Disclosure of Invention
The technical problem solved by the invention is as follows: the invention provides a copper metal nano catalyst (PNBI/CB/Cu) immobilized by a crosslinked norbornene copolymer/carbon black three-dimensional network. According to the PNBI/CB/Cu catalyst, the nano copper is wrapped in a crosslinked norbornene copolymer/carbon black three-dimensional network (PNBI/CB) carrier, a crosslinked polymer is insoluble in a conventional solvent, and the effect of immobilizing the nano metal copper is good; compared with bivalent copper, the heterogeneous zero-valent copper is not easy to fall off in the reaction process; the catalyst has high activity and long service life, and still has high activity after being repeatedly recycled.
The scheme provided by the invention is as follows:
the invention provides a copper nano catalyst loaded on a crosslinked norbornene copolymer/carbon black three-dimensional network, which is characterized by comprising the following components in percentage by weight: the catalyst comprises a cross-linked norbornene copolymer/carbon black three-dimensional network (PNBI/CB) carrier and nano copper loaded on the PNBI/CB carrier, wherein the mass percentage of copper in a copper nano catalyst PNBI/CB/Cu loaded on the cross-linked norbornene copolymer/carbon black three-dimensional network is 1.0-2.0%.
According to the crosslinked norbornene copolymer/carbon black three-dimensional network loaded copper nano catalyst, the nano copper is wrapped in the PNBI/CB carrier, the nano copper is easy to separate and recycle after reaction, the loss of metal copper is small, the pollution caused by the metal copper is small, heterogeneous zero-valent copper is not easy to fall off in the reaction process compared with bivalent copper, the service life of the catalyst is long, and the catalyst still has high activity after repeated recycling; the metallic copper exists in the PNBI/CB/Cu catalyst in the form of nano particles, is uniformly dispersed, has the copper content of only 1.0 to 2.0 percent, small content, high activity and low use cost; the PNBI/CB/Cu catalyst can be stored well, and is not easy to drop metal or damage a structure.
Specifically, the carbon black is commercially available activated carbon powder, is cheap and easily available, is amorphous carbon, is loose, light and extremely fine black powder, has very large surface area, can improve the immobilization stability of metal nanoparticles in the catalyst by adding the carbon black, and has high specific surface area so that metal copper on the carrier has high dispersibility.
On the basis of the scheme, the following improvements can be made:
further, the norbornene copolymer is prepared by mixing a first monomer (formula I), a second monomer (formula II) and a third monomer (formula III) according to a molar ratio of 1: (0.75-1.25): (0.75-1.25) polymerized product.
The cross-linked norbornene copolymer prepared under the condition contains a proper amount of free hydroxyl, has a proper hydrophilic-lipophilic balance (HLB), has good dispersibility in both an organic phase and a water phase, can be suitable for reaction of the organic phase and the water phase and reaction of an organic/water mixed phase, can be conveniently separated from other components in a reaction system by a conventional solid-liquid separation method (centrifugation, filtration and the like) after the reaction is finished, and is convenient to reuse.
Further, the molecular weight of the norbornene copolymer was 12000-17000.
Therefore, the PNBI/CB/Cu catalyst obtained by crosslinking the norbornene copolymer has better dispersibility and stability in an organic/water mixed phase.
The invention provides a preparation method of a copper nano catalyst loaded on a crosslinked norbornene copolymer/carbon black three-dimensional network, which is characterized by comprising the following steps:
1) reacting a reaction solution A containing the first monomer, the second monomer, the third monomer and a catalyst for 1-3h under an inert atmosphere, wherein the molar ratio of the first monomer to the second monomer to the third monomer to the catalyst is 1: (0.75-1.25): (0.75-1.25): (1% -5%).
2) Adding a quenching agent into the reaction liquid A, continuously stirring for 5-20min to obtain a reaction liquid B, and concentrating and precipitating the reaction liquid B to obtain the norbornene copolymer.
3) And dispersing a norbornene polymer and activated carbon powder mixed material in dichloromethane to obtain a mixed dispersion liquid, wherein the mass fraction of the norbornene polymer in the mixed material is 30% -70%.
