CN107774329A - A kind of metal-organic framework materials and preparation method thereof - Google Patents

A kind of metal-organic framework materials and preparation method thereof Download PDF

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CN107774329A
CN107774329A CN201610736797.0A CN201610736797A CN107774329A CN 107774329 A CN107774329 A CN 107774329A CN 201610736797 A CN201610736797 A CN 201610736797A CN 107774329 A CN107774329 A CN 107774329A
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metal
organic framework
framework materials
solvent
accordance
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CN107774329B (en
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王海洋
张英
王刚
邢兵
赵亮
马蕊英
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China Petroleum and Chemical Corp
Sinopec Fushun Research Institute of Petroleum and Petrochemicals
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China Petroleum and Chemical Corp
Sinopec Fushun Research Institute of Petroleum and Petrochemicals
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    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2204Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/2208Oxygen, e.g. acetylacetonates
    • B01J31/2213At least two complexing oxygen atoms present in an at least bidentate or bridging ligand
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28064Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28066Surface area, e.g. B.E.T specific surface area being more than 1000 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28069Pore volume, e.g. total pore volume, mesopore volume, micropore volume
    • B01J20/28071Pore volume, e.g. total pore volume, mesopore volume, micropore volume being less than 0.5 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28069Pore volume, e.g. total pore volume, mesopore volume, micropore volume
    • B01J20/28073Pore volume, e.g. total pore volume, mesopore volume, micropore volume being in the range 0.5-1.0 ml/g
    • B01J35/618
    • B01J35/635
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/10Complexes comprising metals of Group I (IA or IB) as the central metal
    • B01J2531/16Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/60Complexes comprising metals of Group VI (VIA or VIB) as the central metal
    • B01J2531/62Chromium
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/80Complexes comprising metals of Group VIII as the central metal
    • B01J2531/84Metals of the iron group
    • B01J2531/842Iron

Abstract

The invention discloses a kind of metal-organic framework materials and preparation method thereof.This method includes:(1)By thick 1,3,5 benzenetricarboxylic acids are added in the first solvent and recrystallized, 1 after being purified, 3,5 benzenetricarboxylic acids, the step of recrystallization includes rising temperature for dissolving, cooling separates out, surfactant is introduced wherein before thick 1,3,5 benzenetricarboxylic acid rising temperature for dissolving, during rising temperature for dissolving and/or after rising temperature for dissolving and before cooling separates out;(2)By 1 after purification, 3,5 benzenetricarboxylic acids, metal salt and the second solvent are well mixed, then crystallization, separation, washing and drying, obtain described metal-organic framework materials.This method is 1,3, surfactant is added in 5 benzenetricarboxylic acid recrystallization processes, not only increase 1, the purity of 3,5 benzenetricarboxylic acids, and a small amount of surfactant can also enter the crystals of recrystallization, so as to avoid reunion of the metal-organic framework materials in building-up process between crystal, the specific surface area and pore volume of metal-organic framework materials are improved.

Description

A kind of metal-organic framework materials and preparation method thereof
Technical field
The present invention relates to a kind of metal-organic framework materials and preparation method thereof.
Background technology
Metal-organic framework materials(Metal-Organic Frameworks, abbreviation MOFs)Refer to by oxygen-containing, nitrogen etc. What multiple tooth organic ligand formed with transition metal ions self assembly, there is the class zeolitic frameworks material of special pore passage structure.They have Have that porosity is high, specific surface area is big, density is small, aperture structure, the advantages that composition and Functional Design are adjustable, this is deposited to develop height Storage capacity, the energy gas adsorbent of high shape-selective separating effect and release agent provide opportunity.
Cu3(BTC)2Also referred to as HKUST-1 types metal-organic framework materials, the coordination polymer is by double-core copper bunch and equal benzene Tricarboxylic acid self assembly forms.It is crystallized in cubic system, belongs to space group Fm-3m.When the removing copper ion combination from skeleton During water, Cu3(BTC)2The three-dimensional porous structure with ligand unsatuated metal structure will be become, the main pore size of the structure is big Small is 9, and slightly smaller tetrahedron side pocket size is 5, and passes through tri-angle-holed window and main aperture road phase of the size for 3.5 Even.Just because of Cu3(BTC)2Possessing two kinds of typical holes so that it is not only the excellent material of gas molecule absorption, and The excellent material of mixed gas separation.
