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

Biochar-supported iron catalyst and application thereof Download PDF

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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
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biochar
catalyst
butanone
iron
reaction
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任兰会
姜莉雅
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Institute of Zhejiang University Quzhou
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    • 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

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  • 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

一种生物炭负载的铁催化剂及其应用A biochar-loaded iron catalyst and its application

技术领域Technical field

本发明涉及生物炭负载的铁单原子催化剂、苯胺类化合物和4-羟基-2-丁酮的醇胺化反应。The present invention relates to the alcohol amination reaction of biochar-supported iron single atom catalyst, aniline compounds and 4-hydroxy-2-butanone.

背景技术Background technique

C-N键作为一种重要的结构片段存在于众多生物活性分子和药物分子中,被广泛用于精细化工和医药领域中,列如合成β-氨基酸、β-氨基醇、1,3-二氨基烷烃、内酰胺、尼可霉素等。合成C-N键的方法很多,比如卤代烃取代反应、Aza-Michael加成反应、芳香卤代烃偶联反应、Mannich反应、高烯醇或烯丙醇氧化胺化反应等。胺直接取代醇羟基是制备C-N键的重要方法之一,原料易得,副产品为H2O,绿色环保而且原子经济性高。但是,无论是热力学性质还是动力学性质,羟基都不是一个好的离去基团,需要事先转变成卤代烃、对甲苯磺酸酯、磺酸酯等。醇羟基的直接取代反应被 药物圆桌会议选为十大绿色化学关键研究领域之一。As an important structural fragment, the CN bond exists in many biologically active molecules and pharmaceutical molecules, and is widely used in the fields of fine chemicals and medicine, such as the synthesis of β-amino acids, β-aminoalcohols, and 1,3-diaminoalkanes. , lactam, nikkomycin, etc. There are many methods to synthesize CN bonds, such as halogenated hydrocarbon substitution reaction, Aza-Michael addition reaction, aromatic halogenated hydrocarbon coupling reaction, Mannich reaction, homoenol or allyl alcohol oxidative amination reaction, etc. Direct substitution of alcoholic hydroxyl groups with amines is one of the important methods for preparing CN bonds. The raw materials are easily available, and the by-product is H 2 O. It is environmentally friendly and has high atom economy. However, whether it is thermodynamic or kinetic properties, hydroxyl is not a good leaving group and needs to be converted into halogenated hydrocarbons, p-toluenesulfonate, sulfonate, etc. in advance. The direct substitution reaction of alcoholic hydroxyl group is Selected by the Drug Roundtable as one of the top ten key research areas for green chemistry.

1981年,Grigg和Watanabe几乎同时报道了铑、铱和钌催化胺直接取代醇羟基的反应,开启了胺直接取代醇羟基的研究。此后,多种催化胺直接取代醇羟基的方法被报道,催化剂涉及银、金、铱、钯、铼、钌、钴、铜、铁、锰、镍等金属盐或配合物,双金属催化体系和非金属催化体系(酶、醛、酮、碘、碳材料和有机膦)也被报道。In 1981, Grigg and Watanabe almost simultaneously reported the reaction of rhodium, iridium and ruthenium catalyzing the direct substitution of alcoholic hydroxyl groups with amines, starting the study of direct substitution of alcoholic hydroxyl groups with amines. Since then, a variety of methods for directly substituting alcoholic hydroxyl groups with catalytic amines have been reported. The catalysts involve metal salts or complexes such as silver, gold, iridium, palladium, rhenium, ruthenium, cobalt, copper, iron, manganese, and nickel, bimetallic catalytic systems and Non-metal catalytic systems (enzymes, aldehydes, ketones, iodine, carbon materials and organophosphines) have also been reported.

本发明首次将生物炭负载的铁单原子催化剂用于催化4-羟基-2-丁酮和苯胺类化合物的醇胺化反应。本发明的方法快速简便、环保、成本低廉、易于工业化,制备的生物炭负载铁单原子催化剂稳定性好,在醇胺化反应领域具有良好的应用前景。In this invention, for the first time, a biochar-supported iron single-atom catalyst is used to catalyze the alcohol amination reaction of 4-hydroxy-2-butanone and aniline compounds. The method of the invention is fast, simple, environmentally friendly, low-cost and easy to industrialize. The prepared biochar-loaded iron single-atom catalyst has good stability and has good application prospects in the field of alcohol amination reaction.

