CN106040182B - A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent - Google Patents
A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent Download PDFInfo
- Publication number
- CN106040182B CN106040182B CN201610592278.1A CN201610592278A CN106040182B CN 106040182 B CN106040182 B CN 106040182B CN 201610592278 A CN201610592278 A CN 201610592278A CN 106040182 B CN106040182 B CN 106040182B
- Authority
- CN
- China
- Prior art keywords
- boric acid
- phenyl boric
- organic framework
- preparation
- modified carbon
- 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.)
- Expired - Fee Related
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/223—Solid 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
- B01J20/205—Carbon nanostructures, e.g. nanotubes, nanohorns, nanocones, nanoballs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3204—Inorganic carriers, supports or substrates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D311/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
- C07D311/02—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D311/04—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
- C07D311/22—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4
- C07D311/26—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3
- C07D311/28—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3 with aromatic rings attached in position 2 only
- C07D311/30—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 4 with aromatic rings attached in position 2 or 3 with aromatic rings attached in position 2 only not hydrogenated in the hetero ring, e.g. flavones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
Abstract
The invention belongs to technical field of environment function material preparation, specifically disclose a kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent.High internal phase material resistant to high temperature is synthesized first, secondly carbon foam is sintered into tube furnace, and then carbon foam bubble in the solution of zinc ion, then organic ligand (terephthalic acid (TPA)) and ligand fragment (3 is added, 5- dicarboxyl phenyl boric acid) carry out a series of processing after obtain adsorbent, and adsorbent to be used for Selective recognition and the separation of luteolin.The lotion imprinted polymer microballoon of preparation has very strong thermal stability, with efficient absorption luteolin and can have soda acid to control release performance.
Description
Technical field:
The invention belongs to technical field of environment function material preparation, are related to a kind of phenyl boric acid type metal-organic framework material modification
The method of carbon foam adsorbent.
Background technique
Large pore material is because numerous areas is widely paid close attention to and be applied to its significant anti-pressure ability, such as is catalyzed
Agent, organizational project, absorption and separation etc.;The conventional method for preparing this large pore material is exactly to pass through polymerization with surfactant
Carry out stable High Internal Phase Emulsion to produce, High Internal Phase Emulsion (High Internal Phase Emulsion, HIPE) is also known as height
Concentrated emulsions, it is a kind of lotion of the dispersed phase volume fraction greater than 74.05%.
Metal organic frame is that have three by what coordinate bond was self-assembly of by organic ligand and metal ion or cluster
Tie up porous material.Since it has huge specific surface area and aperture, metal-organic framework material is applied in recent ten years
It is recycled to a large amount of field, such as gas, pharmaceutical carrier, catalysis, the fields such as separation.Nearest functional form metal-organic framework material is inhaled
Draw very big concern, goes synthesis metal-organic framework material by introducing functional monomer as organic ligand segment.In this way
Strategy the use scope of metal framework material is greatly facilitated.
Luteolin is natural flavonoid compound, has a variety of pharmacological activity, such as antibacterial, anticancer is antiviral, anti-oxidant
Etc. abilities.The conventional method that luteolin in purification peanut shell commonly isolates and purifies mainly has macroporous resin adsorption separation
Method, acid heavy method, gradient extraction etc..Although these methods respectively there are particular advantages, also respectively there is its limitation, wherein general character is scarce
Falling into is poor selectivity, and reuse rate is low, costly.Therefore, it establishes and improves Selective recognition and isolate and purify peanut shell
Higher degree, which is obtained, while the new strategy of luteolin, increase product yield in extracting solution has attracted very big concern.
Therefore this work is the method by growth in situ, then grows metal organic frame material in phase template in height
Material, and introduce boronic acid monomer in metal-organic framework material and then be used to adsorb the original that luteolin utilizes boron affinity interaction
Reason.
Summary of the invention
The present invention prepares boric acid modified type metal-organic framework material modified carbon foamed absorbent using in-situ growth technology
(MOF-5-B-CF).High Internal Phase Emulsion material is synthesized first, and a mixed solution is formed by formaldehyde and melamine, is then introduced
Triethanolamine, poly- liquid before eventually forming one, poly- liquid and toluene are vigorously stirred before then taking, and are formed High Internal Phase Emulsion, are then used
Ethyl alcohol removes impurity, and the High Internal Phase Emulsion material of acquisition is dipped into zinc ion solution, and organic ligand is then added (to benzene two
Formic acid) and ligand fragment (3,5- dicarboxyl phenyl boric acid) grow metal organic frame material in high internal phase material at high temperature under high pressure
Material.Then it is used to isolate and purify luteolin.