At present, Cu is mainly prepared using hydrothermal synthesis method3(BTC)2Material.Such as the A of CN 102863463 disclose one kind The method for preparing Cu-BTC and nanometer Cu-BTC, first by Cu (ClO4)2The aqueous solution and 1,3,5- benzenetricarboxylic acids ethanol solution Prepare synthesis Cu (C9H406)(H2O), then it is immersed under organic solvent or steam ambient, obtains Cu-BTC.
CN102336774A discloses a kind of nano level metal organic bone of Fast back-projection algorithm at room temperature based on trimesic acid The method of frame nano material.At room temperature, reacted, obtained after the metal acetate aqueous solution is mixed with trimesic acid solution Metal organic framework nano particle.This method belongs to dynamic synthesis technique and carried out at room temperature, have quick, easy, energy-conservation, The advantages that yield is high.
CN103920158A discloses a kind of synthetic method of Nanosized metal organic backbone, using surfactant as mould Plate, using can be provided containing N or O lone electron pair atom rigid ligand as organic ligand, with alkali earth metal, group of the lanthanides gold It is metal ion to belong to element, transition metal, the ion of one or more kinds of metallic elements in amphotere, use Hydro-thermal method or microwave method or ultrasonic method are synthesized.
But above-mentioned metal-organic framework materials are used as former in preparation process using the benzenetricarboxylic acid of high-purity 1,3,5- Material, so as to cause higher production cost, is unfavorable for industrialized popularization.It is used for synthesizing using the relatively low technical grade part of purity Metal-organic framework materials, its crystallinity is poor, and specific surface area is smaller, greatly reduces the feasibility of its practical application.
The content of the invention
In order to overcome weak point of the prior art, the invention provides a kind of metal-organic framework materials and its preparation Method.This method with purity than the relatively low benzenetricarboxylic acid of technical grade 1,3,5- for Material synthesis metal-organic framework materials, and make Metal-organic framework materials not only have very high crystallinity, specific surface area, total pore volume and heat endurance, but also with very High yield.
A kind of preparation method of metal-organic framework materials provided by the invention, comprises the following steps:
(1)Thick 1,3,5- benzenetricarboxylic acid is added in the first solvent and recrystallized, 1 after being purified, 3,5- benzene front threes Acid, the recrystallization includes rising temperature for dissolving, cool the step of separating out, wherein before thick 1,3,5- benzenetricarboxylic acid rising temperature for dissolving, rising Surfactant is introduced in warm course of dissolution and/or after rising temperature for dissolving and before cooling separates out;
(2)By 1 after purification, 3,5- benzenetricarboxylic acids, metal salt and the second solvent are well mixed, then crystallization, separation, washing and Dry, obtain described metal-organic framework materials.
The surfactant be 1-METHYLPYRROLIDONE, Tween-20, Tween-40, Tween-60, Tween-80, sapn- 20th, the one or more in Arlacel-40, Arlacel-60, Arlacel-80, neopelex, preferably N- crassitudes Ketone.
First solvent is low-carbon alcohols, preferably the one or more in methanol, ethanol, propyl alcohol, butanol, ethylene glycol, More preferably ethanol.
Thick 1,3,5- benzenetricarboxylic acids can be with purity than relatively low 1,3,5- benzenetricarboxylic acid, such as the benzene front three of technical grade 1,3,5- Acid, described thick 1, the purity of 3,5- benzenetricarboxylic acids can be 50wt%~70wt%.
After being purified by the inventive method, 1 after the purification, the purity of 3,5- benzenetricarboxylic acids can be 80.00wt%~ 99.99wt%, preferably 90.0wt%~99.9wt%.
The part by weight of the thick 1,3,5- benzenetricarboxylic acids, surfactant and the first solvent is 1:(0.01~0.5):(1 ~50), preferably 1:(0.02~0.1):(2~5).
In step(1)In, the specific steps of the rising temperature for dissolving can be:With 0.5 DEG C/min~10 DEG C/min heating Speed is increased to 30 DEG C~100 DEG C, and keeps 30min~2h.In step(1)In, the specific steps that the cooling separates out can be with For:10 DEG C~25 DEG C are cooled to 0.5 DEG C/min~10 DEG C/min rate of temperature fall, and keeps 30min~2h.
In step(1)In, the recrystallization is additionally may included in after cooling separates out, the step that is separated, washed and dried Suddenly.Separation can select conventional separation method, can be filtering, centrifuge etc., drying condition does not have particular/special requirement, realizes It drying, can be dried in the shade, can also be dried with normal temperature, drying temperature is 50 DEG C~150 DEG C.