发明内容Contents of the invention

本发明公开了一种生物炭负载的铁单原子催化剂及其用于催化4-羟基-2-丁酮和苯胺类化合物的醇胺化反应,所述方法,采用桑黄菌丝作为生物炭热解前体,在生理盐水中超声分散,表面络合铁离子,冷冻干燥后在惰性气体氛围中高温热解获得生物炭负载的铁单原子催化剂。The invention discloses a biochar-supported iron single-atom catalyst and its use for catalyzing the alcohol amination reaction of 4-hydroxy-2-butanone and aniline compounds. In the method, Phellinus linteum mycelium is used as the biochar heat The decomposed precursor is ultrasonically dispersed in physiological saline, complexed with iron ions on the surface, freeze-dried and pyrolyzed at high temperature in an inert gas atmosphere to obtain a biochar-loaded iron single-atom catalyst.

以4-羟基-2-丁酮和不同的苯胺类化合物为反应底物,使用生物炭负载的铁单原子催化剂,丙酮或丁酮为溶剂,在氮气氛围中,室温下反应得N-烷基化产物。本发明首次使用桑黄菌作为炭载体的热解前体制备单原子催化剂。本发明制备的生物炭单原子催化剂具有类似碳纳米管的形貌。本发明首次将铁单原子催化剂用于催化苯胺和4-羟基-2-丁酮的醇胺化反应。Using 4-hydroxy-2-butanone and different aniline compounds as reaction substrates, using biochar-supported iron single-atom catalyst, acetone or butanone as solvent, react in a nitrogen atmosphere at room temperature to obtain N-alkyl chemical products. The present invention uses Phellinus linteus as the pyrolysis precursor of the carbon carrier to prepare a single-atom catalyst for the first time. The biochar single-atom catalyst prepared by the invention has a morphology similar to carbon nanotubes. In the present invention, an iron single-atom catalyst is used for the first time to catalyze the alcohol amination reaction of aniline and 4-hydroxy-2-butanone.

上述技术方案中,2-5g(优选3-4g)桑黄菌丝先在150mL生理盐水中超声分散,然后于分散液中加入铁离子的摩尔量为2-6mmol(优选5-5.5mmol)的可溶性铁盐,在60-100℃(优选80-90℃)条件下表面络合铁离子。In the above technical solution, 2-5g (preferably 3-4g) Phellinus linteum mycelium is first ultrasonically dispersed in 150mL physiological saline, and then a molar amount of iron ions of 2-6mmol (preferably 5-5.5mmol) is added to the dispersion. Soluble iron salts complex iron ions on the surface at 60-100°C (preferably 80-90°C).

上述技术方案中,超声分散预处理的时间为20-50min,优选30-40min;超声处理功率40-100kw;表面络合铁离子的时间为12-24h;桑黄菌丝表面络合铁离子后,冷却到室温,离心,收集桑黄菌丝用水洗涤后,冷冻干燥。In the above technical solution, the time for ultrasonic dispersion pretreatment is 20-50min, preferably 30-40min; the ultrasonic treatment power is 40-100kw; the time for surface complexation of iron ions is 12-24h; , cooled to room temperature, centrifuged, collected Phellinus linteum mycelium, washed with water, and freeze-dried.

上述技术方案中,可溶性锰盐为氯化铁、硝酸铁、或硫酸铁中的一种。In the above technical solution, the soluble manganese salt is one of ferric chloride, ferric nitrate, or ferric sulfate.

上述技术方案中,桑黄菌丝热解温度600-1000℃(优选700-800℃),时间1-4h(优选1-2h)。In the above technical solution, the pyrolysis temperature of Phellinus linteum mycelium is 600-1000°C (preferably 700-800°C), and the time is 1-4h (preferably 1-2h).

上述技术方案中,惰性气氛为氮气或氩气中的一种;1g干燥后桑黄菌丝通惰性气氛的气流速率为10-30mL/min;从室温升温到热解温度的升温速率为2-5℃/min;热解后从热解温度降温到40℃的降温速率为2-5℃/min;制备的生物炭负载的铁单原子催化剂具有类似碳纳米管的形貌。铁以单原子形式分散于生物炭载体上。In the above technical solution, the inert atmosphere is one of nitrogen or argon; the air flow rate of 1g of dried Phellinus linteus mycelium through the inert atmosphere is 10-30mL/min; the temperature rise rate from room temperature to the pyrolysis temperature is 2- 5°C/min; the cooling rate from the pyrolysis temperature to 40°C after pyrolysis is 2-5°C/min; the prepared biochar-loaded iron single-atom catalyst has a morphology similar to carbon nanotubes. Iron is dispersed in the form of single atoms on the biochar carrier.

