CN116410389A - Organic phosphine ligand polymer and preparation method and application thereof - Google Patents

Organic phosphine ligand polymer and preparation method and application thereof Download PDF

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CN116410389A
CN116410389A CN202111674374.8A CN202111674374A CN116410389A CN 116410389 A CN116410389 A CN 116410389A CN 202111674374 A CN202111674374 A CN 202111674374A CN 116410389 A CN116410389 A CN 116410389A
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ligand polymer
compound
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organic phosphine
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杨春基
杨勇
赵光辉
高萌
刘金成
曾群英
陈谦
李琛
周一思
李文鹏
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Petrochina Co Ltd
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    • B01J31/18Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
    • B01J31/1845Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
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    • B01J31/2495Ligands comprising a phosphine-P atom and one or more further complexing phosphorus atoms covered by groups B01J31/1845 - B01J31/1885, e.g. phosphine/phosphinate or phospholyl/phosphonate ligands
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Abstract

The invention provides an organic phosphine ligand polymer, a preparation method and application thereof, wherein the structure of the organic phosphine ligand polymer is shown as a general formula (I),
Figure DDA0003451041290000011
wherein R is 1 And R is 2 Selected from the same or different phosphorus-containing groups, m is 35-45, n is 35-1350. The organophosphine ligand polymers of the present invention are prepared by forming heterogeneous rhodiumThe catalyst system not only has high activity and high selectivity of a homogeneous catalyst, but also has the convenience in separating the catalyst from products, and can greatly reduce the production cost.

Description

Organic phosphine ligand polymer and preparation method and application thereof
Technical Field
The invention relates to the technical field of olefin hydroformylation, in particular to an organic phosphine ligand polymer, a preparation method and application thereof.
Background
The hydroformylation of olefins is a reaction for converting olefins, hydrogen and carbon monoxide into aldehydes using a transition metal catalyst, and has been developed as one of the most important industrial homogeneous catalytic reactions. The ability to produce aldehydes and alcohols by hydroformylation has been statistically more than 1000 ten thousand t/a worldwide.
The hydroformylation reaction process has the characteristics of strong atom economy, wide product application and the like, but olefin substrates are mainly concentrated on a-olefin and internal olefin in industrial production so far, but the hydroformylation reaction of butadiene is challenging, and mainly because the hydroformylation reaction process of butadiene is relatively complex, multiple reaction paths such as 1, 4-addition carbonylation, 1, 2-addition carbonylation, carbon-carbon double bond isomerization and the like can occur, and meanwhile, the reaction rate is slow, the regioselectivity is difficult to control, and more than ten isomerization products and byproducts are simultaneously generated. Butadiene is therefore a very challenging substrate in hydroformylation reactions, where the design synthesis of phosphine ligands of different structural types is critical to the development of this technology.
Based on the current situation, researchers design and synthesize phosphine ligands and ligand polymers with novel structures, apply the phosphine ligands and ligand polymers to hydroformylation reaction, and realize the recycling of ligands and catalysts through heterogeneous catalysis. EP33554A2 discloses a process for the carbonylation of conjugated dienes, the product being predominantly valeraldehyde with little formation of dialdehydes; US4769498A discloses that polyphosphite ligand polymers with rhodium catalysts can be used in the hydroformylation of 1, 4-hexadiene and 1, 7-octadiene; WO9740003a discloses a class of phosphite bidentate ligands and their use in the hydroformylation of 1, 3-butadiene with a glyoxal selectivity of 22%; CN1087078A discloses a class of polyphosphite ligands, wherein the optimal ligand is 110 ℃, the conversion of 1, 3-butadiene reaches 99% at 900psig, and the glyoxal selectivity is 30%; CN108137451a discloses a class of bidentate phosphine ligands for hydroformylation of 1, 3-butadiene, diacetal of 1, 6-glyoxal accounting for 73% of the total product at 3MPa, 120 ℃ for 18 h; CN110343209a and CN109942750a disclose a phosphoramidite bidentate phosphine ligand copolymer with a conversion of approximately 100%, a linear aldehyde selectivity of 90%, and an l/b value of about 150; CN109836318A discloses an organic phosphine ligand polymer containing Xantphos, and the ligand is applied to a fixed bed catalytic hydroformylation reaction of 1-octene, the TOF value of the optimal condition can be more than 700, and the l/b value can also be about 30.
