CN111454455B - Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof - Google Patents
Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof Download PDFInfo
- Publication number
- CN111454455B CN111454455B CN202010234790.5A CN202010234790A CN111454455B CN 111454455 B CN111454455 B CN 111454455B CN 202010234790 A CN202010234790 A CN 202010234790A CN 111454455 B CN111454455 B CN 111454455B
- Authority
- CN
- China
- Prior art keywords
- poss
- php
- porous hybrid
- hybrid polymer
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229920000642 polymer Polymers 0.000 title claims abstract description 37
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 24
- 229910052710 silicon Inorganic materials 0.000 title claims abstract description 13
- 239000010703 silicon Substances 0.000 title claims abstract description 13
- 238000002360 preparation method Methods 0.000 title description 11
- 238000005805 hydroxylation reaction Methods 0.000 title description 2
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 23
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 3
- 239000003054 catalyst Substances 0.000 claims description 28
- 239000004593 Epoxy Substances 0.000 claims description 17
- 150000001875 compounds Chemical class 0.000 claims description 13
- 238000006352 cycloaddition reaction Methods 0.000 claims description 13
- 239000000758 substrate Substances 0.000 claims description 10
- 125000005997 bromomethyl group Chemical group 0.000 claims description 3
- 125000004218 chloromethyl group Chemical group [H]C([H])(Cl)* 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 125000001280 n-hexyl group Chemical group C(CCCCC)* 0.000 claims description 3
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 3
- 239000012298 atmosphere Substances 0.000 claims description 2
- 125000000051 benzyloxy group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])O* 0.000 claims description 2
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 abstract description 8
- QARVLSVVCXYDNA-UHFFFAOYSA-N bromobenzene Chemical compound BrC1=CC=CC=C1 QARVLSVVCXYDNA-UHFFFAOYSA-N 0.000 abstract description 8
- 239000002638 heterogeneous catalyst Substances 0.000 abstract description 8
- XNNIJZZVUCWDJQ-UHFFFAOYSA-N C.BrC1=CC=CC=C1.BrC1=CC=CC=C1.BrC1=CC=CC=C1.BrC1=CC=CC=C1 Chemical compound C.BrC1=CC=CC=C1.BrC1=CC=CC=C1.BrC1=CC=CC=C1.BrC1=CC=CC=C1 XNNIJZZVUCWDJQ-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052736 halogen Inorganic materials 0.000 abstract description 6
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 abstract description 6
- 229920002554 vinyl polymer Polymers 0.000 abstract description 6
- 150000002367 halogens Chemical class 0.000 abstract description 4
- 238000007341 Heck reaction Methods 0.000 abstract description 3
- 229910052755 nonmetal Inorganic materials 0.000 abstract description 3
- 239000011148 porous material Substances 0.000 abstract description 3
- 229910008051 Si-OH Inorganic materials 0.000 abstract description 2
- 229910006358 Si—OH Inorganic materials 0.000 abstract description 2
- 150000005676 cyclic carbonates Chemical class 0.000 abstract description 2
- 238000011065 in-situ storage Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 9
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000007983 Tris buffer Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- -1 halogen anions Chemical class 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 3
- 102100029290 Transthyretin Human genes 0.000 description 3
- 108050000089 Transthyretin Proteins 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000002815 homogeneous catalyst Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- UQPUONNXJVWHRM-UHFFFAOYSA-N palladium;triphenylphosphane Chemical group [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 UQPUONNXJVWHRM-UHFFFAOYSA-N 0.000 description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical group [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- JCVHIWLGFNCDAR-UHFFFAOYSA-N 2-bromo-3-methyloxirane Chemical compound CC1OC1Br JCVHIWLGFNCDAR-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910018557 Si O Inorganic materials 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000002329 infrared spectrum Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Inorganic materials [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- LRWZZZWJMFNZIK-UHFFFAOYSA-N 2-chloro-3-methyloxirane Chemical compound CC1OC1Cl LRWZZZWJMFNZIK-UHFFFAOYSA-N 0.000 description 1
- DHSRFGJMOVMDPI-UHFFFAOYSA-N 2-methyloxirane hydrobromide Chemical compound CC1OC1.Br DHSRFGJMOVMDPI-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 1
- 229910018540 Si C Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910002808 Si–O–Si Inorganic materials 0.000 description 1
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000002159 adsorption--desorption isotherm Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000011278 co-treatment Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000001212 derivatisation Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 239000002149 hierarchical pore Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000000269 nucleophilic effect Effects 0.000 description 1
- 150000002924 oxiranes Chemical class 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/38—Polysiloxanes modified by chemical after-treatment
- C08G77/382—Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon
- C08G77/388—Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon containing nitrogen
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
- C07D317/32—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D317/34—Oxygen atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/045—Polysiloxanes containing less than 25 silicon atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/38—Polysiloxanes modified by chemical after-treatment
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
Abstract
A porous hybrid polymer rich in POSS derived silicon hydroxyl is shown in one of the following structural formulas, and is prepared by respectively reacting rigid building units of vinyl POSS with tri (4-bromobenzene) amine or tetra (4-bromobenzene) methane through Heck reaction. The prepared porous hybrid polymer has large specific surface area, abundant mesoporous pores and Si-OH active groups derived in situ, and N-PHPs and C-PHPs are used as nonmetal non-halogen heterogeneous catalysts, so that the high-added-value cyclic carbonate can be prepared by the efficient catalytic conversion of carbon dioxide under mild conditions.
Description
Technical Field
The invention relates to the field of preparation and catalytic application of porous polymers, in particular to porous hybrid polymers rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl, a preparation method thereof and application thereof in CO2Application in catalytic conversion.
Background
With the increasing deterioration of global environment, the greenhouse gas CO2The capture and utilization of CO is becoming increasingly important, and CO2The source is rich, and the product can be used as renewable C1 resource to synthesize chemical products with high added value. In a large number of uses of CO2In the strategy of (1), from CO2And epoxy compounds are one of the most promising strategies for the synthesis of cyclic carbonates by cycloaddition reactions. At present, many homogeneous and heterogeneous catalysts have been developed for CO2And (4) transformation. Homogeneous catalysts are generally highly efficient, but suffer from the disadvantages of difficulty in catalyst recovery and product separation. Heterogeneous catalysts can solve these problems relatively speaking, but most heterogeneous catalytic systems often require severe reaction conditions of high temperature and high pressure. At present, against CO2The catalytic activity sites of the cycloaddition reaction, whether a homogeneous catalyst or a heterogeneous catalyst, mainly depend on nucleophilic halogen anions and electrophilic metal sites, and the catalytic system is not green and environment-friendly. Therefore, the green and high-efficiency nonmetal non-halogen heterogeneous catalyst is constructed, and the CO is treated under the conditions of normal pressure and low temperature2The efficient transformation of (A) is a very important research topic.
As a common heterogeneous catalyst, Porous Organic Polymers (POPs) are known to have high surface area, adjustable chemical functionality and excellent chemical stability in CO2There is increasing interest in capture and conversion. These excellent features of POPs not only enhance the CO-pair of the catalyst in the catalytic reaction2The adsorption capacity of the epoxy resin can be effectively promoted, and the mass transfer of the epoxy substrate can be effectively promoted. In addition, various catalytic functional groups can be introduced into the POP framework, so that the POP framework has abundant active sites and can effectively activate CO2Molecules and epoxy substrates. However, the device is not suitable for use in a kitchenIn contrast, the active sites in current POP heterogeneous catalysts are mainly halogen anion sites and metal sites for CO2POP catalysts free of metal and halogen sites for cycloaddition reactions are very rare. Polyhedral oligomeric silsesquioxanes (POSS) are a novel, nanoscale, inorganic-organic hybrid molecule. POSS is considered to be an ideal building block for the construction of porous polymers due to its regular cage structure, functionalized reactable groups, and excellent hydrothermal stability. In general, porous hybrid polymers based on POSS all have large specific surface areas and excellent hydrothermal stability. However, during the preparation of POSS-based porous polymers, the Si-C and Si-O bonds in the POSS cage may be partially cleaved, resulting in partial collapse of the cage structure and subsequent derivatization of the silicon hydroxyl (Si-OH) groups. From the point of view of the synthesis of ordered porous materials, the destruction of POSS cages is not perfect; from a catalytic application perspective, it is these defective POSS cages that provide catalytically active Hydrogen Bond Donor (HBD) Si-OH groups. The Si-OH group can be used as an auxiliary catalytic active site and can greatly promote the activation of epoxy compounds and CO2The transformation of (3). However, no catalyst using Si-OH groups alone as the catalytically active center has been reported. Therefore, the invention develops a porous hybrid organic polymer rich in POSS derived Si-OH based on POSS unit, which is used as a non-metal non-halogen catalyst to realize CO treatment under normal pressure and mild condition under the conditions of no solvent and no promoter2High efficiency catalytic conversion.