上述技术方案中,在氮气氛围中,生物炭负载的铁单原子催化剂催化4-羟基-2-丁酮和不同的苯胺类化合物发生醇胺化反应制备4-(N-苯基)-2-丁酮类化合物。In the above technical solution, in a nitrogen atmosphere, a biochar-supported iron single atom catalyst catalyzes the alcohol amination reaction of 4-hydroxy-2-butanone and different aniline compounds to prepare 4-(N-phenyl)-2- Butanone compounds.

上述技术方案中,不同的苯胺类化合物为苯胺、2-氯苯胺、3-溴苯胺、4-氟苯胺、2-甲基苯胺、3-甲氧基苯胺、4-硝基苯胺、4-三氟甲基苯胺In the above technical solution, the different aniline compounds are aniline, 2-chloroaniline, 3-bromoaniline, 4-fluoroaniline, 2-methylaniline, 3-methoxyaniline, 4-nitroaniline, 4-tris Fluoromethylaniline

上述技术方案中,4-羟基-2-丁酮于溶剂中的浓度为0.5-1mol/L,优选浓度0.5mol/L;苯胺类化合物于溶剂中的浓度为0.5-1mol/L,优选浓度0.5mol/L。4-羟基-2-丁酮和苯胺类化合物的用量摩尔比为1:2-2:1,优选摩尔比为1:1。生物炭负载的铁单原子催化剂的用量为10-30mg,优选20mg。反应时间为4-12h,优选为8h。In the above technical solution, the concentration of 4-hydroxy-2-butanone in the solvent is 0.5-1mol/L, and the preferred concentration is 0.5mol/L; the concentration of aniline compounds in the solvent is 0.5-1mol/L, and the preferred concentration is 0.5 mol/L. The molar ratio of 4-hydroxy-2-butanone and aniline compounds is 1:2-2:1, and the preferred molar ratio is 1:1. The dosage of biochar-supported iron single atom catalyst is 10-30 mg, preferably 20 mg. The reaction time is 4-12h, preferably 8h.

由于上述方案运用,本发明与现有的技术相比具有下列优点:Due to the application of the above solution, the present invention has the following advantages compared with the existing technology:

1.本发明首次使用桑黄菌丝作为炭载体的热解前体制备生物炭负载的铁单原子催化剂,无需使用不可再生的碳源、昂贵的模板剂、活化剂和杂原子源,生物炭负载的铁单原子催化剂可以回收再使用;1. This invention uses Phellinus linteum mycelium as the pyrolysis precursor of the carbon carrier for the first time to prepare biochar-loaded iron single-atom catalyst without using non-renewable carbon sources, expensive templates, activators and heteroatom sources. Biochar The supported iron single-atom catalyst can be recycled and reused;

2.该反应无需额外添加碱性添加剂;2. This reaction does not require the addition of additional alkaline additives;

3.该反应在室温条件下进行,无需加热;3. The reaction is carried out at room temperature without heating;

4.该反应选择性好,没有其他的副产品。4. The reaction has good selectivity and no other by-products.

附图说明Description of the drawings

图1.催化剂(Cat-700)扫描电子显微镜谱图;Figure 1. Catalyst (Cat-700) scanning electron microscope spectrum;

图2.催化剂(Cat-700)球差矫正透射电镜谱图。Figure 2. Catalyst (Cat-700) spherical aberration corrected transmission electron microscope spectrum.

具体实施方式Detailed ways

下面结合实施例详述本发明,但本发明范围并不限于下述的实施例。The present invention will be described in detail below with reference to the examples, but the scope of the present invention is not limited to the following examples.

实施例Example

实施例1生物炭负载的铁单原子催化剂制备方法Example 1 Preparation method of biochar-supported iron single-atom catalyst

