CN110512224A - A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously - Google Patents

A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously Download PDF

Info

Publication number
CN110512224A
CN110512224A CN201910812985.0A CN201910812985A CN110512224A CN 110512224 A CN110512224 A CN 110512224A CN 201910812985 A CN201910812985 A CN 201910812985A CN 110512224 A CN110512224 A CN 110512224A
Authority
CN
China
Prior art keywords
nitrogen
mof
fixed nitrogen
carbon cloth
ammonification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910812985.0A
Other languages
Chinese (zh)
Inventor
赵璐
王志玲
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.)
University of Jinan
Original Assignee
University of Jinan
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 University of Jinan filed Critical University of Jinan
Priority to CN201910812985.0A priority Critical patent/CN110512224A/en
Publication of CN110512224A publication Critical patent/CN110512224A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/1691Coordination polymers, e.g. metal-organic frameworks [MOF]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22Organic complexes
    • B01J31/2204Organic complexes the ligands containing oxygen or sulfur as complexing atoms
    • B01J31/2208Oxygen, e.g. acetylacetonates
    • B01J31/2226Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
    • B01J31/223At least two oxygen atoms present in one at least bidentate or bridging ligand
    • B01J31/2239Bridging ligands, e.g. OAc in Cr2(OAc)4, Pt4(OAc)8 or dicarboxylate ligands
    • 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
    • B01J35/33Electric or magnetic properties
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • 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
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/02Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
    • C25B11/03Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
    • C25B11/031Porous electrodes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/055Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material
    • C25B11/057Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material consisting of a single element or compound
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • C25B11/091Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/10Complexes comprising metals of Group I (IA or IB) as the central metal
    • B01J2531/16Copper

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses a kind of methods that chemical oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously, belong to electrochemical catalysis technical field.It has main steps that using potentiostatic electrodeposition technology, and the Cu-MOF composite catalyst being supported on carbon cloth is made;It is electrolyte by urea-containing KOH solution, is passed through without nitrogen, under permanent oxidizing potential, catalyzing urea is oxidized to nitrogen and restores fixed nitrogen ammonification simultaneously, and this method is convenient and simple for operation, and catalyst has good electro catalytic activity and electrochemical stability.This method can not only solve in environment urea pollution problem green is clean again to be prepared for ammonia, energy consumption of reaction is low, with prospects for commercial application using being electrolyte containing urea wastewater.

