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CN109942518B - A metal-free method for the one-pot preparation of 5-methylfurfural from biomass resources - Google Patents

A metal-free method for the one-pot preparation of 5-methylfurfural from biomass resources Download PDF

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CN109942518B
CN109942518B CN201910216132.0A CN201910216132A CN109942518B CN 109942518 B CN109942518 B CN 109942518B CN 201910216132 A CN201910216132 A CN 201910216132A CN 109942518 B CN109942518 B CN 109942518B
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methylfurfural
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CN109942518A (en
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杨维冉
彭阳
高天
李香花
施鹤贤
李腾
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Abstract

The invention relates to the technical field of catalysis, in particular to a method for preparing 5-methylfurfural from biomass resources in one pot without metal participation, which comprises the following steps: sequentially adding biomass or derivatives thereof, iodide, solvent and acid into a high-temperature high-pressure reaction kettle, introducing certain hydrogen, reacting for a certain time, and collecting an organic phase for fractionation after the reaction is finished to obtain the 5-methylfurfural with the yield of up to 51.9%. The method has low requirements on production equipment under the low-temperature and low-pressure conditions, and accords with the principle of safe production; the biomass or the derivative thereof is converted into the 5-methylfurfural without metal participation in selective hydrogenolysis, the raw materials are low in renewable cost, good in circularity, simple in process, mild in condition and easy to separate products, the material loss caused by the intermediate steps is avoided, and the maximum utilization of resources is realized.

Description

一种无金属参与的从生物质资源一锅制备5-甲基糠醛的方法A metal-free method for the one-pot preparation of 5-methylfurfural from biomass resources

技术领域technical field

本发明属于催化技术领域,涉及一种无金属参与的从生物质资源一锅制备5-甲基糠醛的方法。The invention belongs to the technical field of catalysis, and relates to a metal-free method for preparing 5-methylfurfural from biomass resources in one pot.

背景技术Background technique

生物质是目前地球上唯一可持续的有机碳来源,是生产燃料、化学品和材料的理想石油替代品。但大多数生物基原料复杂的结构和化学性制约着其大规模应用。生物质纤维素和淀粉都是由葡萄糖组成的大分子多糖在自然界中分布广泛,占植物界碳含量的50%以上。在自然界淀粉含量丰富,存在于马铃薯、小麦、玉米、大米和木薯等主食,是人类饮食中最常见的生物基原料。葡萄糖和果糖是自然界最常见的己糖,其下游衍生物5-羟甲基糠醛被认为是最有潜力的生物基平台分子化合物。5-甲基糠醛(5-MF)是5-羟甲基糠醛(HMF)的脱氧加氢产物,也是一种重要的精细化学品广泛应用于医药、农药、化妆品等行业,还是通用食用香料的一种重要组成,甚至还被认为是一种重要的抗癌药物。此外,它还可以作为可再生燃料的重要中间体。Biomass is currently the only sustainable source of organic carbon on Earth and is an ideal petroleum substitute for the production of fuels, chemicals and materials. However, the complex structure and chemistry of most bio-based raw materials restrict their large-scale application. Biomass cellulose and starch are both macromolecular polysaccharides composed of glucose, which are widely distributed in nature and account for more than 50% of the carbon content in the plant kingdom. Starch is abundant in nature and exists in staple foods such as potatoes, wheat, corn, rice, and cassava, and is the most common bio-based raw material in the human diet. Glucose and fructose are the most common hexoses in nature, and their downstream derivatives, 5-hydroxymethylfurfural, are considered to be the most potential bio-based platform molecular compounds. 5-Methylfurfural (5-MF) is the deoxygenated hydrogenation product of 5-Hydroxymethylfurfural (HMF). It is also an important fine chemical widely used in medicine, pesticides, cosmetics and other industries, and it is also a general edible spice. An important component, it is even considered an important anticancer drug. In addition, it can serve as an important intermediate for renewable fuels.