在250mL圆底烧瓶中,加入磁力搅拌器转子、3g桑黄菌丝和150mL生理盐水,超声处理(功率40kw,时间30min)。在室温下磁力搅拌,慢慢加入5mmol氯化铁,继续搅拌30min。然后在80℃条件下,搅拌12h。冷却到室温,离心处理(10000r/min,10min),收集桑黄菌丝用去离子水洗涤3次,冷冻干燥。取1g上述步骤制备的冷冻干燥材料于石英舟内,将石英舟放置于管式炉中,在室温下通氮气30min(气流速率为10mL/min)。然后保持氮气气流速率不变,升温到700℃(从室温升温到热解温度的升温速率为5℃/min)。依然保持氮气气流速率不变,保持700℃热解1h后,慢慢降温到30℃(降温速率为5℃/min)。In a 250 mL round-bottomed flask, add the magnetic stirrer rotor, 3 g of Phellinus linteum mycelium and 150 mL of physiological saline, and perform ultrasonic treatment (power 40 kw, time 30 min). Stir magnetically at room temperature, slowly add 5 mmol ferric chloride, and continue stirring for 30 minutes. Then stir for 12 hours at 80°C. Cool to room temperature, centrifuge (10000r/min, 10min), collect Phellinus linteus mycelium, wash it 3 times with deionized water, and freeze-dry. Put 1 g of the freeze-dried material prepared in the above steps into a quartz boat, place the quartz boat in a tube furnace, and circulate nitrogen at room temperature for 30 minutes (gas flow rate is 10 mL/min). Then, keeping the nitrogen gas flow rate constant, the temperature was raised to 700°C (the heating rate from room temperature to the pyrolysis temperature was 5°C/min). Still keeping the nitrogen gas flow rate unchanged, after maintaining pyrolysis at 700°C for 1 hour, slowly cool down to 30°C (cooling rate is 5°C/min).

将石英舟内的黑色固体在玛瑙研钵中研磨成粉末,获得生物炭负载的铁单原子催化剂(标记为Cat-700)质量收率为27%(相对于桑黄菌丝)。The black solid in the quartz boat was ground into powder in an agate mortar, and the biochar-supported iron single-atom catalyst (labeled Cat-700) was obtained with a mass yield of 27% (relative to Phellinus linteum mycelium).

Cat-800和Cat-900的制备方法和上述Cat-700的制备过程一致,与其不同之处仅在于热解温度不同。Cat-800和Cat-900的热解温度分别是800℃和900℃,收率分别是28%和27%。The preparation methods of Cat-800 and Cat-900 are the same as the preparation process of Cat-700 mentioned above. The only difference lies in the pyrolysis temperature. The pyrolysis temperatures of Cat-800 and Cat-900 are 800°C and 900°C respectively, and the yields are 28% and 27% respectively.

使用X射线光电子能谱技术分析了生物炭负载的铁单原子催化剂表面的元素组成和原子数百分含量。生物炭负载的铁单原子催化剂的表面由碳、氮、氧、磷和铁组成,其中碳元素的含量最大,超过84at%;其次是氮元素,含量为6.35-7.07at%;氧元素的含量为5.61-6.15at%;磷元素的含量为为1.32-1.71at%;铁元素的含量最少(0.77-0.96at%)。不同热解温度下制备的生物炭负载的铁单原子催化剂表面的元素含量不同。The elemental composition and atomic percentage content on the surface of the biochar-supported iron single-atom catalyst were analyzed using X-ray photoelectron spectroscopy. The surface of the biochar-supported iron single-atom catalyst is composed of carbon, nitrogen, oxygen, phosphorus and iron. The content of carbon element is the largest, exceeding 84at%; followed by nitrogen element, with a content of 6.35-7.07at%; and the content of oxygen element The content of phosphorus is 5.61-6.15at%; the content of phosphorus is 1.32-1.71at%; the content of iron is the least (0.77-0.96at%). The element content on the surface of biochar-supported iron single-atom catalysts prepared at different pyrolysis temperatures is different.

表1.生物炭负载的铁单原子催化剂的表面元素含量Table 1. Surface element content of biochar-supported iron single-atom catalysts

Cat-700扫描电子显微镜(图1)显示生物炭负载的铁单原子催化剂的形貌和碳纳米管的形貌十分相似。球差矫正透射电镜谱图(图2)显示铁元素均匀分布在生物炭载体上,且可以观察到均匀分散的亮点,说明铁元素的原子级分布。Cat-700 scanning electron microscope (Figure 1) shows that the morphology of biochar-supported iron single-atom catalyst is very similar to that of carbon nanotubes. The spherical aberration-corrected transmission electron microscope spectrum (Figure 2) shows that iron elements are evenly distributed on the biochar carrier, and uniformly dispersed bright spots can be observed, indicating the atomic-level distribution of iron elements.

