CN111151145A - Super-hydrophobic separation membrane and preparation method and application thereof - Google Patents

Super-hydrophobic separation membrane and preparation method and application thereof Download PDF

Info

Publication number
CN111151145A
CN111151145A CN201811326859.6A CN201811326859A CN111151145A CN 111151145 A CN111151145 A CN 111151145A CN 201811326859 A CN201811326859 A CN 201811326859A CN 111151145 A CN111151145 A CN 111151145A
Authority
CN
China
Prior art keywords
separation membrane
inorganic
super
acid
organic
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.)
Granted
Application number
CN201811326859.6A
Other languages
Chinese (zh)
Other versions
CN111151145B (en
Inventor
赵宇鑫
薛铭
刘全桢
李娜
方煜
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.)
China Petroleum and Chemical Corp
Sinopec Safety Engineering Research Institute Co Ltd
Original Assignee
China Petroleum and Chemical Corp
Sinopec Qingdao Safety Engineering Institute
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 China Petroleum and Chemical Corp, Sinopec Qingdao Safety Engineering Institute filed Critical China Petroleum and Chemical Corp
Priority to CN201811326859.6A priority Critical patent/CN111151145B/en
Publication of CN111151145A publication Critical patent/CN111151145A/en
Application granted granted Critical
Publication of CN111151145B publication Critical patent/CN111151145B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0202Separation of non-miscible liquids by ab- or adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/08Thickening liquid suspensions by filtration
    • B01D17/085Thickening liquid suspensions by filtration with membranes
    • 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
    • B01D2323/00Details relating to membrane preparation
    • B01D2323/50Control of the membrane preparation process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/38Hydrophobic membranes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention belongs to the field of separation membranes, and discloses a super-hydrophobic separation membrane, a preparation method of the super-hydrophobic separation membrane and application of the super-hydrophobic separation membrane in oil-water separation. The super-hydrophobic separation membrane comprises a substrate and nano sheets loaded on the substrate, wherein the nano sheets are formed by inorganic-organic coordination polymers, and the inorganic-organic coordination polymers are formed by coordination of transition elements and organic carboxylic acids. The super-hydrophobic separation membrane can be used for quickly and efficiently separating various grease, can be repeatedly used and has a simple preparation method.

