenum oxide disulfide, piperazine, PEG1000 and diethylamine in the aqueous phase solution is 0.01 wt%, 3 wt%, 1 wt% and 1 wt% in sequence;
(3) ultrasonically treating an alumina ceramic membrane tube with the aperture of 80nm and the length of about 50cm after cutting for 10 hours, soaking the alumina ceramic membrane tube in 5mol/L sodium hydroxide for 24 hours, drying the tube for 10 hours at the temperature of 100 ℃, washing the ceramic membrane tube by using cellulose after cooling, then washing the ceramic membrane tube by using ethanol and deionized water for a plurality of times in sequence, drying the tube for 12 hours at the temperature of 100 ℃ in a drying oven, and cooling the tube along with the oven to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a 2 mmol/L3-aminopropyltriethoxysilane ethanol solution, reacting for 12 hours at room temperature, washing with ethanol and deionized water for several times, drying for 12 hours in a drying oven at a set temperature of 150 ℃, and cooling with the oven to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride with the concentration of 2 wt%, carrying out soaking and blow-drying after reacting for 3min at room temperature, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after reacting for 3min at room temperature; repeating the step for 1 time;
(6) and (5) placing the material obtained in the step (5) in a shade place for air drying, then placing the material in an oven at 80 ℃ for heat treatment for 15min, and then cooling along with the oven to obtain the dopamine modified molybdenum oxide disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
Testing the performance of the membrane tube: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is tested under the conditions of room temperature and pressure of 0.69MPa, the pure water flux is 80LHM, and the rejection rate of 0.2 wt% magnesium sulfate solution is 97%.
And (3) acid and alkali resistance test: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is respectively placed in a nitric acid solution with the pH value of 2 and a sodium hydroxide solution with the pH value of 12, after the membrane is soaked for 168 hours at the temperature of 85 ℃, pure water fluxes are respectively 78LHM and 75LHM, retention rates are respectively 95.3% and 96.4%, and performances are basically kept unchanged.
Example 3
(1) Preparing a dopamine modified molybdenum disulfide oxide aqueous solution with the concentration of 5mg/mL by using an improved Hummers method, adding dopamine hydrochloride, and adjusting the pH value to 8.5 by using a Tris-HCl buffer solution to obtain a mixed suspension; magnetically stirring the mixed suspension at 60 ℃ to react for 12 hours, and then carrying out centrifugal water washing to remove unreacted dopamine hydrochloride completely to obtain a dopamine modified molybdenum disulfide oxide aqueous solution;
(2) fully mixing the dopamine modified molybdenum oxide disulfide aqueous solution, piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution, wherein the content of the dopamine modified molybdenum oxide disulfide, piperazine, PEG1000 and diethylamine in the aqueous phase solution is 0.05 wt%, 0.2 wt%, 1 wt% and 1 wt% in sequence;
(3) ultrasonically treating an aluminum oxide ceramic membrane tube with the length of about 50cm and the aperture of 10m for 10 hours after cutting, soaking the aluminum oxide ceramic membrane tube in 2mol/L sodium hydroxide for 24 hours, drying the aluminum oxide ceramic membrane tube for 10 hours at the temperature of 100 ℃, washing the ceramic membrane tube by using cellulose after cooling, then washing the ceramic membrane tube by using ethanol and deionized water for a plurality of times in sequence, drying the ceramic membrane tube for 12 hours at the temperature set value of 100 ℃ in a drying oven, and cooling the ceramic membrane tube along with the oven to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a 2 mmol/L3-aminopropyltriethoxysilane ethanol solution, reacting for 12 hours at room temperature, washing with ethanol and deionized water for several times, drying for 12 hours in a drying oven at a set temperature of 150 ℃, and cooling with the oven to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a normal hexane solution of trimesoyl chloride with the concentration of 10 wt%, carrying out soaking and blow-drying after reacting for 15min at room temperature, soaking in the aqueous phase solution prepared in the step (2), and carrying out soaking and blow-drying after reacting for 15min at room temperature; repeating the step for 1 time;
(6) and (5) placing the material obtained in the step (5) in a shade place for air drying, then placing the material in a 50 ℃ oven for heat treatment for 15min, and then cooling along with the oven to obtain the dopamine modified molybdenum oxide disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
Testing the performance of the membrane tube: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is tested under the conditions of room temperature and pressure of 0.69MPa, the pure water flux is 75LHM, and the rejection rate of 0.2 wt% magnesium sulfate solution is 95%.
And (3) acid and alkali resistance test: the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane prepared in the embodiment is respectively placed in a nitric acid solution with the pH value of 2 and a sodium hydroxide solution with the pH value of 12, after the membrane is soaked for 168 hours at the temperature of 85 ℃, pure water fluxes are respectively 75.6 LHM and 74.9LHM, retention rates are respectively 93.2% and 92.9%, and performances are basically kept unchanged.
