Nothing Special   »   [go: up one dir, main page]

CN117443380A - Biochar-supported iron catalyst and application thereof - Google Patents

Biochar-supported iron catalyst and application thereof Download PDF

Info

Publication number
CN117443380A
CN117443380A CN202311298943.2A CN202311298943A CN117443380A CN 117443380 A CN117443380 A CN 117443380A CN 202311298943 A CN202311298943 A CN 202311298943A CN 117443380 A CN117443380 A CN 117443380A
Authority
CN
China
Prior art keywords
catalyst
biochar
butanone
iron
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.)
Pending
Application number
CN202311298943.2A
Other languages
Chinese (zh)
Inventor
任兰会
姜莉雅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Quzhou Research Institute of Zhejiang University
Original Assignee
Quzhou Research Institute of Zhejiang University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Quzhou Research Institute of Zhejiang University filed Critical Quzhou Research Institute of Zhejiang University
Priority to CN202311298943.2A priority Critical patent/CN117443380A/en
Publication of CN117443380A publication Critical patent/CN117443380A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • B01J37/082Decomposition and pyrolysis
    • B01J37/084Decomposition of carbon-containing compounds into carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • B01J37/082Decomposition and pyrolysis
    • B01J37/088Decomposition of a metal salt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/32Freeze drying, i.e. lyophilisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C221/00Preparation of compounds containing amino groups and doubly-bound oxygen atoms bound to the same carbon skeleton

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a biochar-supported iron monoatomic catalyst and application thereof, wherein Phellinus linteus mycelium is used as a biochar pyrolysis precursor, iron ions are complexed on the surface of the biochar pyrolysis precursor, and the biochar-supported iron monoatomic catalyst is obtained by pyrolysis in an inert gas atmosphere. 4-hydroxy-2-butanone and different aniline compounds are used as reaction substrates, a biochar-supported iron single-atom catalyst is used, acetone or butanone is used as a solvent, and the N-alkylation product is obtained by reaction at room temperature in a nitrogen atmosphere. The invention uses Phellinus as a pyrolysis precursor of a carbon carrier for the first time to prepare the monoatomic catalyst. The biochar single-atom catalyst prepared by the invention has the appearance similar to that of a carbon nano tube. The invention uses the iron monoatomic catalyst for catalyzing the alcohol amination reaction of aniline and 4-hydroxy-2-butanone for the first time.

