CN112921341A - Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production - Google Patents

Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production Download PDF

Info

Publication number
CN112921341A
CN112921341A CN202110099774.4A CN202110099774A CN112921341A CN 112921341 A CN112921341 A CN 112921341A CN 202110099774 A CN202110099774 A CN 202110099774A CN 112921341 A CN112921341 A CN 112921341A
Authority
CN
China
Prior art keywords
cathode
oxidation
anode
hydrogen
oxygen reduction
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.)
Granted
Application number
CN202110099774.4A
Other languages
Chinese (zh)
Other versions
CN112921341B (en
Inventor
邵明飞
宋英杰
栗振华
卫敏
段雪
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.)
Beijing University of Chemical Technology
Original Assignee
Beijing University of Chemical Technology
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 Beijing University of Chemical Technology filed Critical Beijing University of Chemical Technology
Priority to CN202110099774.4A priority Critical patent/CN112921341B/en
Publication of CN112921341A publication Critical patent/CN112921341A/en
Application granted granted Critical
Publication of CN112921341B publication Critical patent/CN112921341B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention discloses a high-efficiency micromolecule catalytic oxidation and hydrogen production coupled reaction system, which comprises an electrolytic cell and a two-electrode coupled reaction mechanism, wherein the two-electrode coupled reaction mechanism comprises a hydrogen precipitation cathode and a No. I micromolecule oxidation anode which are respectively connected with the positive electrode and the negative electrode of a No. I external power supply; the device also comprises an oxygen reduction reaction mechanism and a proton exchange membrane, wherein the oxygen reduction reaction mechanism comprises an oxygen reduction cathode and a small molecular oxidation anode II which are respectively connected with the anode and the cathode of the external power supply II; the proton exchange membrane is arranged between the hydrogen evolution cathode and the I-type small molecule oxidation anode, and the interior of the electrolytic cell is divided into a I-type electrolytic area and a II-type electrolytic area; no. I electrolysis district and No. II electrolysis district fill electrolyte. The invention realizes high hydrogen yield and biomass oxidation rate and improves energy conversion efficiency.