Disclosure of Invention
The inventor researches and develops a preparation method of a porous hybrid polymer rich in POSS derived Si-OH through a large amount of experimental researches, and designs and synthesizes a series of POSS-based porous hybrid polymers N-PHPs and C-PHPs. Experimental research shows that the N-PHPs and C-PHPs synthesized by the method can be used as high-efficiency catalysts applied to CO2In the cycloaddition reaction.
As a first aspect of the invention, the invention provides a class of porous hybrid polymers rich in POSS-derived silicon hydroxyl groups,
the structural formula is shown as one of the following formulas:
as a second aspect of the present invention, there is also provided a process for preparing a porous hybrid polymer rich in POSS-derived silicon hydroxyl groups of the above-mentioned class, comprising: dissolving vinyl POSS shown in the following formula 1 and tri (4-bromobenzene) amine shown in the following formula 2 or tetra (4-bromobenzene) methane shown in the following formula 3 in an organic solvent, and preparing the POSS-derived silicon hydroxyl-rich porous hybrid polymer through Heck reaction.
Further, the preparation method specifically comprises the following steps:
s1: weighing a certain amount of the vinyl POSS shown in the formula 1 and the tri (4-bromobenzene) amine shown in the formula 2 or the tetra (4-bromobenzene) methane shown in the formula 3, and dissolving in an organic solvent to obtain a uniform solution;
s2: transferring the uniform solution into a reaction kettle, adding an alkaline acid-absorbing agent and a catalyst, and heating for reaction for a period of time;
s3: and after the reaction is finished, filtering, washing and drying to obtain the porous hybrid polymer rich in POSS derived silicon hydroxyl.
In step S1, the molar ratio of the vinyl POSS represented by formula 1 to the tris (4-bromobenzene) amine represented by formula 2 or the tetrakis (4-bromobenzene) methane represented by formula 3 is 1:1 to 3.
Further, the alkaline acid acceptor is K2CO3。
Further, the catalyst is palladium triphenylphosphine.
Further, the reaction temperature in the step S2 is 120 ℃, and the reaction time is 72 h.
As a third aspect of the invention, there is also provided the use of the above-mentioned POSS-derived Si-OH-rich porous hybrid polymer in CO2Application in catalytic conversion.
Further, the application specifically includes: using an epoxy compound as a substrate, using the porous hybrid polymer rich in POSS derived silicon hydroxyl as a catalyst, and using CO at normal pressure2In the atmosphere, CO is carried out under heating2Cycloaddition reaction with an epoxy compound.
Further, the structural formula of the epoxy compound is shown as the following formula 4
Wherein R is chloromethyl, bromomethyl, phenyl, n-butyl, n-hexyl or benzyloxy.