Description

Biochar-supported iron catalyst and application thereof
Technical Field
The invention relates to an iron monoatomic catalyst loaded by biochar, an aniline compound and alcohol amination reaction of 4-hydroxy-2-butanone.
Background
The C-N bond exists as an important structural fragment in a large number of bioactive molecules and pharmaceutical molecules, and is widely used in the fields of fine chemistry and medicine, such as synthesis of beta-amino acids, beta-amino alcohols, 1, 3-diaminoalkanes, lactams, nikkomycins, and the like. Methods for synthesizing C-N bonds are numerous, such as halogenSubstituted hydrocarbon substitution reaction, aza-Michael addition reaction, aromatic halohydrocarbon coupling reaction, mannich reaction, high enol or allyl alcohol oxidative amination reaction, and the like. The direct substitution of the alcoholic hydroxyl group by the amine is one of important methods for preparing the C-N bond, the raw materials are easy to obtain, and the byproduct is H 2 O, green and environment-friendly and has high atom economy. However, neither thermodynamic nor kinetic, hydroxyl is a good leaving group and requires prior conversion to halogenated hydrocarbons, p-toluenesulfonates, sulfonates, and the like. The direct substitution reaction of the alcoholic hydroxyl group is carried out The medicine round table conference is selected as one of ten green chemical key research fields.
In 1981, grigg and Watanabe reported almost simultaneously that rhodium, iridium and ruthenium catalyzed the reaction of amine directly substituted alcoholic hydroxyl groups, and opened the study of amine directly substituted alcoholic hydroxyl groups. Thereafter, various methods for catalyzing the direct substitution of an alcoholic hydroxyl group by an amine have been reported, and catalysts involving metal salts or complexes of silver, gold, iridium, palladium, rhenium, ruthenium, cobalt, copper, iron, manganese, nickel, and the like, bimetallic catalytic systems and nonmetallic catalytic systems (enzymes, aldehydes, ketones, iodine, carbon materials, and organophosphines) have also been reported.
The invention uses the iron single-atom catalyst loaded by the biochar for catalyzing the alcohol amination reaction of 4-hydroxy-2-butanone and aniline compounds for the first time. The method provided by the invention is quick, simple, convenient, environment-friendly, low in cost and easy to industrialize, and the prepared biochar loaded iron monoatomic catalyst is good in stability and has a good application prospect in the field of alcohol amination reaction.
Disclosure of Invention
The invention discloses a biochar-supported iron monoatomic catalyst and an application thereof in catalyzing alcohol amination reaction of 4-hydroxy-2-butanone and aniline compounds.
4-hydroxy-2-butanone and different aniline compounds are used as reaction substrates, a biochar-supported iron single-atom catalyst is used, acetone or butanone is used as a solvent, and the N-alkylation product is obtained by reaction at room temperature in a nitrogen atmosphere. The invention uses Phellinus as a pyrolysis precursor of a carbon carrier for the first time to prepare the monoatomic catalyst. The biochar single-atom catalyst prepared by the invention has the appearance similar to that of a carbon nano tube. The invention uses the iron monoatomic catalyst for catalyzing the alcohol amination reaction of aniline and 4-hydroxy-2-butanone for the first time.
In the technical scheme, 2-5g (preferably 3-4 g) of Phellinus linteus mycelium is firstly dispersed in 150mL of physiological saline by ultrasonic, then 2-6mmol (preferably 5-5.5 mmol) of soluble ferric salt is added into the dispersion liquid, and the ferric ion is surface-complexed under the condition of 60-100 ℃ (preferably 80-90 ℃).
In the technical scheme, the ultrasonic dispersion pretreatment time is 20-50min, preferably 30-40min; the ultrasonic treatment power is 40-100kw; the time for complexing the iron ions on the surface is 12-24 hours; after complexing iron ions on the surface of Phellinus linteus mycelium, cooling to room temperature, centrifuging, collecting Phellinus linteus mycelium, washing with water, and freeze drying.
In the technical scheme, the soluble manganese salt is one of ferric chloride, ferric nitrate or ferric sulfate.
In the technical scheme, the pyrolysis temperature of the Phellinus linteus mycelium is 600-1000 ℃ (preferably 700-800 ℃) for 1-4 hours (preferably 1-2 hours).