Description

Super-hydrophobic separation membrane and preparation method and application thereof
Technical Field
The invention relates to the field of separation membranes, in particular to a super-hydrophobic separation membrane, a preparation method of the super-hydrophobic separation membrane and application of the super-hydrophobic separation membrane in oil-water separation.
Background
Oily sewage is widely available, such as petrochemical, oil extraction, mechanical processing, transportation, leather, textile, food, medicine, etc. About ten million tons of oil in the world flow into the ocean by various ways every year, and the oily sewage has high Chemical Oxygen Demand (COD), large oil content and serious environmental pollution, and particularly the leakage of petroleum and harmful industrial poisons is a very concern. The transportation, storage and use of petroleum are ubiquitous, and the aspects require huge cleaning cost, so that the oil-water separation material and the technology have important scientific and technological significance and application prospects in the fields of environmental management, oil recovery and recycling and the like.
The main methods for oil-water separation include gravity settling, centrifugation, adsorption, flotation, emulsion breaking, and chemical methods. Some traditional treatment methods have low separation efficiency, and some have the problems of secondary pollution caused by adding excessive chemical agents, too high energy consumption, large occupied area, long use time and the like. In recent years, new laws and regulations have stricter limits on the degree of environmental pollution, so that the traditional oil-water separation method is difficult to meet the requirements. In the presence of complex conventional processes, membrane separation techniques have significant advantages: the energy consumption is low; the separation efficiency is high; almost zero emission is achieved; the space is saved; simple and convenient operation and the like. At present, membranes for treating oily sewage comprise organic membranes, microfiltration membranes and ultrafiltration membranes made of modified composite membranes and the like, the traditional separation membranes are easily polluted, and preparation conditions have certain limitations, so that the development of an oil-water separation membrane with super-hydrophobic property has great significance.
Disclosure of Invention
The invention aims to provide a super-hydrophobic separation membrane which can be used for separating various grease rapidly and efficiently and can be reused, a preparation method thereof and application of the super-hydrophobic separation membrane in oil-water separation.
The invention provides a super-hydrophobic separation membrane, which comprises a substrate and nano sheets loaded on the substrate, wherein the nano sheets are formed by inorganic-organic coordination polymers, and the inorganic-organic coordination polymers are formed by coordination of transition elements and organic carboxylic acids.
Preferably, the transition element is Ni; the organic carboxylic acid is one or more of 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid, 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid.
Preferably, the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-benzenedicarboxylic acid.
Preferably, the organic carboxylic acid contains a functionalized functional group, the functionalized functional group being-CH3、 -CHO、-COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、 -COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、 -NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
Preferably, the size of the nano-sheet is 1.8-12 μm, and the thickness of the nano-sheet is 1.9-10 nm;
preferably, the substrate is a porous carrier, and the pore diameter of the substrate is 5-80 μm.
Preferably, the content of the nano-sheets is 3-9.5 wt% based on the total weight of the super-hydrophobic separation membrane.
The invention also provides a preparation method of the super-hydrophobic separation membrane, which comprises the following steps:
1) a step of preparing an inorganic-organic coordination polymer crystal;
2) a step of exfoliating the nanosheets from the inorganic-organic coordination polymer crystals;
3) a step of bringing the suspension containing the nanoplatelets into contact with a porous substrate and removing the solvent,
wherein the inorganic-organic coordination polymer is formed by coordination of a transition element and an organic carboxylic acid.
Preferably, the transition element is Ni; the organic carboxylic acid is one or more of 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid, 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid.
Preferably, the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-benzenedicarboxylic acid.
Preferably, the organic carboxylic acid contains a functionalized functional group, the functionalized functional group being-CH3、 -CHO、-COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、 -COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、 -NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
Preferably, the method of exfoliating nanoplatelets from said inorganic-organic coordination polymer crystals comprises: the suspension containing the inorganic-organic coordination polymer crystals was subjected to ultrasonic treatment, and then the non-exfoliated crystal particles were removed by centrifugation.
Preferably, the method of exfoliating nanoplatelets from said inorganic-organic coordination polymer crystals comprises: the step of subjecting the suspension containing the inorganic-organic coordination polymer crystals to heat treatment and then to freezing treatment is repeated, and then the non-exfoliated crystal particles are removed by centrifugation.
Preferably, the substrate is a porous carrier, and the pore diameter of the substrate is 5-80 μm;
preferably, the suspension containing the nanoplatelets is contacted with the porous substrate in such a way that the suspension containing the nanoplatelets is coated on the porous substrate.
In addition, the invention also provides application of the super-hydrophobic separation membrane in oil-water separation.
According to the super-hydrophobic separation membrane, the nano-sheets formed by the inorganic-organic coordination polymer are loaded on the porous carrier, so that the separation effect of the super-hydrophobic separation membrane on oil-water separation can be improved, the super-hydrophobic separation membrane can be repeatedly used, and the preparation method is simple.
Additional features and advantages of the invention will be set forth in the detailed description which follows.
Drawings
FIG. 1 is an XRD pattern of the inorganic-organic coordination polymer crystals prepared in example 1;
FIG. 2 is a scanning electron microscope photograph of the crystals of the inorganic-organic coordination polymer prepared in example 1;
FIG. 3 is a TEM spectrum of the two-dimensional nanoplate prepared in example 1;
FIG. 4 is a photograph of a contact angle of the two-dimensional superhydrophobic separation membrane prepared in example 1 to oil droplets (1, 2-dichloroethane) in air;
FIG. 5 is a photograph showing an oil-water separation experiment according to the present invention, in which a shows a photograph before oil-water separation and b shows a photograph after oil-water separation.
Detailed Description
The endpoints of the ranges and any values disclosed herein are not limited to the precise range or value, and such ranges or values should be understood to encompass values close to those ranges or values. For ranges of values, between the endpoints of each of the ranges and the individual points, and between the individual points may be combined with each other to give one or more new ranges of values, and these ranges of values should be considered as specifically disclosed herein.
The following describes in detail specific embodiments of the present invention. It should be understood that the detailed description and specific examples, while indicating the present invention, are given by way of illustration and explanation only, not limitation.
In the present invention, the term "inorganic-organic coordination polymer" refers to a periodic network structure formed by bonding an inorganic metal center (single metal or metal cluster) and an organic small molecule ligand.