Compared with the prior art, the invention has the beneficial effects that:
according to the preparation method, the vinyl POSS and the tri (4-bromobenzene) amine or tetra (4-bromobenzene) methane are subjected to Heck reaction to prepare the POSS-derived Si-OH-rich porous hybrid polymer, the reaction conditions required by the preparation process are mild, the reaction time is short, the used equipment is simple, and the preparation method has a wide industrial/large-scale application prospect;
the prepared polymer has excellent catalytic activity by introducing the hydrogen bond donor Si-OH group into the polymer in situ;
the porous hybrid polymer rich in POSS derived Si-OH is prepared by reacting an epoxy compound and CO under the conditions of no solvent and no promoter2The cycloaddition reaction has excellent catalytic performance, and the reaction also has the advantages of small catalyst consumption and easy separation and recovery.
Drawings
FIG. 1 is an XRD spectrum of N-PHP-2, C-PHP-2 in example 1;
FIG. 2 is an IR spectrum of N-PHP-2, C-PHP-2 in example 1;
FIG. 3 is an SEM photograph of N-PHP-2, C-PHP-2 in example 1;
FIG. 4 shows N at 77K for N-PHP-2, C-PHP-2 in example 12Adsorption and desorption curves and an NLDFT aperture distribution diagram;
FIGS. 5-9 are for the respective reaction products of example 31H NMAnd (4) an R spectrogram.
The specific implementation mode is as follows:
the technical solutions of the present invention are specifically described below with reference to examples, and it should be noted that the implementation examples only describe the preferred examples of the present invention, and do not limit the concept and scope of the present invention. Without departing from the design concept of the present invention, those skilled in the art can change the linker of the novel POSS-enriched Si-OH derived porous hybrid polymer, change the reaction conditions of the synthesis method, change the specific surface area of the synthesized polymer and change the specific surface area of the synthesized polymer in CO2Variations in the application of catalytic conversion are within the scope of the present invention.
Example 1: preparation of POSS-derived Si-OH-rich porous hybrid polymers N-PHPs and C-PHPs
The synthetic route is as follows:
vinyl POSS (VPOSS) and tris (4-bromobenzene) amine (TBPA) were weighed into 10mL of N, N' -dimethylformamide, stirred to dissolve completely, and the two solutions were mixed and charged into a stainless steel reactor lined with polytetrafluoroethylene. Weighing alkaline acid-absorbing agent K2CO32mL of water was added, dissolved by stirring, and transferred to the above reaction vessel. And weighing catalyst triphenylphosphine palladium, adding the catalyst triphenylphosphine palladium into the reaction kettle, and uniformly stirring. And (3) placing the reaction kettle in an oven at 120 ℃ for reaction for 72 hours. And after the reaction is finished, cooling the reaction kettle to room temperature, transferring the solution into a beaker, performing suction filtration, and washing with tetrahydrofuran, deionized water and ethanol respectively. And finally, drying the filter cake in a vacuum oven (80 ℃) for 12 hours to obtain the porous hybrid polymer N-PHPs. A series of porous hybrid polymers N-PHP-N (N is 1,2,3) are obtained by adjusting the molar ratio of VPOSS to TBPA (1: 1-1: 3). The obtained N-PHP-2 has the highest specific surface area and moderate nitrogen content, and is selected as a typical sample for subsequent characterization and application.
The porous hybrid polymer C-PHP-n (n is 1,2,3) can be obtained by replacing TBPA with tetra (4-bromobenzene) methane (TBPM) and repeating the experiment with the molar ratio of VPOSS to TBPM being 1: 1-3.