目前工业上5-甲基糠醛的合成方法:日本专利JPS5791982A报道了一种光气先与2-甲基呋喃与N,N-二甲基甲酰胺的混合物反应,然后将所得反应产物水解得到5-甲基糠醛的方法。该方法在工业上大规模应用生产5-甲基糠醛。但此方法存在着许多弊端:1.原料来源于石油化工不可再生。2.原料昂贵。3.光气对人体有害。The synthetic method of 5-methylfurfural in industry at present: Japanese patent JPS5791982A has reported that a kind of phosgene reacts with the mixture of 2-methylfuran and N,N-dimethylformamide earlier, then the gained reaction product is hydrolyzed to obtain 5 - Methylfurfural method. The method is widely used in industry to produce 5-methylfurfural. But there are many disadvantages in this method: 1. The raw material comes from petrochemical industry and is non-renewable. 2. Raw materials are expensive. 3. Phosgene is harmful to human body.

文献中报道的从生物质制备5-甲基糠醛的方法主要有以下几种:1.Mascal等利用微晶纤维素在氯化锂和浓盐酸条件下转化为5-氯甲基糠醛,然后在氢气氛围中再经氯化钯催化氢解得到5-甲基糠醛(Angew.Chem.2008,120,8042–8044)。2.Yang等在氢气氛围下用RhCl3和HI催化葡萄糖和果糖转化为5-甲基糠醛其产率可达68%(ChemSusChem2011,4,349-352)。 3.中国专利CN102766119A公布了一种果糖基生物质在酸催化剂催化下进行热解得到含 20%摩尔产率5-甲基糠醛的生物油。The method for preparing 5-methylfurfural from biomass reported in the literature mainly contains the following: 1.Mascal etc. utilize microcrystalline cellulose to be converted into 5-chloromethylfurfural under lithium chloride and concentrated hydrochloric acid conditions, and then in In a hydrogen atmosphere, catalyzed hydrogenolysis with palladium chloride was performed to obtain 5-methylfurfural (Angew. Chem. 2008, 120, 8042–8044). 2. Yang et al. used RhCl 3 and HI to catalyze the conversion of glucose and fructose into 5-methylfurfural with a yield of 68% under a hydrogen atmosphere (ChemSusChem2011, 4, 349-352). 3. Chinese patent CN102766119A discloses that a fructo-based biomass is pyrolyzed under the catalysis of an acid catalyst to obtain bio-oil containing 20% molar yield of 5-methylfurfural.

从生物质衍生物合成的方法包括:5-羟甲基糠醛是己糖的脱水产物,近年来不断有人研究从5-羟甲基糠醛制备5-甲基糠醛的方法。2014年Huang等以HMF为原料W2C/AC为催化剂在氢气和THF体系中在200℃反应3h得到87.1%产率的5-MF。2017年Li等以非均相铁为催化剂在氢气和THF单相体系中催化HMF获得了22.1%收率的 5-MF(ChemSusChem2017,10,1436–1447)。同年中国专利CN107353268A报道了一种以 Pd-PVP/ZrO2为催化剂,以甲酸为氢源在四氢呋喃(THF)中催化5-羟甲基糠醛转化为5-甲基糠醛的方法并得到86%的摩尔产率。但以上所述方法都存在催化剂昂贵,工艺复杂,条件苛刻,循环性差等问题。为此,我们急需一种催化剂价格低廉,反应条件温和,工艺简单的快速制备5-甲基糠醛的方法。The synthesis methods from biomass derivatives include: 5-hydroxymethylfurfural is the dehydration product of hexose. In recent years, people have continuously studied the method of preparing 5-methylfurfural from 5-hydroxymethylfurfural. In 2014, Huang et al. used HMF as a raw material and W 2 C/AC as a catalyst to react in hydrogen and THF at 200°C for 3 hours to obtain 5-MF with a yield of 87.1%. In 2017, Li et al. used heterogeneous iron as a catalyst to catalyze HMF in a single-phase system of hydrogen and THF to obtain 5-MF with a yield of 22.1% (ChemSusChem2017, 10, 1436–1447). In the same year, Chinese patent CN107353268A reported a kind of Pd-PVP/ZrO 2 as catalyzer, taking formic acid as hydrogen source in tetrahydrofuran (THF) to catalyze the method that 5-hydroxymethylfurfural is converted into 5-methylfurfural and obtain 86% molar yield. However, the above-mentioned methods all have problems such as expensive catalysts, complex processes, harsh conditions, and poor recyclability. For this reason, we are badly in need of a kind of catalyst that is cheap, and reaction condition is mild, the method for preparing 5-methylfurfural rapidly with simple technique.