Cat-800和Cat-900的扫描电子显微镜谱图显示生物炭负载的铁单原子催化剂的形貌和碳纳米管的形貌十分相似。球差矫正透射电镜谱图显示铁元素均匀分布在生物炭载体上,且可以观察到均匀分散的亮点,说明铁元素的原子级分布。The scanning electron microscopy spectra of Cat-800 and Cat-900 show that the morphology of the biochar-supported iron single-atom catalyst is very similar to that of carbon nanotubes. The spherical aberration-corrected transmission electron microscope spectrum shows that iron elements are evenly distributed on the biochar carrier, and evenly dispersed bright spots can be observed, indicating the atomic-level distribution of iron elements.

其它生物炭负载的铁单原子催化剂的制备:采用的制备过程与上述Cat-700的制备过程一致,与其不同之处在于制备生物炭负载的铁单原子催化剂时改变金属铁盐的用量(2-6mmol),即金属铁盐的加入量由5mmol分别采用2mmol、3mmol、4mmol、6mmol进行替换,均能制备出生物炭负载的铁单原子催化剂。扫描电子显微镜谱图显示生物炭负载的铁单原子催化剂的形貌和碳纳米管的形貌十分相似。球差矫正透射电镜谱图显示铁元素均匀分布在生物炭载体上,且可以观察到均匀分散的亮点,说明铁元素的原子级分布。Preparation of other biochar-supported iron single-atom catalysts: The preparation process used is consistent with the preparation process of Cat-700 mentioned above. The difference is that the amount of metal iron salt is changed when preparing biochar-loaded iron single-atom catalysts (2- 6mmol), that is, the addition amount of metal iron salt is replaced from 5mmol with 2mmol, 3mmol, 4mmol, and 6mmol respectively, and biochar-supported iron single-atom catalyst can be prepared. Scanning electron microscopy spectra show that the morphology of biochar-supported iron single-atom catalyst is very similar to that of carbon nanotubes. The spherical aberration-corrected transmission electron microscope spectrum shows that iron elements are evenly distributed on the biochar carrier, and uniformly dispersed bright spots can be observed, indicating the atomic-level distribution of iron elements.

实施例2 4-(苯基氨基)-2-丁酮Example 2 4-(phenylamino)-2-butanone

在25mL的反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-700)、1mmol 4-羟基-2-丁酮、1mmol苯胺(R为氢)和2mL丙酮,反应体系在室温下氮气氛围中搅拌反应8h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-(苯基氨基)-2-丁酮,收率为83%(135.5mg),黄色油。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ208.16,147.83,129.45,117.74,113.15,42.73,38.48,30.38.HRMS(ESI)for C10H13NO,calcd:163.0993,found:163.0984.Magnets, 20 mg biochar-loaded iron single atom catalyst (Cat-700), 1 mmol 4-hydroxy-2-butanone, 1 mmol aniline (R is hydrogen) and 2 mL acetone were added in sequence to a 25 mL reaction bottle. The reaction system was at The reaction was stirred for 8 hours in a nitrogen atmosphere at room temperature. The reaction solution was evaporated under reduced pressure, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-(phenylamino)- 2-Butanone, yield 83% (135.5 mg), 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.

实施例2’Example 2’

过程同上实施例2,与上述过程不同之处在于,使用2mL丁酮(替代2mL丙酮)作溶剂时,4-(苯基氨基)-2-丁酮的收率为81%。The process is the same as in Example 2, except that when 2 mL of butanone (instead of 2 mL of acetone) is used as the solvent, the yield of 4-(phenylamino)-2-butanone is 81%.

过程同上实施例2,与上述过程不同之处在于,反应时间为4h,6h,10h,12h时,4-(苯基氨基)-2-丁酮的收率分别为60%、71%、83%和87%。The process is the same as in Example 2. The difference from the above process is that when the reaction time is 4h, 6h, 10h, and 12h, the yields of 4-(phenylamino)-2-butanone are 60%, 71%, and 83% respectively. % and 87%.

过程同上实施例2,与上述过程不同之处在于,当生物炭负载的铁单原子催化剂的用量为10mg或30mg,4-(苯基氨基)-2-丁酮的收率分别为51%和84%;The process is the same as in Example 2. The difference from the above process is that when the dosage of the biochar-loaded iron single atom catalyst is 10 mg or 30 mg, the yields of 4-(phenylamino)-2-butanone are 51% and 51% respectively. 84%;

实施例3 4-((2-氯苯基)氨基)-2-丁酮Example 3 4-((2-chlorophenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-800)、0.5mmol 4-羟基-2-丁酮、1mmol 2-氯苯胺和2mL丁酮,反应体系在室温下氮气氛围中搅拌反应9h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((2-氯苯基)氨基)-2-丁酮,黄色油,收率为80%(79.1mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ207.57,143.63,129.38,127.90,119.54,117.51,111.17,42.66,38.15,30.42.HRMS(ESI)for C10H12ClNO,calcd:197.0610,found:197.0612.Add magnetons, 20 mg biochar-supported iron single atom catalyst (Cat-800), 0.5 mmol 4-hydroxy-2-butanone, 1 mmol 2-chloroaniline and 2 mL methyl butanone in sequence into a 25 mL reaction bottle. The reaction system is at room temperature. The reaction was stirred for 9 hours in a nitrogen atmosphere, the reaction solution was evaporated under reduced pressure, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((2-chlorophenyl) )Amino)-2-butanone, yellow oil, yield 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.