The invention provides a super-hydrophobic separation membrane, which comprises a substrate and nano sheets loaded on the substrate, wherein the nano sheets are formed by inorganic-organic coordination polymers, and the inorganic-organic coordination polymers are formed by coordination of transition elements and organic carboxylic acids.
According to the superhydrophobic separation membrane of the present invention, the transition element is preferably Ni.
The superhydrophobic separation membrane according to the present invention is not particularly limited, and the organic carboxylic acid is preferably a dibasic acid. Specifically, the organic carboxylic acid may be, for example, 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid (H)2BDC), 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid; preferably, the organic carboxylic acid is 5-tert-butyl-1, 3-benzenedicarboxylic acid.
In addition, the molar ratio of the inorganic element in the inorganic-organic coordination polymer to the inorganic element and the organic ligand in the inorganic-organic coordination polymer is preferably 1: 0.6-1.5, more preferably 1: 0.6-1.1.
In a preferred embodiment of the present invention, the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-phthalic acid.
In the present invention, the organic carboxylic acid may be any of various organic carboxylic acids having a functional group, and preferably, the organic carboxylic acid has a functional group-CH3、-CHO、 -COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、 -COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、-NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
According to the super-hydrophobic separation membrane, the size of the nano sheet is 1.8-12 μm, and the thickness of the nano sheet is 1.9-10 nm; more preferably; the size of the nano sheet is 2-10 μm, and the thickness of the nano sheet is 2-8 nm. Here, "size of nanosheet" means the longest straight-line distance between two points of the nanosheet; similarly, the thickness of the nanosheet refers to the longest distance between two points in the thickness direction perpendicular to a straight line.
The super-hydrophobic separation membrane according to the present invention, which is not particularly limited to the porous substrate, may be any existing support having a porous structure, for example, a porous support of a metal or a non-metal material, including, but not limited to, a stainless steel mesh, a nickel mesh, a copper mesh, an aluminum mesh, porous alumina, porous silica, and the like.
The pore size of the substrate is also not particularly limited, and preferably, the pore size of the substrate is 5 to 80 μm.
The thickness of the substrate is also not particularly limited, and is preferably 500nm to 3 μm, more preferably 0.5 to 2 μm.
According to the superhydrophobic separation membrane of the present invention, the content of the nano sheet is preferably 3-9.5 wt%, more preferably 4-9 wt%, based on the total weight of the superhydrophobic separation membrane.
The invention also provides a preparation method of the super-hydrophobic separation membrane, which comprises the following steps:
1) a step of preparing an inorganic-organic coordination polymer crystal;
2) a step of exfoliating the nanosheets from the inorganic-organic coordination polymer crystals;
3) a step of bringing the suspension containing the nanoplatelets into contact with a porous substrate and removing the solvent,
wherein the inorganic-organic coordination polymer is formed by coordination of a transition element and an organic carboxylic acid.
According to the method for preparing the superhydrophobic separation membrane of the present invention, the transition element is preferably Ni.
According to the method for preparing the super-hydrophobic separation membrane, the organic carboxylic acid is subjected toThe acid is not particularly limited, but is preferably a dibasic acid. Specifically, the organic carboxylic acid may be, for example, 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid (H)2BDC), 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid; preferably, the organic carboxylic acid is 5-tert-butyl-1, 3-benzenedicarboxylic acid.
In addition, the molar ratio of the inorganic element in the inorganic-organic coordination polymer to the inorganic element and the organic ligand in the inorganic-organic coordination polymer is preferably 1: 0.6-1.5, more preferably 1: 0.62-1.1.
In a preferred embodiment of the present invention, the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-phthalic acid.
In the present invention, the organic carboxylic acid may be any of various organic carboxylic acids having a functional group, and preferably, the organic carboxylic acid has a functional group-CH3、、 -CHO、-COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、 -COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、-NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
According to the method for preparing a superhydrophobic separation membrane of the present invention, the inorganic-organic coordination polymer crystals can be obtained by a method generally used in the art for preparing inorganic-organic coordination polymer crystals. For example, the organic carboxylic acid can be obtained by heat-treating a solution containing an organic carboxylic acid and a salt containing a transition element. Specifically, the solution containing the organic carboxylic acid and the salt containing the transition element may be reacted at a temperature of 190 ℃ to 220 ℃ at a temperature rate of 1 to 3 ℃/min in an autoclave for 6 to 48 hours.
According to the preparation method of the super-hydrophobic separation membrane, preferably, the method for stripping the nanosheets from the inorganic-organic coordination polymer crystals comprises the following steps: subjecting a suspension containing inorganic-organic coordination polymer crystals to ultrasonic treatment, and then removing non-exfoliated crystal particles by centrifugation; or comprises the following steps: the step of subjecting the suspension containing the inorganic-organic coordination polymer crystals to heat treatment and then to freezing treatment is repeated, and then the non-exfoliated crystal particles are removed by centrifugation.
Preferably, the ultrasonic treatment conditions include: the ultrasonic power is 80-120W, the ultrasonic temperature is 10-40 ℃, and the ultrasonic time is 10-30 min.
Preferably, the conditions of the above heat treatment include: the heat treatment temperature is 60-100 deg.C, and the heat treatment time is 3-5 min.
Preferably, the conditions of the freezing treatment include: the freezing temperature is-40 to-196 ℃, and the freezing time is based on complete freezing.
Preferably, the step of subjecting the suspension containing the inorganic-organic coordination polymer crystals to heat treatment and then to freezing treatment is repeated 3 to 5 times.
Preferably, the content of the inorganic-organic coordination polymer crystals in the above suspension containing inorganic-organic coordination polymer crystals is 0.1 to 1.5 mg/mL.
Preferably, the conditions of the centrifugation include: the centrifugation temperature is 10-40 ℃, the centrifugation speed is 8000-12000r.p.m, and the centrifugation time is 10-30 min.
In order to further increase the purity of the nanosheets obtained, the resulting colloidal suspension is preferably allowed to stand for 1-4 weeks after the non-exfoliated crystalline particles are removed by centrifugation.
The method for preparing the superhydrophobic separation membrane according to the present invention is not particularly limited, and may be any existing support having a porous structure, for example, a porous support of a metal or a non-metal material, including, but not limited to, a stainless steel mesh, a nickel mesh, a copper mesh, an aluminum mesh, porous alumina, porous silica, and the like.
The pore size of the substrate is also not particularly limited, and preferably, the pore size of the substrate is 5 to 80 μm.
The thickness of the substrate is also not particularly limited, and is preferably 500nm to 3 μm, more preferably 0.5 to 2 μm.