Metallic element in the metal salt is Pd, Pt, Ru, Ag, Ni, Cu, Au, Li, Rh, Ir, Ce, Sc, Fe, Mo, Co, One or more in W, the metal salt is the sulfate of above-mentioned metallic element, nitrate, acetate, carbonate, chlorate, One or more in Bromide, preferably copper nitrate or iron chloride.
The molar ratio of metal ion and 1,3,5- benzenetricarboxylic acids is in the metal salt(0.5~5):1, be preferably(0.9 ~3):1, described 1, the part by weight of 3,5- benzenetricarboxylic acids and the second solvent is 1:(0.5~100), preferably 1:(1~40).
Second solvent is the mixed solution containing alcohols solvent and nitrogen-containing compound solvent.The alcohols solvent is with containing The part by weight of nitrogen compound solvent is(0.1~10):1, be preferably(0.5~5):1.The alcohols solvent be methanol, ethanol, It is propyl alcohol, isopropanol, butanol, isobutanol, amylalcohol, 3- methyl -2- butanol, hexanol, 2- ethyl butanols, 2- methyl anyl alcohols, enanthol, pungent Alcohol, lauryl alcohol, tetradecyl alchohol, pentadecanol, hexadecanol, heptadecanol, octadecyl alcolol, cyclopentanol, cyclohexanol, benzyl carbinol, ethylene glycol, the third two One or more in alcohol, butanediol, pentaerythrite, preferably methanol, ethanol, propyl alcohol, butanol, isobutanol, hexanol, 2- ethyls One or more in butanol, enanthol, cyclopentanol, butanediol, pentaerythrite, more preferably methanol;
The nitrogen-containing compound solvent be nitrobenzene, acetonitrile, propionitrile, succinonitrile, methylamine, dimethylamine, ethamine, triethylamine, butylamine, Isobutyl amine, sec-butylamine, tert-butylamine, tri-n-butylamine, aniline, cyclohexylamine, pyrroles, pyridine, quinoline, formamide, N-METHYLFORMAMIDE, N, Dinethylformamide, N, in N- diethylformamides, DMAC N,N' dimethyl acetamide, N- methylacetamides, N- methyl propanamides One or more, preferably nitrobenzene, ethamine, tri-n-butylamine, pyrroles, pyridine, quinoline, DMF, N, N- bis- One or more in ethyl-formamide, N- methyl propanamides, more preferably DMA.
In step(2)In, 80 DEG C~300 DEG C, time 5h~40h of the temperature of the crystallization, drying temperature 100 DEG C~300 DEG C, drying time 5h~24h.Separation can select filtering, centrifuge the methods of, solvent used in washing can be water, One or more in ethanol, methanol, chloroform, preferably water, can be to carry out during washing under heating condition, and wash temperature is 30 DEG C ~50 DEG C.
Present invention also offers a kind of metal-organic framework materials prepared such as above-mentioned method.
The property of metal-organic framework materials of the present invention is as follows:Specific surface area is 500m2/ g~3000m2/ g, it is excellent Elect 1000m as2/ g~2500m2/ g, total pore volume 0.3cm3/ g~0.9cm3/ g, preferably 0.4cm3/ g~0.7cm3/g。
The relative crystallinity of metal-organic framework materials of the present invention is 95%~100%.
The average grain diameter of metal-organic framework materials of the present invention is 0.1 μm~10 μm, preferably 0.5 μm~6 μm.
Present invention also offers above-mentioned metal-organic framework materials in middle gas absorption, gas absorption storage, gas absorption Application in separation.
Described metal-organic framework materials are inhaled in carbon dioxide, hydrogen, methane, carbon monoxide, nitrogen, ethane, propane Attached storage, and carbon dioxide/methane, carbon dioxide/carbon monoxide, titanium dioxide carbon/nitrogen gas, carbon dioxide/oxygen, hydrogen/ Carbon dioxide, hydrogen/nitrogen, methane/nitrogen, ethane/ethylene, propane/propylene gaseous mixture be selectively adsorbing and separating in application.
Compared with prior art, the inventive method has following outstanding advantages:
(1)The preparation method of the metal-organic framework materials of the present invention, using the cheap benzenetricarboxylic acid of technical grade 1,3,5- As raw material, and a certain amount of surfactant is with the addition of in 1,3,5- benzenetricarboxylic acid recrystallizes dedoping step, not only enter one Step improves the purity of 1,3,5- benzenetricarboxylic acids, controls the further growth of crystal, and a small amount of surfactant can also enter Enter the crystals of recrystallization, match somebody with somebody so as to enhance 1,3,5- benzenetricarboxylic acids in metal organic framework building-up process as organic Body synthesizes the reactivity of metal-organic framework materials, avoids the reunion between metal-organic framework materials crystal, raising has The utilization rate and product yield of machine part, specific surface area is higher and the high metal-organic framework materials of pore volume for synthesis, greatly carries High industrial application value.