发明内容Contents of the invention

本发明的目的是为解决现有制备5-甲基糠醛的技术中存在的催化剂昂贵,工艺复杂等缺点,本发明提供一种无金属参与的从生物质制备5-甲基糠醛的方法。The purpose of the invention is to solve the shortcomings of expensive catalysts and complex processes in the existing technology for preparing 5-methylfurfural. The invention provides a metal-free method for preparing 5-methylfurfural from biomass.

本发明是通过以下技术方案实现的,步骤如下:The present invention is realized through the following technical solutions, and the steps are as follows:

依次将生物质或其衍生物、碘化物、溶剂、酸加入到高温高压反应釜,并通入一定氢气。反应一定时间后,结束后收集有机相分馏即可得到5-甲基糠醛。反应式如下:The biomass or its derivatives, iodide, solvent, and acid are added to the high-temperature and high-pressure reactor in sequence, and a certain amount of hydrogen is introduced. After reacting for a certain period of time, the organic phase is collected and fractionated to obtain 5-methylfurfural. The reaction formula is as follows:

Figure RE-GDA0002053307670000021
Figure RE-GDA0002053307670000021

进一步地,所述生物质或其衍生物︰碘化物摩尔比为0.01~100;生物质或其衍生物︰溶剂质量比为0.001-100;溶剂︰酸体积比为10~1000;反应温度为50~300℃,优选为120~200℃;氢气压力为10~1000psi,优选为100~500psi;反应时间为0.1~24h,优选为1~12h。Further, the biomass or its derivatives: iodide molar ratio is 0.01-100; the biomass or its derivatives: solvent mass ratio is 0.001-100; solvent: acid volume ratio is 10-1000; the reaction temperature is 50 ~300°C, preferably 120~200°C; hydrogen pressure is 10~1000psi, preferably 100~500psi; reaction time is 0.1~24h, preferably 1~12h.

进一步地,所述生物质及其衍生物包括:木质纤维素类生物质、纤维素、淀粉、菊粉、蔗糖、麦芽糖、葡萄糖、果糖和5-羟甲基糠醛(HMF),或其混合物。Further, the biomass and its derivatives include: lignocellulosic biomass, cellulose, starch, inulin, sucrose, maltose, glucose, fructose and 5-hydroxymethylfurfural (HMF), or a mixture thereof.

进一步地,所述酸为盐酸、硫酸、硝酸、磷酸、氢碘酸、氢溴酸、高氯酸、醋酸、3- 氟苯磺酸、甲酸和负载在活性炭、二氧化锆、二氧化钛、二氧化硅、三氧化二铝或分子筛载体上的固体酸催化剂、或其混合物。Further, the acid is hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, hydroiodic acid, hydrobromic acid, perchloric acid, acetic acid, 3-fluorobenzenesulfonic acid, formic acid and supported on activated carbon, zirconium dioxide, titanium dioxide, A solid acid catalyst supported on silicon, aluminum oxide or molecular sieve, or a mixture thereof.

进一步地,所述碘化物包括:碘化钠、碘化钾、碘化锂、碘化氢、碘化铑、碘化钯、碘化钌和碘化铂,或其混合物。Further, the iodide includes: sodium iodide, potassium iodide, lithium iodide, hydrogen iodide, rhodium iodide, palladium iodide, ruthenium iodide and platinum iodide, or a mixture thereof.

进一步地,所述的溶剂包括水、苯、甲苯、氯苯、呋喃、四氢呋喃、2-甲基四氢呋喃、2,5-二甲基四氢呋喃、甲基异丁基甲酮、1,4-环氧六烷、环己烷和正己烷、或其混合物。Further, the solvent includes water, benzene, toluene, chlorobenzene, furan, tetrahydrofuran, 2-methyltetrahydrofuran, 2,5-dimethyltetrahydrofuran, methyl isobutyl ketone, 1,4-epoxyhexane , cyclohexane and n-hexane, or mixtures thereof.