4) Drying the mixed dispersion liquid to obtain a norbornene polymer/carbon black mixture;
5) and dispersing the polynorbornene polymer/carbon black and sodium borohydride in a diethylene glycol dimethyl ether/dichloromethane mixed solvent, adding copper acetate, and stirring for 2-6h to obtain a reaction liquid C, wherein the molar ratio of the sodium borohydride to the copper acetate is (3-5): 1.
6) Adding ether into the reaction solution C to precipitate a norbornene polymer/carbon black/copper primary product, washing and drying the primary product, and heating at the temperature of 150 ℃ for 4-7h under inert gas to obtain the crosslinked norbornene copolymer/carbon black three-dimensional network supported copper catalyst PNBI/CB/Cu.
According to the method, norbornene is used as a polymer framework, under the action of a catalyst, a first monomer, a second monomer and a third monomer are subjected to ring-opening disproportionation polymerization to obtain a crosslinked norbornene copolymer, and the relative content of free hydroxyl in the catalyst can be adjusted by changing the proportion of the monomers, so that the hydrophilic-lipophilic balance value of the catalyst is regulated and controlled to adapt to different organic phase and aqueous phase reactions or organic phase/aqueous phase reactions, and higher catalytic efficiency and higher recovery rate are achieved.
On the basis of the scheme, the following improvements can be made:
further, the catalyst is selected from one of Grubbs catalyst and Schrock catalyst, and the quenching agent is vinyl ethyl ether.
The catalyst catalyzes ring-opening disproportionation polymerization to be activity-controllable polymerization, and the polymerization degree and molecular weight of the polymer can be adjusted by changing the amount of the catalyst, so that the obtained molecular weight is accurate and controllable, and the molecular weight Distribution (DPI) is narrow; the relative content of Cu (copper) in the copper nano catalyst in PNBI/CB/Cu can be adjusted by changing the volume or concentration of the copper acetate solution; and the size of the copper nanoparticles in PNBI/CB/Cu can be adjusted by changing the using amount of the sodium borohydride.
Further, the washing treatment in step 6) includes washing with deionized water, tetrahydrofuran, and dichloromethane in this order.
This enables the polar and nonpolar impurities on the catalyst surface to be removed successively and completely.
Further, the steps 1) to 5) are all carried out at room temperature.
Therefore, the reaction is carried out at normal temperature, the conditions are mild, the preparation is simple, and the industrial production is convenient.
According to the preparation method, the relative content of free hydroxyl in the catalyst is controlled by changing the monomer ratio, so that the hydrophilic-lipophilic balance (HLB) of the catalyst is regulated and controlled to adapt to different reaction systems (organic phase, water phase and organic/water mixed phase).
Specifically, the solvent in the reaction solution a in the step 1) is any one selected from dichloromethane, toluene and tetrahydrofuran.
Preferably, the solvent in the reaction solution a is dichloromethane.
The reaction raw materials and the catalyst can be sufficiently dissolved in the dichloromethane, and a norbornene copolymer with high yield and high purity can be prepared.
Preferably, the organic solvent in step 3) is dichloromethane.
Can sufficiently disperse the mixture of the norbornene polymer and the activated carbon powder and further dissolve and remove incompletely reacted reaction raw materials.
Preferably, the mixed dispersion liquid is filtered, washed and dried in the step 4) to obtain a polynorbornene polymer/carbon black mixture.
Thereby removing redundant impurities and obtaining a polynorbornene polymer/carbon black mixture with higher purity.
Specifically, the concentration of the polynorbornene polymer/carbon black in the step 5) is 15-25g/L, and the concentration of the sodium borohydride is 0.5-1.5 g/L.
The concentration of the used copper acetate solution is adjusted, the relative content of copper in the PNBI/CB/Cu nano catalyst can be adjusted, the concentration of sodium borohydride is changed, the size of copper nanoparticles in the PNBI/CB/Cu copper nano catalyst can be adjusted, and the copper nanoparticles which are uniformly distributed in the PNBI/CB carrier, small in size (the particle size is 2-8nm) and highly dispersed can be obtained under the condition.