The above description is only a preferred embodiment of the present invention, and therefore should not be taken as limiting the scope of the invention, which is defined by the appended claims.

Claims (10)

1. A dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane is characterized in that: the organic functional layer is formed by taking a water phase monomer, an organic phase monomer and an acid acceptor as raw materials and performing interfacial polymerization reaction on the porous ceramic membrane support;
the water phase monomer contains dopamine modified molybdenum disulfide oxide and piperazine;
the organic phase monomer is trimesoyl chloride;
the acid acceptor is polyamine;
the amino group on the silane coupling agent reacts with trimesoyl chloride to be connected.
2. The dopamine-modified molybdenum oxide disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane according to claim 1, wherein the dopamine-modified molybdenum oxide-doped piperazine polyamide composite ceramic nanofiltration membrane comprises: the polyamine is diethylamine.
3. The dopamine-modified molybdenum oxide disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane according to claim 1, wherein the dopamine-modified molybdenum oxide-doped piperazine polyamide composite ceramic nanofiltration membrane comprises: the aperture of the porous ceramic membrane support is 10-100 nm.
4. The dopamine-modified molybdenum oxide disulfide-doped piperazine polyamide composite ceramic nanofiltration membrane according to claim 1, wherein the dopamine-modified molybdenum oxide-doped piperazine polyamide composite ceramic nanofiltration membrane comprises: the material of the porous ceramic membrane support body is alumina, titanium oxide or zirconium oxide.
5. The nanofiltration membrane of any one of claims 1 to 4, wherein the dopamine-modified molybdenum disulfide oxide-doped piperazine polyamide composite ceramic nanofiltration membrane comprises: the mass ratio of the piperazine to the dopamine modified molybdenum disulfide oxide to the polyamine is 0.2-3: 0.01-0.05: 1.
6. The preparation method of the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane according to any one of claims 1 to 5, wherein the preparation method comprises the following steps: the method comprises the following steps: preparing molybdenum disulfide oxide by an improved Hummers method, and reacting the molybdenum disulfide oxide with dopamine hydrochloride to prepare dopamine modified molybdenum disulfide oxide; and (2) taking the mixture of the dopamine modified molybdenum disulfide oxide and piperazine as a water phase monomer, taking phthaloyl chloride as an organic monomer, taking polyamine as an acid acceptor, and forming the organic functional layer on the porous ceramic membrane support activated by strong alkali and grafted with the silane coupling agent through interfacial polymerization, wherein amino on the silane coupling agent reacts with trimesoyl chloride to be connected, so that the dopamine modified molybdenum disulfide oxide doped piperazine polyamide composite ceramic nanofiltration membrane is obtained.
7. The method of claim 6, wherein: the method comprises the following steps:
(1) preparing a molybdenum disulfide oxide aqueous solution by using an improved Hummers method, adding dopamine hydrochloride, and adjusting the pH to 8.5 by using a Tris-HCl buffer solution to obtain a mixed suspension; magnetically stirring the mixed suspension at 58-62 ℃ for reaction for 11-13h, and then carrying out centrifugal water washing to remove unreacted dopamine hydrochloride completely to obtain a dopamine modified molybdenum disulfide oxide aqueous solution;
(2) fully mixing the dopamine modified molybdenum disulfide oxide aqueous solution, piperazine aqueous solution, PEG1000 and polyamine to obtain an aqueous phase solution;
(3) after ultrasonic treatment, soaking the ceramic membrane support body in a strong alkali solution for activation treatment, and then drying to obtain an activated ceramic membrane support body;
(4) soaking the activated ceramic membrane support body in a silane coupling agent solution, then cleaning with ethanol and water, and drying to obtain a grafted ceramic membrane support body;
(5) soaking the grafted ceramic membrane support body in a n-hexane solution of trimesoyl chloride, carrying out soaking and blow-drying after room temperature reaction, soaking in the water phase solution prepared in the step (2), and carrying out soaking and blow-drying after room temperature reaction; repeating the step at least 1 time;
(6) and (5) drying the material obtained in the step (5) in the shade, then carrying out heat treatment at 50-80 ℃, and then cooling along with a furnace to obtain the dopamine modified molybdenum oxide and molybdenum disulfide doped piperazine polyamide composite ceramic nanofiltration membrane.
8. The method of claim 7, wherein: in the aqueous phase solution, the concentration of the piperazine is 0.2-3 wt%, the concentration of the dopamine modified molybdenum disulfide oxide is 0.01-0.05 wt%, and the concentration of the polyamine is 1 wt%.
9. The method of claim 9, wherein: in the aqueous phase solution, the concentration of the PEG1000 is 0.8-1.2 wt%.
10. The method of claim 7, wherein: the concentration of the n-hexane solution of trimesoyl chloride is 2-10 wt%.
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