实施例4 4-((3-溴苯基)氨基)-2-丁酮Example 4 4-((3-bromophenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-900)、1mmol 4-羟基-2-丁酮、0.5mmol 3-溴苯胺和2mL丙酮,反应体系在室温下氮气氛围中搅拌反应12h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((3-溴苯基)氨基)-2-丁酮,黄色油,收率为77%(93.2mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ207.91,149.13,130.54,123.22,120.07,115.19,111.68,42.24,38.03,30.21.HRMS(ESI)for C10H12BrNO,calcd:241.0103,found:241.0108.Magnets, 20 mg biochar-supported iron single atom catalyst (Cat-900), 1 mmol 4-hydroxy-2-butanone, 0.5 mmol 3-bromoaniline and 2 mL acetone were added in sequence to the 25 mL reaction bottle. The reaction system was at room temperature. The reaction was stirred for 12 hours in a nitrogen atmosphere. The reaction solution was evaporated under reduced pressure, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((3-bromophenyl) Amino)-2-butanone, yellow oil, yield 77% (93.2 mg). 1 H NMR (400MHz, CDCl 3 ) δ6.97 (t, J = 8.0 Hz, 1H), 6.76 (d, J = 8.0 Hz, 1H), 6.68 (s, 1H), 6.47 (d, J = 8.2 Hz ,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.

实施例5 4-((4-氟苯基)氨基)-2-丁酮Example 5 4-((4-fluorophenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-700)、1mmol 4-羟基-2-丁酮、1mmol 4-氟苯胺和2mL丙酮,反应体系在室温下氮气氛围中搅拌反应9h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((4-氟苯基)氨基)-2-丁酮,黄色油,收率为77%(139.5mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ207.03,146.45,131.07,113.35,108.08,42.24,38.12,30.21.HRMS(ESI)for C10H12FNO,calcd:181.0905,found:181.0907.Magnets, 20 mg biochar-loaded iron single atom catalyst (Cat-700), 1 mmol 4-hydroxy-2-butanone, 1 mmol 4-fluoroaniline and 2 mL acetone were added in sequence to the 25 mL reaction bottle. The reaction system was filled with nitrogen at room temperature. The reaction was stirred in the atmosphere for 9 hours, the reaction solution was decompressed, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((4-fluorophenyl)amino )-2-butanone, yellow oil, yield 77% (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.

实施例6 4-(邻甲苯胺)-2-丁酮Example 6 4-(o-toluidine)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-900)、1mmol 4-羟基-2-丁酮、1mmol邻甲苯胺和2mL丙酮,反应体系在室温下氮气氛围中搅拌反应9h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-(邻甲苯胺)-2-丁酮,黄色油,收率为71%(125.9mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)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 C11H15NO,calcd:177.1155,found:177.1153.Magnets, 20 mg of biochar-loaded iron single atom catalyst (Cat-900), 1 mmol of 4-hydroxy-2-butanone, 1 mmol of o-toluidine and 2 mL of acetone were added in sequence to the 25 mL reaction bottle. The reaction system was placed in a nitrogen atmosphere at room temperature. The reaction was stirred for 9 hours, the reaction solution was decompressed, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-(o-toluidine)-2-butanone. , yellow oil, yield 71% (125.9mg). 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:177.115 5, found:177.1153.