Description

A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously
Technical field
The present invention relates to a kind of methods that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously, belong to nano material, electricity Chemical catalysis technical field.
Background technique
From start for the first time twenty years ago electrochemistry nitrogen reduction (NRR) prepare ammonia since, ever-increasing ecological requirements and it Mild reaction conditions make it more more attractive than traditional Haber-Bosch method.NRR is to utilize nitrogen and H2O conduct Nitrogen and hydrogen source control voltage by electro-catalysis under the conditions of environment reaction and complete the reaction that nitrogen is restored to ammonia.Although NRR is grasped Make convenient and abundant raw material, but since tri- key of N ≡ N strong between nitrogen-atoms, kinetics and its reaction efficiency are up for improving. In recent years, researcher develops many approach for improving NRR, such as by ionic liquid as electrolyte progress NRR and benefit With the catalyst with high catalytic efficiency such as Ru, Au and high Lacking oxygen material etc..These methods exist catalyst it is at high cost and Inefficient bottleneck problem, therefore, seeking can be improved nitrogen-fixing efficiency and low-cost method is of great significance.
To reduce cost, exploitation non-precious metal catalyst be numerous researchers frequently with approach.Using oxidizable Waste water solution does electrolyte solution, it generates the nitrogen source that nitrogen is reacted as NRR to electrochemical oxidation, and reduce simultaneously electrolyte at Up to the present this strategy has no research achievement as far as we know.Therefore we have developed a kind of electrochemistry fixed nitrogen newly to think Road makes its selfdecomposition generate nitrogen, not only can achieve the purpose of processing sewage, but also can be with fixed nitrogen, In using certain predetermined substance Solve the reduction that nitrogen is completed while nitrogen pollution problem in environment.In the same electrolytic cell, it is anti-that fixed nitrogen belongs to reduction It answers, belongs to competitive relation with evolving hydrogen reaction, however the two complements each other again, we aoxidize the electron-transport efficiency at end by improving The efficiency of reduction reaction entirety is improved, NRR and HER can be correspondingly improved.In numerous catalyst, have for metal- The research of machine framework material (Metal-OrganicFrameworks, MOFs) is more and more extensive and gos deep into.MOFs refers to transition gold Belong to ion and organic ligand passes through the crystalline porous material with periodic network structure being self-assembly of.It has high hole Rate, low-density, bigger serface, duct rule, aperture is adjustable and topological structure diversity and the advantages that Scalability, so that MOFs has been widely used in fields such as gas storage, separation, catalysis, identification and drug deliveries.
Summary of the invention
Technical assignment of the invention first is that in order to make up for the deficiencies of the prior art, provide a kind of electrochemistry oxygen metaplasia nitrogen simultaneously The method for restoring fixed nitrogen ammonification simultaneously, this method is raw materials used at low cost, and preparation process is simple, and energy consumption of reaction is low, the catalyst With good electro catalytic activity and electrochemical stability, there is prospects for commercial application.
To achieve the above object, electrochemistry oxygen metaplasia nitrogen of the present invention simultaneously restores the technical solution of fixed nitrogen ammonification use such as simultaneously Under:
(1) Cu-MOF/CC composite catalyst is prepared
By 0.30-0.50 g H4L powder and 0.10-0.30 g copper nitrate are dissolved in 4-6 mL n,N-Dimethylformamide, are dripped After adding 60-100 μ L water, 180 W ultrasounds 1-3 minutes obtain green clear solution, and the nitre that 90-110 μ L mass fraction is 68% is added dropwise Acid is stirred until homogeneous, and obtains copper ion and H4The mixed solution of L;
Using this mixed solution as electrolyte, using three-electrode electro Chemical work station, by the activated cm carbon cloth of 0.5 cm × 2 CC As working electrode, platinized platinum is to electrode, and calomel electrode is reference electrode, is supported on using the synthesis of constant potential electrochemical deposition method Cu-MOF composite material on carbon cloth CC;Obtained composite material is activated to constant weight in 85 DEG C, it is compound that Cu-MOF/CC is made Catalyst;
The H4L, structural formula are as follows:
The activation carbon cloth is successively to remove carbon cloth in acetone, dehydrated alcohol and distillation underwater ultrasound 2-4min, washing Surface irregularities, then carbon cloth is immersed in the nitric acid ultrasound 1-3min that mass fraction is 40 %, it is washed with water to wash and is made three times.
The Cu-MOF, basic structural unit are [Cu24L12(H2O)12]·30DMF·14H2O, DMF N, N- diformazan Base formamide;A structural unit of Cu-MOF is by 24 Cu2+, 12 L4-, 12 main body hydrones, 30 object DMF molecules It is formed with 14 object hydrones;The L4-, structural formula is as follows:
The H4L is the ligand of Cu-MOF preparation, and preparation step is as follows:
By 0.02 mol amino isophthalic acid, 0.03 mol NaOH and 5 mol NaHCO3It is added in 60 ml distilled water, 30 min are stirred after mixing at room temperature;The 1,4- dioxane solution of cyanuric trichloride is added dropwise dropwise simultaneously;The mixed liquor is at 110 DEG C 12 h of lower heating adjust the pH=2 of mixture solution with HCl, and filtering is washed with distilled water several times, obtain after drying at room temperature H4L ligand, yield are 81.3 %.
Isosorbide-5-Nitrae-dioxane solution of the cyanuric trichloride is the Isosorbide-5-Nitrae-that the cyanuric trichloride of 0.01 mol is dissolved in 10 mL Six alkane of dioxy is made.
The Cu-MOF/CC composite catalyst is the composite material that nanometer stick array is supported on activation carbon cloth, nanometer rods Shape crystal is formed along the longitudinal arrangement, and nano-micrometre is porous high-visible between crystal, and it is compound to belong to self-supporting integration nanometer three-dimensional Material.
The constant potential electrochemical deposition method, current potential are -1.6~-2.0V, and sedimentation time is 5-15 min.
(2) electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously
By 80 mL, 0.50 molL containing urea-10.5 molL-1KOH solution as electrolyte, electrochemical workstation Working electrode connects a Cu-MOF/CC composite catalyst, and being connected to electrode and reference electrode for electrochemical workstation is another A Cu-MOF/CC composite catalyst, two composite catalysts are immersed in same electrolyte, are passed through without nitrogen, utilize perseverance 0.5 V method of current potential, the raw nitrogen of electrochemical oxidation urea simultaneously restore fixed nitrogen ammonification simultaneously.
(3) electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification performance simultaneously
Above-mentioned electrochemistry oxygen metaplasia nitrogen and the method for restoring fixed nitrogen ammonification simultaneously, ammonia yield are 63-77 μ g h-1 mgcat -1, Faradic efficiency is 12-14%, and after the stability test for having carried out 12 h, ammonia yield is still able to maintain the water being basically unchanged It is flat, illustrate that this method can be realized without the efficient generation nitrogen fixed nitrogen certainly under additional condition of nitrogen gas, and have good stability.
The fixed nitrogen ammonification, yield test method are as follows:
1) standard curve is drawn
With 0.1 M PBS buffer solution of ammonium chloride and pH=7, the NH of series of concentrations is prepared4 +Standard solution;
2mL series standard solution is pipetted, sequentially adds that 2 mL concentration are the NaOH solution of 1.0 M, 1 mL concentration is 0.05 M NaClO solution, the sodium nitroprusside solution that 0.2 mL mass fraction is 1%, quickly shake up, 25 DEG C of 2 h of placement, with UV- Vis spectrophotometer detects the absorbance peak at the 655 nm wavelength of solution, and it is bent to draw absorbance-concentration, that is, A-c standard Line obtains calibration curve equation;
The NaOH solution of 1.0 M is 5% salicylic acid and 5% sodium citrate containing mass fraction;
2) fixed nitrogen ammonification calculation of yield
Measure NH in reaction solution4 +Concentration, pipette the reaction solution of 2 h of 2mL catalysis reaction, the 2mL standard in alternative steps (2) Solution calculates the yield of ammonia according to calibration curve equation.
Beneficial technical effect of the invention:
1. a kind of electrochemistry oxygen metaplasia nitrogen produced by the present invention and the method for restoring fixed nitrogen ammonification simultaneously, this method, which can be used, to be contained Urea industry waste liquid aoxidizes under constant potential as electrolyte, because of the nitrogen that urea oxidation generates, is urging with the water in electrolyte It is synchronized under the conditions of change and is reduced to ammonia, the method had not only handled urea pollution problem in environment but also had been the clean production ammonia of green Provide new direction.
2. the present invention is method, raw materials used at low cost, preparation process is simple, and energy consumption of reaction is low, before having industrial application Scape.
3. Cu-MOF/CC composite catalyst produced by the present invention, Cu-MOF therein refer to transition metal Cu2+With it is organic Ligand H4L passes through the crystalline porous material with periodic network structure that is self-assembly of, it is with high porosity, low close Degree, bigger serface, duct rule, aperture is adjustable and topological structure diversity and the advantages that Scalability.Cu-MOF/CC is multiple Closing catalyst is the composite material that nanometer stick array is supported on activation carbon cloth, and nanoclub-like crystal is formed along the longitudinal arrangement, brilliant Nano-micrometre is porous high-visible between body, belongs to self-supporting integration nanometer three-dimensional composite material.The structure exposes more Active site, collaboration enhance conductive and catalytic performance, high catalytic efficiency.Because of the weak acid (- OH) and weak base (pyrrole contained in ligand Pyridine N, imido grpup N) special soda acid buffering to structure, enables fixed nitrogen process high stability to carry out.