The invention also provides an application of the crosslinked norbornene copolymer/carbon black three-dimensional network loaded copper nano catalyst, and the PNBI/CB/Cu catalyst is applied to boron addition reaction of alpha, beta-unsaturated aldehyde ketone.
The PNBI/CB/Cu catalyst provided by the invention is applied to the boron addition reaction of alpha, beta-unsaturated aldehyde ketone, can obtain higher product yield, has long service life, and still has higher activity after being recycled for a plurality of times.
The application of the crosslinked norbornene copolymer/carbon black three-dimensional network loaded copper nano catalyst comprises the following steps:
1) mixing alpha, beta-unsaturated aldehyde ketone, bis-pinacol borate and palladium in the crosslinked norbornene copolymer/carbon black three-dimensional network supported copper nano catalyst according to a molar ratio of 1 (1-1.2) to 0.1-0.3%, and mixing according to a volume ratio of 1: (0.5-1.5) adding tetrahydrofuran and water to obtain a mixed reaction solution;
2) and reacting the mixed reaction liquid for 8-16h to generate a boron addition product of the alpha, beta-unsaturated aldehyde ketone.
When the cross-linked norbornene copolymer is prepared by mixing the first monomer, the second monomer and the third monomer according to a molar ratio of 1: (0.75-1.25): (0.75-1.25) polymerizing and crosslinking to obtain a product, wherein the catalyst obtained under the condition has appropriate hydrophilic and lipophilic properties, has good dispersibility in the tetrahydrofuran/water system, can be fully separated and recycled after the reaction is finished, and is convenient to recycle.
Specifically, after the mixed reaction liquid reacts for 8-16h in the step 2), the mixed reaction liquid is filtered, the PNBI/CB/Cu catalyst is recovered, the solvent is removed by rotary evaporation of the filtrate, and the boron addition reaction product of the alpha, beta-unsaturated aldehyde ketone is obtained after column chromatography.
Further, the method comprises the step 3) of adding sodium perborate into the mixed reaction liquid of the boron addition product for generating the alpha, beta-unsaturated aldehyde ketone, and reacting for 1-3 hours to generate a hydroxyl compound.
Since boron compounds are less stable and are not easily separated, they can be converted into hydroxy compounds. With an excess of sodium perborate, THF and H2O is taken as a solvent, oxidized for 2 hours, extracted, dried by spinning, and separated by column chromatography to obtain the product. The conversion of the organoboron compound to the beta-hydroxy compound is an important application in industrial production, because the beta-hydroxy structure is widely existed in a drug molecular structure, if a strategy of 'one-pot method' is adopted, firstly, the boron addition of a substrate alpha, beta-unsaturated aldehyde ketone is realized, and then, the substrate alpha, beta-unsaturated aldehyde ketone is continuously converted into the beta-hydroxy compound without separation, so that the synthesis steps of the beta-hydroxy product are simplified, and the method has very important application value in the fields of drug synthesis and the like.
Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.
Detailed Description
For a better understanding of the present invention, the following further illustrates the present invention with reference to the accompanying fig. 1-5 and the specific embodiments, but the present invention is not limited to the following embodiments.
The specific solution provided by the invention is as follows:
example 1
(1) Preparation of norbornene copolymer: mixing a first monomer, a second monomer and a third monomer of the norborneol according to a ratio of 1:1, taking 345.44mg of first monomer, 311.38mg of second monomer, 431.53mg of third monomer and 20mg of catalyst Grubbs-I, adding 50mL of dichloromethane to dissolve to obtain reaction liquid A, stirring at room temperature for 2 hours under argon atmosphere, adding 5mL of vinyl ether, continuously stirring for 10min to obtain reaction liquid B, carrying out rotary evaporation concentration on the reaction liquid B, slowly pouring the reaction liquid B into ether to separate out precipitate, filtering, washing the separated precipitate with ether, and drying to obtain the norbornene copolymer.