In the technical scheme, the inert atmosphere is one of nitrogen or argon; 1g of dried Phellinus linteus mycelium is introduced into an inert atmosphere at an air flow rate of 10-30mL/min; the heating rate from room temperature to pyrolysis temperature is 2-5 ℃/min; the temperature reduction rate from the pyrolysis temperature to 40 ℃ after pyrolysis is 2-5 ℃/min; the prepared biochar-supported iron single-atom catalyst has a morphology similar to that of a carbon nano tube. Iron is dispersed on the biochar carrier in the form of single atoms.
In the technical scheme, in the nitrogen atmosphere, the biochar-supported iron single-atom catalyst catalyzes 4-hydroxy-2-butanone and different aniline compounds to perform an alcohol amination reaction to prepare 4- (N-phenyl) -2-butanone compounds.
In the technical proposal, the different aniline compounds are aniline, 2-chloroaniline, 3-bromoaniline, 4-fluoroaniline, 2-methylaniline, 3-methoxyaniline, 4-nitroaniline and 4-trifluoromethyl aniline
In the technical scheme, the concentration of the 4-hydroxy-2-butanone in the solvent is 0.5-1mol/L, preferably 0.5mol/L; the concentration of the aniline compound in the solvent is 0.5-1mol/L, preferably 0.5mol/L. The molar ratio of the 4-hydroxy-2-butanone to the aniline compound is 1:2-2:1, and the preferable molar ratio is 1:1. The amount of the biochar-supported iron single-atom catalyst is 10-30mg, preferably 20mg. The reaction time is 4 to 12 hours, preferably 8 hours.
Due to the application of the scheme, compared with the prior art, the invention has the following advantages:
1. according to the preparation method, phellinus linteus mycelium is used as a pyrolyzing precursor of a carbon carrier for the first time to prepare the biochar-supported iron single-atom catalyst, a non-renewable carbon source, an expensive template agent, an activating agent and a hetero-atom source are not required to be used, and the biochar-supported iron single-atom catalyst can be recycled;
2. the reaction does not need to add an alkaline additive additionally;
3. the reaction is carried out at room temperature without heating;
4. the reaction has good selectivity and no other byproducts.
Drawings
FIG. 1A scanning electron microscope spectrogram of a catalyst (Cat-700);
FIG. 2A transmission electron microscope spectrum of the catalyst (Cat-700) for spherical aberration correction.
Detailed Description
The present invention will be described in detail with reference to examples, but the scope of the present invention is not limited to the examples.
Examples
Example 1 preparation method of biochar-supported iron monatomic catalyst
In a 250mL round bottom flask, a magnetic stirrer rotor, 3g Phellinus linteus mycelium and 150mL physiological saline were added and sonicated (power 40kw for 30 min). At room temperature, 5mmol of ferric chloride was slowly added and stirring was continued for 30min. Then stirred at 80℃for 12h. Cooling to room temperature, centrifuging (10000 r/min,10 min), collecting Phellinus linteus mycelium, washing with deionized water for 3 times, and freeze drying. 1g of the freeze-dried material prepared in the above step was taken in a quartz boat, and the quartz boat was placed in a tube furnace, and nitrogen gas was introduced at room temperature for 30 minutes (gas flow rate: 10 mL/min). Then, the nitrogen flow rate was kept unchanged, and the temperature was raised to 700 ℃ (the temperature raising rate from room temperature to pyrolysis temperature was 5 ℃/min). The nitrogen flow rate is kept unchanged, and after pyrolysis is kept at 700 ℃ for 1h, the temperature is slowly reduced to 30 ℃ (the temperature reduction rate is 5 ℃/min).
The black solid in the quartz boat was ground into powder in an agate mortar to obtain a biochar-supported iron monoatomic catalyst (labeled Cat-700) in a mass yield of 27% (relative to Phellinus linteus mycelium).
The preparation methods of Cat-800 and Cat-900 are identical to the preparation process of Cat-700 described above, except that the pyrolysis temperatures are different. The pyrolysis temperatures of Cat-800 and Cat-900 were 800℃and 900℃respectively, and the yields were 28% and 27%, respectively.