4. two reactions of catalysis fixed nitrogen and oxidation occurred present invention uses an electrolytic cell, it is anti-that fixed nitrogen belongs to reduction It answers, complements each other with urea oxidation reaction, the electron-transport efficiency for improving oxidation end, Lai Tigao fixed nitrogen are aoxidized by catalyzing urea The efficiency of reduction reaction entirety has prior meaning.
Specific embodiment
The present invention will be further described below with reference to examples, but protection scope of the present invention is not only limited to implement Example, professionals in the field change to made by technical solution of the present invention, are within the scope of protection of the invention interior.
1 H of embodiment4The preparation method of L ligand
By 0.02 mol amino isophthalic acid, 0.03 mol NaOH and 5 mol NaHCO3It is added in 60 ml distilled water, 30 min are stirred after mixing at room temperature;The 1,4- dioxane solution of cyanuric trichloride is added dropwise dropwise simultaneously;The mixed liquor is at 110 DEG C 12 h of lower heating adjust the pH=2 of mixture solution with HCl, and filtering is washed with distilled water several times, obtain after drying at room temperature H4L ligand, yield are 81.3 %.
Isosorbide-5-Nitrae-dioxane solution of the cyanuric trichloride is the Isosorbide-5-Nitrae-that the cyanuric trichloride of 0.01 mol is dissolved in 10 mL Six alkane of dioxy is made.
A kind of preparation method of the Cu-MOF/CC composite catalyst of embodiment 2
By 0.30 g H4L powder and 0.10 g copper nitrate are dissolved in 4 mL n,N-Dimethylformamide, after 60 μ L water are added dropwise, 180 W ultrasound obtains green clear solution in 1 minute, and the nitric acid that 90 μ L mass fractions are 68% is added dropwise, is stirred until homogeneous, obtains copper ion And H4The mixed solution of L;
Using this mixed solution as electrolyte, using three-electrode electro Chemical work station, by the activated cm carbon cloth of 0.5 cm × 2 CC As working electrode, platinized platinum is to electrode, and calomel electrode is reference electrode, is supported on using the synthesis of constant potential electrochemical deposition method Cu-MOF composite material on carbon cloth CC;Obtained composite material is activated to constant weight in 85 DEG C, it is compound that Cu-MOF/CC is made Catalyst;
The H4L, structural formula are as follows:
The activation carbon cloth is by carbon cloth successively in acetone, dehydrated alcohol and distillation underwater ultrasound 2min, and it is miscellaneous that washing removes surface Object, then carbon cloth is immersed in nitric acid 1 min of ultrasound that mass fraction is 40 %, it is washed with water to wash and is made three times;
The Cu-MOF, basic structural unit are [Cu24L12(H2O)12]·30DMF·14H2O, DMF N, N- dimethyl methyl Amide;A structural unit of Cu-MOF is by 24 Cu2+, 12 L4-, 12 main body hydrones, 30 object DMF molecules and 14 A object hydrone composition;The L4-, structural formula is as follows:
The Cu-MOF/CC composite catalyst, is the composite material that nanometer stick array is supported on activation carbon cloth, and nano bar-shape is brilliant Body is formed along the longitudinal arrangement, and nano-micrometre is porous high-visible between crystal, belongs to self-supporting integration nanometer three-dimensional composite wood Material;
The constant potential electrochemical deposition method, current potential are -1.6V, and sedimentation time is 15 min.
A kind of preparation method of the Cu-MOF/CC composite catalyst of embodiment 2
By 0.40 g H4L powder and 0.20 g copper nitrate are dissolved in 5 mL n,N-Dimethylformamide, after 80 μ L water are added dropwise, 180 W ultrasound 2 minutes green clear solution, be added dropwise 100 μ L mass fractions be 68% nitric acid, be stirred until homogeneous, obtain copper from Son and H4The mixed solution of L;
Using this mixed solution as electrolyte, using three-electrode electro Chemical work station, by the activated cm carbon cloth of 0.5 cm × 2 CC As working electrode, platinized platinum is to electrode, and calomel electrode is reference electrode, is supported on using the synthesis of constant potential electrochemical deposition method Cu-MOF composite material on carbon cloth CC;Obtained composite material is activated to constant weight in 85 DEG C, it is compound that Cu-MOF/CC is made Catalyst;
The H4L, structural formula is the same as embodiment 2;
The activation carbon cloth is that carbon cloth is successively removed surface in acetone, dehydrated alcohol and distillation 3 min of underwater ultrasound, washing Sundries, then carbon cloth is immersed in nitric acid 2 min of ultrasound that mass fraction is 40 %, it is washed with water to wash and is made three times;
The Cu-MOF, basic structural unit and composition are the same as embodiment 2;
The L4-, structural formula is the same as embodiment 2;
The Cu-MOF/CC composite catalyst, structure is the same as embodiment 2;
The constant potential electrochemical deposition method, current potential are -1.8V, and sedimentation time is 10 min.
A kind of preparation method of the Cu-MOF/CC composite catalyst of embodiment 4
By 0.50 g H4L powder and 0.30 g copper nitrate are dissolved in 6 mL n,N-Dimethylformamide, after 100 μ L water are added dropwise, 180 W ultrasound 3 minutes green clear solution, be added dropwise 110 μ L mass fractions be 68% nitric acid, be stirred until homogeneous, obtain copper from Son and H4The mixed solution of L;