Structural characterization:
FIG. 1 is an infrared spectrum of N-PHP-2 and C-PHP-2 porous hybrid polymers prepared in example 1 (POSS is an abbreviation for polyhedral oligomeric silsesquioxane, and PHPs is an abbreviation for porous hybrid polymer). As can be seen from the figure, N-PHP-2 and C-PHP-2 substantially retain the Si-O-Si structure of the POSS cage, but due to the coexisting T's in the POSS cagenAnd QnCollapse and regeneration of silicon units with characteristic peak positions from 1110cm of VPOSS monomer-1Is shifted to 1062, 1147 and 1142cm-1To (3). It is at 3674/3650cm-1Si-OH and 967/966cm-1Stretching vibration of the Si-O bond confirmed the presence of Si-OH groups in N-PHP-2 and C-PHP-2. In addition, 1506cm-1The characteristic peaks in (a) are assigned to the C-N bond in tris (4-bromobenzene) amine, further illustrating the successful incorporation of the tris (4-bromobenzene) amine monomer into the polymer backbone. FIG. 2 is an XRD spectrum of N-PHP-2 and C-PHP-2, which has distinct peaks at 20.9-21.5 degrees, indicating that N-PHP-2 and C-PHP-2 are amorphous structures. FIG. 3 is an SEM image of N-PHP-2 and C-PHP-2, showing that they have a fluffy, nano-like morphology. The porous nature of the porous hybrid polymer was confirmed by nitrogen desorption testing at 77K. As shown in FIG. 4A, the N-PHP-2 and C-PHP-2 isotherms are at low relative pressures (P/P)0<0.1) exhibits considerable absorption at high pressures P/P0(0.85-0.99) shows a certain hysteresis ring, which indicates that the materials have a hierarchical pore structure of micropores and mesopores. In addition, they have a high specific surface area, 547 and 715m respectively2g-1. The pore size distribution of the sample was calculated by using NLDFT model, as shown in FIG. 4B, the polymers N-PHP-2 and C-PHP-2 have narrower micropore distribution at 1.41 and 1.29nm, and some disordered mesopore distribution appears at 2.89/3.32, 5.44/4.54 and 11.17/15.31nm, which is similar to N2The type of adsorption desorption isotherms is consistent.
Example 2: catalytic conversion of CO by N-PHP-2 and C-PHP-22Reactivity comparison and recyclability of
Obtained by working example 1The porous hybrid polymer catalysts N-PHP-2 and C-PHP-2 are used for CO2And cycloaddition reaction with epoxy chloropropane. The reaction conditions are as follows: epichlorohydrin (2mmol), the catalyst from example 1 (0.05g), was charged to a 25mL reaction tube, stirred at 80 ℃ and first connected to CO2The air in the reaction tube is discharged through the vent pipe of the gas cylinder, and then a balloon (0.1MPa) filled with carbon dioxide is inserted on the reaction tube to react for 72 hours. After the reaction, a certain amount of ethyl acetate was added to dilute the reaction solution, and the mixture was stirred at room temperature for 20 minutes. The solution was removed, centrifuged, and the supernatant removed and the yield calculated using Gas Chromatography (GC) analysis, the results of which are shown in table 1. As can be seen from Table 1, under the same conditions, the catalysts N-PHP-2 and C-PHP-2 have almost the same catalytic activity and can exhibit excellent catalytic activity.
TABLE 1 CO catalyzed by N-PHP-2 and C-PHP-2 catalysts2Cycloaddition reaction result with epichlorohydrin
The above experiment was repeated using the above catalyst C-PHP-2, and the cycle was repeated 1 to 5 times under the same conditions of reaction temperature and reaction time, and the results of the experiment are shown in Table 2. As can be seen from Table 2, catalyst C-PHP-2 has good recyclability.
TABLE 2C-PHP-2 catalyzed CO2Recycling results of cycloaddition reaction with epichlorohydrin
Example 3: catalysts N-PHP-2 and C-PHP-2 for catalyzing CO2Activity comparison and substrate suitability in cycloaddition reactions with different epoxides
This example uses N-PHP-2 and C-PHP-2 catalysts and various epoxy compounds as substrates to compare the activities of the N-PHP-2 and C-PHP-2 catalysts and CO2Substrate expansibility study of cycloaddition catalytic reaction, epoxy compound is
Wherein, R is chloromethyl, bromomethyl, phenyl, benzyloxy, n-butyl, n-hexyl experimental result is shown in Table 3.
As can be seen from the data in Table 3, the catalytic activity of the catalyst C-PHP-2 is slightly better than that of N-PHP-2, which is probably because the C-PHP-2 has a very high specific surface area and a large number of mesopores, which are beneficial to the mass transfer of the epoxy substrate in the reaction. In addition, both catalysts can have relatively mild conditions and high yield on inert and long-chain epoxy substrates, which shows that the two catalysts have good substrate applicability and can be used as efficient heterogeneous catalysts to realize CO under mild conditions2The catalytic conversion of (2).