The elemental composition and atomic percentage content of the biochar-supported iron monoatomic catalyst surface were analyzed using X-ray photoelectron spectroscopy techniques. The surface of the biochar-supported iron single-atom catalyst consists of carbon, nitrogen, oxygen, phosphorus and iron, wherein the content of carbon element is maximum and exceeds 84at%; secondly, nitrogen element with the content of 6.35 to 7.07at percent; the content of oxygen element is 5.61-6.15at%; the content of the phosphorus element is 1.32 to 1.71at%; the content of iron element is minimum (0.77-0.96 at%). The element content of the surface of the biochar-supported iron monoatomic catalyst prepared at different pyrolysis temperatures is different.
TABLE 1 surface element content of biochar Supported iron monatomic catalyst
Cat-700 scanning electron microscope (FIG. 1) shows that the morphology of the biochar-supported iron single-atom catalyst is very similar to that of the carbon nanotubes. The spherical aberration correction transmission electron microscope spectrogram (figure 2) shows that the iron element is uniformly distributed on the biochar carrier, and uniformly dispersed bright spots can be observed, which shows the atomic-level distribution of the iron element.
Scanning electron microscope spectrograms of Cat-800 and Cat-900 show that the morphology of the biochar-supported iron single-atom catalyst is very similar to that of the carbon nano tube. The spherical aberration correction transmission electron microscope spectrogram shows that the iron element is uniformly distributed on the biochar carrier, and uniformly dispersed bright spots can be observed, so that the atomic-level distribution of the iron element is illustrated.
Preparation of other biochar-supported iron monoatomic catalysts: the preparation process adopted is identical to the preparation process of Cat-700, and is different from the preparation process in that the dosage of the metal ferric salt (2-6 mmol) is changed when the biochar-supported iron single-atom catalyst is prepared, namely, the adding quantity of the metal ferric salt is replaced by 5mmol respectively by 2mmol, 3mmol, 4mmol and 6mmol, and the biochar-supported iron single-atom catalyst can be prepared. The scanning electron microscope spectrogram shows that the appearance of the biochar-supported iron single-atom catalyst is very similar to that of a carbon nano tube. The spherical aberration correction transmission electron microscope spectrogram shows that the iron element is uniformly distributed on the biochar carrier, and uniformly dispersed bright spots can be observed, so that the atomic-level distribution of the iron element is illustrated.
Example 2 4- (phenylamino) -2-butanone
The magneton, 20mg of charcoal-supported iron monoatomic catalyst (Cat-700), 1mmol of 4-hydroxy-2-butanone, 1mmol of aniline (R is hydrogen) and 2mL of acetone are sequentially added into a 25mL reaction bottle, the reaction system is stirred at room temperature under nitrogen atmosphere for reaction for 8h, the reaction solution is decompressed and desolventized, and the residue is subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain the 4- (phenylamino) -2-butanone, wherein the yield is 83% (135.5 mg) and yellow oil. 1 H NMR(400MHz,CDCl 3 )δ7.17(t,J=7.8Hz,2H),6.73(t,J=7.3Hz,1H),6.63(d,J=8.2Hz,2H),3.40(t,J=6.1Hz,2H),2.74(t,J=6.1Hz,2H),2.14(s,3H); 13 C NMR(101MHz,CDCl 3 )δ208.16,147.83,129.45,117.74,113.15,42.73,38.48,30.38.HRMS(ESI)for C 10 H 13 NO,calcd:163.0993,found:163.0984.
Example 2'
The procedure was as in example 2 above, except that 2mL of butanone (instead of 2mL of acetone) was used as the solvent, and the yield of 4- (phenylamino) -2-butanone was 81%.
The procedure was as in example 2 above, except that the reaction times were 4h,6h,10h, and 12h, and the yields of 4- (phenylamino) -2-butanone were 60%, 71%, 83%, and 87%, respectively.
The procedure was as in example 2 above, except that when the amount of the biochar-supported iron single-atom catalyst was 10mg or 30mg, the yields of 4- (phenylamino) -2-butanone were 51% and 84%, respectively;
example 3 4- ((2-chlorophenyl) amino) -2-butanone
The magneton, 20mg of charcoal-supported iron monoatomic catalyst (Cat-800), 0.5mmol of 4-hydroxy-2-butanone, 1mmol of 2-chloroaniline and 2mL of butanone are sequentially added into a 25mL reaction bottle, the reaction system is stirred at room temperature under nitrogen atmosphere for reaction for 9h, the reaction solution is decompressed and desolventized, and the residue is subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain 4- ((2-chlorophenyl) amino) -2-butanone as yellow oil, wherein the yield is 80% (79.1 mg). 1 H NMR(400MHz,CDCl 3 )δ7.14(d,J=7.8Hz,1H),7.06(t,J=8.3Hz,1H),6.55(dd,J=15.8,7.9Hz,2H),4.44(s,1H),3.35(s,2H),2.67(t,J=6.3Hz,2H),2.09(s,3H); 13 C NMR(101MHz,CDCl 3 )δ207.57,143.63,129.38,127.90,119.54,117.51,111.17,42.66,38.15,30.42.HRMS(ESI)for C 10 H 12 ClNO,calcd:197.0610,found:197.0612.