Using this mixed solution as electrolyte, using three-electrode electro Chemical work station, by the activated cm carbon cloth of 0.5 cm × 2 CC As working electrode, platinized platinum is to electrode, and calomel electrode is reference electrode, is supported on using the synthesis of constant potential electrochemical deposition method Cu-MOF composite material on carbon cloth CC;Obtained composite material is activated to constant weight in 85 DEG C, it is compound that Cu-MOF/CC is made Catalyst;
The H4L, structural formula is the same as embodiment 2;
The activation carbon cloth is by carbon cloth successively in acetone, dehydrated alcohol and distillation underwater ultrasound 4min, and it is miscellaneous that washing removes surface Object, then carbon cloth is immersed in the nitric acid ultrasound 3min that mass fraction is 40 %, it is washed with water to wash and is made three times;
The Cu-MOF, basic structural unit and composition are the same as embodiment 2;
The L4-, structural formula is the same as embodiment 2;
The Cu-MOF/CC composite catalyst, structure is the same as embodiment 2;The constant potential electrochemical deposition method, current potential be- 2.0V, sedimentation time are 5 min.
5 electrochemistry oxygen metaplasia nitrogen of embodiment simultaneously restores fixed nitrogen ammonification simultaneously
By 70 mL 0.42-0.55 containing urea molL-10.5 molL-1KOH solution is as electrolyte, electrochemical operation The working electrode stood connects a Cu-MOF/CC composite catalyst, and electrochemical workstation is connected to electrode and reference electrode Another Cu-MOF/CC composite catalyst, two composite catalysts are immersed in same electrolyte, are passed through without nitrogen, benefit With constant potential 0.4-0.6 V method, the raw nitrogen of electrochemical oxidation urea simultaneously restores fixed nitrogen ammonification simultaneously.
(3) electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification performance simultaneously
Above-mentioned electrochemistry oxygen metaplasia nitrogen and the method for restoring fixed nitrogen ammonification simultaneously, under the oxidation constant potential of 0.4-0.6 V, ammonia Yield is 63-77 μ g h-1 mgcat -1, faradic efficiency 12-14%, and after the stability test for carrying out 12h, ammonia Yield is still able to maintain the level being basically unchanged, and illustrates that this method can be realized without solid efficiently from nitrogen is generated under additional condition of nitrogen gas Nitrogen, and have good stability.
6 electrochemistry oxygen metaplasia nitrogen of embodiment and the method for restoring fixed nitrogen ammonification simultaneously
By 80 mL, 0.50 molL containing urea-10.5 molL-1KOH solution as electrolyte, electrochemical workstation Working electrode connects a Cu-MOF/CC composite catalyst, and being connected to electrode and reference electrode for electrochemical workstation is another A Cu-MOF/CC composite catalyst, two composite catalysts are immersed in same electrolyte, are passed through without nitrogen, utilize perseverance 0.5 V method of current potential, the raw nitrogen of electrochemical oxidation urea simultaneously restore fixed nitrogen ammonification simultaneously;
Cu-MOF/CC composite catalyst made from embodiment 1, ammonia yield are 63 μ g h-1 mgcat -1, faradic efficiency is 12%, and after the stability test for carrying out 12h, ammonia yield is still able to maintain the level being basically unchanged, and illustrates that this method can be real Now without the efficient generation nitrogen fixed nitrogen certainly under additional condition of nitrogen gas, and have good stability;
Cu-MOF/CC composite catalyst made from embodiment 2, ammonia yield are 77 μ g h-1 mgcat -1, faradic efficiency is 17%, and after the stability test for carrying out 12h, ammonia yield is still able to maintain the level being basically unchanged, and illustrates that this method can be real Now without the efficient generation nitrogen fixed nitrogen certainly under additional condition of nitrogen gas, and have good stability;
Cu-MOF/CC composite catalyst made from embodiment 3, ammonia yield are 70 μ g h-1 mgcat -1, faradic efficiency is 13%, and after the stability test for carrying out 12h, ammonia yield is still able to maintain the level being basically unchanged, and illustrates that this method can be real Now without the efficient generation nitrogen fixed nitrogen certainly under additional condition of nitrogen gas, and have good stability.
Fixed nitrogen ammonification described in 7 embodiment 6 of embodiment, yield performance test methods
(1) standard curve is drawn
With 0.1 M PBS buffer solution of ammonium chloride and pH=7, the NH of series of concentrations is prepared4 +Standard solution;
2mL series standard solution is pipetted, sequentially adds that 2 mL concentration are the NaOH solution of 1.0 M, 1 mL concentration is 0.05 M NaClO solution, the sodium nitroprusside solution that 0.2 mL mass fraction is 1%, quickly shake up, 25 DEG C of 2 h of placement, with UV- Vis spectrophotometer detects the absorbance peak at the 655 nm wavelength of solution, and it is bent to draw absorbance-concentration, that is, A-c standard Line obtains calibration curve equation;
The NaOH solution of 1.0 M is 5% salicylic acid and 5% sodium citrate containing mass fraction;
(2) fixed nitrogen ammonification calculation of yield
Measure NH in reaction solution4 +Concentration, pipette the reaction solution of 2 h of 2mL catalysis reaction, the 2mL standard in alternative steps (2) Solution calculates the yield of ammonia according to calibration curve equation.