In addition, many publications report on the preparation of 1, 6-hexanedial by hydroformylation of 1, 3-butadiene, such as J.mol.Catal.A: chem.,1998,133,289 screened a series of phosphine ligands, found that DIOP was most selective for hydroformylation of 1, 3-butadiene, and that 1, 6-hexanedial could reach 37%; organometallics,2015,34,841; ACS catalyst.2016, 6,2802; mol.catalyst, 2020,484,110721 also gives similar results, 1, 6-hexanedial selectivity can be increased to 40% by condition optimization; organometallics,2011,30,3643-3651; ACS catalyst, 2014,4,3593-3604; the optimal structural glyoxal selectivity in phosphonite ligands reported in the literature for Organometallics,2015,34,4102-4108, et al, is close to 50%.
Among them, WO9740003a and CN1087078A disclose a class of phosphite bidentate ligands and polyphosphite ligands, and apply them to the hydroformylation of 1, 3-butadiene with a glyoxal selectivity of less than 30%, a disadvantage of this technique or a disadvantage relative to the present invention: the ligand has low catalytic efficiency for the hydroformylation of butadiene; CN110343209A, CN109942750a and CN109836318A disclose a bidentate phosphine ligand copolymer polymerized with an organophosphine ligand to form a catalytic system with transition metal salts for hydroformylation of terminal olefins or isomerization-hydroformylation of internal olefins; the disadvantages of this technique or the shortcomings with respect to the present invention are: the ligand is used for terminal olefin hydroformylation or isomerization-hydroformylation of internal olefins.
Through research and study for many years, the technology for preparing glyoxal by hydroformylation of butadiene still has the problems of low reaction rate, poor regioselectivity and difficult product separation, industrial production is not realized yet, and the technology is still in a laboratory stage at present. Based on the current situation, the novel heterogeneous catalytic system is developed, so that the heterogeneous catalyst has high activity and high selectivity, and simultaneously has the convenience in separating the catalyst from a product, and is a research key point and a main development direction for realizing the directional preparation of the glyoxal by the hydroformylation of butadiene in the future.
Disclosure of Invention
In order to solve the technical problems, the invention aims to provide an organic phosphine ligand polymer, a preparation method and application thereof, and a heterogeneous rhodium catalyst system is formed, so that the heterogeneous rhodium catalyst system has high activity and high selectivity of a homogeneous catalyst, and simultaneously has the convenience in separating the catalyst from a product, and the production cost can be greatly reduced.
In order to achieve the aim, the invention provides an organic phosphine ligand polymer, the structure of which is shown as a general formula (I),
Figure BDA0003451041270000031
wherein R is 1 And R is 2 Selected from the same or different phosphorus-containing groups, R 1 And R is 2 Each independently selected from the following structures, wherein "," means the attachment location, and the same applies below.
Figure BDA0003451041270000032
R 3 Selected from the group consisting of
Figure BDA0003451041270000033
m is 35-45, n is 35-1350.
According to a specific embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, R 1 And R is 2 Each independently selected from
Figure BDA0003451041270000034
According to a specific embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, R 3 Selected from the group consisting of
Figure BDA0003451041270000035
Figure BDA0003451041270000036
According to an embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, the organophosphine ligand polymer is formed by copolymerizing a bidentate phosphine monomer having a structure represented by the general formula (II) and a vinyl monomer having a structure of
Figure BDA0003451041270000041
Figure BDA0003451041270000042
According to a specific embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, the vinyl monomer is selected from one or more of the following structures.