Description

Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production
Technical Field
The invention belongs to the technical field of biomass catalytic conversion and chemical engineering, and particularly relates to a high-efficiency reaction system for coupling small-molecule catalytic oxidation and hydrogen production.
Background
Due to the increased environmental pollution and the consumption of fossil fuels, there is a need to find eco-friendly renewable energy sources. Hydrogen energy is one of the most desirable alternative energy carriers due to its clean, sustainable and renewable advantages. Conventional routes to large scale production of hydrogen include steam reforming of methane and coal gasification to produce hydrogen and conversion of water to hydrogen (H)2) The former process releases a large amount of carbon dioxide, which is the most important greenhouse gas. And the latter catalytically produces H by water decomposition2Although a promising and environmentally sustainable way of production, there are still drawbacks: for example, due to the slow kinetics of the anodic Oxygen Evolution Reaction (OER), considerable overpotentials are often required to produce hydrogen at appreciable rates. There have been many recent studies that have shown that this limitation can be overcome by coupling the traditional OER with the Hydrogen Evolution Reaction (HER) with a more facile oxidation of small molecules. Numerous research works have demonstrated that the introduction of molecules such as methanol, ethanol, hydrazine, 5-hydroxymethylfurfural, and urea, etc., can increase the efficiency of energy conversion.
In the last decade, researchers have made a lot of research work to find excellent biomass small-molecule oxidation reaction (BOR) electrocatalysts, and through doping, anion replacement, defect engineering, etc., the kinetics of the catalyst reaction is improved, and many electrocatalysts such as alloys, metal oxides, sulfides, phosphides, nitrides, etc., with excellent performance and low cost are obtained. However, although these catalysts show excellent catalytic conversion performance of biomass, with the conventional two-electrode (BOR-HER) coupled system, due to the inevitable competition of OER in the aqueous electrolyte, the biomass oxidation reaction can only be operated at a low potential with a relatively low current density, and thus the reaction rate and conversion efficiency are greatly reduced, failing to meet the requirements of industrial production.
Disclosure of Invention
The invention aims to overcome the defect of the existing method for catalytically producing H by water decomposition2The system has the defects, and the aim is to provide a reaction system for coupling the high-efficiency small-molecule catalytic oxidation and hydrogen production.
The invention is realized by the following technical scheme:
a reaction system for coupling high-efficiency micromolecule catalytic oxidation with hydrogen production comprises an electrolytic cell and a two-electrode coupling reaction mechanism, wherein the two-electrode coupling reaction mechanism comprises a hydrogen precipitation cathode and a No. I micromolecule oxidation anode which are respectively connected with the anode and the cathode of a No. I external power supply; the device also comprises an oxygen reduction reaction mechanism and a proton exchange membrane, wherein the oxygen reduction reaction mechanism comprises an oxygen reduction cathode and a small molecular oxidation anode II which are respectively connected with the anode and the cathode of the external power supply II; the proton exchange membrane is arranged between the hydrogen evolution cathode and the I-type small molecule oxidation anode, and the interior of the electrolytic cell is divided into a I-type electrolytic area and a II-type electrolytic area; no. I electrolysis district and No. II electrolysis district fill electrolyte.
In the technical scheme, the electrolyte filled in the No. I electrolysis region is alkaline electrolyte; the electrolyte filled in the No. II electrolysis area is alkaline electrolyte added with biomass micromolecules.
In the technical scheme, the hydrogen evolution cathode and the oxygen reduction cathode are commercial Pt/C electrodes.
In the technical scheme, the hydrogen evolution cathode, the I small molecular oxidation anode, the oxygen reduction cathode and the II small molecular oxidation anode are immersed in the electrolyte.
In the technical scheme, the No. I small molecular oxidation anode and the No. II small molecular oxidation anode are hydrotalcite nanosheet array electrodes.
The invention has the beneficial effects that:
the invention provides a micromolecule capable of realizing high-efficiency biomassThe catalytic oxidation and hydrogen production coupled reaction system introduces an oxygen reduction reaction system (ORR) into a traditional two-electrode (BOR-HER) coupled reaction system, simultaneously realizes high hydrogen yield and biomass oxidation rate, avoids energy consumption caused by competition of oxygen precipitation reaction, and improves energy conversion efficiency. Compared with the reaction of the traditional two-electrode (BOR-HER) coupled reaction system, the high value-added oxidation product and H2The yield is respectively improved by 68 times and 46 times, and the system can be driven by using a 3V solar cell, thereby proving the super practicability.
Drawings
FIG. 1 is a schematic structural diagram of a reaction system for coupling high-efficiency small-molecule catalytic oxidation and hydrogen production;