Example 4 4- ((3-bromophenyl) amino) -2-butanone
Sequentially adding magneton, 20mg of biochar-supported iron monoatomic catalyst (Cat-900), 1mmol of 4-hydroxy-2-butanone, 0.5mmol of 3-bromoaniline and 2mL of acetone into a 25mL reaction bottle, stirring the reaction system at room temperature under nitrogen atmosphere for reacting for 12h, decompressing and desolventizing the reaction solution, and performing column chromatography treatment on residues (eluent)Ethyl acetate/petroleum ether=1:4, volume ratio) to give 4- ((3-bromophenyl) amino) -2-butanone as a yellow oil in 77% (93.2 mg) yield. 1 H NMR(400MHz,CDCl 3 )δ6.97(t,J=8.0Hz,1H),6.76(d,J=8.0Hz,1H),6.68(s,1H),6.47(d,J=8.2Hz,1H),4.16(s,1H),3.32(t,J=6.1Hz,2H),2.69(t,J=6.1Hz,2H),2.12(s,3H); 13 C NMR(101MHz,CDCl 3 )δ207.91,149.13,130.54,123.22,120.07,115.19,111.68,42.24,38.03,30.21.HRMS(ESI)for C 10 H 12 BrNO,calcd:241.0103,found:241.0108.
Example 5 4- ((4-fluorophenyl) amino) -2-butanone
To a 25mL reaction flask, a magneton, 20mg of a charcoal-supported iron monoatomic catalyst (Cat-700), 1mmol of 4-hydroxy-2-butanone, 1mmol of 4-fluoroaniline and 2mL of acetone were sequentially added, the reaction system was stirred at room temperature under nitrogen atmosphere for reaction for 9 hours, the reaction solution was desolventized under reduced pressure, and the residue was subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain 4- ((4-fluorophenyl) amino) -2-butanone as a yellow oil in 77% yield (139.5 mg). 1 H NMR(400MHz,CDCl 3 )δ7.13(d,J=8.7Hz,2H),6.32(d,J=8.7Hz,2H),3.96(s,1H),3.14(t,J=6.1Hz,2H),2.61(t,J=6.1Hz,2H),2.05(s,3H); 13 C NMR(101MHz,CDCl 3 )δ207.03,146.45,131.07,113.35,108.08,42.24,38.12,30.21.HRMS(ESI)for C 10 H 12 FNO,calcd:181.0905,found:181.0907.
Example 6 4- (ortho-toluidine) -2-butanone
The magneton, 20mg of charcoal-supported iron monoatomic catalyst (Cat-900), 1mmol of 4-hydroxy-2-butanone, 1mmol of o-toluidine and 2mL of acetone are sequentially added into a 25mL reaction bottle, the reaction system is stirred and reacted for 9h in a nitrogen atmosphere at room temperature, the reaction liquid is decompressed and desolventized, and the residue is subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain the 4- (o-toluidine) -2-butanone, yellow oil, and the yield is 71% (125.9 mg). 1 H NMR(400MHz,CDCl 3 )δ7.15(t,J=7.7Hz,1H),7.09(d,J=7.2Hz,1H),6.73(t,J=7.3Hz,1H),6.66(d,J=8.0Hz,1H),3.90(s,1H),3.49(t,J=6.1Hz,2H),2.81(t,J=6.1Hz,2H),2.19(s,3H),2.14(s,3H); 13 C NMR(101MHz,CDCl 3 )δ208.27,145.76,130.33,127.16,122.58,117.20,109.67,42.60,38.38,30.33,17.49.HRMS(ESI)for C 11 H 15 NO,calcd:177.1155,found:177.1153.
Example 7 4- ((3-methoxyphenyl) amino) -2-butanone
To a 25mL reaction flask, a magneton, 20mg of a charcoal-supported iron monoatomic catalyst (Cat-800), 1mmol of 4-hydroxy-2-butanone, 1mmol of m-methoxyaniline and 2mL of butanone were sequentially added, the reaction system was stirred at room temperature under nitrogen atmosphere for reaction for 8 hours, the reaction solution was desolventized under reduced pressure, and the residue was subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain 4- ((3-methoxyphenyl) amino) -2-butanone as a yellow oil, with a yield of 89% (172.0 mg). 1 H NMR(400MHz,CDCl 3 )δ7.08(t,J=8.1Hz,1H),6.27(d,J=8.1Hz,1H),6.24(d,J=8.1Hz,1H),6.15(s,1H),3.77(s,3H),3.38(t,J=6.1Hz,2H),2.72(t,J=6.1Hz,2H),2.14(s,3H); 13 C NMR(101MHz,CDCl 3 )δ208.19,160.95,149.20,130.12,106.19,102.72,99.01,55.13,42.61,38.38,30.32.HRMS(ESI)for C 11 H 15 NO 2 ,calcd:193.1101,found:193.1117.
Example 8 4- ((4-nitrophenyl) amino) -2-butanone
The magneton, 20mg of charcoal-supported iron monoatomic catalyst (Cat-800), 1mmol of 4-hydroxy-2-butanone, 1mmol of p-nitroaniline and 2mL of butanone are sequentially added into a 25mL reaction bottle, the reaction system is stirred and reacted for 12h in a nitrogen atmosphere at room temperature, the reaction liquid is decompressed and desolventized, and the residue is subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain 4- ((4-nitrophenyl) amino) -2-butanone as a yellow solid, the melting point is 89-91 ℃, and the yield is 50% (104.1 mg). 1 H NMR(400MHz,CDCl 3 )δ8.03(d,J=9.0Hz,2H),6.45(d,J=9.2Hz,2H),5.12(s,1H),3.46(q,J=5.9Hz,2H),2.78(t,J=6.0Hz,2H),2.18(s,3H); 13 C NMR(101MHz,CDCl 3 )δ207.59,153.22,137.74,126.50,111.09,42.14,37.67,30.32.HRMS(ESI)for C 10 H 12 N 2 O 3 ,calcd:208.0844,found:208.0839.