实施例7 4-((3-甲氧基苯基)氨基)-2-丁酮Example 7 4-((3-methoxyphenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-800)、1mmol 4-羟基-2-丁酮、1mmol间甲氧基苯胺和2mL丁酮,反应体系在室温下氮气氛围中搅拌反应8h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((3-甲氧基苯基)氨基)-2-丁酮,黄色油,收率为89%(172.0mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)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 C11H15NO2,calcd:193.1101,found:193.1117.Add magnetons, 20 mg biochar-loaded iron single atom catalyst (Cat-800), 1 mmol 4-hydroxy-2-butanone, 1 mmol m-methoxyaniline and 2 mL butanone in sequence to the 25 mL reaction bottle. The reaction system is at room temperature. The reaction was stirred for 8 hours in a nitrogen atmosphere, and the reaction solution was desolvated under reduced pressure. The residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((3-methoxy). Phenyl)amino)-2-butanone, yellow oil, yield 89% (172.0 mg). 1 H NMR (400MHz, CDCl 3 ) δ7.08 (t, J = 8.1 Hz, 1H), 6.27 (d, J = 8.1 Hz, 1H), 6.24 (d, J = 8.1 Hz, 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.

实施例8 4-((4-硝基苯基)氨基)-2-丁酮Example 8 4-((4-nitrophenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-800)、1mmol 4-羟基-2-丁酮、1mmol对硝基苯胺和2mL丁酮,反应体系在室温下氮气氛围中搅拌反应12h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((4-硝基苯基)氨基)-2-丁酮,黄色固体,熔点为89-91℃,收率为50%(104.1mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ207.59,153.22,137.74,126.50,111.09,42.14,37.67,30.32.HRMS(ESI)for C10H12N2O3,calcd:208.0844,found:208.0839.Add magnets, 20 mg biochar-supported iron single atom catalyst (Cat-800), 1 mmol 4-hydroxy-2-butanone, 1 mmol p-nitroaniline and 2 mL butanone in sequence to the 25 mL reaction bottle. The reaction system is at room temperature. The reaction was stirred for 12 hours in a nitrogen atmosphere. The reaction solution was decompressed and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((4-nitrophenyl) )Amino)-2-butanone, yellow solid, melting point 89-91°C, yield 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.

实施例9 4-((4-三氟甲基苯基)氨基)-2-丁酮Example 9 4-((4-trifluoromethylphenyl)amino)-2-butanone

在25mL反应瓶中依次加入磁子、20mg生物炭负载的铁单原子催化剂(Cat-700)、1mmol 4-羟基-2-丁酮、1mmol对三氟甲基苯胺和2mL丙酮,反应体系在室温下氮气氛围中搅拌反应12h,反应液减压脱溶,残留物柱层析处理(洗脱液,乙酸乙酯/石油醚=1:4,体积比)得4-((4-三氟甲基苯基)氨基)-2-丁酮,黄色固体,熔点为89-91℃,收率为49%(113.3mg)。1H NMR(400MHz,CDCl3)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);13C NMR(101MHz,CDCl3)δ207.87,150.34,126.84,126.45,123.75,118.97,112.09,42.41,37.94,30.46.HRMS(ESI)for C11H12F3NO,calcd:231.0872,found:231.0869.Add magnetons, 20 mg biochar-supported iron single atom catalyst (Cat-700), 1 mmol 4-hydroxy-2-butanone, 1 mmol p-trifluoromethylaniline and 2 mL acetone into the 25 mL reaction bottle in sequence. The reaction system is at room temperature. The reaction was stirred for 12 hours in a nitrogen atmosphere, the reaction solution was evaporated under reduced pressure, and the residue was treated with column chromatography (eluent, ethyl acetate/petroleum ether = 1:4, volume ratio) to obtain 4-((4-trifluoromethyl) (Phenyl)amino)-2-butanone, yellow solid, melting point 89-91°C, yield 49% (113.3 mg). 1 H NMR (400MHz, CDCl 3 ) δ7.38 (d, J = 8.5 Hz, 2H), 6.57 (d, J = 8.5 Hz, 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 ) δ 207.87, 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.

对比例Comparative ratio

1.相比其他溶剂,本发明使用的丙酮或丁酮溶剂具有明显的优势,产物的收率明显高于其他溶剂,具体数据详见表2(除溶剂不同(用量均分别为2mL),其它过程和条件同实施例2)。1. Compared with other solvents, the acetone or butanone solvent used in the present invention has obvious advantages, and the yield of the product is significantly higher than other solvents. The specific data are shown in Table 2 (except for different solvents (the dosage is 2 mL respectively), the other The process and conditions are the same as in Example 2).

表2 4-(苯基氨基)-2-丁酮在不同溶剂下的分离收率Table 2 Isolation yields of 4-(phenylamino)-2-butanone in different solvents

2.与实施例2的反应过程和条件相同,与其不同之处在于,在反应过程不使用催化剂;和不使用催化剂的反应结果对比,本发明使用的生物炭负载的铁单原子催化剂具有明显的优势,具体数据详见表3(除不加入生物炭负载的铁单原子催化剂外,其它同实施例2)。2. The reaction process and conditions are the same as those of Example 2, except that no catalyst is used in the reaction process; compared with the reaction results without using a catalyst, the biochar-loaded iron single-atom catalyst used in the present invention has obvious Advantages, detailed data are shown in Table 3 (except that the biochar-supported iron single-atom catalyst is not added, the others are the same as Example 2).