Figure BDA0003451041270000043
According to an embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, the molar ratio of the bidentate phosphine monomer to the vinyl monomer is 1 (1-30).
According to a specific embodiment of the present invention, in the above-mentioned organophosphine ligand polymer, preferably, m: n is 1 (1-30), more preferably, 1:10.
According to a specific embodiment of the present invention, preferably, the molecular weight of the organophosphine ligand polymer ranges from 50000 to 200000g/mol.
According to a specific embodiment of the present invention, preferably, the polymerization degree of the organophosphine ligand polymer is 35 to 55.
According to a particular embodiment of the invention, preferably the organophosphine ligand polymer is selected from the group consisting of L 1 Or L 2 The structural formula is as follows.
Figure BDA0003451041270000044
Figure BDA0003451041270000051
Wherein m is 35-45, n is 35-1350.
The invention also provides a preparation method of the organic phosphine ligand polymer, which comprises the following steps:
s1: under the condition of inert gas atmosphere and triethylamine, R is reacted with the mixture 1 -Cl and/or R 2 -Cl, compound 2, in a first solvent, to perform a reaction, quenching the reaction, collecting and purifying the reaction product, obtaining the bidentate phosphine monomer;
s2: under the condition of inert gas atmosphere and the existence of azodiisobutyronitrile, enabling the bidentate phosphine monomer and the vinyl monomer to fully contact in a second solvent for copolymerization reaction, terminating the reaction, and collecting and purifying a reaction product to obtain the organic phosphine ligand polymer;
wherein the structure of the compound 2 is
Figure BDA0003451041270000052
According to a specific embodiment of the present invention, in the above preparation method, preferably, in S2, the copolymerization reaction temperature is 60-100 ℃ and the reaction time is 2-6h.
According to a specific embodiment of the present invention, in the above preparation method, preferably, in S2, the second solvent is selected from one or more of tetrahydrofuran, 2-methyltetrahydrofuran, and toluene.
According to a specific embodiment of the present invention, in the above preparation method, preferably, in S1, the reaction temperature is 0 to 30 ℃ and the reaction time is 5 to 10 hours.
According to a specific embodiment of the present invention, in the above preparation method, preferably, in S1, the first solvent is one or more selected from tetrahydrofuran, toluene, and N, N-dimethylformamide.
According to a specific embodiment of the present invention, preferably, the above preparation method further includes a step of preparing the compound 2, and the preparation method of the compound 2 includes: and (3) under the action of nitrogen atmosphere and a catalyst, enabling the compound 1 and an vinylation reagent to be fully contacted in a third solvent for performing vinylation reaction, and collecting and purifying a reaction product to obtain the compound 2.
According to a specific embodiment of the present invention, in the preparation method of the compound 2, preferably, the vinylation reaction temperature is 10-60 ℃ and the reaction time is 5-10h.
According to a specific embodiment of the present invention, in the method for producing compound 2, preferably, the vinylating agent is selected from the group consisting of
Figure BDA0003451041270000061
One or more of the following.
According to a specific embodiment of the present invention, in the preparation method of the compound 2, preferably, the catalyst is selected from tetra (triphenylphosphine) palladium, pdCl 2 (dppf) or PdCl 2 (PPh3) 2 One or more of the following.
According to a specific embodiment of the present invention, in the preparation method of the compound 2, preferably, the third solvent is selected from one or more of toluene, tetrahydrofuran, and 1, 4-dioxane.