Invention the technical solution adopted is that:
(1) preparation of carbon foam (CF):
Formalin and melamine are mixed, triethanolamine is added, is vigorously stirred 20- under 500rpm at 50-70 DEG C
40min, poly- liquid before obtaining;
Then to toluene solution is gradually added dropwise in the preceding poly- liquid, 2min is stirred under 1000rpm;Obtained lotion is in 60-
Polyase 13-5 hours at 80 DEG C is dried 12-48 hours at 50-70 DEG C of vacuum, and obtained High Internal Phase Emulsion burns kettle with tube furnace respectively
2 hours, it is heated to 400-600 DEG C with 5 DEG C/min, obtains CF-T;
(2) CF-T-B-MOF is prepared:
Zinc nitrate hexahydrate is dissolved in first in the mixed solution of second alcohol and water, the CF-T for adding step (1) preparation is obtained
To solution A, 3,5- dicarboxyl phenyl boric acid (BBDC) and terephthalic acid (TPA) (H is then added into solution A again2BDC solution) is obtained
Solution B is placed in the reaction kettle of polytetrafluoroethylene (PTFE) by B, is reacted 6-24 hours at 100-200 DEG C, and the product finally obtained is used
Ethyl alcohol is washed 3 times, is dried at 50-70 DEG C of vacuum.
In step (1), the formaldehyde, triethanolamine, melamine, the ratio of toluene is 3-4mL:2-3mL:1.5-
2g:6-10mL。
In step (2), the ratio of the CF-T, zinc nitrate hexahydrate, the mixed solution of second alcohol and water are 50-100mg:
0.1-0.2g:5-15mL。
In the mixed solution of the second alcohol and water, the volume ratio of second alcohol and water is 1:1.
In step (2), 3, the 5- dicarboxyl phenyl boric acid (BBDC), terephthalic acid (TPA) (H2BDC ratio) is 40-
50mg:40-50mg。
The 3,5- dicarboxyl phenyl boric acid (BBDC): the amount ratio of CF-T is 40-50mg:50-100mg.
Phenyl boric acid type metal-organic framework material modified carbon foamed absorbent prepared by the present invention is for isolating and purifying sweet-scented osmanthus
Careless element.
Technological merit of the invention:
The product is by preparing boric acid modified type metal-organic framework material modified carbon foamed absorbent, first in MOF-5
Middle introducing boric acid function monomer, and growth in situ goes out metal-organic framework material on large pore material, material has high temperature resistant, tool
There is excellent chemical property, furthermore also there is material pH response function can simplify adsorption/desorption operation.
Detailed description of the invention
Fig. 1 is the SEM figure that the high internal phase material of kettle is burnt in different temperatures, wherein A1, A2 are not through burning kettle, B1, B2
For the SEM figure of the high internal phase material of 400 DEG C of burning kettles, C1, C2 are the SEM figure of the high internal phase material of 500 DEG C of burning kettles, D1, D2 600
The SEM figure of the high internal phase material of DEG C burning kettle.
Fig. 2 growth in situ metal on high internal phase material (500 DEG C) for the polymerization time in embodiment 1 by 6 hours
Organic framework materials (A1-A2), by the polymerization time of 12 hours, growth in situ metal has on high internal phase material (500 DEG C)
Machine frame frame material (B1-B2), by the polymerization time of 24 hours, growth in situ metal is organic on high internal phase material (500 DEG C)
The SEM of frame material (C1-C2) schemes.
Fig. 3 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) Raman figure.
Fig. 4 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) X-ray diffraction spectrogram.
Fig. 5 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) x-ray photoelectron spectroscopy
Figure.
Fig. 6 is the curve of adsorption kinetics figure of 1 products therefrom of embodiment.
Fig. 7 is the adsorption isothermal curve figure of 1 products therefrom of embodiment.
Fig. 8 is the competitor adsorption curve figure of 1 products therefrom of embodiment.