FIG. 2 is a graph showing the variation of the content of substances in the process of oxidizing biomass micromolecules 5-hydroxymethylfurfural by using a reaction system coupling efficient micromolecule catalytic oxidation and hydrogen production in example 2 of the present invention;
FIG. 3 is a graph of data comparing the yields of 2, 5-furandicarboxylic acid (FDCA) from a system constructed in example 2 of the present invention and a conventional two-electrode system;
FIG. 4 is a graph of data comparing hydrogen production for a system constructed in accordance with example 2 of the present invention with a conventional two-electrode system.
Wherein:
1 electrolytic cell
2 hydrogen evolution cathode
3I small molecular oxidation anode
4 proton exchange membrane
5I external power supply
6 oxygen reduction cathode
No. 7 II small molecule oxidation anode
8 II external power supply
No. 9I electrolysis zone
No. 10 II electrolysis zone.
For a person skilled in the art, other relevant figures can be obtained from the above figures without inventive effort.
Detailed Description
In order to make the technical scheme of the invention better understood by those skilled in the art, the technical scheme of the high-efficiency small-molecule catalytic oxidation and hydrogen production coupled reaction system of the invention is further described by combining the drawings of the specification and through a specific implementation mode.
Example 1
As shown in fig. 1, a high-efficiency reaction system for coupling small-molecule catalytic oxidation with hydrogen production comprises an electrolytic cell 1 and a two-electrode coupling reaction mechanism, wherein the two-electrode coupling reaction mechanism comprises a hydrogen evolution cathode (HER)2 and a No. i small-molecule oxidation anode (BOR)3 which are respectively connected with the positive electrode and the negative electrode of a No. i external power supply 5; the device also comprises an oxygen reduction reaction mechanism and a proton exchange membrane 4, wherein the oxygen reduction reaction mechanism comprises an oxygen reduction cathode (ORR)6 and a small molecular oxidation anode (BOR)7 which are respectively connected with the anode and the cathode of a No. II external power supply 8; the proton exchange membrane 4 is arranged between the hydrogen evolution cathode 2 and the I-type small molecular oxidation anode 3, and divides the interior of the electrolytic cell 1 into a I-type electrolytic area 9 and a II-type electrolytic area 10; no. I electrolysis zone 9 and No. II electrolysis zone 10 are filled with electrolyte.
The electrolyte filled in the No. I electrolysis region 9 is alkaline electrolyte; the electrolyte filled in the No. II electrolysis area 10 is alkaline electrolyte added with biomass micromolecules.
The hydrogen evolution cathode 2 and the oxygen reduction cathode 6 are commercial Pt/C electrodes.
The hydrogen separation cathode 2, the I small molecular oxidation anode 3, the oxygen reduction cathode 6 and the II small molecular oxidation anode 7 are immersed in the electrolyte.
The electrolytic tank 1 is a glass electrolytic tank.
The No. I small molecular oxidation anode 3 and the No. II small molecular oxidation anode 7 are cobalt-iron hydrotalcite nanosheet array electrodes.
The preparation method of the hydrotalcite nanosheet array electrode comprises the following steps:
respectively carrying out ultrasonic treatment on the foamed nickel of the conductive substrate for 10min by using absolute ethyl alcohol, acetone and deionized water, and removing impurities on the surface;
(ii) preparation of 0.5mg/mL cobalt nitrate (Co (NO)3)2) 0.25mg/mL ferrous sulfate (FeSO)4) 50mL of the mixed salt solution is used as an electrolyte solution;
and (iii) in the electrolyte solution prepared in the step (i), taking a saturated calomel electrode as a reference electrode and a platinum wire as a counter electrode, directly growing a ferrocobalt hydrotalcite nanosheet array on the foamed nickel by using a potentiostatic method, setting the potential of electrochemical synthesis to be-1V, setting the synthesis time to be 100s, and setting the synthesis temperature to be 25 ℃.
In the embodiment, biomass micromolecules 5-hydroxymethylfurfural (5-HMF) are oxidized to obtain 2, 5-furandicarboxylic acid (FDCA) with huge application potential, and hydrogen is efficiently produced at the same time.
In this embodiment, the voltage of the external power supply 5 i is 1V; the voltage of the external power supply 8 No. II is 2V; the No. I small molecular oxidation anode 3 and the No. II small molecular oxidation anode 7 both adopt cobalt-iron hydrotalcite nanosheet array electrodes; the alkaline electrolyte filled in the No. I electrolysis region 9 is 1.0M KOH aqueous solution; electrolytic zone II, 10, was filled with electrolyte as a 1.0M aqueous KOH solution containing 50mM 5-HMF.
For further proving the effect of the system of the present invention, as a comparison, a conventional two-electrode (BOR-HER) coupled system reaction is constructed, the electrode material and the electrolyte are used, and the voltage selection is the same as that of the reaction system coupling the high-efficiency small-molecule catalytic oxidation and hydrogen production in this embodiment.
Under the above conditions, the reaction system of the present embodiment, which couples the high-efficiency small-molecule catalytic oxidation and hydrogen production, is operated for about 30 minutes, the electrolyte in the reaction process is collected, the content of substances in the electrolyte in the reaction process is analyzed by using high performance liquid chromatography HPLC, and the conversion rate and selectivity of the product are calculated.