According to the preparation method of the superhydrophobic separation membrane of the present invention, preferably, the suspension containing the nanosheets is contacted with the porous substrate in such a manner that the suspension containing the nanosheets is coated on the porous substrate.
According to the method for preparing the superhydrophobic separation membrane of the present invention, preferably, the solvent is removed by drying.
According to the preparation method of the superhydrophobic separation membrane of the present invention, preferably, the suspension containing the nano-sheets is used in an amount such that the content of the nano-sheets is 3 to 9.5 wt%, more preferably 4 to 9 wt%, based on the total weight of the superhydrophobic separation membrane.
In addition, the invention also provides application of the super-hydrophobic separation membrane in oil-water separation.
The oil phase which can be separated by the super-hydrophobic separation membrane provided by the invention comprises pure components which are not dissolved in water and low-polarity solvents such as petroleum, vegetable oil, gasoline, diesel oil, n-hexane, cyclohexane, n-heptane, n-octane, n-butanol, ethyl acetate, benzene, toluene, chloroform and the like or a mixture of the pure components.
The water phase that can be separated by the super-hydrophobic separation membrane provided by the invention includes, but is not limited to, pure water, aqueous sodium chloride solution, aqueous potassium chloride solution, aqueous copper chloride solution, aqueous iron chloride solution, aqueous sodium nitrate solution, aqueous potassium nitrate solution, aqueous copper sulfate solution and other pure water solutions with single solute or mixed solution thereof.
The present invention will be described in detail below by way of examples, but the present invention is not limited to the following examples.
The surface morphology of the nano-sheet prepared by the invention is observed through a transmission electron microscope spectrogram (purchased from JSM-2200FS model of JEOL company).
The surface appearance of the super-hydrophobic separation membrane prepared by the invention is observed by a scanning electron microscope (purchased from JEOL JSM-6510A).
The contact angle was measured by a contact angle measuring instrument (purchased from shanghai chinno precision instruments ltd. CA100A model), the volume of the sample used was 5uL, six positions were selected at different positions for the same sample to be measured, and the average value was taken as the hydrophobic angle of the sample.
In the case where no particular mention is made, commercially available products are used as the starting materials.
Example 1
(1) Synthetic crystal
0.075g of 5-tert-butyl-1, 3-phthalic acid and 0.15g of nickel nitrate hexahydrate are suspended in 7.5mL of 20 v% ethylene glycol aqueous solution, then the mixture is placed into a 20mL autoclave, heated to 210 ℃ at a heating rate of 2 ℃/min, and after 24h, the reaction is stopped by cooling to room temperature, and light green needle crystals are obtained. Washing with deionized water and methanol for 5 times to completely remove residual ligand and metal salt, and drying at 60 deg.C to obtain inorganic-organic coordination polymer crystal formed by coordination of nickel and 5-tert-butyl-1, 3-phthalic acid.
(2) Stripping the nano-sheets:
treating the n-hexane suspension containing nanosheet crystals at a concentration of 1.0mg/mL in an ultrasonic bath for 20min (ultrasonic power of 100W and ultrasonic temperature of 25 ℃), centrifuging at 10000 r.p.m. for 20min to obtain a colloidal suspension of the nanosheets to remove non-exfoliated particles, and further purifying the nanosheets by allowing the colloidal suspension to stand for about 1 week.
(3) Preparation of two-dimensional super-hydrophobic separation membrane
And (3) dripping the n-hexane suspension containing the stripped nano sheets on a stainless steel net in a manner that the content of the nano sheets in the obtained two-dimensional super-hydrophobic separation membrane is 4.02 wt%, and heating a treated stainless steel net carrier (the mesh is 400 meshes, and the thickness is 2 microns) on an electric hot plate to keep the liquid drop temperature at 100 ℃ so as to completely evaporate the n-hexane, thereby obtaining the two-dimensional super-hydrophobic separation membrane A1.
FIG. 1 is an XRD pattern of the inorganic-organic coordination polymer crystal prepared in this example, from which it can be seen that Ni and an organic carboxylic acid coordinated inorganic-organic coordination polymer crystal were successfully synthesized by a solvothermal method; the sharp peak type shows that the diffraction intensity is high, and the synthesized crystal has good crystallinity.
FIG. 2 is a scanning electron microscope photograph of an inorganic-organic coordination polymer crystal prepared in this example, from which it can be seen that the inorganic-organic coordination polymer crystal has a layered structure; the atoms in each layer of the 2D layered structure are linked by strong covalent and coordination bonds, while the layers are loosely linked together by van der waals interactions, which are easily broken to give the nanosheets.
Fig. 3 is a transmission electron microscope spectrogram of the two-dimensional nanosheet prepared in this example, from which it can be seen that the size of the two-dimensional nanosheet is 10 μm and the thickness is 2 nm.
According to a scanning electron microscope picture of the two-dimensional super-hydrophobic separation membrane prepared by the embodiment, the two-dimensional nanosheets are loaded on the porous metal substrate in a wrapping manner.
The contact angle of the two-dimensional super-hydrophobic separation membrane prepared in the embodiment to a water drop in air is 151 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in air is verified.
Fig. 4 is a photograph of a contact angle of the two-dimensional super-hydrophobic separation membrane prepared in this example to an oil drop (1, 2-dichloroethane) in air, wherein the contact angle is 0 degree, and the super-oleophilic property of the two-dimensional super-hydrophobic separation membrane is verified.
Example 2
(1) Synthetic crystal
0.075g of 5-tert-butyl-1, 3-phthalic acid and 0.15g of zinc nitrate hexahydrate are suspended in 7.5mL of 20 v% aqueous ethylene glycol solution, and then the mixture is placed into a 20mL autoclave and heated to 210 ℃ at a heating rate of 2 ℃/min for 24h, and then the reaction is stopped by cooling to room temperature to obtain pale green needle crystals. Washing with deionized water and methanol for 5 times to completely remove residual ligand and metal salt, and drying at 60 deg.C to obtain inorganic-organic coordination polymer crystal formed by coordination of zinc and 5-tert-butyl-1, 3-phthalic acid.
(2) Stripping the nano-sheets:
bulk crystals were dispersed in n-hexane at a concentration of 1.0mg/mL and heated in a hot water bath (80 ℃) for 3min, then immediately cooled in a liquid nitrogen bath (-196 ℃) until completely frozen. After that, the solidified mixture was thawed again in a hot water bath (80 ℃). The freeze-thaw cycle was repeated 3 times depending on the solvent. And centrifuging at 10000r.p.m for 20min to remove the unexfoliated blocky crystals from the supernatant to obtain a colloidal suspension of the nanosheets, and further purifying the nanosheets by allowing the colloidal suspension to stand for about 1 week.
(3) Preparation of two-dimensional super-hydrophobic separation membrane
And (3) dripping the n-hexane suspension containing the stripped nano sheets on a stainless steel net in a manner that the content of the nano sheets in the obtained two-dimensional super-hydrophobic separation membrane is 8.88 wt%, and heating a treated stainless steel net carrier (the mesh is 400 meshes, and the thickness is 2 microns) on an electric hot plate to keep the liquid drop temperature at 100 ℃ so as to completely evaporate the n-hexane, thereby obtaining the two-dimensional super-hydrophobic separation membrane A2.
The size of the two-dimensional nanosheet is 2 μm and the thickness is 8nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150.4 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 3
(1) Synthesis of bulk crystals and (2) exfoliation of the nanosheets was the same as in example 2.
(3) Preparation of two-dimensional super-hydrophobic separation membrane