According to a specific embodiment of the present invention, preferably, as shown in reaction formula 1, the above preparation method includes the steps of:
Figure BDA0003451041270000062
(1) Adding the compound 1 and a solvent into a reactor, then adding an vinylation reagent and a catalyst, carrying out reflux reaction under the protection of nitrogen for overnight, cooling to room temperature, distilling under reduced pressure to remove the solvent, purifying by column chromatography, and separating to obtain a compound 2;
(2) Adding phosphine chloride compound (R) into a reactor under the protection of nitrogen 1 -Cl and/or R 2 -Cl) and a solvent, cooling to 0 ℃, additionally taking the compound 2 and triethylamine to dissolve in the solvent, dripping the mixture into the reactor at 0 ℃, naturally heating to room temperature for reaction, adding water for quenching reaction, adding ethyl acetate for extraction, drying an organic phase by using anhydrous sodium sulfate, and separating by column chromatography to obtain a bidentate phosphine monomer shown in the general formula (II);
(3) Adding bidentate phosphine monomer and comonomer into reactor
Figure BDA0003451041270000063
AIBN and solvent react under the protection of nitrogen, after the reaction is finished, the reaction is cooled to room temperature, methanol is added for precipitation, filtration, methanol washing and vacuum drying are carried out, and the organic phosphine ligand polymer shown in the general formula (I) is obtained.
The invention also provides application of the organic phosphine ligand polymer in olefin hydroformylation reaction.
In accordance with a specific embodiment of the present invention, in the above application, preferably, the olefin is selected from C 4 -C 10 The olefin is more preferably butadiene.
In accordance with a specific embodiment of the present invention, in the above application, preferably, the organophosphine ligand polymer forms a heterogeneous rhodium catalyst system.
The organic phosphine ligand polymer is applied to the hydroformylation of low-carbon olefin by forming a heterogeneous rhodium catalyst system, replaces the current widely used rhodium low-pressure oxo synthesis liquid-phase circulation process in industry, simplifies the process flow and greatly reduces the production cost.
The organic phosphine ligand polymer is applied to the hydroformylation of high-carbon olefin by forming a heterogeneous rhodium catalyst system, so that the technical problem that the catalyst is difficult to separate in the hydroformylation process of the high-carbon olefin by using a homogeneous catalyst is thoroughly solved.
(1) The preparation process of the organic phosphine polymer ligand is simple, raw materials are easy to obtain, the phosphine ligand used in the method for synthesizing the copolymer ligand can be directly purchased or synthesized, and the copolymer bidentate phosphine ligand monomer can be copolymerized with a cheap and commercially available vinyl-containing compound, so that the copolymer ligand is cheap and easy to obtain. The raw materials directly react in one step to generate a bidentate phosphine ligand copolymer containing phosphite ester structures;
(2) The preparation method has high yield and good product quality. The bidentate phosphine ligand copolymer containing phosphite ester structure prepared by the method provided by the invention has the advantages that the product yield and purity are higher than 95%, and recrystallization is not needed, so that the level which cannot be achieved by the prior preparation technology is reached;
(3) The preparation method of the invention can realize the preparation of copolymer ligands in various scales. The method provided by the invention can prepare several to hundreds of grams of bidentate phosphine ligand copolymer containing phosphite ester structure at one time;
(4) The application of the organic phosphine ligand polymer simplifies the oxo process flow and reduces the production cost. The industrial device for oxo synthesis generally adopts rhodium low-pressure oxo synthesis liquid-phase circulation process, which has very wide application, but has the problems of complex flow and high production and operation cost. The organic phosphine ligand polymer developed by the invention is used as a carrier and a ligand, and the traditional oxo synthesis process is changed from the aspects of a reaction system, a separation system, a circulation system and the like, so that the production cost is greatly reduced;
(5) The application of the organic phosphine ligand polymer solves the stability problems of separation, recycling and the like of a homogeneous catalyst. In order to overcome the technical problem that a homogeneous catalyst is difficult to separate, a water-oil two-phase catalyst is usually adopted in the hydroformylation reaction of the high-carbon olefin, but in order to improve the intersolubility of the water and the oil, the reaction efficiency of the catalyst is improved, and a certain amount of surfactant is usually added into a reaction system, so that the emulsification of the reaction system is caused, and the difficulty of separating subsequent products is further increased. The organic phosphine ligand polymer developed by the invention is used as a carrier and a ligand to form single-point coordination structure catalysis, so that the activity is improved, and the problems of catalyst separation, recycling and the like are solved.