Example 9 4- ((4-trifluoromethylphenyl) amino) -2-butanone
The magneton, 20mg of charcoal-supported iron monoatomic catalyst (Cat-700), 1mmol of 4-hydroxy-2-butanone, 1mmol of para-trifluoromethylaniline and 2mL of acetone are sequentially added into a 25mL reaction bottle, the reaction system is stirred at room temperature under nitrogen atmosphere for reaction for 12h, the reaction solution is decompressed and desolventized, and the residue is subjected to column chromatography (eluent, ethyl acetate/petroleum ether=1:4, volume ratio) to obtain 4- ((4-trifluoromethylphenyl) amino) -2-butanone as a yellow solid, the melting point is 89-91 ℃, and the yield is 49% (113.3 mg). 1 H NMR(400MHz,CDCl 3 )δ7.38(d,J=8.5Hz,2H),6.57(d,J=8.5Hz,2H),4.36(s,1H),3.46(s,2H),2.76(t,J=6.0Hz,2H),2.19(s,3H); 13 C NMR(101MHz,CDCl 3 )δ207.87,150.34,126.84,126.45,123.75,118.97,112.09,42.41,37.94,30.46.HRMS(ESI)for C 11 H 12 F 3 NO,calcd:231.0872,found:231.0869.
Comparative example
1. Compared with other solvents, the acetone or butanone solvents used in the invention have obvious advantages, the yield of the product is obviously higher than that of the other solvents, and specific data are shown in Table 2 (except that the solvents are different (the dosage is 2mL respectively), and other processes and conditions are the same as in example 2).
Table 24 isolation yields of- (phenylamino) -2-butanone in different solvents
2. The same reaction procedure and conditions as in example 2 were used, except that no catalyst was used in the reaction procedure; compared with the reaction result without using the catalyst, the biochar-supported iron monoatomic catalyst used in the invention has obvious advantages, and specific data are shown in Table 3 (the same as in example 2 except that the biochar-supported iron monoatomic catalyst is not added).
Table 3 4 isolation yields of- (phenylamino) -2-butanone in different solvents
3. In contrast to palladium-catalyzed oxidative amination of homoenols (chem. Commun.2017,53, 10422-10425) or allylic alcohols (J. Org. Chem.2018,83, 3941-3951), the present invention has the following advantages:
(1) The reaction uses an iron single-atom catalyst loaded by biochar, and an expensive palladium catalyst is not needed;
(2) The reaction does not require an oxidant;
(3) The reaction was carried out at room temperature without heating.
We have verified experimentally: palladium catalysts do not catalyze the reaction of 4-hydroxy-2-butanone with aromatic amines to beta-aminoketones under the conditions of the present reaction (the procedure is as in example 1 except for the catalyst).
4. In contrast to the iodine-catalyzed nucleophilic substitution reaction of benzyl alcohol (Synlett 2008,7,1045-1049;Tetrahedron Lett.2007,48,8120-8124), the present invention has the following advantages: the nucleophilic substitution reaction of benzyl alcohol catalyzed by iodine (Synlett 2008,7,1045-1049;Tetrahedron Lett.2007,48,8120-8124) can only be the reaction of benzyl alcohol with other alcohols to form ethers, which we have experimentally verified that iodine catalysis cannot catalyze the reaction of benzyl alcohol with amines. The invention relates to an iron monoatomic catalyst loaded by biochar for catalyzing aniline and 4-hydroxy-2-butanone to generate an alcohol amination reaction, which is obviously different from the prior art.
Compared with the patent 'a method for catalyzing N-alkylation reaction by TEMPO and TBN (CN 201910743878.7)' or the patent 'a method for generating beta-aminoketone compound by iodine catalysis (CN201811374694. X)', the invention has the following obvious differences and advantages: the content of the invention is that the iron monoatomic catalyst loaded by biochar catalyzes aniline and 4-hydroxy-2-butanone to generate alcohol amination reaction, and the catalyst is obviously different from the prior art; the iron single-atom catalyst loaded by the biochar can be recycled, the catalytic activity is not obviously reduced after six times of continuous use, and neither TEMPO/TBN nor iodine catalyst can be recycled.