Claims (5)

1. a kind of electrochemistry oxygen metaplasia nitrogen and the method for restoring fixed nitrogen ammonification simultaneously, which is characterized in that steps are as follows:
(1) Cu-MOF/CC composite catalyst is prepared
By 0.30-0.50 g H4L powder and 0.10-0.30 g copper nitrate are dissolved in 4-6 mL n,N-Dimethylformamide, are added dropwise After 60-100 μ L water, 180 W ultrasounds 1-3 minutes obtain green clear solution, and the nitre that 90-110 μ L mass fraction is 68% is added dropwise Acid is stirred until homogeneous, and obtains copper ion and H4The mixed solution of L;
Using this mixed solution as electrolyte, using three-electrode electro Chemical work station, by the activated cm carbon cloth of 0.5 cm × 2 CC As working electrode, platinized platinum is to electrode, and calomel electrode is reference electrode, is supported on using the synthesis of constant potential electrochemical deposition method Cu-MOF composite material on carbon cloth CC;Obtained composite material is activated to constant weight in 85 DEG C, it is compound that Cu-MOF/CC is made Catalyst;
(2) electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously
By 70-90 mL 0.42-0.55 containing urea molL-10.5 molL-1KOH solution is as electrolyte, electrochemistry work Make the working electrode stood and connect a Cu-MOF/CC composite catalyst, electrochemical workstation connects electrode with reference electrode In another Cu-MOF/CC composite catalyst, two composite catalysts are immersed in same electrolyte, are passed through without nitrogen, Using constant potential 0.4-0.6 V method, the raw nitrogen of electrochemical oxidation urea simultaneously restores fixed nitrogen ammonification simultaneously.
2. a kind of electrochemistry oxygen metaplasia nitrogen as described in claim 1 and the method for restoring fixed nitrogen ammonification simultaneously, which is characterized in that The H4L, structural formula are as follows:
3. a kind of electrochemistry oxygen metaplasia nitrogen as described in claim 1 and the method for restoring fixed nitrogen ammonification simultaneously, which is characterized in that The activation carbon cloth is by carbon cloth successively in acetone, dehydrated alcohol and distillation underwater ultrasound 2-4min, and it is miscellaneous that washing removes surface Object, then carbon cloth is immersed in the nitric acid ultrasound 1-3min that mass fraction is 40 %, it is washed with water to wash and is made three times.
4. a kind of electrochemistry oxygen metaplasia nitrogen as described in claim 1 and the method for restoring fixed nitrogen ammonification simultaneously, which is characterized in that The Cu-MOF, basic structural unit are [Cu24L12(H2O)12]·30DMF·14H2O, DMF are n,N-Dimethylformamide; A structural unit of Cu-MOF is by 24 Cu2+, 12 L4-, 12 main body hydrone, 30 object DMF molecules and 14 visitors Body hydrone composition;The L4-, structural formula is as follows:
5. a kind of electrochemistry oxygen metaplasia nitrogen as described in claim 1 and the method for restoring fixed nitrogen ammonification simultaneously, which is characterized in that The constant potential electrochemical deposition method, current potential are -1.6~-2.0V, and sedimentation time is 5-15 min.
CN201910812985.0A 2019-08-30 2019-08-30 A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously Pending CN110512224A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910812985.0A CN110512224A (en) 2019-08-30 2019-08-30 A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910812985.0A CN110512224A (en) 2019-08-30 2019-08-30 A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously

Publications (1)

Publication Number Publication Date
CN110512224A true CN110512224A (en) 2019-11-29

Family

ID=68629348

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910812985.0A Pending CN110512224A (en) 2019-08-30 2019-08-30 A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously

Country Status (1)

Country Link
CN (1) CN110512224A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270254A (en) * 2020-03-12 2020-06-12 济南大学 Method for promoting room-temperature nitrogen reduction by Cu/Ca-MOF nano composite catalyst
CN111330645A (en) * 2020-03-12 2020-06-26 济南大学 Preparation method and application of bifunctional MOF (metal organic framework) nano catalyst for degrading p-nitrophenol and fixing nitrogen at room temperature simultaneously
CN112226781A (en) * 2020-09-30 2021-01-15 湖南大学 Device and method for generating ammonia gas from nitrogen
CN116315065A (en) * 2023-02-20 2023-06-23 安徽瑞柏新材料有限公司 Preparation method of electrolyte and application of electrolyte in lithium ion battery

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090095636A1 (en) * 2007-10-15 2009-04-16 Ohio University Electrolytic Cells and Methods for the Production of Ammonia and Hydrogen
CN103201411A (en) * 2010-08-23 2013-07-10 俄亥俄州立大学 Selective catalytic reducton via electrolysis of urea
CN108970640A (en) * 2018-08-29 2018-12-11 济南大学 A kind of Metal-organic frame method for preparing catalyst having acid complete solution water function and application
CN109759136A (en) * 2019-02-12 2019-05-17 济南大学 A kind of preparation method and application of Cu-MOF nano-array composite catalyst

