CN113024370B - Method for preparing formic acid from biomass polyol - Google Patents

Method for preparing formic acid from biomass polyol Download PDF

Info

Publication number
CN113024370B
CN113024370B CN201911250187.XA CN201911250187A CN113024370B CN 113024370 B CN113024370 B CN 113024370B CN 201911250187 A CN201911250187 A CN 201911250187A CN 113024370 B CN113024370 B CN 113024370B
Authority
CN
China
Prior art keywords
reaction
ceo
formic acid
glycerol
cerium dioxide
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.)
Active
Application number
CN201911250187.XA
Other languages
Chinese (zh)
Other versions
CN113024370A (en
Inventor
王峰
任濮宁
罗能超
高著衍
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.)
Dalian Institute of Chemical Physics of CAS
Original Assignee
Dalian Institute of Chemical Physics of CAS
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 Dalian Institute of Chemical Physics of CAS filed Critical Dalian Institute of Chemical Physics of CAS
Priority to CN201911250187.XA priority Critical patent/CN113024370B/en
Publication of CN113024370A publication Critical patent/CN113024370A/en
Application granted granted Critical
Publication of CN113024370B publication Critical patent/CN113024370B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/23Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups
    • 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
    • B01J23/002Mixed oxides other than spinels, e.g. perovskite
    • 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
    • B01J23/10Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
    • 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
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/20Vanadium, niobium or tantalum
    • B01J23/22Vanadium
    • 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
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32Manganese, technetium or rhenium
    • B01J23/34Manganese
    • 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
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/66Silver or gold
    • 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
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/83Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/31Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
    • C07C51/313Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting with molecular oxygen
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

The invention relates to a method for preparing formic acid by photo-thermally catalyzing biomass polyalcohol C-C bond oxidation and fracture with a cerium dioxide-based catalyst. The method uses glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch as a reaction substrate, oxygen as an oxidant, cerium dioxide or supported cerium dioxide as a catalyst, and realizes the selective oxidation of the reaction substrate to formic acid under the irradiation of visible light of 400-650 nm at a certain temperature. The reaction process is as follows: dissolving a substrate in a solvent, adding a catalyst, sealing a reactor, replacing with oxygen for three times, keeping a certain pressure, and irradiating with 400-650 nm visible light at 40-150 ℃ for reaction to generate formic acid. The synthesis method can play an important role in preparing the formic acid by the high-selectivity oxidation of the biomass polyol.