Drawings
FIG. 1 is a liquid nuclear magnetic resonance hydrogen spectrum of compound 2 in example 2;
FIG. 2 is a liquid nuclear magnetic resonance hydrogen spectrum of compound 3 in example 3;
FIG. 3 is a liquid nuclear magnetic resonance phosphorus spectrum of compound 3 of example 3;
FIG. 4 is an organic phosphine ligand polymer L of example 4 1 Hydrogen nuclear magnetic resonance spectrum of (2);
FIG. 5 is an organic phosphine ligand polymer L of example 4 1 Nuclear magnetic resonance phosphorus spectrum of (2);
FIG. 6 is an organic phosphine ligand polymer L of example 8 2 Nuclear magnetic resonance phosphorus spectrum of (2).
Detailed Description
The technical solution of the present invention will be described in detail below for a clearer understanding of technical features, objects and advantageous effects of the present invention, but should not be construed as limiting the scope of the present invention.
The present examples provide two organophosphine ligand polymers L 1 、L 2 The chemical structure of the preparation method is as follows,
Figure BDA0003451041270000081
wherein m is 35-45, n is 35-1350.
Organic phosphine ligand polymer L 1 The synthetic route of (2) is shown as the reaction scheme 2, the organic phosphine ligand polymer L 2 The synthetic route of (2) is shown in the reaction formula 3; wherein, the compound 3 is a bidentate phosphine monomer.
Figure BDA0003451041270000091
Example 1
This example synthesizes compound 1, for its synthesis, see document CN113004326a.
Example 2:
compound 2 was synthesized in this example as follows:
5g of Compound 1 was charged into a reactor, 100ml of toluene was added, and then 12g of vinyl tri-n-butyltin and 0.73g of tetrakis (triphenylphosphine) palladium were added, and the reaction was refluxed under nitrogen protection overnight. Cooling to room temperature, distilling under reduced pressure to remove solvent, purifying by column chromatography, eluting with petroleum ether: ethyl acetate=2:1, isolated to give compound 2.
As shown in fig. 1, the nuclear magnetic data thereof are as follows: 1 H NMR(400MHz,DMSO)δ9.39(s,1H),7.16(dt,J=11.2,8.2Hz,2H),6.60(d,J=8.5Hz,1H),5.56(d,J=1.4Hz,1H),5.18(dd,J=11.0,1.4Hz,1H),5.10(d,J=1.7Hz,1H),1.51(s,2H)。
example 3
Compound 3 was synthesized in this example as follows:
1.27g of the phosphine chloride in the above step 3 was taken
Figure BDA0003451041270000101
Adding the mixture into a reactor, adding 6ml of ultra-dry tetrahydrofuran under the protection of nitrogen, and cooling to 0 ℃. Another 400mg of Compound 2 and 418mg of triethylamine were dissolved in 2ml of ultra-dry tetrahydrofuran, and the mixture was added dropwise to the above-mentioned reactor at 0 ℃Naturally heating to room temperature, and reacting for 1h. Quenched by adding 20ml of water, extracted by adding 20ml of ethyl acetate, and the organic phase is dried over anhydrous sodium sulfate and separated by column chromatography to obtain the compound 3.
As shown in fig. 2 and 3, the nuclear magnetic data thereof are as follows: 1 H NMR(400MHz,CDCl 3 )δ7.22(d,J=8.5Hz,2H),7.14(dd,J=17.4,11.0Hz,2H),7.03(d,J=3.8Hz,5H),6.97(d,J=8.5Hz,2H),6.92(d,J=8.3Hz,5H),5.61(dd,J=17.4,1.2Hz,2H),5.42(s,1H),5.34(dd,J=11.0,1.2Hz,2H),5.15(s,0H),2.31(d,J=7.2Hz,12H),2.21(d,J=3.6Hz,12H),1.67(q,J=9.1Hz,4H)。
example 4
This example Synthesis of an organophosphine ligand Polymer L 1 The method comprises the following steps:
400mg of Compound 3 was charged into a reactor, 450mg of styrene, 50mg of AIBN,9ml of ultra-dry tetrahydrofuran was added, and the mixture was reacted at 100℃for 4 hours under the protection of nitrogen. Cooling to room temperature, adding 20ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine polymer L 1 The nuclear magnetic hydrogen spectrum and the nuclear magnetic phosphorus spectrum are shown in fig. 4 and 5 respectively.