(2)The preparation method of the metal-organic framework materials of the present invention, with the mixed of alcohols solvent and nitrogen-containing compound solvent Solvent of the solution as synthesis metal-organic framework materials is closed, provide not only the growth of metal-organic framework materials crystalline framework Environment, also acted on template, further improve product yield, easily controllable pore passage structure and size, metal organic framework Stability of material is good, service life length, improves the applicability of metal-organic framework materials.
(3)The metal-organic framework materials of the present invention, there is very high crystallinity, specific surface area, total pore volume, Ke Yiyong Application in gas absorption, gas absorption storage, gas absorption separation, especially in carbon dioxide, hydrogen, methane, an oxygen Change the storage of the gas absorptions such as carbon, nitrogen, ethane, propane, and carbon dioxide/methane, carbon dioxide/carbon monoxide, titanium dioxide Carbon/nitrogen gas, carbon dioxide/oxygen, hydrogen/carbon dioxide, hydrogen/nitrogen, methane/nitrogen, ethane/ethylene, propane/propylene etc. Gaseous mixture be selectively adsorbing and separating in application.
Brief description of the drawings
Fig. 1 is the XRD for the Cu Base Metal organic framework materials that embodiment 1,2,3,6,7 synthesizes with comparative example 1,2,3,4 Spectrum;
Fig. 2 is the XRD spectrum for the Fe Base Metal organic framework materials that embodiment 4 synthesizes;
Fig. 3 is the XRD spectrum for the Cr Base Metal organic framework materials that embodiment 5 synthesizes;
Fig. 4 is the ESEM of metal-organic framework materials of the sample A of embodiment 1 after 200 DEG C of roastings(SEM)Figure;
The ESEM of metal-organic framework materials of the sample B of Fig. 5 embodiments 2 after 200 DEG C of roastings(SEM)Figure;
Fig. 6 is the ESEM of metal-organic framework materials of the sample C of embodiment 3 after 200 DEG C of roastings(SEM)Figure;
Fig. 7 is the ESEM of metal-organic framework materials of the sample F of embodiment 6 after 200 DEG C of roastings(SEM)Figure;
Fig. 8 is the ESEM of metal-organic framework materials of the sample H of comparative example 1 after 200 DEG C of roastings(SEM)Figure;
Fig. 9 is the ESEM of metal-organic framework materials of the sample I of comparative example 2 after 200 DEG C of roastings(SEM)Figure;
Figure 10 is the sample C adsorbed methane curves of embodiment 3.
Embodiment
Further illustrate the preparation process of metal-organic framework materials of the present invention below by embodiment, but it is not considered that Present invention is limited only by following embodiment, wherein wt% is mass fraction.
Embodiment 1
(1)Purify 1,3,5- benzenetricarboxylic acids
By thick the 1 of 100.12g, 3,5- benzenetricarboxylic acids, 2.84g 1-METHYLPYRROLIDONE, it is added in 260mL ethanol, with 0.5 DEG C/min heating rates are warming up to 30 DEG C, it is completely dissolved under conditions of stirring and keeps 30min, then filters out micro 1, 3,5- benzenetricarboxylic acids and impurity, filtrate is cooled to 10 DEG C with 0.5 DEG C/min rate of temperature fall and keeps 30min, thick 1,3,5- benzene Tricarboxylic acid progressively separates out crystallization, then through separation of solid and liquid, dry after purified after 1,3,5- benzenetricarboxylic acids.
(2)Prepare metal-organic framework materials
By the 1,3,5- benzenetricarboxylic acids, 8.82g copper nitrates, the solvents of 12mL second of 10.12g purifications(Methanol:N, N- dimethylacetamide Amine=0.5:1)Well mixed to be put into reactor, 120 DEG C of crystallization 12h, crystallization is washed products therefrom after terminating, filtering Product is placed at 200 DEG C afterwards and dries 12h, obtains Cu Base Metal organic framework material A, particle size range is 4 μm~5 μm.