And (3) dripping the n-hexane suspension containing the stripped nano sheets on a stainless steel net in a manner that the content of the nano sheets in the obtained two-dimensional super-hydrophobic separation membrane is 4.44 wt%, and heating a treated stainless steel net carrier (500 meshes, the thickness of 2 mu m) on an electric hot plate to keep the temperature of the liquid drops at 100 ℃ so as to completely evaporate the n-hexane, thereby obtaining the two-dimensional super-hydrophobic separation membrane A3.
The size of the two-dimensional nanosheet is 8 μm and the thickness is 6nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 151 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 4
(1) Synthesis of bulk crystals and (2) exfoliation of the nanosheets was the same as in example 2.
(3) Preparation of two-dimensional super-hydrophobic separation membrane
And (3) dripping the n-hexane suspension containing the stripped nano sheets on a stainless steel net in a manner that the content of the nano sheets in the obtained two-dimensional separation membrane is 5.01 wt%, and heating the treated stainless steel net carrier (800 meshes and the thickness of 2 mu m) on an electric hot plate to keep the temperature of the liquid drops at 100 ℃ so as to completely evaporate the n-hexane, thereby obtaining the two-dimensional super-hydrophobic separation membrane A4.
The size of the two-dimensional nanosheet is 6 μm and the thickness is 6nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 5
(1) Bulk crystals were synthesized as in example 2.
(2) Exfoliated nanoplatelets are the same as in example 1.
(3) The preparation of the two-dimensional superhydrophobic separation membrane was the same as in example 3, to obtain a two-dimensional superhydrophobic separation membrane a 5.
The size of the two-dimensional nanosheet is 4 μm and the thickness is 4nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150.1 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 6
(1) Bulk crystals were synthesized as in example 2.
(2) Exfoliated nanoplatelets are the same as in example 1.
(3) The preparation of the two-dimensional superhydrophobic separation membrane was the same as in example 4, to obtain a two-dimensional superhydrophobic separation membrane a 6.
The size of the two-dimensional nanosheet is 12 μm and the thickness is 8nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 7
(1) Bulk crystals were synthesized as in example 2.
(2) Stripping the nanosheets:
the crystals were dispersed in ethanol at a concentration of 1.0mg/mL and heated in a hot water bath (80 ℃) for 3min, then immediately cooled in a liquid nitrogen bath (-196 ℃) until complete freezing. After that, the solidified mixture was thawed again in a hot water bath (80 ℃). The freeze-thaw cycle was repeated 5 times depending on the solvent. The non-exfoliated crystal particles were removed from the supernatant by centrifugation at 10000r.p.m for 20min, resulting in a colloidal suspension of nanoplatelets (the tyndall effect was observed), which was further purified by allowing the colloidal suspension to stand for about 1 week.
(3) Preparing a two-dimensional super-hydrophobic separation membrane:
and (3) dripping the n-hexane suspension containing the stripped nano sheets on a stainless steel net in a manner that the content of the nano sheets in the obtained two-dimensional super-hydrophobic separation membrane is 6.03 weight percent, and heating a treated stainless steel net carrier (400 meshes, the thickness of 2 mu m) on an electric hot plate to keep the temperature of the liquid drops at 100 ℃ so as to completely evaporate ethanol, thereby obtaining the two-dimensional super-hydrophobic separation membrane A7.
The size of the two-dimensional nanosheet is 4 μm and the thickness is 8nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150.1 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Example 8
(1) Bulk crystals were synthesized as in example 2.
(2) Stripping the nanosheets:
the ethanol suspension containing crystals with a concentration of 1.0mg/mL is treated in an ultrasonic bath for 20min (ultrasonic power 100W, ultrasonic temperature 25 ℃), a colloidal suspension of the nanoplatelets is obtained after centrifugation at 10000 r.p.m. for 20min to remove the non-exfoliated particles, and further purification of the nanoplatelets is performed by leaving the colloidal suspension to stand for about 1 week.
(3) The two-dimensional superhydrophobic separation membrane was prepared in the same manner as in example 7 to obtain a two-dimensional superhydrophobic separation membrane A8.
The size of the two-dimensional nanosheet is 10 μm and the thickness is 4nm as can be seen from a spectrogram of a transmission electron microscope.
According to a scanning electron microscope picture, the two-dimensional nano sheets are loaded on the porous metal substrate in a wrapping mode.
The contact angle of the two-dimensional super-hydrophobic separation membrane on a water drop in the air is 150 degrees, and the hydrophobic property of the two-dimensional super-hydrophobic separation membrane in the air is verified.
The super-oleophilic property of the oil drop (1, 2-dichloroethane) is verified by a contact angle photo of a two-dimensional super-hydrophobic separation membrane in air, wherein the contact angle photo is 0 degree.
Test example 1
The two-dimensional super-hydrophobic separation membranes prepared in examples 1 to 8 were fixed in an oil-water separation apparatus shown in fig. 5, and a mixture of cyclohexane and water (volume ratio 1: 1) was poured into the oil-water separation apparatus, and the oil phase flowed into a glass bottle rapidly, and the water phase was retained by the super-hydrophobic separation membrane and was not flowed, and after a period of time (40 minutes), no water was dropped, and it was confirmed that the water phase and the oil phase were completely separated.
Test example 2
The two-dimensional superhydrophobic separation membranes prepared according to examples 1-8 were used to separate various oil/water mixtures according to the following methods, and the test structures are shown in table 1.
1) Experimental apparatus as shown in fig. 5, a separation membrane was fixed between two glassware articles shown as a in fig. 5, a glass tube having an outer diameter of 30 mm and a length of 20 cm was attached, the middle was sealed with a silica gel pad, the upper and lower portions of the glassware articles were fixed together with metal clips, the glassware articles were fixed on a stand, a beaker was used as a receiving vessel, and the apparatus was tilted to allow oil to permeate through a hydrophobic membrane (water-dyed blue and oil-dyed red) when testing a light oil/water mixture.
2) Mixing the water phase and the oil phase according to a volume ratio of 1: 1 mixing to obtain an oil-water mixed phase.
3) The oil-water mixed phase was poured into an oil-water separation apparatus shown as a in FIG. 5, and the oil phase rapidly flowed into a beaker.
TABLE 1
Figure RE-GDA0001937458480000161
In test example 2, the super-hydrophobic separation membrane provided by the invention has hydrophobic performance, oil permeates through the membrane and water is trapped under the action of gravity based on good hydrophobicity, an oil phase is collected by a beaker, and a water phase is stably trapped on the membrane and cannot flow through the membrane, so that oil-water separation is effectively realized.
Moreover, as can be seen from table 1, the super-hydrophobic separation membrane provided by the present invention has a separation efficiency of 98.5% or more, a good oil-water separation performance, and can be recycled for many times. In addition, since Dichloromethane (DCM) is slightly soluble in water, the separation efficiency of the mixture of dichloromethane and water is about 96.5%.
The preferred embodiments of the present invention have been described above in detail, but the present invention is not limited thereto. Within the scope of the technical idea of the invention, many simple modifications can be made to the technical solution of the invention, including combinations of various technical features in any other suitable way, and these simple modifications and combinations should also be regarded as the disclosure of the invention, and all fall within the scope of the invention.