与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:

(1)生物质或其衍生物一锅制5-甲基糠醛,简化操作流程,避免中间步骤带来的物料损失,实现资源的最大化利用。(2)本发明只需在低温,低压条件下进行,对生产设备要求不高,符合安全生产的原则。(3)本发明以常见生物质为原料,无金属催化剂,可循环使用,产物易分离便于工业应用。(1) One-pot production of 5-methylfurfural from biomass or its derivatives, which simplifies the operation process, avoids material loss caused by intermediate steps, and maximizes the utilization of resources. (2) The present invention only needs to be carried out under low temperature and low pressure conditions, and the requirements for production equipment are not high, which meets the principle of safe production. (3) The present invention uses common biomass as a raw material, has no metal catalyst, can be recycled, and the product is easy to separate to facilitate industrial application.

具体实施方式Detailed ways

下面将结合本发明实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

实施例1Example 1

在50mL高温高压反应釜中依次加入100mg淀粉、2mmol碘化钠、2ml水、0.18mmolHCl(37wt%)、5ml2-甲基四氢呋喃,密封反应釜,充入氢气(300psi),搅拌并快速加热至160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测其产物中2-甲基呋喃的产率为4.9%,糠醛的产率为1.9%,5-甲基糠醛的产率为37.7%,总产率为44.5%。Add 100mg of starch, 2mmol of sodium iodide, 2ml of water, 0.18mmol of HCl (37wt%), 5ml of 2-methyltetrahydrofuran in a 50mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (300psi), stir and rapidly heat to 160 ℃, keep 2h. Reactor ice-water bath is cooled to room temperature, collects organic phase and detects that the productive rate of 2-methylfuran in its product is 4.9%, the productive rate of furfural is 1.9%, the productive rate of 5-methylfurfural is 37.7%, total The yield was 44.5%.

5-甲基糠醛产率的检测和计算依据下述方法进行:The detection and calculation of 5-methylfurfural productive rate are carried out according to the following method:

定量分析采用气相色谱仪安捷伦7820A系列(FID检测器,AgilentHP-5色谱柱:30m*32um*0.25um)。定性分析采用气相质谱仪ThermoscientificTRACE1310(HP-5毛细色谱柱30m*320μm*0.25μm)。Quantitative analysis adopts gas chromatograph Agilent 7820A series (FID detector, AgilentHP-5 chromatographic column: 30m*32um*0.25um). Qualitative analysis was carried out using a gas phase mass spectrometer ThermoscientificTRACE1310 (HP-5 capillary column 30m*320μm*0.25μm).

5-甲基糠醛产率计算公式;5-Methylfurfural yield calculation formula;

5-甲基糠醛产率=(有机相中5-甲基糠醛摩尔量/生物质中葡萄糖的摩尔量)×100%5-methylfurfural yield=(the molar amount of 5-methylfurfural in the organic phase/the molar amount of glucose in the biomass)×100%

实施例2Example 2

在50mL高温高压反应釜中依次加入100mg淀粉、4mmol碘化钠、2ml水、0.18mmolH2SO4、3ml呋喃,搅拌并快速加热至160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测其产物中2-甲基呋喃的产率为4.8%,糠醛的产率为2.1%,5-甲基糠醛的产率为34.3%,总产率为41.2%。Add 100mg of starch, 4mmol of sodium iodide, 2ml of water, 0.18mmol of H 2 SO 4 , and 3ml of furan into a 50mL high-temperature and high-pressure reactor, stir and rapidly heat to 160°C for 2 hours. Reactor ice water bath is cooled to room temperature, collects organic phase and detects that the productive rate of 2-methylfuran in its product is 4.8%, the productive rate of furfural is 2.1%, the productive rate of 5-methylfurfural is 34.3%, total The yield was 41.2%.

实施例3Example 3

在50mL高温高压反应釜中依次加入100mg淀粉、2mmol碘化钠、2ml水、0.18mmolCF3SO3H、3ml2-甲基四氢呋喃,密封反应釜,充入氢气(300psi),搅拌并快速加热至160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相经气相色谱检测,其产物中2-甲基呋喃的产率为1.9%,糠醛的产率为1.6%,5-甲基糠醛的产率为29.0%,总产率为31.5%。Add 100mg of starch, 2mmol of sodium iodide, 2ml of water, 0.18mmol of CF 3 SO 3 H, 3ml of 2-methyltetrahydrofuran into a 50mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (300psi), stir and rapidly heat to 160 ℃, keep 2h. Reactor ice-water bath is cooled to room temperature, collects organic phase and detects through gas chromatography, and the productive rate of 2-methylfuran in its product is 1.9%, the productive rate of furfural is 1.6%, and the productive rate of 5-methylfurfural is 29.0%. %, the total yield is 31.5%.