Embodiment 2
(1)Purify 1,3,5- benzenetricarboxylic acids
By thick the 1 of 100.45g, 3,5- benzenetricarboxylic acids, 10.12g 1-METHYLPYRROLIDONE, it is added in 640mL ethanol, with 10 DEG C/min heating rates are warming up to 100 DEG C, it is completely dissolved under conditions of stirring and keeps 120min, is then filtered out micro 1,3,5- benzenetricarboxylic acid and impurity, filtrate is cooled to 25 DEG C with 10 DEG C/min rate of temperature fall and keeps 120min, thick 1,3,5- Benzenetricarboxylic acid progressively separates out crystallization, then through separation of solid and liquid, dry after purified after 1,3,5- benzenetricarboxylic acids.
(2)Prepare metal-organic framework materials
By the 1,3,5- benzenetricarboxylic acids, 26.45g copper nitrates, the solvents of 500mL second of 10g purifications(Methanol:N, N- dimethylacetamide Amine=5:1)Well mixed to be put into reactor, 120 DEG C of crystallization 12h, crystallization is washed products therefrom after terminating, after filtering Product is placed at 200 DEG C and dries 12h, obtains Cu Base Metal organic framework material B, particle size range is 4 μm~6 μm.
Embodiment 3
(1)Purify 1,3,5- benzenetricarboxylic acids
By thick the 1 of 100.12g, 3,5- benzenetricarboxylic acids, 4.14g 1-METHYLPYRROLIDONE, it is added in 400mL ethanol, with 5 DEG C/min heating rates are warming up to 80 DEG C, it is completely dissolved under conditions of stirring and keeps 60min, then filters out micro 1, 3,5- benzenetricarboxylic acids and impurity, filtrate is cooled to 15 DEG C with 5 DEG C/min rate of temperature fall and keeps 60min, thick 1,3,5- benzene three Formic acid progressively separates out crystallization, then through separation of solid and liquid, dry after purified after 1,3,5- benzenetricarboxylic acids.
(2)Prepare metal-organic framework materials
By the 1,3,5- benzenetricarboxylic acids, 23.58g copper nitrates, the solvents of 240mL second of 10.12g purifications(Methanol:N, N- dimethyl second Acid amides=1:1)Well mixed to be put into reactor, 120 DEG C of crystallization 12h, crystallization is washed products therefrom after terminating, filtering Product is placed at 200 DEG C afterwards and dries 12h, obtains Cu Base Metal organic framework material C, particle size range is 0.5 μm~1.2 μm.
Embodiment 4
(1)Purify 1,3,5- benzenetricarboxylic acids
By thick the 1 of 100.12g, 3,5- benzenetricarboxylic acids, 4.14g 1-METHYLPYRROLIDONE, it is added in 400mL ethanol, with 5 DEG C/min heating rates are warming up to 80 DEG C, it is completely dissolved under conditions of stirring and keeps 60min, then filters out micro 1, 3,5- benzenetricarboxylic acids and impurity, filtrate is cooled to 15 DEG C with 5 DEG C/min rate of temperature fall and keeps 60min, thick 1,3,5- benzene three Formic acid progressively separates out crystallization, then through separation of solid and liquid, dry after purified after 1,3,5- benzenetricarboxylic acids.
(2)Prepare metal-organic framework materials
By the 1,3,5- benzenetricarboxylic acids, 12.93g iron chloride, the solvents of 300mL second of 10g purifications(Methanol:N, N- dimethylacetamide Amine=1:1)Well mixed to be put into reactor, 180 DEG C of crystallization 8h, crystallization is washed products therefrom after terminating, will after filtering Product, which is placed at 200 DEG C, dries 5h, obtains Fe Base Metal organic framework material D, and particle size range is 1.2 μm~2.6 μm.
Embodiment 5
(1)Purify 1,3,5- benzenetricarboxylic acids
By thick the 1 of 100.12g, 3,5- benzenetricarboxylic acids, 4.14g 1-METHYLPYRROLIDONE, it is added in 400mL ethanol, with 5 DEG C/min heating rates are warming up to 80 DEG C, it is completely dissolved under conditions of stirring and keeps 60min, then filters out micro 1, 3,5- benzenetricarboxylic acids and impurity, filtrate is cooled to 15 DEG C with 5 DEG C/min rate of temperature fall and keeps 60min, thick 1,3,5- benzene three Formic acid progressively separates out crystallization, then through separation of solid and liquid, dry after purified after 1,3,5- benzenetricarboxylic acids.
(2)Prepare metal-organic framework materials
By the 1,3,5- benzenetricarboxylic acids, 15.19g chromic nitrates, the solvents of 400mL second of 10g purifications(Methanol:N, N- dimethylacetamide Amine=1:1)Well mixed to be put into reactor, 220 DEG C of crystallization 36h, crystallization is washed products therefrom after terminating, after filtering Product is placed at 200 DEG C and dries 5h, obtains Cr Base Metal organic framework material E, particle size range is 0.1 μm~0.6 μm.