Claims (9)

1. A biochar-supported iron catalyst characterized by: the Phellinus linteus mycelium is used as a charcoal pyrolysis precursor, the Phellinus linteus mycelium is dispersed in normal saline, then soluble ferric salt is added into the dispersion liquid, and iron ions are complexed on the surface of the Phellinus linteus mycelium; and (3) solid-liquid separation is carried out to collect Phellinus linteus mycelium, washing is carried out, freeze drying is carried out, and then the Phellinus linteus mycelium is pyrolyzed in inert atmosphere to obtain the biochar-loaded iron monoatomic catalyst.
2. The catalyst of claim 1, wherein:
the specific process is that 2-5g (preferably 3-4 g) Phellinus linteus mycelium is firstly ultrasonically dispersed in 150mL physiological saline to obtain dispersion liquid; then, a soluble iron salt having a molar amount of iron ions of 2 to 6mmol (preferably 5 to 5.5 mmol) is added to the dispersion, and the iron ions are surface-complexed under conditions of 60 to 100 ℃ (preferably 80 to 90 ℃).
3. The catalyst according to claim 1 or 2, characterized in that:
the ultrasonic dispersion pretreatment time is 20-50min, preferably 30-40min; the ultrasonic treatment power is 40-100kw;
the time for complexing the iron ions on the surface is 12-24 hours;
after complexing iron ions on the surface of Phellinus linteus mycelium, cooling to room temperature, centrifuging, collecting Phellinus linteus mycelium, washing with water, and freeze drying.
4. The catalyst of claim 1, wherein:
the soluble manganese salt is one or more of ferric chloride, ferric nitrate or ferric sulfate.
5. The catalyst of claim 1, wherein:
the pyrolysis temperature of Phellinus linteus mycelium is 600-1000deg.C (preferably 700-800deg.C) for 1-4 hr (preferably 1-2 hr).
6. The catalyst according to claim 1 or 5, characterized in that:
the inert atmosphere is one or more than two of nitrogen and argon;
1g of dried Phellinus linteus mycelium is introduced into an inert atmosphere at an air flow rate of 10-30mL/min;
the heating rate from room temperature to pyrolysis temperature is 2-5 ℃/min; cooling to room temperature-40 ℃ after pyrolysis to obtain the catalyst, and cooling from the pyrolysis temperature to the room temperature-40 ℃ after pyrolysis at a cooling rate of 2-5 ℃/min.
7. Use of the biochar-supported catalyst of any one of claims 1-6 in an alcohol amination reaction of 4-hydroxy-2-butanone and aniline compounds.
8. The use according to claim 7, characterized in that: the method is characterized in that:
in a nitrogen atmosphere, catalyzing 4-hydroxy-2-butanone and different aniline compounds to perform an alcohol amination reaction by using an iron single-atom catalyst loaded by biochar to prepare 4- (N-phenyl) -2-butanone compounds;
r substituent groups in the formula 1 are one or more than two of hydrogen, halogen (one or more than two of F, cl and Br), methyl, methoxy, nitro and trifluoromethyl, and the number is 1-5.
9. Use according to claim 7 or 8, characterized in that:
the concentration of 4-hydroxy-2-butanone in the solvent is 0.25-1mol/L, preferably 0.5mol/L; the concentration of the aniline compound in the solvent is 0.25-1mol/L, preferably 0.5mol/L;
the molar ratio of the 4-hydroxy-2-butanone to the aniline compound is 1:2-2:1, and the preferable molar ratio is 1:1;
the solvent is acetone and/or butanone;
the dosage of the biochar-supported iron single-atom catalyst in 2mL of solvent is 10-30mg, preferably 15-20mg;
the reaction time is 4 to 12 hours, preferably 6 to 8 hours.
CN202311298943.2A 2023-10-09 2023-10-09 Biochar-supported iron catalyst and application thereof Pending CN117443380A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202311298943.2A CN117443380A (en) 2023-10-09 2023-10-09 Biochar-supported iron catalyst and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202311298943.2A CN117443380A (en) 2023-10-09 2023-10-09 Biochar-supported iron catalyst and application thereof