Claims (14)

1. The super-hydrophobic separation membrane is characterized by comprising a substrate and nano sheets loaded on the substrate, wherein the nano sheets are formed by inorganic-organic coordination polymers, and the inorganic-organic coordination polymers are formed by coordination of transition elements and organic carboxylic acids.
2. The superhydrophobic separation membrane of claim 1, wherein the transition element is Ni or Zn;
the organic carboxylic acid is one or more of 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid, 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid.
3. The superhydrophobic separation membrane of claim 2, wherein the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-phthalic acid.
4. The superhydrophobic separation membrane of claim 1 or 2, wherein the organic carboxylic acid comprises a functionalized functional group that is-CH3、-CHO、-COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、-COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、-NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
5. The superhydrophobic separation membrane of claim 1, wherein the nanoplatelets have a size of 1.8-12 μ ι η in size and a thickness of 1.9-10 nm;
preferably, the substrate is a porous carrier, and the pore diameter of the substrate is 5-80 μm;
preferably, the content of the nano-sheets is 3-9.5 wt% based on the total weight of the super-hydrophobic separation membrane.
6. A preparation method of a super-hydrophobic separation membrane is characterized by comprising the following steps:
1) a step of preparing an inorganic-organic coordination polymer crystal;
2) a step of exfoliating the nanosheets from the inorganic-organic coordination polymer crystals;
3) a step of bringing the suspension containing the nanoplatelets into contact with a porous substrate and removing the solvent,
wherein the inorganic-organic coordination polymer is formed by coordination of a transition element and an organic carboxylic acid.
7. The production method according to claim 6, wherein the transition element is Ni;
the organic carboxylic acid is one or more of 5-tert-butyl-1, 3-phthalic acid, 1, 4-terephthalic acid, 4 '-biphenyldicarboxylic acid, 2, 6-naphthalenedicarboxylic acid, 1, 4-naphthalenedicarboxylic acid, p-terphenyl-4, 4' -dicarboxylic acid and trans-1, 6-hexadiene diacid.
8. The production method according to claim 7, wherein the transition element is Ni and the organic carboxylic acid is 5-tert-butyl-1, 3-phthalic acid.
9. The production method according to claim 6 or 7, wherein the organic carboxylic acid has a functional group which is a-CH functional group3、-CHO、-COOH、-COOCH3、-NO2、-NH2、-SO3H、-OH、-COCH3、-COCH2CH3、-COC(CH3)=CH2、-CO-OC(CH3)3、-NHCOCH3、-NHCOCH2CH3、-NHCOC(CH3)=CH2and-NHCO-OC (CH)3)3One or more of (a).
10. The production method according to claim 6, wherein the method of exfoliating the nanosheets from the inorganic-organic coordination polymer crystal comprises: the suspension containing the inorganic-organic coordination polymer crystals was subjected to ultrasonic treatment, and then the non-exfoliated crystal particles were removed by centrifugation.
11. The production method according to claim 6, wherein the method of exfoliating the nanosheets from the inorganic-organic coordination polymer crystal comprises: the step of subjecting the suspension containing the inorganic-organic coordination polymer crystals to heat treatment and then to freezing treatment is repeated, and then the non-exfoliated crystal particles are removed by centrifugation.
12. The production method according to claim 6, wherein the substrate is a porous support, and the pore size of the substrate is 5 to 80 μm.
13. The production method according to claim 6, wherein the suspension containing nanosheets is contacted with the porous substrate by coating the suspension containing nanosheets on the porous substrate.
14. Use of the superhydrophobic separation membrane of any one of claims 1-5 or the superhydrophobic separation membrane obtained by the method of any one of claims 6-13 in oil-water separation.
CN201811326859.6A 2018-11-08 2018-11-08 Super-hydrophobic separation membrane and preparation method and application thereof Active CN111151145B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811326859.6A CN111151145B (en) 2018-11-08 2018-11-08 Super-hydrophobic separation membrane and preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811326859.6A CN111151145B (en) 2018-11-08 2018-11-08 Super-hydrophobic separation membrane and preparation method and application thereof