Description

Method for preparing formic acid from biomass polyol
Technical Field
The invention relates to a method for preparing formic acid, in particular to a method for photo-thermally catalyzing biomass polyol glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch to be oxidized into formic acid by using cerium dioxide or supported cerium dioxide.
Background
The development of renewable resources is imminent due to the increasing exhaustion of fossil energy and environmental pollution and greenhouse effect caused by the use of fossil energy, and the development of biomass, which is a carbon resource rich in natural content and unique in renewable energy, plays an important role in solving the energy crisis (chem.rev.2018,118(2), 505-. The biomass includes lignocellulose, sugar, biological oil and fat, etc., and is a polymer with rich oxygen content and composed of C skeleton. The selective oxidative cleavage of the biomass C-C bond not only can convert the biomass C-C bond into a high value-added small molecular compound, but also can introduce a new functional group such as a carboxylic acid group.
Formic acid is one of basic organic chemical raw materials, and can be widely used for tanning pesticides, dyes, leather and the likeBesides, formic acid can be converted into high-purity H by a photo-electric or thermal method2Are excellent hydrogen storage materials (Energy Fuels 2017,31(11),12603-&Environmental Science 2019) and formic acid direct fuel cell is also a way of direct supply of formic acid (chem.rev.2014,114(10), 5117-. The C-C bond of biomass polyol such as glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch is selectively oxidized and broken to formic acid, so that the efficient utilization of biomass can be realized, a hydrogen donor raw material with a high additional value can be provided, and the method has important significance for the high-value utilization of biomass and the application to the current energy problem.
At present, the method for breaking the C-C bond of the biomass polyol is mostly a reaction catalyzed by solid acid under hydrothermal conditions, and the method usually needs to load noble metal, have higher reaction temperature and high concentration of H2O2Meanwhile, the problem of low selectivity also often exists; photocatalysis and electrocatalysis due to mild reaction conditions, selective oxidative cleavage of the C-C bond of catalytic biomass to formic acid has been increasingly emphasized in recent years (ACS Catal.2018,8 (3); 2129-. By TiO2The photocatalytic oxidation of glucose in 0.03M NaOH solution can result in 35% formic acid yield (ACS Sustainable Chemistry)&Engineering 2017,5(8),6377-2After the Au nano particles are loaded, the catalyst can efficiently convert glycerol into formic acid under visible light due to the LSPR effect of the Au particles under illumination. In the photocatalytic conversion of biomass polyols, H is often used in an alkaline solution to increase the selectivity of the reaction2O2As an oxidizing agent, there are other problems such as low reactivity and low conversion rate.
Reactions which can not be realized by pure photocatalysis or thermal catalysis can be realized by utilizing the photo-thermal synergistic effect, and high reaction activity and selectivity can be obtained in the process. Recent studies show that the ceria-based catalyst has higher activity in the aspect of photothermal catalytic organic matter conversion (ACS Catal.2015,5,3278-3286, J.Phys.chem.C 2013,117,24242-24249, J.Phys.chem.C 2011,115, 14050-14057). The cerium dioxide-based catalyst is of great significance for biomass conversion under photothermal conditions.
Disclosure of Invention
The invention relates to a method for preparing formic acid by using a cerium dioxide-based catalyst to photo-thermally catalyze the oxidative cleavage of a C-C bond of biomass polyol. The method uses glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch as a reaction substrate, oxygen as an oxidant, cerium dioxide or supported cerium dioxide as a catalyst, and realizes selective oxidation to formic acid by irradiation of 400-650 nm visible light at 40-150 ℃. The invention realizes the high-selectivity conversion of renewable biomass polyol to formic acid under the photo-thermal condition, and the synthesis method has important effect on the high-selectivity oxidation of the biomass polyol to the formic acid.
The technical scheme adopted by the invention is as follows:
dissolving a substrate in a solvent, adding a catalyst, sealing a reactor, replacing with oxygen for three times, keeping a certain pressure, irradiating with 400-650 nm visible light at 40-150 ℃ for reaction for not less than 0.5h, and generating formic acid.
The catalyst is loaded with metal in an amount of 0.5mol% -2.0 mol% except pure cerium dioxide.
The catalyst used in the reaction is cerium dioxide or supported metal cerium dioxide, wherein: loaded with cerium dioxide M/CeO2Can be as follows: ag2O/CeO2,NiO/CeO2,ZnO/CeO2,Fe2O3/CeO2,CuO/CeO2,V2O5/CeO2,Co3O4/CeO2,MnO2/CeO2,Mg/CeO2One or more than two of them.
The biomass polyol is glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch.
The concentration of a reaction substrate is 0.05-0.5 mmol/mL, the dosage of a catalyst is 50-100 mg, and the volume of a solvent is 25 mL.
The solvent is acetonitrile or water.
The reaction system is carried out in an oxygen atmosphere of 0.1 to 0.6 MPa.
The reaction temperature is 40-150 ℃.
The wavelength of a visible light source used for the reaction is 400-650 nm, the light source has a single wavelength, a mixed wavelength or a continuous wavelength, and the light intensity can be 50-240 mW/cm2
The reaction time is more than 0.5 h.
Compared with the traditional method for preparing formic acid, the method has the following advantages:
1. the raw materials are easy to obtain and can be regenerated;
2. the reaction condition is mild, and the energy consumption is low;
3. the catalyst has high activity, the highest conversion rate can reach 100 percent, and the highest selectivity is more than 90 percent
Detailed Description
In order to further explain the present invention in detail, several specific embodiments are given below, but the present invention is not limited to these embodiments.
Example 1
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 2
Mixing 1.25mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 99%.
Example 3
12.5mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2Irradiating visible light with a wavelength of 455nm for 10h to reactAfter the end of the reaction, the conversion of glycerol was 198% and the yield of formic acid was 95% by HPLC.
Example 4
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C with 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 5
10mmol of glycerol, 100mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 99%.