实施例4Example 4

在50mL高温高压反应釜中依次加入100mg葡萄糖、2mmol碘化钠、2ml水、0.18mmolHI(57wt%)、3ml环己烷,密封反应釜,充入氢气(200psi),搅拌并快速加热至 160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测其产物中2-甲基呋喃的产率为2.4%,5-甲基糠醛的产率为32.5%,总产率为34.9%。Add 100mg of glucose, 2mmol of sodium iodide, 2ml of water, 0.18mmol of HI (57wt%), and 3ml of cyclohexane in sequence in a 50mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (200psi), stir and rapidly heat to 160°C , keep 2h. The reactor was cooled to room temperature in an ice-water bath, and the organic phase was collected to detect that the yield of 2-methylfuran in the product was 2.4%, the yield of 5-methylfurfural was 32.5%, and the total yield was 34.9%.

实施例5Example 5

在50mL高温高压反应釜中依次加入100mg果糖、2mmol碘化钠、2ml水、0.18mmolHCl(37wt%)、3ml甲基异丁基甲酮,密封反应釜,充入氢气(200psi)搅拌并快速加热至160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测,其产物中2- 甲基呋喃的产率为3.1%,5-甲基糠醛的产率为31.2%,总产率为34.3%。Add 100mg fructose, 2mmol sodium iodide, 2ml water, 0.18mmol HCl (37wt%), and 3ml methyl isobutyl ketone successively in a 50mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (200psi) and stir and rapidly heat to 160 ℃, keep 2h. The reactor was cooled to room temperature in an ice-water bath, and the organic phase was collected and detected. The yield of 2-methylfuran in the product was 3.1%, the yield of 5-methylfurfural was 31.2%, and the total yield was 34.3%.

实施例6Example 6

在50mL高温高压反应釜中依次加入0.5mmolHMF、0.18mlHCl(37wt%)、2mmolNaI、3ml2-甲基四氢呋喃,密封反应釜,充入氢气(300psi),搅拌并快速加热至160℃,保持 2h。将反应釜冰水浴冷却至室温,收集有机相并检测其产物中5-甲基糠醛的产率为51.9%, 2,5-二甲酰基呋喃的产率为35.6%,总产率为87.5%。Add 0.5mmol HMF, 0.18ml HCl (37wt%), 2mmolNaI, 3ml 2-methyltetrahydrofuran to a 50mL high-temperature and high-pressure reactor in sequence, seal the reactor, fill it with hydrogen (300psi), stir and rapidly heat to 160°C and keep for 2h. Cool the reactor to room temperature in an ice-water bath, collect the organic phase and detect that the yield of 5-methylfurfural in the product is 51.9%, the yield of 2,5-diformylfuran is 35.6%, and the total yield is 87.5%. .

实施例7Example 7

在50mL高温高压反应釜中依次加入100mg淀粉、2mmol碘化钠、2ml水、0.18mmolHCl(37wt%)、3ml正辛烷,密封反应釜,充入氢气(100psi),搅拌并快速加热至180℃,保持1h。将反应釜冰水浴冷却至室温,收集有机相并检测,其产物中2-甲基呋喃的产率为4.2%,糠醛的产率为1.6%,5-甲基糠醛的产率为10.1%,总产率为15.9%。Add 100mg of starch, 2mmol of sodium iodide, 2ml of water, 0.18mmol of HCl (37wt%), and 3ml of n-octane in sequence into a 50mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (100psi), stir and rapidly heat to 180°C , keep 1h. Reactor ice-water bath is cooled to room temperature, collects organic phase and detects, and the productive rate of 2-methylfuran in its product is 4.2%, and the productive rate of furfural is 1.6%, and the productive rate of 5-methylfurfural is 10.1%, The overall yield is 15.9%.