Publications (2)

Publication Number Publication Date
CN111151145A true CN111151145A (en) 2020-05-15
CN111151145B CN111151145B (en) 2022-04-05

Family

ID=70555131

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811326859.6A Active CN111151145B (en) 2018-11-08 2018-11-08 Super-hydrophobic separation membrane and preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN111151145B (en)

Citations (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1771264A (en) * 2002-09-17 2006-05-10 科瓦伦特合伙责任有限公司 Nanofilm compositions with polymeric components
US20060230926A1 (en) * 2005-04-13 2006-10-19 Gkss-Forschungszentrum Geesthacht Gmbh Composite material, in particular composite membrane, and process for the production of the same
CN101912737A (en) * 2010-08-26 2010-12-15 南京工业大学 Method for preparing metal organic frame supported film
CN102617646A (en) * 2012-02-29 2012-08-01 中国科学院宁波材料技术与工程研究所 Preparation method of nanoscale metal organic framework materials
CN102728236A (en) * 2012-06-15 2012-10-17 吉林大学 Coordination polymer membrane material, preparation method for same and application of same in membrane separation
CN102974229A (en) * 2012-12-25 2013-03-20 中国科学院大连化学物理研究所 Layer perforation of two-dimensional layer-shaped metal organic framework and application
US20150047505A1 (en) * 2012-03-27 2015-02-19 The University Of Nottingham Metal-organic frameworks (mof) for gas capture
CN104973593A (en) * 2015-06-18 2015-10-14 湖南大学 Stripping method of stratified materials
CN104984665A (en) * 2015-05-27 2015-10-21 天津工业大学 Preparation method of composite separation membrane
CN204768300U (en) * 2015-08-13 2015-11-18 仲崇立 Organic skeleton gas separation membrane of zeolite iminazole metalloid
CN105148752A (en) * 2015-09-29 2015-12-16 北京林业大学 Polyamide reverse-osmosis composite membrane containing MIL type metal-organic framework material and preparation method thereof
CN105348198A (en) * 2015-09-29 2016-02-24 中能科泰(北京)科技有限公司 Metal organic framework film and preparation method therefor
CN105668530A (en) * 2016-01-14 2016-06-15 苏州微格纳米科技有限公司 Preparation method of two-dimensional nanomaterial
CN105839189A (en) * 2015-01-16 2016-08-10 中国科学院理化技术研究所 Two-dimensional atomic layer thickness ZnO single-crystal nanosheet and preparation method thereof
CN106000118A (en) * 2016-06-06 2016-10-12 西北大学 MOF particle filled silicone rubber pervaporation desulfurization film and preparation method thereof
CN106163647A (en) * 2014-03-26 2016-11-23 应用仿生学有限公司 Film manufacturing method
CN107020014A (en) * 2017-05-04 2017-08-08 天津大学 Using metal-organic framework materials as the method for Simulation moving bed stationary phase Separation of boron isotopes
CN107050928A (en) * 2017-04-28 2017-08-18 华南理工大学 A kind of water-oil separating porous nethike embrane of super-hydrophobic super-oleophylic and preparation method and application
CN107106467A (en) * 2014-12-18 2017-08-29 欧莱雅 Include the composition of stable polymer beads and hydrophobic film-forming polymers
US20170341033A1 (en) * 2016-05-26 2017-11-30 Toyota Jidosha Kabushiki Kaisha Method for manufacturing porous body
CN107875674A (en) * 2017-11-03 2018-04-06 中国日用化学工业研究院 A kind of preparation method of super-hydrophobic super-oleophylic stainless (steel) wire
CN108114612A (en) * 2016-11-26 2018-06-05 中国科学院大连化学物理研究所 Stratiform MOF nanometer sheet composite membranes
CN108404683A (en) * 2018-03-09 2018-08-17 宁夏大学 With high efficiency oil-water separating property ZIF-8/ metal mesh composite membranes and preparation method thereof
CN108465385A (en) * 2018-03-13 2018-08-31 中山大学 A kind of MAF-4 metallic organic frame films and its application
CN108467490A (en) * 2018-03-29 2018-08-31 中国农业科学院蔬菜花卉研究所 Functional metal organic frame porous material and its preparation method and application
US20210016232A1 (en) * 2018-03-29 2021-01-21 G20 Water Technologies Limited Membranes comprising a layer of metal organic framework particles

Patent Citations (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1771264A (en) * 2002-09-17 2006-05-10 科瓦伦特合伙责任有限公司 Nanofilm compositions with polymeric components
US20060230926A1 (en) * 2005-04-13 2006-10-19 Gkss-Forschungszentrum Geesthacht Gmbh Composite material, in particular composite membrane, and process for the production of the same
CN101912737A (en) * 2010-08-26 2010-12-15 南京工业大学 Method for preparing metal organic frame supported film
CN102617646A (en) * 2012-02-29 2012-08-01 中国科学院宁波材料技术与工程研究所 Preparation method of nanoscale metal organic framework materials
US20150047505A1 (en) * 2012-03-27 2015-02-19 The University Of Nottingham Metal-organic frameworks (mof) for gas capture
CN102728236A (en) * 2012-06-15 2012-10-17 吉林大学 Coordination polymer membrane material, preparation method for same and application of same in membrane separation
CN102974229A (en) * 2012-12-25 2013-03-20 中国科学院大连化学物理研究所 Layer perforation of two-dimensional layer-shaped metal organic framework and application
CN106163647A (en) * 2014-03-26 2016-11-23 应用仿生学有限公司 Film manufacturing method
CN107106467A (en) * 2014-12-18 2017-08-29 欧莱雅 Include the composition of stable polymer beads and hydrophobic film-forming polymers
CN105839189A (en) * 2015-01-16 2016-08-10 中国科学院理化技术研究所 Two-dimensional atomic layer thickness ZnO single-crystal nanosheet and preparation method thereof
CN104984665A (en) * 2015-05-27 2015-10-21 天津工业大学 Preparation method of composite separation membrane
CN104973593A (en) * 2015-06-18 2015-10-14 湖南大学 Stripping method of stratified materials
CN204768300U (en) * 2015-08-13 2015-11-18 仲崇立 Organic skeleton gas separation membrane of zeolite iminazole metalloid
CN105148752A (en) * 2015-09-29 2015-12-16 北京林业大学 Polyamide reverse-osmosis composite membrane containing MIL type metal-organic framework material and preparation method thereof
CN105348198A (en) * 2015-09-29 2016-02-24 中能科泰(北京)科技有限公司 Metal organic framework film and preparation method therefor
CN105668530A (en) * 2016-01-14 2016-06-15 苏州微格纳米科技有限公司 Preparation method of two-dimensional nanomaterial
US20170341033A1 (en) * 2016-05-26 2017-11-30 Toyota Jidosha Kabushiki Kaisha Method for manufacturing porous body
CN106000118A (en) * 2016-06-06 2016-10-12 西北大学 MOF particle filled silicone rubber pervaporation desulfurization film and preparation method thereof
CN108114612A (en) * 2016-11-26 2018-06-05 中国科学院大连化学物理研究所 Stratiform MOF nanometer sheet composite membranes
CN107050928A (en) * 2017-04-28 2017-08-18 华南理工大学 A kind of water-oil separating porous nethike embrane of super-hydrophobic super-oleophylic and preparation method and application
CN107020014A (en) * 2017-05-04 2017-08-08 天津大学 Using metal-organic framework materials as the method for Simulation moving bed stationary phase Separation of boron isotopes
CN107875674A (en) * 2017-11-03 2018-04-06 中国日用化学工业研究院 A kind of preparation method of super-hydrophobic super-oleophylic stainless (steel) wire
CN108404683A (en) * 2018-03-09 2018-08-17 宁夏大学 With high efficiency oil-water separating property ZIF-8/ metal mesh composite membranes and preparation method thereof
CN108465385A (en) * 2018-03-13 2018-08-31 中山大学 A kind of MAF-4 metallic organic frame films and its application
CN108467490A (en) * 2018-03-29 2018-08-31 中国农业科学院蔬菜花卉研究所 Functional metal organic frame porous material and its preparation method and application
US20210016232A1 (en) * 2018-03-29 2021-01-21 G20 Water Technologies Limited Membranes comprising a layer of metal organic framework particles