TABLE 3 CO catalyzed by N-PHP-2 and C-PHP-2 catalysts2Cycloaddition reaction performance with different epoxy compounds
The following specific experimental procedure, using C-PHP-2 as an example:
3.1 catalytic conversion of CO by C-PHP-22Catalytic performance of reaction with bromopropylene oxide
Propylene oxide bromide (2mmol), the C-PHP-2 catalyst from example 1 (0.05g) was added to a 25mL reaction tube and stirred at 80 deg.C, first with a CO linker2The air in the reaction tube is discharged by the vent tube of the gas cylinder and then filled with CO2The balloon (0.1MPa) was inserted into the reaction tube and reacted for 72 hours. After the reaction, a certain amount of ethyl acetate was added to dilute the reaction solution, and the mixture was stirred at room temperature for 20 minutes. Taking out the solution, centrifuging, taking out the supernatant, evaporating the solvent by using a vacuum rotary evaporator, and calculating the yield of the obtained crude product by nuclear magnetic hydrogen spectrum. Of the reaction products1The H NMR spectrum is shown in FIG. 5.
Under similar reaction conditions, styrene oxide, epoxypropylphenyl ether, 1,2Replacement of bromopropylene oxide by Hexane oxide and 1, 2-Octane oxide, testing of the catalyst C-PHP-2 in the catalytic conversion of CO by changing the reaction temperature (100 ℃ C.) and 120 ℃ C.) under otherwise unchanged conditions2Catalytic performance in reactions with other epoxy compounds. Reaction product1The H NMR spectrum is shown in FIGS. 6 to 9.
Claims (2)
1. The application of the porous hybrid polymer rich in POSS derived silicon hydroxyl in the catalytic conversion of carbon dioxide is characterized in that the structural formula of the porous hybrid polymer rich in POSS derived silicon hydroxyl is shown as one of the following formulas:
the application specifically comprises: using an epoxy compound as a substrate, using the porous hybrid polymer rich in POSS derived silicon hydroxyl as a catalyst, and using CO at normal pressure2In the atmosphere, CO is carried out under heating2Cycloaddition reaction with an epoxy compound.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010234790.5A CN111454455B (en) | 2020-03-30 | 2020-03-30 | Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010234790.5A CN111454455B (en) | 2020-03-30 | 2020-03-30 | Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111454455A CN111454455A (en) | 2020-07-28 |
CN111454455B true CN111454455B (en) | 2022-04-12 |
Family
ID=71677336
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010234790.5A Active CN111454455B (en) | 2020-03-30 | 2020-03-30 | Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111454455B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114014833B (en) * | 2021-12-09 | 2023-09-15 | 浙江理工大学 | Method for preparing cyclic carbonate from low-concentration carbon dioxide and catalyst used by method |
CN115216156B (en) * | 2022-09-14 | 2022-12-09 | 浙江葆润应用材料有限公司 | Foamed silicone rubber sealing sheet and preparation method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107167462A (en) * | 2017-07-28 | 2017-09-15 | 山东大学 | A kind of fluorescence detection test of quick detection Nitroaromatic explosive and preparation method and application |
-
2020
- 2020-03-30 CN CN202010234790.5A patent/CN111454455B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107167462A (en) * | 2017-07-28 | 2017-09-15 | 山东大学 | A kind of fluorescence detection test of quick detection Nitroaromatic explosive and preparation method and application |
Non-Patent Citations (6)
Title |
---|
Dengxu Wang等.POSS-based luminescent porous polymers for carbon dioxide sorption and nitroaromatic explosives detection.《RSC Advances》.2014,第4卷第59877-59884页. * |
Imidazolium-based ionic porous hybrid polymers with POSS-derived silanols for efficient heterogeneous catalytic CO2 conversion under mild conditions;Guojian Chen等;《Chemical Engineering Journal》;20190907;第381卷;122765 * |