Example 6
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL acetonitrile, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation of visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 90% and the yield of formic acid was 85%.
Example 7
10mmol of glycerol and 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.1Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 82% and the yield of formic acid was 80%.
Example 8
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.6Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 99%.
Example 9
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 10
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 40 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 50% and the yield of formic acid was 48%.
Example 11
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 150 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 100% and the yield of formic acid was 89% by HPLC.
Example 12
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation with a wavelength of 400nm, and after completion of the reaction, the conversion of glycerol was 100% and the yield of formic acid was 90% by HPLC.
Example 13
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 650nm, and after completion of the reaction, the conversion of glycerol was 80% and the yield of formic acid was 78% by HPLC.
Example 14
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, and maintaining pressureThe force is 0.5Mpa, and the light intensity is 50mW/cm at 120 DEG C2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 60% and the yield of formic acid was 55%.
Example 15
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and irradiating at 120 deg.C with light intensity of 240mW/cm2The reaction was carried out for 10 hours under irradiation of visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 97%.
Example 16
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 0.5h under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 30% and the yield of formic acid was 27%.
Example 17
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 9 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 95% and the yield of formic acid was 90%.
Example 18
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 19
Mixing 10mmol of glycerol and 50mg of CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2Irradiating with visible light with wavelength of 455nm for 10 hr, and quantifying by HPLC to obtain glycerol conversion rateThe yield of formic acid was 56% and 60%.
Example 20
10mmol of glycerol, 50mg of 0.5mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 80% and the yield of formic acid was 76%.
Example 21
10mmol of glycerol and 50mg2 mol% of CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 99%.
Example 22
Mixing 10mmol of glycerol and 50mg of 1 mol% Ag2O/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation of visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 78% and the yield of formic acid was 70%.
Example 23
10mmol of glycerol and 50mg of 1mol percent NiO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 58% and the yield of formic acid was 55%.
Example 24
10mmol of glycerol, 50mg of 1 mol% ZnO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 70% and the yield of formic acid was 66% by HPLC.
Example 25
Adding 10mmol ofGlycerol, 50mg 1 mol% Fe2O3/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 88% and the yield of formic acid was 78%.
Example 26
10mmol of glycerol, 50mg of 1 mol% V2O5/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 77% and the yield of formic acid was 58% by HPLC.
Example 27
Mixing 10mmol of glycerol and 50mg of 1 mol% Co3O4/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 80% and the yield of formic acid was 68% by HPLC.
Example 28
Mixing 10mmol of glycerol and 50mg of 1 mol% MnO2/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 40% and the yield of formic acid was 33% by HPLC.
Example 29
10mmol of glycerol, 50mg of 1 mol% MgO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 30
Mixing 8mmol xylose, 50mg 1 mol% CuO/CeO2Dispersed in 25mL of waterAdding magnetons, replacing with oxygen for three times, maintaining the pressure at 0.5Mpa, and maintaining the light intensity at 120 deg.C under 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 98% and the yield of formic acid was 96%.
Example 31
Mixing 8mmol glucose, 50mg 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 97% and the yield of formic acid was 96%.
Example 32
Mixing 8mmol of fructose, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 96% and the yield of formic acid was 94%.
Example 33
Mixing 8mmol xylose, 50mg 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 98% and the yield of formic acid was 96%.
Example 34
6mmol of sucrose, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 99% and the yield of formic acid was 96%.
Example 35
5mmol of cellobiose, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2Irradiating visible light with wavelength of 455nm for reaction for 10 hr, and reactingThe conversion, determined by HPLC, was 90% and the formic acid yield was 85%.
Example 36
4mmol of starch, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation of visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion was 89% and the yield of formic acid was 85%.
Example 37
Dispersing 10mmol glycerol and 50mg CuO in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C with 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 5% and the yield of formic acid was 0% by HPLC.
Example 38
Mixing 10mmol of glycerol and 50mg of TiO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, the conversion of glycerol was 20% and the yield of formic acid was 10% by HPLC.
Example 39
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, replacing with oxygen for three times, maintaining pressure at 0.5Mpa, and maintaining light intensity at 120 deg.C of 200mW/cm2The reaction was carried out for 10 hours under visible light irradiation at a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 100% and the yield of formic acid was 98%.
Example 40
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magnetons, replacing with oxygen for three times, maintaining the pressure at 0.5Mpa, reacting at 120 deg.C for 10h, and quantifying by HPLC after the reaction is finished, wherein the conversion rate of glycerol is 5% and the yield of formic acid is 0%.
EXAMPLE 41
10mmol of glycerol, 50mg of 1 mol% CuO/CeO2Dispersing in 25mL water, adding magneton, and replacing with oxygenMaintaining the pressure at 0.5Mpa after three times, and applying light intensity at 200mW/cm at 25 deg.C2The reaction was carried out for 10 hours under irradiation with visible light having a wavelength of 455nm, and after completion of the reaction, quantitative determination was carried out by HPLC, whereby the conversion of glycerol was 10% and the yield of formic acid was 8%.