(2) Preparation of norbornene copolymer/carbon black/copper: and (2) mixing 500mg of the norbornene copolymer obtained in the step (1) and 500mg of activated carbon powder, adding dichloromethane, fully dispersing, filtering, washing and drying to obtain a polynorbornene/carbon black mixture, adding the synthesized polynorbornene/carbon black into 50ml of anhydrous diethylene glycol dimethyl ether/dichloromethane mixed solvent, uniformly dispersing, adding 50.23mg of sodium borohydride, dissolving the sodium borohydride, adding 60.30mg of copper acetate, stirring at room temperature for 4 hours to obtain a reaction liquid C, dropwise adding excessive ether into the reaction liquid C, filtering, repeatedly washing with ether and removing residual solvent to obtain a black solid.
(3) Preparation of crosslinked norbornene copolymer/carbon Black three-dimensional network/copper: and heating the black solid at 160 ℃ for 6h under an argon atmosphere to obtain the PNBI/CB/Cu catalyst.
The catalyst and the intermediate product are characterized, fig. 1 is a Transmission Electron Microscope (TEM) of the crosslinked norbornene copolymer/carbon black three-dimensional network loaded copper nano catalyst PNBI/CB/Cu prepared in example 1, and it can be seen from the TEM that the copper nano particles are highly dispersed in the polymer, and the average particle size is 5 ± 3 nm. The average grain diameter of copper in the PNBI/CB/Cu catalyst prepared by the method is small and the dispersity is good; FIG. 2 is a gel permeation chromatography elution curve of a sample of the norbornene copolymer prepared in the step (1), the spectrum of the norbornene copolymer is good, and Table 1 is an average molecular weight scale of the norbornene copolymer, and the number average molecular weight M of the norbornene copolymer can be knownp15425.
Table 1:
note: mnNumber average molecular weight, MwWeight average molecular weight, MpPeak molecular weight, Mz-z average molecular weight, Mz+1-z +1 average molecular weight, Polydispersity-Polydispersity.
Example 2
(1) Preparation of norbornene copolymer: mixing a first monomer, a second monomer and a third monomer of the norborneol according to a ratio of 1: 0.75: 0.75, adding 345.44mg of the first monomer, 233.53mg of the second monomer, 323.66mg of the third monomer and 8.23mg of Grubbs-I as a catalyst into 50mL of dichloromethane for dissolution to obtain a reaction solution A, stirring at room temperature for 1h under an argon atmosphere, adding 2mL of vinyl ether, stirring for 5min to obtain a reaction solution B, carrying out rotary evaporation and concentration on the reaction solution B, slowly pouring the reaction solution B into ether to separate out a precipitate, filtering, washing the separated precipitate with ether, and drying to obtain the norbornene copolymer.
(2) Preparation of norbornene copolymer/carbon black/copper: mixing 500mg of the norbornene copolymer polymer prepared in the step (1) and 214mg of activated carbon powder, adding dichloromethane, fully dispersing, filtering, washing and drying to obtain a polynorbornene/carbon black mixture, adding the synthesized polynorbornene/carbon black into 50ml of anhydrous diethylene glycol dimethyl ether/dichloromethane mixed solvent for uniform dispersion, adding 25.82mg of sodium borohydride, adding 24.01mg of copper acetate after the sodium borohydride is dissolved, stirring at room temperature for 2 hours to obtain a reaction liquid C, dropwise adding excessive ether into the reaction liquid C, filtering, repeatedly washing with ether and removing residual solvent to obtain a black solid.
(3) Preparation of crosslinked norbornene copolymer/carbon Black three-dimensional network/copper: and heating the black solid at 150 ℃ for 7h under an argon atmosphere to obtain the PNBI/CB/Cu catalyst.
Example 3
(1) Preparation of norbornene copolymer: mixing a first monomer, a second monomer and a third monomer of the norborneol according to a ratio of 1: 1.25: 1.25, taking 345.44mg of the first monomer, 389.23mg of the second monomer, 539.41mg of the third monomer and 41.14mg of Grubbs-I as a catalyst, adding 50mL of dichloromethane to dissolve the first monomer, obtaining a reaction solution A, stirring the reaction solution A for 3 hours at room temperature under an argon atmosphere, adding 8mL of vinyl ether, stirring the reaction solution B for 20 minutes to obtain a reaction solution B, performing rotary evaporation and concentration on the reaction solution B, slowly pouring the reaction solution B into ether to separate out a precipitate, filtering the precipitate, washing the precipitate with ether, and drying the precipitate to obtain the norbornene copolymer.