Embodiment 6
For the preparation method of metal-organic framework materials with embodiment 3, difference is that surfactant is addition dodecyl Benzene sulfonic acid sodium salt, other reaction condition and material compositions are constant, obtain Cu Base Metal organic framework materials F.
Embodiment 7
The preparation method of metal-organic framework materials is with embodiment 3, and difference is that the second solvent is propyl alcohol and ethamine, and it compares Example is 1:1, other reaction condition and material compositions are constant, obtain Cu Base Metal organic framework materials G.
Comparative example 1
With embodiment 3, difference is in step the preparation method of metal-organic framework materials(1)Purify 1,3,5- benzene front threes 1-METHYLPYRROLIDONE is not added in the process of acid, and step(2)Mixed in 1,3,5- benzenetricarboxylic acids, copper nitrate and the second solvent Shi Tianjia 4.14g 1-METHYLPYRROLIDONE, obtains Cu Base Metal organic framework material H, and particle size range is 0.1 μm~0.3 μm.
Comparative example 2
With embodiment 3, difference is without using surfactant the preparation method of metal-organic framework materials, obtains Cu bases Metal-organic framework materials I, particle size range are 0.1 μm~0.2 μm.
Comparative example 3
For the preparation method of metal-organic framework materials with embodiment 3, difference is that the second solvent is methanol, obtains Cu funds Belong to organic framework material J.
Comparative example 4
The preparation method of metal-organic framework materials is with embodiment 3, and difference is that the second solvent is N, N- dimethylacetamides Amine, obtain Cu Base Metal organic framework materials K.
Table 1
Industrial 1,3,5- benzenetricarboxylic acids purity/wt% 1,3,5- benzenetricarboxylic acids purity/wt% after purification Utilization rate/wt% of 1,3,5- benzenetricarboxylic acids
Embodiment 1 65 99.5 92
Embodiment 2 65 99.5 91
Embodiment 3 65 99.5 98
Embodiment 4 65 99.5 96
Embodiment 5 65 99.5 95
Embodiment 6 65 98.4 93
Embodiment 7 65 99.5 92
Comparative example 1 65 97.1 88
Comparative example 2 65 91.5 81
Comparative example 3 65 99.5 85
Comparative example 4 65 99.5 84
As can be seen from Table 1, thick 1, the purity of 1,3,5- benzenetricarboxylic acids is increased substantially after 3,5- benzenetricarboxylic acids are purified, it is reachable To more than 99.5%, the surfactant of addition further increases the ligand 1 in metal-organic framework materials building-up process, and 3, The utilization rate of 5- benzenetricarboxylic acids, up to 98wt%.
Test case 1
The physico-chemical property of embodiment 1-4,6-7 and comparative example 1-4 metal-organic framework materials is determined, concrete outcome is shown in Table 2.Its In, BET specific surface area, pore volume are measured by low temperature liquid nitrogen absorption method.For the measure of relative crystallinity, embodiment 1-3,6-7 and With comparative example 1-4 sample to buy the metal-organic framework materials Cu of BASF Corp. of Germany3(BTC)2On the basis of(Basolite ® C300), set its crystallinity and be calculated as 100%, crystallinity is determined by XRD methods.The sample of embodiment 4 is to buy moral The metal-organic framework materials Fe-BTC of BASF AG of state(Basolite® F300)On the basis of, its crystallinity is set as 100% It is calculated, crystallinity is determined by XRD methods.
The physicochemical property of 2 each metal-organic framework materials of table
Sample BET specific surface area/m2·g-1 Total pore volume/cm3·g-1 Relative crystallinity/% Heat endurance(250 DEG C of roasting 10h)
A 1293 0.54 93 Structural integrity
B 1366 0.55 95 Structural integrity
C 1480 0.62 105 Structural integrity
D 2600 0.74 98 Structural integrity
E 1980 0.71 - Structural integrity
F 1341 0.57 92 Structural integrity
G 1284 0.51 93 Structural integrity
H 927 0.45 90 Structure collapse
I 862 0.44 78 Structure collapse
J 956 0.45 82 Structure collapse
K 929 0.43 80 Structure collapse
As can be seen from Table 2, the metal-organic framework materials that prepared by 1-7 of the embodiment of the present invention have very high specific surface area, But also there is higher crystallinity and preferable heat endurance, the metal-organic framework materials prepared far above comparative example 1-4.