Claims (8)

1. A method for preparing formic acid, which is characterized in that: the method comprises the steps of taking cerium dioxide and/or supported cerium dioxide as a catalyst, taking one or more than two of glycerol, xylose, glucose, fructose, sucrose, cellobiose and starch as a reaction substrate, forming a photo-thermal catalysis system by the catalyst and the reaction substrate, adding acetonitrile and/or water as a solvent, taking oxygen as an oxidant, irradiating the mixture at the oxygen pressure of 0.1-0.8 MPa and 400-650 nm visible light at the temperature of 40-150 ℃ to convert the biomass polyol into formic acid.
2. The method of claim 1, wherein:
the method comprises the following specific steps: dissolving one or more of glycerol, xylose, glucose, fructose, sucrose, cellobiose or starch in a solvent, adding cerium dioxide and/or supported cerium dioxide, sealing the reactor, replacing the gas in the reactor with oxygen for more than 1 time, keeping the pressure of 0.1-0.8 MPa, and irradiating with 400-650 nm visible light at the temperature of 40-150 ℃ for reaction to generate an oxidation product formic acid.
3. A method according to claim 1 or 2, characterized in that: the catalyst used in the reaction is cerium dioxide or supported cerium dioxide, wherein:
(1) the cerium dioxide is CeO2(ii) a (2) Loaded with cerium dioxide M/CeO2Can be as follows: ag2O/CeO2,NiO/CeO2,ZnO/CeO2,Fe2O3/CeO2,CuO/CeO2,V2O5/CeO2,Co3O4/CeO2,MnO2/CeO2,MgO/CeO2One or more than two of the above; a in A/B is supported metal oxide, whereinThe supported metal mole fraction is 0.5mol% -2.0 mol%.
4. A method according to claim 3, characterized by:
the supported metal catalyst is prepared by an impregnation method: dispersing the loaded metal oxide in the loaded metal precursor solution, stirring for 12-20 h, evaporating water at 80-120 ℃, and treating in air at 400 ℃ for 2-4 h.
5. The method of claim 1, wherein: the concentration of the biomass polyol reaction substrate is 0.05-0.5 mmol/mL, the dosage of the catalyst is 50-100 mg, and the volume of the solvent is 25 mL.
6. The method of claim 1, wherein: the temperature of the reaction system is 40-150 ℃.
7. The method of claim 1, wherein: the wavelength of a visible light source used for the reaction is 400-650 nm, the light source has a single wavelength, a mixed wavelength or a continuous wavelength, and the light intensity can be 50-240 mW/cm2
8. The method of claim 1, wherein: the reaction time is more than or equal to 0.5 h.
CN201911250187.XA 2019-12-09 2019-12-09 Method for preparing formic acid from biomass polyol Active CN113024370B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911250187.XA CN113024370B (en) 2019-12-09 2019-12-09 Method for preparing formic acid from biomass polyol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911250187.XA CN113024370B (en) 2019-12-09 2019-12-09 Method for preparing formic acid from biomass polyol

Publications (2)

Publication Number Publication Date
CN113024370A CN113024370A (en) 2021-06-25
CN113024370B true CN113024370B (en) 2022-05-17

Family

ID=76451012

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911250187.XA Active CN113024370B (en) 2019-12-09 2019-12-09 Method for preparing formic acid from biomass polyol

Country Status (1)

Country Link
CN (1) CN113024370B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114644553B (en) * 2022-03-24 2023-08-22 西咸新区青氢华屹能源科技有限公司 Method for preparing formic acid by catalyzing biomass through light-induced iron