As shown in fig. 2, as the reaction proceeds, 5-hydroxymethylfurfural (5-HMF) is gradually oxidized in the system to obtain a final product 2, 5-furandicarboxylic acid (FDCA), and after the reaction is finished, 5-hydroxymethylfurfural (5-HMF) is completely converted into the product 2, 5-furandicarboxylic acid (FDCA), no other by-product is generated, and the conversion rate and the selectivity are both greater than 99%.
As shown in FIGS. 3 and 4, the 2, 5-furandimethanol of the system constructed in this example was reacted during the same reaction timeThe yield of acid (FDCA) and hydrogen is far greater than that of the traditional two-electrode (BOR-HER) coupling system, and the high value-added oxidation products and H2The yield is improved by 68 times and 46 times respectively.
Example 2
Based on example 1, this example oxidizes small molecule furfuryl alcohol to obtain furoic acid, while efficiently producing hydrogen.
In this embodiment, the voltage of the external power supply 5 i is 1V; the voltage of the external power supply 8 No. II is 2V; the No. I micromolecular oxidation anode 3 and the No. II micromolecular oxidation anode 7 both adopt cobalt-aluminum hydrotalcite nanosheet array electrodes; the alkaline electrolyte filled in the No. I electrolysis region 9 is 1.0M KOH aqueous solution; electrolytic zone II, 10, was filled with electrolyte as a 1.0M aqueous KOH solution containing 10mM furfuryl alcohol.
Example 3
Based on example 1, this example oxidizes small-molecule benzyl alcohol to obtain benzoic acid, and simultaneously produces hydrogen gas with high efficiency.
In this embodiment, the voltage of the external power supply 5 i is 1V; the voltage of the external power supply 8 No. II is 2V; the No. I small molecular oxidation anode 3 and the No. II small molecular oxidation anode 7 both adopt nickel iron hydrotalcite nanosheet array electrodes; the alkaline electrolyte filled in the No. I electrolysis region 9 is 1.0M KOH aqueous solution; electrolytic zone II, 10, was filled with electrolyte as a 1.0M aqueous KOH solution containing 10mM benzyl alcohol.
The working principle of the invention is as follows:
in the novel system, the No. I electrolysis area uses alkaline electrolyte, and the No. II electrolysis area uses alkaline electrolyte added with small molecules. After the external power supply is electrified, the surface of a Hydrogen Evolution (HER) cathode in the No. I electrolysis area is subjected to water molecule reduction to form hydrogen reaction, the water molecules produce hydrogen through electrons transmitted by an external circuit, and meanwhile, protons are transmitted to the No. II electrolysis area through a proton exchange membrane. The No. II electrolysis area is a core component of the system, wherein, biomass micromolecule oxidation reaction and oxygen precipitation reaction occur on the surface of the No. I micromolecule oxidation anode, and meanwhile, micromolecule oxidation reaction and oxygen precipitation reaction occur on the surface of the No. II micromolecule oxidation anode in the No. II electrolysis area. In the No. I small molecular oxidation anodeOxygen generated on the surfaces of the electrode and the II small-molecule oxidation anode is reduced on the surface of an oxygen reduction cathode (ORR), and an intermediate product HO generated by reduction is generated2Further participate in the small molecule oxidation reaction on the surface of the small molecule oxidation anode, thereby improving the oxidation efficiency and avoiding O2Energy loss due to precipitation.
Compared with the existing small molecule oxidation technology, the novel system designed by the invention has the following advantages:
the traditional small molecule oxidation process needs high temperature, high pressure and addition of external oxygen, and meanwhile, a reactor required by the reaction has a complex structure, consumes energy and time, and has low efficiency, low reaction selectivity and low substrate conversion rate. The novel system is carried out at normal temperature and normal pressure, does not need to add an oxidant, has small applied voltage, high reaction selectivity and high substrate conversion rate.
(ii) compared with the traditional two-electrode (BOR-HER) coupled system reaction, the novel system designed by the invention has high hydrogen and high value-added micromolecule production rate and high energy utilization efficiency, more economically utilizes the oxygen byproduct generated in the reaction process, and realizes that the oxygen atoms in the water are completely added into the biomass molecules instead of O2The form of (A) is separated out.
(iii) the novel system designed by the invention can be driven by solar energy to stably operate, so that the conversion of the solar energy into hydrogen energy and chemicals with high added values is realized, and the practicability is high.
It should be noted that the embodiments and features of the embodiments may be combined with each other without conflict.
The applicant declares that the above description is only a specific embodiment of the present invention, but the scope of the present invention is not limited thereto, and it should be understood by those skilled in the art that any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention are within the scope and disclosure of the present invention.