Specific embodiment
Recognition performance evaluation carries out by the following method in the specific embodiment of the invention: complete using Staticadsorption experiment
At.The certain density LTL solution of 10ml is added in centrifuge tube, a certain amount of phenyl boric acid type metal-organic framework material is added
Modified carbon foamed absorbent is placed in 25 DEG C of constant temperature waters and stands several hours, and LTL content is divided light with UV, visible light after absorption
Degree meter measurement, and adsorption capacity is calculated according to result;After saturation absorption, metal-organic framework material modified carbon foamed absorbent
It is collected with high speed centrifugation, selects several structures and kin hydroxy kind compound, as competitive Adsorption object, it is poly- to participate in research
Close the recognition performance of object.
Below with reference to specific implementation example, the present invention will be further described.
Embodiment 1:
(1) preparation of carbon foam (CF)
3mL formalin and the mixing of 1.5mL melamine, then add 2g triethanolamine, then under 50 degree
20min is vigorously stirred under 500rpm, poly- liquid before then obtaining.Then 6mL toluene solution is gradually added dropwise in poly- liquid before, then exists
2min is stirred under 1000rpm.Then the lotion obtained polyase 13 hour under 60 degree.Then it is dried 12 hours under 50 degree of vacuum.
Obtained 50mg High Internal Phase Emulsion is burnt kettle 2 hours with tube furnace respectively, is heated to 400,500,600 degree with 5 DEG C/min, is obtained
CF-400,CF-500,CF-600。
(2) CF-500-B-MOF is prepared
First the CF-500 of 50mg is put into and to be made of in the zinc nitrate hexahydrate solution of 0.1g the second alcohol and water of 5mL
Mixed solution (v:v, 1:1) stirs 6 hours in the reaction kettle of polytetrafluoroethylene (PTFE).Then the 3,5- dicarboxyl benzene of 40mg is added
Terephthalic acid (TPA) (the H of boric acid (BBDC) and 40mg2BDC it) is reacted 6 hours under 100 degree.The product finally obtained washes 3 with ethyl alcohol
Time, then 50 degree of vacuum lower drying again.
Embodiment 2:
(1) preparation of carbon foam (CF)
4mL formalin and the mixing of 2mL melamine, then add 3g triethanolamine, then the 500rpm under 70 degree
Under be vigorously stirred 40min, then obtain before poly- liquid.Then 10mL toluene solution is gradually added dropwise in poly- liquid before, then in 1000rpm
Lower stirring 2min.Then the lotion obtained polymerize 5 hours under 80 degree.Then it is dried 48 hours under 70 degree of vacuum.It obtains
50mg High Internal Phase Emulsion is burnt kettle 2 hours with tube furnace respectively, is heated to 400,500,600 degree with 5 DEG C/min, is obtained CF-400,
CF-500,CF-600。
(2) CF-500-B-MOF is prepared
The CF-500 of 100mg is put into the zinc nitrate hexahydrate solution of 0.2g first and is made of the second alcohol and water of 15mL
Mixed solution (v:v, 1:1) stir 24 hours in the reaction kettle of polytetrafluoroethylene (PTFE).Then the 3,5- dicarboxyl of 50mg is added
Terephthalic acid (TPA) (the H of base phenyl boric acid (BBDC) and 50mg2BDC it) is reacted 24 hours under 200 degree.The product second finally obtained
Alcohol is washed 3 times, then 70 degree of vacuum lower drying again.
Embodiment 3:
(1) preparation of carbon foam (CF)
3.5mL formalin and the mixing of 2mL melamine, then add 2.5g triethanolamine, then under 60 degree
30min is vigorously stirred under 500rpm, poly- liquid before then obtaining.Then 8mL toluene solution is gradually added dropwise in poly- liquid before, then exists
2min is stirred under 1000rpm.Then the lotion obtained polymerize 4 hours under 70 degree.Then it is dried 24 hours under 60 degree of vacuum.
Obtained 50mg High Internal Phase Emulsion is burnt kettle 2 hours with tube furnace respectively, is heated to 400,500,600 degree with 5 DEG C/min, is obtained
CF-400,CF-500,CF-600。
(2) CF-500-B-MOF is prepared
The CF-500 of 75mg is put into the zinc nitrate hexahydrate solution of 0.15g first and is made of the second alcohol and water of 10mL
Mixed solution (v:v, 1:1) stir 12 hours in the reaction kettle of polytetrafluoroethylene (PTFE).Then the 3,5- dicarboxyl of 45mg is added
Terephthalic acid (TPA) (the H of base phenyl boric acid (BBDC) and 45mg2BDC it) is reacted 12 hours under 120 degree, the product second finally obtained
Alcohol is washed 3 times, then 60 degree of vacuum lower drying again.
