CN110237860A - A kind of electrolysis water and electrolysis urea anode catalyst and preparation method thereof - Google Patents

A kind of electrolysis water and electrolysis urea anode catalyst and preparation method thereof Download PDF

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Publication number
CN110237860A
CN110237860A CN201910575353.7A CN201910575353A CN110237860A CN 110237860 A CN110237860 A CN 110237860A CN 201910575353 A CN201910575353 A CN 201910575353A CN 110237860 A CN110237860 A CN 110237860A
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electrolysis
pba
urea
cube
anode catalyst
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CN110237860B (en
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冯永强
王潇
董沛沛
黄剑锋
曹丽云
王琳琳
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Shaanxi University of Science and Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/18Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
    • B01J31/1805Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
    • 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
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • 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
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0018Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • B01J37/10Heat treatment in the presence of water, e.g. steam
    • 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
    • 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
    • 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
    • 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
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    • 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

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Abstract

The present invention discloses a kind of electrolysis water and electrolysis urea anode catalyst and preparation method thereof, synthesizes PBA cube using the precipitation method;Using hydro-thermal method, PBA cube is performed etching using dehydrated alcohol, finally obtains hollow PBA cube, as electrolysis water and electrolysis urea anode catalyst;Preparation method reaction of the invention is heated evenly, easy to control, and institute is low using cost of material, be easy to get to target product, operation is simple, and the pattern of the PBA of gained hollow structure is good, easy-regulating, with excellent electrolysis water OER performance and electrolysis urea UOR performance.