Claims (5)

1. A reaction system for coupling high-efficiency micromolecule catalytic oxidation with hydrogen production comprises an electrolytic cell (1) and a two-electrode coupling reaction mechanism, wherein the two-electrode coupling reaction mechanism comprises a hydrogen precipitation cathode (2) and a No. I micromolecule oxidation anode (3) which are respectively connected with the anode and the cathode of a No. I external power supply (5);
the method is characterized in that: the device also comprises an oxygen reduction reaction mechanism and a proton exchange membrane (4), wherein the oxygen reduction reaction mechanism comprises an oxygen reduction cathode (6) and a small molecular oxidation anode (7) which are respectively connected with the anode and the cathode of a No. II external power supply (8); the proton exchange membrane (4) is arranged between the hydrogen evolution cathode (2) and the I-type small molecule oxidation anode (3), and divides the interior of the electrolytic cell (1) into a I-type electrolytic area (9) and a II-type electrolytic area (10); the No. I electrolysis area (9) and the No. II electrolysis area (10) are filled with electrolyte.
2. The efficient small-molecule catalytic oxidation and hydrogen production coupled reaction system of claim 1, characterized in that: the electrolyte filled in the No. I electrolysis region (9) is alkaline electrolyte; the electrolyte filled in the No. II electrolysis area (10) is alkaline electrolyte added with biomass micromolecules.
3. The efficient small-molecule catalytic oxidation and hydrogen production coupled reaction system of claim 1, characterized in that: the hydrogen evolution cathode (2) and the oxygen reduction cathode (6) are commercial Pt/C electrodes.
4. The efficient small-molecule catalytic oxidation and hydrogen production coupled reaction system of claim 1, characterized in that: the hydrogen separation cathode (2), the I small molecular oxidation anode (3), the oxygen reduction cathode (6) and the II small molecular oxidation anode (7) are immersed in the electrolyte.
5. The efficient small-molecule catalytic oxidation and hydrogen production coupled reaction system of claim 1, characterized in that: the No. I small molecular oxidation anode (3) and the No. II small molecular oxidation anode (7) are cobalt-iron hydrotalcite nanosheet array electrodes.
CN202110099774.4A 2021-01-25 2021-01-25 Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production Active CN112921341B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110099774.4A CN112921341B (en) 2021-01-25 2021-01-25 Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110099774.4A CN112921341B (en) 2021-01-25 2021-01-25 Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production

Publications (2)

Publication Number Publication Date
CN112921341A true CN112921341A (en) 2021-06-08
CN112921341B CN112921341B (en) 2022-06-21

Family

ID=76167507

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110099774.4A Active CN112921341B (en) 2021-01-25 2021-01-25 Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production

Country Status (1)

Country Link
CN (1) CN112921341B (en)

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040256247A1 (en) * 2001-10-22 2004-12-23 Carson Roger W. Mediated electrochemical oxidation of organic waste materials
JP2005232524A (en) * 2004-02-18 2005-09-02 Ebara Corp Hydrogen production system using solid oxide electrolyte
CN105420748A (en) * 2015-11-18 2016-03-23 复旦大学 Two-step method and device for producing hydrogen through water electrolysis on basis of three-electrode system
CN106676564A (en) * 2017-01-18 2017-05-17 邓渝林 Method and system for preparing hydrogen by electrolyzing biomass directly
US20170145572A1 (en) * 2015-01-08 2017-05-25 Wisconsin Alumni Research Foundation Electrochemical and photoelectrochemical oxidation of 5-hydroxymethylfurfural to 2,5-furandicarboxylic acid and 2,5-diformylfuran
US20180023199A1 (en) * 2016-07-19 2018-01-25 Utah State University Electrocatalytic hydrogen evolution and biomass upgrading
US20190020082A1 (en) * 2017-07-12 2019-01-17 Commissariat A L'energie Atomique Et Aux Energies Alternatives Reversible electrochemical system comprising two pem devices in oxidation and reduction electrodes configuration
CN109778218A (en) * 2019-02-01 2019-05-21 南京大学 A kind of electrochemistry hydrogen manufacturing and the device and method for proposing lithium coproduction
CN110205645A (en) * 2019-04-23 2019-09-06 电子科技大学 5 hydroxymethyl furfural electroxidation is the all-hydrolytic device and reaction method of anode reaction
JP2020021658A (en) * 2018-08-01 2020-02-06 国立研究開発法人産業技術総合研究所 Battery system
WO2020152190A1 (en) * 2019-01-22 2020-07-30 Deutsches Zentrum für Luft- und Raumfahrt e.V. Electrolyser and method for splitting water
US20200270755A1 (en) * 2019-02-22 2020-08-27 New York University Methods and electrochemical cells for redox mediated hydrogen production