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
HUANG ZHOU,DAPING HE: "Mesoporous-Silica Induced Doped Carbon Nanotubes Growth From Metal-Organic Frameworks", 《NANOSCALE》 *
MEILIN WEI: "A 3D POM-MOF composite based on Ni(II) ion and 2,2"-bipyridy1-3,3"-dicarboxylic acid: Crystal structure and proton conductivity", 《JOURNAL OF SOLID STATE CHEMISTRY》 *
MINGQIU SONG;YUXIN ZHAO: "A stable ZIF-8-coated mesh membrane with micro-/nano architectures produced by a facile fabrication method for high-efficiency oil-water separation", 《SCIENCE CHINA MATERIALS》 *
杨皓程: "有机-无机复合多孔膜制备与应用", 《化学进展》 *

Also Published As

Publication number Publication date
CN111151145B (en) 2022-04-05

Similar Documents

Publication Publication Date Title
Shi et al. Template-free microwave-assisted synthesis of FeTi coordination complex yolk-shell microspheres for superior catalytic removal of arsenic and chemical degradation of methylene blue from polluted water
Tabesh et al. Preparation of γ-Al2O3 nanoparticles using modified sol-gel method and its use for the adsorption of lead and cadmium ions
Raj et al. Underwater oleophobic-super hydrophilic strontium-MOF for efficient oil/water separation
Yue et al. Oil removal from oily water by a low-cost and durable flexible membrane made of layered double hydroxide nanosheet on cellulose support
Sun et al. Super-performance photothermal conversion of 3D macrostructure graphene-CuFeSe2 aerogel contributes to durable and fast clean-up of highly viscous crude oil in seawater
Hou et al. Nanosized bimetal-organic frameworks as robust coating for multi-functional flexible polyurethane foam: Rapid oil-absorption and excellent fire safety
Xu et al. A facile strategy toward ion-imprinted hierarchical mesoporous material via dual-template method for simultaneous selective extraction of lithium and rubidium
Zhang et al. Ultrasound-assisted adsorption of Congo red from aqueous solution using MgAlCO3 layered double hydroxide
Pan et al. Facile fabrication of graphene-based aerogel with rare earth metal oxide for water purification
CN109126893A (en) A kind of oxidation of coal titanium-metal organic frame composite material and preparation method and application
Song et al. Doping MIL-101 (Cr)@ GO in polyamide nanocomposite membranes with improved water flux
Tan et al. Aminated metal‐organic framework (NH2‐MIL‐101 (Cr)) incorporated polyvinylidene (PVDF) hybrid membranes: Synthesis and application in efficient removal of Congo red from aqueous solution
Azhar et al. Cascade applications of robust MIL-96 metal organic frameworks in environmental remediation: Proof of concept
Jiang et al. MgAl layered double oxide: One powerful sweeper of emulsified water and acid for oil purification
Yuan et al. Removal of Cr (VI) from aqueous solutions via simultaneous reduction and adsorption by modified bimetallic MOF-derived carbon material Cu@ MIL-53 (Fe): Performance, kinetics, and mechanism
CN110182770A (en) A kind of preparation method of hydrophobic type hexagonal boron nitride nanosheet
Chen et al. Crumpled graphene balls as rapid and efficient adsorbents for removal of copper ions
Nezhad et al. One-step Preparation of graphene oxide/polypyrrole magnetic nanocomposite and its application in the removal of methylene blue dye from aqueous solution
Shu et al. A free-standing superhydrophobic film for highly efficient removal of water from turbine oil
CN110152500B (en) Separation membrane and preparation method and application thereof
Zhang et al. Hybridization of Al2O3 microspheres and acrylic ester resins as a synergistic absorbent for selective oil and organic solvent absorption
Yao et al. Hydrothermal synthesis of flower-like Cu2MoS4/g-C3N4 composite and its adsorption performances for Rhodamine B
Faaizatunnisa et al. Facile green synthesis of core–shell magnetic MOF composites (Fe3O4@ SiO2@ HKUST-1) for enhanced adsorption capacity of methylene blue
Kong et al. Structural study on PVA assisted self-assembled 3D hierarchical iron (hydr) oxides
CN111151145B (en) Super-hydrophobic separation membrane and preparation method and application thereof

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
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20220316

Address after: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen

Applicant after: CHINA PETROLEUM & CHEMICAL Corp.

Applicant after: Sinopec Safety Engineering Research Institute Co., Ltd

Address before: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen

Applicant before: CHINA PETROLEUM & CHEMICAL Corp.

Applicant before: Qingdao Safety Engineering Research Institute of Sinopec

GR01 Patent grant
GR01 Patent grant