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2784012A1 (en) * 2009-12-11 2011-06-16 Envirosource, Inc. Systems and methods for processing glycerol
CN102741211A (en) * 2010-01-29 2012-10-17 瓦克化学股份公司 Method for producing carboxylic acids having 1-3 carbon atoms from renewable resources
CN103159601A (en) * 2011-12-16 2013-06-19 中国科学院大连化学物理研究所 Method of utilizing glycerol to prepare glycolic aldehyde
CN103209950A (en) * 2010-09-17 2013-07-17 Jbach有限公司 Method for catalytically producing formic acid
US9090551B1 (en) * 2014-03-27 2015-07-28 King Abdullah University Of Science And Technology Methods of making formic acid from glycerol
CN112371185A (en) * 2020-12-04 2021-02-19 北华大学 Polyacid catalyst and preparation method and application thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2784012A1 (en) * 2009-12-11 2011-06-16 Envirosource, Inc. Systems and methods for processing glycerol
CN102741211A (en) * 2010-01-29 2012-10-17 瓦克化学股份公司 Method for producing carboxylic acids having 1-3 carbon atoms from renewable resources
CN103209950A (en) * 2010-09-17 2013-07-17 Jbach有限公司 Method for catalytically producing formic acid
CN103159601A (en) * 2011-12-16 2013-06-19 中国科学院大连化学物理研究所 Method of utilizing glycerol to prepare glycolic aldehyde
US9090551B1 (en) * 2014-03-27 2015-07-28 King Abdullah University Of Science And Technology Methods of making formic acid from glycerol
CN112371185A (en) * 2020-12-04 2021-02-19 北华大学 Polyacid catalyst and preparation method and application thereof

Also Published As

Publication number Publication date
CN113024370A (en) 2021-06-25

Similar Documents

Publication Publication Date Title
Hu et al. Major routes in the photocatalytic methane conversion into chemicals and fuels under mild conditions
Navarro-Jaén et al. Highlights and challenges in the selective reduction of carbon dioxide to methanol
Spinner et al. Recent progress in the electrochemical conversion and utilization of CO2
Simakov Renewable synthetic fuels and chemicals from carbon dioxide: fundamentals, catalysis, design considerations and technological challenges
Sun et al. Effect of O2 and H2O on the tri-reforming of the simulated biogas to syngas over Ni-based SBA-15 catalysts
Hargreaves et al. Minimizing energy demand and environmental impact for sustainable NH3 and H2O2 production—A perspective on contributions from thermal, electro-, and photo-catalysis
CN107128875B (en) Hydrogen production catalytic system, hydrogen production system comprising catalytic system and application of catalytic system
Kishi et al. Green synthesis of methyl formate via electrolysis of pure methanol
Tang et al. Visible-light-driven organic transformations integrated with H 2 production on semiconductors
CN101428223A (en) Photocatalyst and its preparing process
CN113024370B (en) Method for preparing formic acid from biomass polyol
CN111151245B (en) Gold nanoflower catalyst with biomass activated carbon as carrier and preparation method and application thereof
Xu et al. Photocatalytic reforming of lignocellulose: A review
CN113546661A (en) Carbon-based single-atom photocatalyst and preparation method and application thereof
Chen et al. Design and tailoring of advanced catalytic process for light alkanes upgrading
Wu et al. Alternatives to water oxidation in the photocatalytic water splitting reaction for solar hydrogen production
Jiang et al. Recent advances on aerobic photocatalytic methane conversion under mild conditions
Krishnan et al. Carbon dioxide: No longer a global menace: A future source for chemicals
CN111359644B (en) Non-noble metal-based molybdenum carbide catalyst for dimethyl ether steam reforming hydrogen production and preparation method and application thereof
Kishore et al. Fundamental Limitation in Electrochemical Methane Oxidation to Alcohol: A Review and Theoretical Perspective on Overcoming It
Adebajo et al. Recent advances in catalytic/biocatalytic conversion of greenhouse methane and carbon dioxide to methanol and other oxygenates
CN114572934B (en) Method for preparing hydrogen from biomass through formic acid
CN114602498A (en) Sea urchin shaped In2O3Cu-Ag loaded bimetallic alloy catalyst and preparation method and application thereof
Zhang et al. Photocatalytic upgrading of 5-hydroxymethylfurfural–aerobic or anaerobic?
CN110433850B (en) Bimetallic catalyst for catalyzing hydrogenation deoxidation of veratryl alcohol and preparation method and application thereof

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
GR01 Patent grant
GR01 Patent grant