Publications (1)

Publication Number Publication Date
CN117443380A true CN117443380A (en) 2024-01-26

Family

ID=89595713

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202311298943.2A Pending CN117443380A (en) 2023-10-09 2023-10-09 Biochar-supported iron catalyst and application thereof

Country Status (1)

Country Link
CN (1) CN117443380A (en)

Similar Documents

Publication Publication Date Title
WO2008080832A2 (en) Carbonitrides as catalysts
CN112694375B (en) Application of iron (III) complex containing 1,3-di-tert-butylimidazole cation in synthesis of aryl benzyl ether compounds
CN112645821B (en) Method for synthesizing aryl benzyl ether compound
CN112138698A (en) Preparation method of nitrogen-doped carbon nano material and application of nitrogen-doped carbon nano material in nitrobenzene hydrogenation reaction
Herndon et al. Cyclopentenones from the reaction of alkynes with cyclopropylcarbenechromium complexes
CN114588940B (en) Nickel-based catalyst for hydrogenation of phenolic compounds, and preparation method and application thereof
CN113731441B (en) Cobalt-reduced graphene oxide Co/rGO catalyst and preparation method and application thereof
CN114478648A (en) Pyridine-like pyrrole ruthenium complex, preparation method thereof and application of complex as electrocatalytic ammonia oxidation catalyst
CN118086417A (en) Process for preparing hydrazines
CN116178244B (en) Fullerene pyrrolidine derivative, and preparation method and application thereof
CN117443380A (en) Biochar-supported iron catalyst and application thereof
Arora et al. Valmet Chiral Schiff‐Base Ligands And Their Copper (II) Complexes as Organo, Homogeneous and Heterogeneous Catalysts for Henry, Cyanosilylation and Aldol Coupling Reactions
WO2022155936A1 (en) Method for synthesizing aryl benzyl ether compound
CN113603648A (en) Cobalt complex and preparation method and application thereof
CN111153937A (en) Preparation method and application of cobalt metal organic macrocyclic compound
CN112774662A (en) Monoatomic catalyst, preparation method and application thereof
JPS5869834A (en) Preparation of methyl methoxyacetate
CN110655485A (en) Preparation method of N-substituted indolone
CN116037101B (en) Biochar-supported single-atom catalyst and application thereof in quinazoline compound synthesis
CN115569661B (en) Magnetic Ag-Co@C-N recyclable catalyst, and preparation method and application thereof
Liu et al. Catalytic behavior of silica‐supported methylcellulose–oxalic acid–Pt complex in asymmetric hydrogenation of 2‐butanone and itaconic acid
CN115057808B (en) Synthesis method of Z-3-vinyl substituted isoindolinone compound
CN115872897B (en) Schiff base cobalt complex, preparation method and application thereof
WO2022155932A1 (en) Application of cationic iron(iii) complex containing 1,3-di-tert-butylimidazolium in synthesizing arylbenzyl ether compounds
CN114478198B (en) Method for preparing phenol by catalytic hydrogenation of guaiacol

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