Wherein, m is n=1:6, the molecular weight of the polymer is 70000g/mol, the product yield is 97.8%, and the purity is 98.2%.
Example 5
This example Synthesis of an organophosphine ligand Polymer L 1 The method comprises the following steps:
400mg of Compound 3 was charged into a reactor, 500mg of styrene, 45mg of AIBN,9ml of ultra-dry tetrahydrofuran were added, and reacted at 100℃for 4 hours under the protection of nitrogen. Cooling to room temperature, adding 20ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine polymer L 1
Wherein, m is n=1:10, the molecular weight of the polymer is 95000g/mol, the product yield is 97.6 percent, and the purity is 99.3 percent.
Example 6
This example Synthesis of an organophosphine ligand Polymer L 1 The method comprises the following steps:
400mg of Compound 3 was added to a reactor, 600mg of styrene, 45mg of AIBN,9ml of ultra-dry tetrahydrofuran was added under nitrogenThe reaction was carried out at 100℃for 4 hours. Cooling to room temperature, adding 20ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine polymer L 1
Wherein, m is n=1:20, the molecular weight of the polymer is 140000g/mol, the product yield is 97.3 percent, and the purity is 98.8 percent.
Example 7
This example Synthesis of an organophosphine ligand Polymer L 1 The method comprises the following steps:
400mg of Compound 3 was charged into a reactor, 600mg of styrene, 40mg of AIBN,9ml of ultra-dry tetrahydrofuran were added and reacted at 90℃for 4 hours under the protection of nitrogen. Cooling to room temperature, adding 20ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine polymer L 1
Wherein, m is n=1:30, the molecular weight of the polymer is 180000g/mol, the product yield is 97.5%, and the purity is 99.0%.
Example 8
This example Synthesis of an organophosphine ligand Polymer L 2 The method comprises the following steps:
300mg of Compound 3 was charged into a reactor, and 1.0g of tris (4-vinylphenyl) phosphine, 35mg of AIBN,15ml of ultra-dry tetrahydrofuran were added and reacted at 100℃for 4 hours under nitrogen. Cooling to room temperature, adding 30ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine ligand polymer L 2 The nuclear magnetic phosphorus spectrum is shown in FIG. 6.
Wherein, m is n=1:6, the molecular weight of the polymer is 85000g/mol, the product yield is 96.8 percent, and the purity is 98.9 percent.
Example 9
This example Synthesis of an organophosphine ligand Polymer L 2 The method comprises the following steps:
300mg of Compound 3 was charged into a reactor, and 1.22g of tris (4-vinylphenyl) phosphine, 35mg of AIBN,15ml of ultra-dry tetrahydrofuran were added and reacted at 100℃for 4 hours under nitrogen. Cooling to room temperature, adding 30ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine ligand polymer L 2
Wherein, m is n=1:10, the molecular weight of the polymer is 11000g/mol, the product yield is 97.1 percent, and the purity is 99.1 percent.
Example 10
This example Synthesis of an organophosphine ligand Polymer L 2 The method comprises the following steps:
300mg of Compound 3 was charged into a reactor, and 1.50g of tris (4-vinylphenyl) phosphine, 35mg of AIBN,15ml of ultra-dry tetrahydrofuran were added and reacted at 95℃for 4 hours under nitrogen. Cooling to room temperature, adding 30ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine ligand polymer L 2
Wherein, m is n=1:20, the molecular weight of the polymer is 165000g/mol, the product yield is 96.8 percent, and the purity is 98.8 percent.