表3 4-(苯基氨基)-2-丁酮在不同溶剂下的分离收率Table 3 Isolation yields of 4-(phenylamino)-2-butanone in different solvents

3.和钯催化的高烯醇(Chem.Commun.2017,53,10422-10425)或烯丙醇(J.Org.Chem.2018,83,3941-3951)的氧化胺化反应对比,本发明具有以下优点:3. Compared with the palladium-catalyzed oxidative amination reaction of homoenol (Chem. Commun. 2017, 53, 10422-10425) or allyl alcohol (J. Org. Chem. 2018, 83, 3941-3951), the present invention Has the following advantages:

(1)该反应使用生物炭负载的铁单原子催化剂,无需昂贵的钯催化剂;(1) This reaction uses biochar-supported iron single-atom catalyst and does not require expensive palladium catalyst;

(2)该反应无需氧化剂;(2) This reaction does not require an oxidizing agent;

(3)该反应在室温条件下进行,无需加热。(3) The reaction is carried out at room temperature without heating.

我们已经通过实验验证:钯催化剂在本反应的条件下不能催化4-羟基-2-丁酮和芳香胺反应生成β-氨基酮(除催化剂不同,其它同实施例1)。We have verified through experiments that the palladium catalyst cannot catalyze the reaction of 4-hydroxy-2-butanone and aromatic amines to produce β-aminoketone under the conditions of this reaction (except for the different catalysts, the others are the same as in Example 1).

4.和碘催化的苄醇的亲核取代反应(Synlett 2008,7,1045-1049;TetrahedronLett.2007,48,8120-8124)对比,本发明具有以下优点:碘催化的苄醇的亲核取代反应(Synlett 2008,7,1045-1049;Tetrahedron Lett.2007,48,8120-8124)只能是苄醇和其他醇反应生成醚类化合物,我们已经通过实验验证碘催化不能催化苄醇和胺反应。本发明的内容是生物炭负载的铁单原子催化剂催化苯胺和4-羟基-2-丁酮发生醇胺化反应,和以往技术具有明显的不同。4. Compared with 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: iodine-catalyzed nucleophilic substitution of benzyl alcohol The reaction (Synlett 2008, 7, 1045-1049; Tetrahedron Lett. 2007, 48, 8120-8124) can only be the reaction between benzyl alcohol and other alcohols to form ether compounds. We have experimentally verified that iodine catalysis cannot catalyze the reaction between benzyl alcohol and amines. The content of the present invention is that a biochar-loaded iron single-atom catalyst catalyzes the alcohol amination reaction of aniline and 4-hydroxy-2-butanone, which is significantly different from the previous technology.

和专利“一种TEMPO和TBN催化N-烷基化反应的方法(CN201910743878.7)”或专利“一种碘催化生成β-氨基酮类化合物的方法(CN201811374694.X)”对比,本发明具有以下明显不同和优点:本发明的内容是生物炭负载的铁单原子催化剂催化苯胺和4-羟基-2-丁酮发生醇胺化反应,催化剂和以往技术具有明显的不同;生物炭负载的铁单原子催化剂可以回收再利用,连续使用六次后,催化活性未见明显下降,TEMPO/TBN或碘催化剂都不能回收再利用。Compared with the patent "A method for TEMPO and TBN catalyzing N-alkylation reaction (CN201910743878.7)" or the patent "A method for iodine catalyzing the generation of β-aminoketone compounds (CN201811374694.X)", the present invention has The following are obvious differences and advantages: The content of the present invention is that a biochar-supported iron single-atom catalyst catalyzes the alcohol amination reaction of aniline and 4-hydroxy-2-butanone. The catalyst is significantly different from previous technologies; biochar-supported iron The single-atom catalyst can be recycled and reused. After six consecutive uses, the catalytic activity has not dropped significantly. Neither TEMPO/TBN nor iodine catalysts can be recycled and reused.

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)

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Publication number Priority date Publication date Assignee Title
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN119143611A (en) * 2024-11-15 2024-12-17 浙江大学衢州研究院 A continuous preparation method of N-isopropyl p-fluoroaniline

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