Fig. 1 is the SEM figure that the high internal phase material of kettle is burnt in different temperatures, wherein A1, A2 are not through burning kettle, B1, B2
For the SEM figure of the high internal phase material of 400 DEG C of burning kettles, C1, C2 are the SEM figure of the high internal phase material of 500 DEG C of burning kettles, D1, D2 600
The SEM figure of the high internal phase material of DEG C burning kettle.It can be concluded that, as temperature increases, high internal phase material is deformed more severe from figure,
It was found that porous structure that high internal phase material at 500 DEG C has had and excellent rigidity.
Fig. 2 growth in situ metal on high internal phase material (500 DEG C) for the polymerization time in embodiment 1 by 6 hours
Organic framework materials (A1-A2), by the polymerization time of 12 hours, growth in situ metal has on high internal phase material (500 DEG C)
Machine frame frame material (B1-B2), by the polymerization time of 24 hours, growth in situ metal is organic on high internal phase material (500 DEG C)
The SEM of frame material (C1-C2) schemes.
Fig. 3 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) Raman figure, can from c figure
To obtain in 1489cm-1There is the peak of boric acid, illustrates phase material in the metallo organic metal frame material load height of borate type modification
Expect successfully.
Fig. 4 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) X-ray diffraction spectrogram, according to
Secondary sequence from top to bottom, from c figure it can be concluded that, by borate type metal-organic framework material load after, height in phase material
The peak of material cannot not become sharply, illustrate to load successfully.
Fig. 5 is high internal phase material (a) in embodiment 1, the high internal phase material (b) of kettle is burnt at 500 DEG C, by 24 hours
Polymerization time growth in situ metal-organic framework material (c) on high internal phase material (500 DEG C) x-ray photoelectron spectroscopy
Figure.It can be concluded that there is the peak value of boric acid in 189cm-1 from c figure, illustrate that borate type modified metal organic framework materials load
Success.
Test example 1:
Taking 10ml initial concentration is respectively that the LTL solution of 10mg/l, 15mg/l, 20mg/l, 25mg/l, 30mg/l are added to
In centrifuge tube, the phenyl boric acid type metal-organic framework material modified carbon foamed absorbent (CF- that is separately added into 10mg embodiment 1
500-B-MOF), test fluid is placed on 25 DEG C, 35 DEG C, after standing 6h in 45 DEG C of water-bath, supernatant liquor supercentrifuge point
From collection, unadsorbed LTL molecular concentration is measured with ultraviolet-uisible spectrophotometer, and calculates adsorption capacity according to result.
As a result, when initial concentration is 25mg/L, phenyl boric acid type metal-organic framework material is repaired as can be drawn from Figure 6
The absorption of decorations carbon foam adsorbent (CF-500-B-MOF) tends to balance.
Test example 2:
Taking 10mL initial concentration is that luteolin (LTL) solution of 20mg/L is added in centrifuge tube, is separately added into 10mg
Phenyl boric acid type metal-organic framework material modified carbon foamed absorbent (CF-500-B-MOF) in embodiment 1, puts test fluid
In 25 DEG C of water bath chader, taken out when 5min, 15min, 30min, 60min, 120min and 180min respectively;
By being centrifuged phenyl boric acid type metal-organic framework material modified carbon foamed absorbent (CF-500-B-MOF) and luteolin
(LTL) solution separates, and reuses the micropore nitrocellulose filter that aperture is 0.45mm and is filtered what removal suspended to solution
Particle.LC concentration in filtrate is calculated measurement by ultraviolet specrophotometer under the wavelength of 349nm, and calculates suction according to result
Attached capacity;
As can be drawn from Figure 7 as a result, the adsorption process of MIPFs can be divided into fast phase (preceding 60min) and slow rank
Section, and MIPFs reaches the 96.28% of balancing capacity in the adsorption capacity of fast phase, is slowly increase until balance later, it was demonstrated that
Influence of the binding site to absorption on macropore carbon structure, phenyl boric acid type metal-organic framework material modified carbon foamed absorbent
(CF-500-B-MOF) be conducive to separate luteolin.