Example 11
This example Synthesis of an organophosphine ligand Polymer L 2 The method comprises the following steps:
300mg of Compound 3 was charged into a reactor, and 1.80g of tris (4-vinylphenyl) phosphine, 30mg of AIBN,15ml of ultra-dry tetrahydrofuran were added and reacted at 85℃for 4 hours under nitrogen. Cooling to room temperature, adding 30ml of methanol for precipitation, filtering, washing with methanol, and drying in vacuum to obtain an organic phosphine ligand polymer L 2
Wherein, m is n=1:30, the molecular weight of the polymer is 195000g/mol, the product yield is 96.2 percent, and the purity is 98.6 percent.
Example 12
This example provides an organophosphine ligand polymer L 2 Use of (m=36, n=52, m: n=1:1.44) in the hydroformylation of butadiene, in particular as follows:
in a glove box, 20mg of the organophosphine ligand polymer L was taken separately 2 And 1mg of rhodium metal precursor Rh (acac) (CO) 2 Adding into autoclave, adding 3ml toluene, sealing the autoclave, and introducing H with pressure of 2MPa and volume ratio of 1:1 2 Mixing with CO gas, stirring at 80deg.C for 2 hr to obtain catalyst; cooling, adding 1ml of 1, 3-butadiene toluene solution with the concentration of 3mol/L, pressurizing to 4MPa, and stirring at 80 ℃ for reaction for 12 hours to prepare the 1, 6-glyoxal.
The conversion of 1, 3-butadiene was 99.5% and the selectivity of 1, 6-glyoxal was 53.4% as measured by gas chromatography internal standard method.
Example 13
As in example 12, this example provides an organophosphine ligand polymer L 2 The only difference in the use in olefin polymerization is the organophosphine ligand polymer L of the present example 2 M=25, n=52, m:n=0.48. The method comprises the following steps:
20mg of the organophosphine ligand polymer L2 and 1mg of the rhodium metal precursor Rh (acac) (CO) were taken, respectively, in a glove box 2 Adding into autoclave, adding 3ml toluene, sealing the autoclave, and introducing H with pressure of 2MPa and volume ratio of 1:1 2 Mixing with CO gas, stirring at 80deg.C for 2 hr to obtain catalyst; cooling, adding 1ml of 1, 3-butadiene toluene solution with the concentration of 3mol/L, pressurizing to 4MPa, and stirring at 80 ℃ for reaction for 12 hours to prepare the 1, 6-glyoxal.
The conversion of 1, 3-butadiene was 93.2% and the selectivity of 1, 6-glyoxal was 40.2% as measured by gas chromatography internal standard method.
Comparative example 1
As in example 12, this comparative example provides an organophosphine ligand polymer L 3 Use in olefin polymerization of the organophosphine ligand polymer L of this comparative example 3 With an organophosphine ligand polymer L 2 The only difference in comparison is that where m=36, n=1440, m: n=1:40, the other structures are identical. The method comprises the following steps:
in a glove box, 20mg of the organophosphine ligand polymer L was taken separately 3 And 1mg of rhodium metal precursor Rh (acac) (CO) 2 Adding into autoclave, adding 3ml toluene, sealing the autoclave, and introducing H with pressure of 2MPa and volume ratio of 1:1 2 Mixing with CO gas, stirring at 80deg.C for 2 hr to obtain catalyst; cooling, adding 1ml of 1, 3-butadiene toluene solution with the concentration of 3mol/L, pressurizing to 4MPa, and stirring at 80 ℃ for reaction for 12 hours to prepare the 1, 6-glyoxal.
The conversion of 1, 3-butadiene was 50.5% and the selectivity of 1, 6-glyoxal was 13.7% as measured by gas chromatography internal standard method. The organophosphine ligand polymer L of this comparative example 3 M: the value of n is too small, and the application effect in the hydroformylation of olefinPoor.