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040256247A1 (en) * 2001-10-22 2004-12-23 Carson Roger W. Mediated electrochemical oxidation of organic waste materials
JP2005232524A (en) * 2004-02-18 2005-09-02 Ebara Corp Hydrogen production system using solid oxide electrolyte
US20170145572A1 (en) * 2015-01-08 2017-05-25 Wisconsin Alumni Research Foundation Electrochemical and photoelectrochemical oxidation of 5-hydroxymethylfurfural to 2,5-furandicarboxylic acid and 2,5-diformylfuran
CN105420748A (en) * 2015-11-18 2016-03-23 复旦大学 Two-step method and device for producing hydrogen through water electrolysis on basis of three-electrode system
US20180023199A1 (en) * 2016-07-19 2018-01-25 Utah State University Electrocatalytic hydrogen evolution and biomass upgrading
CN106676564A (en) * 2017-01-18 2017-05-17 邓渝林 Method and system for preparing hydrogen by electrolyzing biomass directly
US20190020082A1 (en) * 2017-07-12 2019-01-17 Commissariat A L'energie Atomique Et Aux Energies Alternatives Reversible electrochemical system comprising two pem devices in oxidation and reduction electrodes configuration
JP2020021658A (en) * 2018-08-01 2020-02-06 国立研究開発法人産業技術総合研究所 Battery system
WO2020152190A1 (en) * 2019-01-22 2020-07-30 Deutsches Zentrum für Luft- und Raumfahrt e.V. Electrolyser and method for splitting water
CN109778218A (en) * 2019-02-01 2019-05-21 南京大学 A kind of electrochemistry hydrogen manufacturing and the device and method for proposing lithium coproduction
US20200270755A1 (en) * 2019-02-22 2020-08-27 New York University Methods and electrochemical cells for redox mediated hydrogen production
CN110205645A (en) * 2019-04-23 2019-09-06 电子科技大学 5 hydroxymethyl furfural electroxidation is the all-hydrolytic device and reaction method of anode reaction

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
YANFEI LI: "TiO2/CuPc/NiFe-LDH photoanode for efficient photoelectrochemical", 《CHINESE CHEMICAL LETTERS》 *
王梦娇: "基于液体催化燃料电池的葡萄糖电解制氢性能分析", 《现代化工》 *

Also Published As

Publication number Publication date
CN112921341B (en) 2022-06-21

Similar Documents

Publication Publication Date Title
Wang et al. Progress in hydrogen production coupled with electrochemical oxidation of small molecules
Li et al. Recent advances on electrolysis for simultaneous generation of valuable chemicals at both anode and cathode
Martínez et al. Paired electrolysis for simultaneous generation of synthetic fuels and chemicals
Yan et al. Innovative electrochemical strategies for hydrogen production: From electricity input to electricity output
CN105420751A (en) Method for preparing hydrocarbon through electrochemical reduction of carbon dioxide
CN106684418A (en) Anolyte, catholyte and biomass fuel cell
Chen et al. Co-electrolysis toward value-added chemicals
CN109576730B (en) Preparation method and application of iron-modified cobaltosic oxide nanosheet array electrode
CN110205645A (en) 5 hydroxymethyl furfural electroxidation is the all-hydrolytic device and reaction method of anode reaction
EP3985145A1 (en) Ferronickel catalytic material, preparation method therefor, and application thereof in preparing hydrogen from electrolyzed water and preparing liquid solar fuel
CN101649465A (en) Method for simultaneously preparing furfuryl alcohol and furoic acid on the basis of bipolar membrane technology
Dolle et al. Electrochemical hydrogen production from biomass
Jiang et al. Electrocatalytic oxidation of 5‐hydroxymethylfurfural for sustainable 2, 5‐furandicarboxylic acid production—From mechanism to catalysts design
Yazdani et al. Perspectives of electrocatalysis in the chemical industry: a platform for energy storage
CN111676484A (en) Method and system for reducing energy consumption, electrolyzing water, producing hydrogen and symbiotically producing value-added chemicals
CN115505945A (en) Process method for co-producing formate by coupling carbon dioxide electroreduction with alcohol oxidation without diaphragm
Liu et al. Energy-efficient monosaccharides electrooxidation coupled with green hydrogen production by bifunctional Co9S8/Ni3S2 electrode
Li et al. Recent advances in paired electrolysis coupling CO2 reduction with alternative oxidation reactions
Chen et al. Coal-assisted water electrolysis for hydrogen production: evolution of carbon structure in different-rank coal
Li et al. Coupled and decoupled electrochemical water splitting for boosting hydrogen evolution: A review and perspective
Li et al. Recent advances in hybrid water electrolysis for energy-saving hydrogen production
Gong et al. Paired electrosynthesis design strategy for sustainable CO2 conversion and product upgrading
CN112921341B (en) Efficient reaction system for coupling small molecular catalytic oxidation and hydrogen production
Meng et al. Electrocatalytic oxidation of biomass-derived 5-hydroxymethylfurfural to 2, 5-furandicarboxylic acid coupled with H2 evolution
CN114592204A (en) Device and method for electrooxidation of furfural and 5-hydroxymethylfurfural

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