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090095636A1 (en) * 2007-10-15 2009-04-16 Ohio University Electrolytic Cells and Methods for the Production of Ammonia and Hydrogen
CN103201411A (en) * 2010-08-23 2013-07-10 俄亥俄州立大学 Selective catalytic reducton via electrolysis of urea
CN108970640A (en) * 2018-08-29 2018-12-11 济南大学 A kind of Metal-organic frame method for preparing catalyst having acid complete solution water function and application
CN109759136A (en) * 2019-02-12 2019-05-17 济南大学 A kind of preparation method and application of Cu-MOF nano-array composite catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
FEI LU AND GERARDINE G. BOTTE1: "Understanding the Electrochemically Induced Conversion of Urea to Ammonia Using Nickel Based Catalysts", 《ELECTROCHIMICA ACTA》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270254A (en) * 2020-03-12 2020-06-12 济南大学 Method for promoting room-temperature nitrogen reduction by Cu/Ca-MOF nano composite catalyst
CN111330645A (en) * 2020-03-12 2020-06-26 济南大学 Preparation method and application of bifunctional MOF (metal organic framework) nano catalyst for degrading p-nitrophenol and fixing nitrogen at room temperature simultaneously
CN111270254B (en) * 2020-03-12 2022-03-11 济南大学 Method for promoting room-temperature nitrogen reduction by Cu/Ca-MOF nano composite catalyst
CN112226781A (en) * 2020-09-30 2021-01-15 湖南大学 Device and method for generating ammonia gas from nitrogen
CN116315065A (en) * 2023-02-20 2023-06-23 安徽瑞柏新材料有限公司 Preparation method of electrolyte and application of electrolyte in lithium ion battery
CN116315065B (en) * 2023-02-20 2023-10-03 安徽瑞柏新材料有限公司 Preparation method of electrolyte and application of electrolyte in lithium ion battery

Similar Documents

Publication Publication Date Title
CN110512224A (en) A kind of method that electrochemistry oxygen metaplasia nitrogen simultaneously restores fixed nitrogen ammonification simultaneously
Du et al. Hybrid water electrolysis: Replacing oxygen evolution reaction for energy-efficient hydrogen production and beyond
Mansingh et al. Cerium-based metal–organic framework nanorods nucleated on CeO2 nanosheets for photocatalytic N2 fixation and water oxidation
CN104549242B (en) Preparation method of nanometer palladium-graphene three-dimensional porous composite electrocatalyst
CN109759143B (en) Co3O4Preparation method and application of NP/CD/Co-MOF composite material
CN109692711A (en) A kind of CeO2And Co3O4The preparation method and application of hydridization Ce-MOF/Co-MOF composite catalyst
CN107829107A (en) A kind of graphene/carbon nano-tube load single dispersion metal atomic composite catalyst and its preparation method and application
CN112206830B (en) CuPc@Ti 3 C 2 T x MXene catalytic material, electrode and application thereof in nitrate radical reduction
CN111359603A (en) Bismuth-based self-supporting electrocatalyst, preparation method thereof and application of bismuth-based self-supporting electrocatalyst in ammonia production by nitrogen reduction
CN112430830B (en) Preparation method and application of electrocatalytic reduction carbon dioxide electrode
CN109759136B (en) Preparation method and application of Cu-MOF nano-array composite catalyst
CN109675639A (en) A kind of preparation method and application of Ni-MOF/NiF bifunctional catalyst that is while preparing hydrogen and glucaric acid
CN109321933A (en) A kind of preparation method and application of MOF/ carbon dots nanocomposite catalyst
CN112206797B (en) Cu(I)@Ti 3 C 2 T x MXene catalytic material, electrode and application thereof in nitrate radical reduction
CN113416316B (en) MOFs-zinc material and preparation method and application thereof
CN105322183B (en) A kind of preparation method of Carbon dioxide electrochemical reduction reaction electrode
CN116670329A (en) Plasma-assisted electrocatalytic conversion
Li et al. Fundamentals and advances in emerging crystalline porous materials for photocatalytic and electrocatalytic nitrogen fixation
CN104801341B (en) A kind of electrochemistry formated catalyst Cu3(BTC)2Method and its NH3SCR is applied
CN109331884B (en) Composite hydrogen production catalyst and preparation method and application thereof
CN103977835A (en) Sulfonated-graphene-based novel Ru(bpy)3<2+> nano heterogeneous catalyst and preparation method thereof
CN106064097A (en) A kind of room temperature synthetic ammonia catalyst and preparation method thereof
CN110368981A (en) A kind of preparation method and application derived from ammonium molybdate doping ZIF-67/ chitosan composite catalyst
CN110038637A (en) Preparation method and application of ternary nanocomposite
CN110965071A (en) Metal catalyst for electrochemical reduction of carbon dioxide and preparation 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
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20191129