POSS-based luminescent porous polymers for carbon dioxide sorption and nitroaromatic explosives detection;Dengxu Wang等;《RSC Advances》;20141027;第4卷;第59877-59884页 * |
Silanediol-Catalyzed Carbon Dioxide Fixation;Andrea M等;《ChemSusChem》;20141019;第7卷;第3275-3278页 * |
Silanol-Enriched Viologen-Based Ionic Porous Hybrid Polymers for Efficient Catalytic CO2 Fixation into Cyclic Carbonates under Mild Conditions;Yadong Zhang等;《ACS Sustainable Chem. Eng.》;20190910;第7卷(第19期);16907-16916 * |
Synthesis of Network Polymers Containing Si-Vinylene Units by Mizoroki-Heck Reaction;Naofumi Naga等;《International Journal of Chemistry》;20170509;第9卷(第3期);第1-9页 * |
Also Published As
Publication number | Publication date |
---|---|
CN111454455A (en) | 2020-07-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110256683B (en) | Preparation method and application of hierarchical pore structure metal organic framework material | |
Jose et al. | Functionalized zeolitic imidazolate framework F-ZIF-90 as efficient catalyst for the cycloaddition of carbon dioxide to allyl glycidyl ether | |
CN112341394B (en) | Method for preparing cyclic carbonate ester by catalysis of hydrogen bond donor functionalized polymeric ionic liquid | |
CN104722212B (en) | A kind of preparation method of covalent triazine skeleton doping hybridized film | |
CN107537569B (en) | Ionic covalent organic framework catalyst, preparation method and catalytic application | |
CN111454455B (en) | Porous hybrid polymer rich in POSS (polyhedral oligomeric silsesquioxane) derived silicon hydroxyl and preparation method and catalytic application thereof | |
CN111013661B (en) | MOF @ POP core-shell material and application thereof in preparation of cyclic carbonate | |
CN110684203B (en) | Two-dimensional bromine-containing covalent organic framework compound and preparation method thereof | |
CN106883419A (en) | A kind of fast synthesis method of cobalt-based metal-organic framework materials and its application | |
CN111229320B (en) | Metal organic framework composite material grafted with ionic liquid and preparation method and application thereof | |
CN112280052B (en) | Hierarchical pore ZIF-8 material and preparation method and application thereof | |
CN113617388B (en) | Silver nano-catalyst based on porous pyridyl covalent organic framework, and preparation method and application thereof | |
CN108821304B (en) | High-activity hierarchical pore titanium silicalite molecular sieve and preparation method and application thereof | |
CN112169836A (en) | Porous ionic polymer heterogeneous catalyst and method for catalytically synthesizing N-formamide by using same | |
CN114276506B (en) | Diamond type three-dimensional covalent organic framework material and preparation method thereof | |
CN110090664B (en) | Acidic ionic liquid @ COF material and preparation method and application thereof | |
CN113912805B (en) | Organic porous polymer for catalyzing cycloaddition of epoxide and carbon dioxide | |
CN113105321B (en) | Copper-based metal organic framework compound, preparation method and application thereof | |
CN109734103A (en) | Synthesize the method with the SAPO-34 molecular sieve of multi-stage artery structure | |
CN114618583B (en) | Membrane catalytic material for catalyzing Knoevenagel condensation reaction at room temperature with high conversion rate | |
CN113398968B (en) | MOF-derived TiO 2 Porous g-C 3 N 4 Composite photocatalyst, preparation method and application thereof | |
Li et al. | Synthesis of hypercrosslinked polymers with a spherical shell structure for highly effective cycloaddition of CO 2 under ambient conditions | |
CN115260512A (en) | Method for directly synthesizing single-component covalent organic framework aerogel | |
CN114433228A (en) | Method for synthesizing cyclic carbonate ester by catalyzing core-shell type polymeric ionic liquid | |
CN109174189B (en) | PCN-222(Co) @ TpPa-1-based porous crystalline core-shell hybrid material 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 | ||
GR01 | Patent grant | ||
GR01 | Patent grant |