(2) Preparation of norbornene copolymer/carbon black/copper: mixing 500mg of the norbornene copolymer polymer prepared in the step (1) and 1167mg of activated carbon powder, adding dichloromethane, fully dispersing, filtering, washing and drying to obtain a polynorbornene/carbon black mixture, adding the synthesized polynorbornene/carbon black into 50ml of an anhydrous diethylene glycol dimethyl ether/dichloromethane mixed solvent for dispersing, adding 75.32mg of sodium borohydride, adding 120.56mg of copper acetate after the sodium borohydride is dissolved, stirring at room temperature for 6 hours to obtain a reaction liquid C, dropwise adding excessive ether into the reaction liquid C, filtering, repeatedly washing with ether and removing residual solvent to obtain a black solid.
(3) Preparation of crosslinked norbornene copolymer/carbon Black three-dimensional network/copper: and heating the black solid at 170 ℃ for 4h under an argon atmosphere to obtain the PNBI/CB/Cu catalyst.
As shown in FIGS. 3 to 5, FIGS. 3, 4 and 5 are NMR spectra of the polymers obtained in example 1, example 2 and example 3, respectively, and the ratios of the characteristic peaks (. delta.7.26-7.41, 4.56, 4.40) are 5.64:0.99:2.00, 5.00:0.75:1.68 and 5.00:1.25:2.50, respectively, which are close to theoretical ratios of 5.00:1.00:2.00, 5.00:0.75:1.50 and 5.00:1.25:2.50, respectively, whereby the structural composition of the polymer can be adjusted by controlling the addition ratio of the three monomers, thereby controlling the hydrophilic-lipophilic balance of the crosslinked norbornene copolymer.
Examples 4 to 6
Similar to example 1, except that: the amount of Grubbs-I added was varied, 10.05mg, 30.23mg and 40.15mg for Grubbs-I in examples 4-6, respectively, and the number average molecular weights of the resulting copolymers were 16510, 14303 and 13569, respectively, i.e., the smaller the amount of catalyst used, the higher the molecular weight, and therefore, by controlling the amount of polymerization catalyst added, the molecular weight of the polymer was controlled, and copolymers of different molecular weights could be synthesized as desired.
Example 7
Adding 0.20mmol of chalcone, 0.24mmol of pinacol diboron and 0.000375mmol of catalyst into a mixed solvent of 1ml of tetrahydrofuran and 1ml of water, stirring for 12 hours at room temperature, filtering the PNBI/CB/Cu catalyst, performing rotary evaporation on the filtrate to remove the solvent, separating by column chromatography to obtain a boron addition reaction product, adding excessive sodium borate, oxidizing the boron addition reaction product into a hydroxyl compound, wherein the yield of the hydroxyl compound product is 94%, and the yield of the product in the Suzuki coupling reaction is still higher than 90% after the catalyst is recycled for 7 times.
The reaction formula is as follows:
wherein, the PNBI/CB/Cu catalyst after reaction is filtered, fully washed by ethyl acetate and ethanol for a plurality of times, and then dried, so that the PNBI/CB/Cu catalyst can be reused.
Example 8
Similar to example 7, except that the α, β -unsaturated aldehyde ketone used was 4-bromochalcone, the yield of the hydroxy compound product reached 90%, and the catalyst was recycled 7 times, the yield of the product was still higher than 85%.
The PNBI/CB/Cu catalyst provided by the embodiment of the invention has high catalytic activity, low feeding, high product yield of catalyzing boron addition reaction of alpha, beta-unsaturated aldehyde ketone and still has higher activity after repeated recycling.
Although embodiments of the present invention have been described in detail above, those of ordinary skill in the art will understand that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the claims and their equivalents.