Test case 2
The methane adsorption of measure embodiment 1-3,6,7 and comparative example 1-4 metal-organic framework materials measures test result and is shown in Table 3.
Methane adsorption amount:Methane High Pressure Absorption uses Micromeritics HPVA-100 type adsorption instruments.Before sample test, 12h is first vacuumized at 200 DEG C on adsorption instrument, evacuated pressure is less than 10 μm of Hg, is then instructed in programmed pressure processing module Under, reach 40bar and 298K, and obtain corresponding quality storage methane content.
The methane adsorption amount of 3 each metal-organic framework materials of table
Sample Methane adsorption amount/cm3/g
A 185
B 189
C 204
F 175
G 181
H 140
I 106
J 127
K 135
The adsorbed methane effect data further explanation that table 2 provides, metal organic framework prepared by 1-3 of the embodiment of the present invention, 6,7 Material has higher methane adsorption amount.
Fig. 1 is the XRD for the Cu Base Metal organic framework materials that embodiment 1,2,3,6,7 synthesizes with comparative example 1,2,3,4 Spectrum;Pass through characteristic peak, present invention synthesis metal-organic framework materials Cu3(BTC)2.Fig. 2 is the Fe funds that embodiment 4 synthesizes Belong to the XRD spectrum of organic framework material, pass through characteristic peak, present invention synthesis metal-organic framework materials Fe-BTC;Fig. 3 is The XRD spectrum for the Cr Base Metal organic framework materials that embodiment 5 synthesizes, by characteristic peak, present invention synthesis metal is organic Framework material Cr-BTC.
Fig. 4 is the ESEM of metal-organic framework materials of the sample A of embodiment 1 after 200 DEG C of roastings(SEM)Figure; The ESEM of metal-organic framework materials of the sample B of Fig. 5 embodiments 2 after 200 DEG C of roastings(SEM)Figure;Fig. 6 is embodiment The ESEM of metal-organic framework materials of the 3 sample C after 200 DEG C of roastings(SEM)Figure;Fig. 7 is the sample F of embodiment 6 The ESEM of metal-organic framework materials after 200 DEG C of roastings(SEM)Figure;Fig. 8 is the sample H of comparative example 1 through 200 DEG C of roastings The ESEM of metal-organic framework materials after burning(SEM)Figure;Fig. 9 is gold of the sample I of comparative example 2 after 200 DEG C of roastings Belong to the ESEM of organic framework material(SEM)Figure;
By contrast, it can be found that after the metal-organic framework materials of embodiment 1,3 and 6 are calcined 10h at 200 DEG C, still protect Complete pattern and skeleton structure have been held, and after the metal-organic framework materials of comparative example 1 and 2 are calcined 10h at 200 DEG C, bone Frame caves in completely, can not differentiate clear pattern.

Claims (19)

1. a kind of preparation method of metal-organic framework materials, it is characterised in that comprise the following steps:
(1)Thick 1,3,5- benzenetricarboxylic acid is added in the first solvent and recrystallized, 1 after being purified, 3,5- benzene front threes Acid, the recrystallization includes rising temperature for dissolving, cool the step of separating out, wherein before thick 1,3,5- benzenetricarboxylic acid rising temperature for dissolving, rising Surfactant is introduced in warm course of dissolution and/or after rising temperature for dissolving and before cooling separates out;
(2)By 1 after purification, 3,5- benzenetricarboxylic acids, metal salt and the second solvent are well mixed, then crystallization, separation, washing and Dry, obtain described metal-organic framework materials.
2. in accordance with the method for claim 1, it is characterised in that:The thick 1,3,5- benzenetricarboxylic acids, surfactant and the The part by weight of one solvent is 1:(0.01~0.5):(1~50), preferably 1:(0.02~0.1):(2~5).
3. in accordance with the method for claim 1, it is characterised in that:The surfactant be 1-METHYLPYRROLIDONE, tween- 20th, in Tween-40, Tween-60, Tween-80, Arlacel-20, Arlacel-40, Arlacel-60, Arlacel-80, neopelex One or more, preferably 1-METHYLPYRROLIDONE.
4. in accordance with the method for claim 1, it is characterised in that:First solvent is low-carbon alcohols, preferably methanol, second One or more in alcohol, propyl alcohol, butanol, ethylene glycol, more preferably ethanol.