实施例8Example 8

在50mL高温高压反应釜中依次加入100mg淀粉、2mmol碘化钾、2ml水、0.18mmolHCl(37wt%)、3ml甲苯,密封反应釜,充入氢气(500psi),搅拌并快速加热至 160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测,其产物中2-甲基呋喃的产率为2.5%,糠醛的产率为2.3%,5-甲基糠醛的产率为36.5%,总产率为41.3%。Add 100mg of starch, 2mmol of potassium iodide, 2ml of water, 0.18mmol of HCl (37wt%), and 3ml of toluene into a 50mL high-temperature and high-pressure reactor in sequence, seal the reactor, fill it with hydrogen (500psi), stir and rapidly heat to 160°C and keep for 2h. Reactor ice-water bath is cooled to room temperature, collects organic phase and detects, and the productive rate of 2-methylfuran in its product is 2.5%, and the productive rate of furfural is 2.3%, and the productive rate of 5-methylfurfural is 36.5%, The overall yield was 41.3%.

实施例9Example 9

在50mL高温高压反应釜中依次加入100mg菊粉、4mmol碘化锂、2ml水、0.18mmolHCl(37wt%)、3ml甲苯,密封反应釜,充入氢气(500psi),搅拌并快速加热至 160℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测,其产物中2-甲基呋喃的产率为1.7%,糠醛的产率为1.3%,5-甲基糠醛的产率为38.5%,总产率为41.5%。Add 100 mg of inulin, 4 mmol of lithium iodide, 2 ml of water, 0.18 mmol of HCl (37 wt%), and 3 ml of toluene in sequence in a 50 mL high-temperature and high-pressure reactor, seal the reactor, fill it with hydrogen (500 psi), stir and rapidly heat to 160 ° C, Keep for 2h. Reactor ice-water bath is cooled to room temperature, collects organic phase and detects, and the productive rate of 2-methylfuran in its product is 1.7%, and the productive rate of furfural is 1.3%, and the productive rate of 5-methylfurfural is 38.5%, The overall yield is 41.5%.

实施例10Example 10

在50mL高温高压反应釜中依次加入1.0mmol麦芽糖、2mmol碘化氢、1ml水、3ml 2,5- 二甲基四氢呋喃,密封反应釜,充入氢气(500psi),搅拌并快速加热至150℃,保持2h。将反应釜冰水浴冷却至室温,收集有机相并检测,其产物中2-甲基呋喃的产率为3.7%,5- 甲基糠醛的产率为42.5%,总产率为46.2%。Add 1.0mmol maltose, 2mmol hydrogen iodide, 1ml water, 3ml 2,5-dimethyltetrahydrofuran to a 50mL high-temperature and high-pressure reactor in sequence, seal the reactor, fill it with hydrogen (500psi), stir and rapidly heat to 150°C, Keep for 2h. The reactor was cooled to room temperature in an ice-water bath, and the organic phase was collected and detected. The yield of 2-methylfuran in the product was 3.7%, the yield of 5-methylfurfural was 42.5%, and the total yield was 46.2%.

Claims (1)

1. A method for preparing 5-methylfurfural from biomass resources in one pot without metal participation is characterized by comprising the following steps: sequentially adding biomass or derivatives thereof, iodide, solvent and acid into a high-temperature high-pressure reaction kettle, introducing certain hydrogen, reacting for a certain time, and collecting an organic phase for fractionation after the reaction is finished to obtain 5-methylfurfural, wherein the biomass or derivatives thereof are prepared by the steps of: iodide mass molar ratio is 25mg to 1mmol or 50mg to 1mmol; biomass or derivatives thereof: the mass volume ratio of the solvent is 100mg to 5mL or 100mg to 7mL; acid: the molar volume ratio of the solvent is 0.18mmol to 5mL or 0.18mmol to 7mL; the reaction temperature is 160-200 ℃, the hydrogen pressure is 200-500 psi, and the reaction time is 2-12 h; the biomass and its derivatives include: lignocellulosic biomass, cellulose, starch, inulin, sucrose, maltose, glucose, fructose and 5-hydroxymethylfurfural or mixtures thereof; the acid is hydrochloric acid or sulfuric acid; the iodide is one or more of sodium iodide, potassium iodide, lithium iodide, hydrogen iodide, rhodium iodide, palladium iodide, ruthenium iodide and platinum iodide; the solvent is one or more of water, benzene, toluene, chlorobenzene, furan, tetrahydrofuran, 2-methyltetrahydrofuran, 2, 5-dimethyltetrahydrofuran, methyl isobutyl ketone, 1, 4-epoxyhexa-ne, cyclohexane and n-hexane.
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