Test example 3: select catechol, p-nitrophenol, resorcinol, Quercetin, luteolin for competitive Adsorption
Hydroxy kind compound, is respectively configured the aqueous solution of above four kinds of hydroxy kind compounds, and the concentration of every kind of competitive adsorbate is all
20mg/l takes the configured solution of 10ml to be added in centrifuge tube, and the phenyl boric acid type metal being separately added into 10mg embodiment 1 has
Machine frame frame material modified carbon foamed absorbent (CF-500-B-MOF) is placed on test fluid in 25 DEG C of water-bath and stands respectively
6.0h, after the completion of time of repose, supernatant liquor is collected with being centrifuged at a high speed, unadsorbed various competitive Adsorption hydroxy kind chemical combination
Object concentration is measured with efficient liquid phase (HPLC).
Result as can be drawn from Figure 8, (CF-500-B-MOF) is to catechol, p-nitrophenol, resorcinol, quercitrin
Plain, luteolin adsorption capacity is respectively 9.04mg/g, 4.15mg/g, 3.28mg/g, 14.58mg/g;26.52mg/g.Table
Bright CF-500-B-MOF has significant specific recognition ability to LTL, and adsorption capacity is higher than other hydroxyl class compounds.
Claims (4)
1. a kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent, which is characterized in that including
Following steps:
(1) preparation of carbon foam CF:
Formalin and melamine are mixed, triethanolamine is added, is vigorously stirred 20- under 500rpm at 50-70 DEG C
40min, poly- liquid before obtaining;
Then to toluene solution is gradually added dropwise in the preceding poly- liquid, 2min is stirred under 1000rpm;Obtained lotion is at 60-80 DEG C
It is dried 12-48 hours at lower polyase 13-5 hours, 50-70 DEG C of vacuum, it is small that obtained High Internal Phase Emulsion burns kettle 2 with tube furnace respectively
When, it is heated to 400-600 DEG C with 5 DEG C/min, obtains CF-T;
The formaldehyde, triethanolamine, melamine, the ratio of toluene are 3-4mL:2-3mL:1.5-2g:6-10mL
(2) CF-T-B-MOF is prepared:
Zinc nitrate hexahydrate is dissolved in first in the mixed solution of second alcohol and water, add step (1) preparation CF-T obtain it is molten
Then 3,5- dicarboxyl phenyl boric acid BBDC and terephthalic acid (TPA) H is added in liquid A into solution A again2BDC obtains solution B, by solution B
It being placed in the reaction kettle of polytetrafluoroethylene (PTFE), is reacted 6-24 hours at 100-200 DEG C, the product finally obtained is washed 3 times with ethyl alcohol,
It is dried at 50-70 DEG C of vacuum;
CF-T, zinc nitrate hexahydrate, the ratio of the mixed solution of second alcohol and water are 50-100mg:0.1-0.2g:5-15mL;
3,5- dicarboxyl the phenyl boric acid BBDC, terephthalic acid (TPA) H2The ratio of BDC is 40-50mg:40-50mg;
The amount ratio of the 3,5- dicarboxyl phenyl boric acid BBDC:CF-T is 40-50mg:50-100mg.
2. a kind of preparation side of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent according to claim 1
Method, which is characterized in that in the mixed solution of the second alcohol and water, the volume ratio of second alcohol and water is 1:1.
3. a kind of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent, which is characterized in that the phenyl boric acid type gold
Belonging to organic framework materials modified carbon foamed absorbent is had by the phenyl boric acid type metal as described in any one of claim 1~2
Obtained by the preparation method of machine frame frame material modified carbon foamed absorbent.