5. in accordance with the method for claim 1, it is characterised in that:The purity of the thick 1,3,5- benzenetricarboxylic acids for 50wt%~ 70wt%。
6. in accordance with the method for claim 1, it is characterised in that:The purity of 1,3,5- benzenetricarboxylic acids after the purification is 80.00wt%~99.99wt%, preferably 90.0wt%~99.9wt%.
7. in accordance with the method for claim 1, it is characterised in that:In step(1)In, the specific steps of the rising temperature for dissolving For:30 DEG C~100 DEG C are increased to 0.5 DEG C/min~10 DEG C/min heating rate, and keeps 30min~2h.
8. in accordance with the method for claim 1, it is characterised in that:In step(1)In, the specific steps of the cooling precipitation For:10 DEG C~25 DEG C are cooled to 0.5 DEG C/min~10 DEG C/min rate of temperature fall, and keeps 30min~2h.
9. in accordance with the method for claim 1, it is characterised in that:The recrystallization also includes:After cooling separates out, divided From, washing and dry step.
10. in accordance with the method for claim 1, it is characterised in that:Metallic element in the metal salt is Pd, Pt, Ru, One or more in Ag, Ni, Cu, Au, Li, Rh, Ir, Ce, Sc, Fe, Mo, Co, W, the metal salt are above-mentioned metallic element Sulfate, nitrate, acetate, carbonate, chlorate, the one or more in Bromide, preferably copper nitrate or chlorination Iron.
11. in accordance with the method for claim 1, it is characterised in that:Metal ion and 1,3,5- benzene front threes in the metal salt Acid molar ratio be(0.5~5):1, be preferably(0.9~3):1, described 1, the weight of 3,5- benzenetricarboxylic acids and the second solvent Ratio is 1:(0.5~100), preferably 1:(1~40).
12. in accordance with the method for claim 1, it is characterised in that:Second solvent is to contain alcohols solvent and nitrogen The mixed solution of compound solvent.
13. in accordance with the method for claim 12, it is characterised in that:The weight of the alcohols solvent and nitrogen-containing compound solvent Ratio is(0.1~10):1, be preferably(0.5~5):1.
14. according to the method described in claim 12 or 13, it is characterised in that:The alcohols solvent be methanol, ethanol, propyl alcohol, Isopropanol, butanol, isobutanol, amylalcohol, 3- methyl -2- butanol, hexanol, 2- ethyl butanols, 2- methyl anyl alcohols, enanthol, octanol, ten Glycol, tetradecyl alchohol, pentadecanol, hexadecanol, heptadecanol, octadecyl alcolol, cyclopentanol, cyclohexanol, benzyl carbinol, ethylene glycol, propane diols, fourth One or more in glycol, pentaerythrite, preferably methanol, ethanol, propyl alcohol, butanol, isobutanol, hexanol, 2- ethyl butanols, One or more in enanthol, cyclopentanol, butanediol, pentaerythrite, more preferably methanol;
The nitrogen-containing compound solvent be nitrobenzene, acetonitrile, propionitrile, succinonitrile, methylamine, dimethylamine, ethamine, triethylamine, butylamine, Isobutyl amine, sec-butylamine, tert-butylamine, tri-n-butylamine, aniline, cyclohexylamine, pyrroles, pyridine, quinoline, formamide, N-METHYLFORMAMIDE, N, Dinethylformamide, N, in N- diethylformamides, DMAC N,N' dimethyl acetamide, N- methylacetamides, N- methyl propanamides One or more, preferably nitrobenzene, ethamine, tri-n-butylamine, pyrroles, pyridine, quinoline, DMF, N, N- bis- One or more in ethyl-formamide, N- methyl propanamides, more preferably DMA.
15. in accordance with the method for claim 1, it is characterised in that:In step(2)In, the temperature 80 DEG C~300 of the crystallization DEG C, time 5h~40h, 100 DEG C~300 DEG C of drying temperature, drying time 5h~24h.
A kind of 16. metal-organic framework materials prepared by method as described in claim 1-15 is any.
17. according to the metal-organic framework materials described in claim 16, it is characterised in that:The metal-organic framework materials Property is as follows:Specific surface area is 500m2/ g~3000m2/ g, preferably 1000m2/ g~2500m2/ g, total pore volume 0.3cm3/g ~0.9cm3/ g, preferably 0.4cm3/ g~0.7cm3/g。
18. according to the metal-organic framework materials described in claim 16, it is characterised in that:The metal-organic framework materials Average grain diameter is 0.1 μm~10 μm, preferably 0.5 μm~6 μm.
19. according to the metal-organic framework materials described in claim 16, it is characterised in that:The metal-organic framework materials Relative crystallinity is 95%~100%.
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