Claims (10)

1. An organic phosphine ligand polymer is characterized in that the structure is shown as a general formula (I),
Figure FDA0003451041260000011
wherein R is 1 And R is 2 Selected from the same or different phosphorus-containing groups, R 1 And R is 2 Each independently selected from the following structures:
Figure FDA0003451041260000012
R 3 selected from the group consisting of
Figure FDA0003451041260000013
m is 35-45, n is 35-1350.
2. The organophosphine ligand polymer according to claim 1, wherein R 1 And R is 2 Each independently selected from
Figure FDA0003451041260000014
Preferably, R 3 Selected from the group consisting of
Figure FDA0003451041260000015
3. The polymer of an organic phosphine ligand according to claim 1 or 2, wherein the polymer of an organic phosphine ligand is formed by copolymerizing a bidentate phosphine monomer and a vinyl monomer, the structure of the bidentate phosphine monomer is shown as a general formula (II), and the structure of the vinyl monomer is that
Figure FDA0003451041260000021
Figure FDA0003451041260000022
4. An organophosphine ligand polymer according to claim 1 or 2, wherein m: n is 1 (1-30);
preferably, the molecular weight range of the organic phosphine ligand polymer is 50000-200000g/mol;
preferably, the organophosphine ligand polymer has a degree of polymerization of 35 to 55.
5. A process for the preparation of an organophosphine ligand polymer according to any one of claims 1 to 4, comprising the steps of:
s1: under the condition of inert gas atmosphere and triethylamine, R is reacted with the mixture 1 -Cl and/or R 2 The Cl and the compound 2 are fully contacted in a first solvent for reaction, the reaction is quenched, and the reaction product is collected and purified to obtain a bidentate phosphine monomer;
s2: under the condition of inert gas atmosphere and the existence of azodiisobutyronitrile, enabling the bidentate phosphine monomer and the vinyl monomer to fully contact in a second solvent for copolymerization reaction, terminating the reaction, and collecting and purifying a reaction product to obtain the organic phosphine ligand polymer;
wherein the structure of the compound 2 is
Figure FDA0003451041260000023
6. The process according to claim 5, wherein in S2, the copolymerization reaction temperature is 60 to 100℃and the reaction time is 2 to 6 hours;
preferably, the second solvent is selected from one or more of tetrahydrofuran, 2-methyltetrahydrofuran and toluene;
preferably, in S1, the reaction temperature is 60-100 ℃ and the reaction time is 2-6h;
preferably, in S1, the first solvent is selected from one or more of tetrahydrofuran, toluene, N-dimethylformamide.
7. The production method according to claim 5, characterized in that the production method further comprises a step of producing the compound 2, the production method of the compound 2 comprising: and (3) under the action of nitrogen atmosphere and a catalyst, enabling the compound 1 and an vinylation reagent to be fully contacted in a third solvent for performing vinylation reaction, and collecting and purifying a reaction product to obtain the compound 2.
8. The process according to claim 7, wherein the vinylation reaction temperature is 10-60 ℃ and the reaction time is 5-10 hours;
preferably, the vinylating agent is selected from
Figure FDA0003451041260000031
One or more of the following;
preferably, the catalyst is selected from tetrakis (triphenylphosphine) palladium, pdCl 2 (dppf) or PdCl 2 (PPh3) 2 One or more of the following;
preferably, the third solvent is selected from one or more of toluene, tetrahydrofuran, 1, 4-dioxane.
9. Use of an organophosphine ligand polymer according to any one of claims 1 to 4, in an olefin hydroformylation reaction.
10. The use according to claim 9, wherein the olefin is selected from C 4 -C 10 Olefins, preferably butadiene;
preferably, the organophosphine ligand polymer forms a heterogeneous rhodium catalyst system.
CN202111674374.8A 2021-12-31 2021-12-31 Organic phosphine ligand polymer and preparation method and application thereof Pending CN116410389A (en)

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