4. a kind of application of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent as claimed in claim 3,
It is characterized in that, is used for the phenyl boric acid type metal-organic framework material modified carbon foamed absorbent to isolate and purify luteolin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610592278.1A CN106040182B (en) | 2016-07-25 | 2016-07-25 | A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610592278.1A CN106040182B (en) | 2016-07-25 | 2016-07-25 | A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106040182A CN106040182A (en) | 2016-10-26 |
CN106040182B true CN106040182B (en) | 2018-12-14 |
Family
ID=57418372
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610592278.1A Expired - Fee Related CN106040182B (en) | 2016-07-25 | 2016-07-25 | A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106040182B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108097015B (en) * | 2016-11-25 | 2021-03-05 | 中国石油化工股份有限公司 | Amine liquid desulfurization absorbent, preparation method and application thereof |
CN106964322A (en) * | 2017-03-29 | 2017-07-21 | 江苏大学 | A kind of preparation method of boric acid functionalization porous adsorbent |
CN107754766B (en) * | 2017-11-28 | 2020-03-24 | 广西大学 | MOF porous foam material and preparation method thereof |
CN108636359A (en) * | 2018-05-16 | 2018-10-12 | 湘潭大学 | A kind of magnetic metal organic framework microballoon of phenyl boric acid functionalization and its preparation method and application |
CN108767247B (en) * | 2018-07-02 | 2021-10-26 | 南京工业大学 | Preparation method and application of carbon-based metal organic framework MOF compound derivative material |
CN110364745A (en) * | 2019-06-04 | 2019-10-22 | 东南大学 | A kind of boron based on ZIF-8, the preparation method of nitrogen co-doped nonmetallic carbon-based oxygen reduction electro-catalyst |
CN110373004B (en) * | 2019-06-18 | 2021-09-03 | 同济大学 | Preparation method of poly (3, 4-ethylenedioxythiophene) -poly (styrenesulfonic acid)/carbon foam composite material |
CN110849854B (en) * | 2019-11-27 | 2022-05-24 | 曲阜师范大学 | Method for determining Hg2+ and CH3Hg + contents by adopting BA-Eu-MOF composite material |
CN111424429B (en) * | 2020-04-30 | 2022-09-23 | 山东交通学院 | Metal sulfide porous framework material, and preparation method and application thereof |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105664880B (en) * | 2016-04-01 | 2018-10-09 | 江苏大学 | The preparation method of graphene oxide/boronate metal organic frame/polyurethane material |
-
2016
- 2016-07-25 CN CN201610592278.1A patent/CN106040182B/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN106040182A (en) | 2016-10-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106040182B (en) | A kind of preparation method of phenyl boric acid type metal-organic framework material modified carbon foamed absorbent | |
Polborn et al. | Biomimetic Catalysis with Immobilised Organometallic Ruthenium Complexes: Substrate‐and Regioselective Transfer Hydrogenation of Ketones | |
Melis et al. | ROMP and RCM catalysed by (R3P) 2Cl2Ru CHPh immobilised on a mesoporous support | |
CN101987291B (en) | Macropore adsorption resin as well as preparation method and application thereof | |
CN105664880B (en) | The preparation method of graphene oxide/boronate metal organic frame/polyurethane material | |
CN106699952B (en) | A kind of preparation method of the magnetic imprinted polymer of phenyl boric acid fundamental mode | |
CN105233801B (en) | A kind of preparation method of the affine dual identification molecular engram material of boron | |
CN111748055A (en) | Molecularly imprinted polymer with eutectic solvent as functional monomer and application thereof | |
CN104448381B (en) | The preparation and its application of imidazoles functionalized ordered mesoporous phenolic resin material | |
CN107602744B (en) | A kind of superhigh cross-linking microporous polymer and preparation method thereof | |
Yang et al. | Tailored design of hierarchically porous UiO-66 with a controlled pore structure and metal sites | |
CN112574370A (en) | Three-dimensional hydroxyl-containing covalent organic framework material and preparation method thereof | |
CN116496506B (en) | Preparation method and application of mesoporous crystalline material with super-large primary three-dimensional cage structure | |
CN110193344A (en) | A kind of aromatic modified zeolite adsorbent material of cation seperation column [5] and its preparation method and application | |
Zhang et al. | Synthesis of molecularly imprinted polymer based on cooperative imprinting for enrichment of gallic acid in Puer tea | |
CN101831076B (en) | Silica gel particle surface artemisinin molecularly imprinted polymer and preparation and application method thereof | |
Yan et al. | Efficient adsorption separation of xylene isomers in zeolitic imidazolate framework-67@ MCF hybrid materials | |
CN113634238B (en) | Flexible porous boron affinity copolymer adsorbent and preparation method and application thereof | |
CN113121352B (en) | Method for separating and purifying chlorogenic acid by using composite imprinted polymer | |
CN108948255A (en) | A kind of styrene resin and preparation method thereof | |
KR101170486B1 (en) | Production method of mesoporous organic polymer catalyst, mesoporous organic polymer catalyst produced using the method, and process for epoxidation of olefins using the catalyst | |
CN109762142A (en) | A kind of conjugate polymer material based on photo-thermal effect regulation carbon dioxide adsorption | |
Du et al. | Template‐assisted Preparation of Self‐standing 2D‐MOF Membranes for Application in Cascade Reactions | |
CN104447588B (en) | Based on Ni (II) metal organic frame and synthetic method thereof and application | |
CN106492764A (en) | A kind of Preparation method and use of folic acid MOFs materials |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181214 Termination date: 20190725 |
|
CF01 | Termination of patent right due to non-payment of annual fee |