Description

A kind of electrolysis water and electrolysis urea anode catalyst and preparation method thereof
Technical field
The present invention relates to electro-catalysis fields, and in particular to a kind of electrolysis water and electrolysis urea anode catalyst and its preparation Method.
Background technique
Prussian blue similar object (Prussian Blue Analogue, abbreviation PBA), is typical face-centred cubic structure Crystal, the exemplary porous multifunctional material being made of metal center/cluster that functional organic ligand connects have redox Property, high surface area and uniform porosity special performance, be applied to catalysis, sensor, battery electrode material and store ion etc. Field receives more and more attention in recent years.The synthetic method of PBA has electrochemical deposition method and chemical synthesis.
Electrochemical energy storage and conversion art, higher specific surface area can provide more electro-chemical activity sites with And the bigger contact area with electrolyte;It is more thin while that there is infiltrative shell structurre greatly to accelerate electronics and ion Transmission;Hollow structure inside can effectively alleviate ion circulation shuttle bring volume expansion problem etc..PBA nanometers will be improved The inherent characteristic of material and its new function is further assigned, so that it is shown the anode of electrolytic water of enhancing reaction (OER) living Property and electrolysis urea anode reaction (UOR) excellent stability.
Summary of the invention
It is obtained it is an object of that present invention to provide a kind of electrolysis water and electrolysis urea anode catalyst and preparation method thereof Catalyst is hollow nanocube structure, with excellent electro catalytic activity and electrolysis urea anode reaction stability.
To achieve the above object, the technical solution adopted by the present invention is that:
A kind of preparation method of electrolysis water and electrolysis urea anode catalyst, comprising the following steps:
S1, PBA cube is synthesized using the precipitation method;
S2, using hydro-thermal method, PBA cube is performed etching using dehydrated alcohol, finally obtains hollow PBA cube, As electrolysis water and electrolysis urea anode catalyst.
Further, the step S1 includes:
S11,0.5-1mmol cobalt metal salt and the dissolution of 0.5-2mmol sodium citrate dehydrate are weighed in deionized water, stirred It mixes and uniformly obtains mixed solution;
S12, certain density metal cyanide aqueous solutions of potassium is added in the stirring of above-mentioned mixed solution side, continues to stir 5min, 20-48h is stood, product is centrifuged, washed, be dried in vacuo with deionized water and dehydrated alcohol, obtains PBA cube.
Further, the step S2 includes: to weigh a certain amount of PBA cube, is dispersed in dehydrated alcohol, then even It pours into the PVP ethanol solution of 100-500mg/ml and stirs evenly under continuous stirring, mixed solution is transferred in water heating kettle, 6-48h is reacted at 160-200 DEG C, is centrifuged after being cooled to room temperature, washed, be dried in vacuo with deionized water and dehydrated alcohol, obtained To hollow PBA cube.
Further, the cobalt metal salt is one or more of nitrate, sulfate, acetate, chloride.
Electrolysis water and electrolysis urea anode catalyst, are hollow nanocube structure.
Compared with prior art, the invention has the following beneficial technical effects:
Preparation method reaction of the invention is heated evenly, easy to control, institute is low using cost of material, be easy to get to target product, Operation is simple, and the pattern of the PBA of gained hollow structure is good, easy-regulating, produces oxygen performance with excellent electro-catalysis, and opposite In the hollow cube PBA that the PBA cube nano material not being etched, the present invention are acted on by the chemical etching of ethyl alcohol With bigger specific surface area and the more active sites of exposure, therefore with more excellent electro catalytic activity and excellent Electrolysis water OER, electrolysis urea UOR performance.
The present invention carries out chemical etching to PBA cube structure using hydro-thermal method, becomes receiving with hollow structure Rice cube structure, the uneven surface reactivity of solid PBA nanocube be the main reason for forming hollow structure, Etching on PBA cube preferentially occurs in apex, and etch-rate is gradually accelerated along the body diagonal direction of cube, Hollow nanocube structure is ultimately formed, the advantage of the structure and function of PBA material is maximized, it is organic to extend metal Application of the skeleton in terms of being electrolysed urea.
Detailed description of the invention
Fig. 1 is the XRD diagram for the CoFe-PBA that embodiment 1 is prepared;
The SEM figure that Fig. 2 is the CoFe-PBA that embodiment 1 is prepared;
Fig. 3 is the SEM phenogram for the Hollow CoFe-PBA that embodiment 1 is prepared;
Fig. 4 is the TEM phenogram for the Hollow CoFe-PBA that embodiment 1 is prepared;
Fig. 5 is CoFe-PBA the and Hollow CoFe-PBA that is prepared of embodiment 1 in the KOH electrolyte of 1M LSV curve graph;
Fig. 6 is KOH and 0.5M urea electricity of the CoFe-PBA and Hollow CoFe-PBA that is prepared of embodiment 1 in 1M Solve the LSV curve graph in liquid;
Specific embodiment
Present invention is further described in detail combined with specific embodiments below, but not as a limitation of the invention.
The preparation method of electrolysis water and electrolysis urea anode catalyst, the specific steps are as follows:
The cobalt metal salt of 0.5-1mmol, the sodium citrate dehydrate of 0.5-2mmol are weighed, is dissolved in 20ml deionized water, Metal cyanide aqueous solutions of potassium is added while stirring, obtains mixed solution, stands a period of time, product is centrifuged, wash, is done It is dry to obtain PBA cube.
A certain amount of PBA cube powder is weighed, is dispersed in dehydrated alcohol, then pours into 100- with continuous stirring In the PVP ethanol solution of 500mg/ml, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 160-200 6-48h is reacted at DEG C, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo with deionized water and dehydrated alcohol, obtained hollow PBA cube;
Below by specific embodiment, the present invention will be described in more detail:
Embodiment 1
The trisodium citrate dihydrate of the cobalt chloride hexahydrate of 143mg and 265mg is dissolved in 20mL deionized water, side stirring 20mL potassium ferricyanide aqueous solution is added in side, obtains mixed solution, stands 20h, product is centrifuged, wash, is dried in vacuo for 24 hours Obtain CoFe-PBA.
The above-mentioned CoFe-PBA powder of 20mg is weighed, is dispersed in 20mL dehydrated alcohol, then pours into continuous stirring In the PVP ethanol solution of 100mg/20mL, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 180 DEG C Lower reaction 48h, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo for 24 hours with deionized water and dehydrated alcohol, obtained hollow CoFe-PBA。
Fig. 1 is the XRD spectrum of CoFe-PBA respectively, it can be seen that about 17.2,24.4,38.1 and 39.1,42.9, Diffraction maximum is shown at 45.7,52.5,53.3,59.5 respectively, is corresponded respectively to (200) of CoFe-PBA, (220), (400), (420), (422), (440), (600) and (620) face show the formation of CoFe-PBA.
Fig. 2 is SEM phenogram of the CoFe-PBA under 100nm amplification factor, it can be seen that synthesized CoFe-PBA tool There are solid cube structure, and size uniformity, is evenly distributed.
Fig. 3 is the SEM phenogram of the CoFe-PBA after ethyl alcohol etches, it can be seen that through over etching, CoFe-PBA is vertical Cube is etched from apex, is in hollow cube structure.
Fig. 4 is the TEM phenogram of the CoFe-PBA after ethyl alcohol etches, it may be clearly seen that by ethyl alcohol etching CoFe-PBA is in hollow structure, and cubic shaped keeps good.
It is CoFe-PBA, Hollow CoFe-PBA, noble metal catalyst IrO respectively in Fig. 52LSV curve graph, can be with Find out that prepared hollow CoFe-PBA in 1M KOH electrolyte there is good electro-catalysis to produce oxygen performance, relative to CoFe- PBA, OER performance are obviously improved, and are reaching 10mA/cm2When, overpotential is about 338mV.
It is CoFe-PBA, Hollow CoFe-PBA, noble metal catalyst IrO respectively in Fig. 62LSV curve graph, can be with Find out that prepared hollow CoFe-PBA in alkaline solution there is good electro-catalysis to produce oxygen performance, relative to CoFe-PBA, Its UOR performance is obviously improved, and is reaching 10mA/cm2When, overpotential is about 170mV.
Embodiment 2
The trisodium citrate dihydrate of the cabaltous nitrate hexahydrate of 175mg and 265mg is dissolved in 20mL deionized water, side stirring 20mL potassium ferricyanide aqueous solution is added in side, obtains mixed solution, stands 48h, product is centrifuged, wash, is dried in vacuo for 24 hours Obtain CoFe-PBA.
The above-mentioned CoFe-PBA powder of 20mg is weighed, is dispersed in 20mL dehydrated alcohol, then pours into continuous stirring In the PVP ethanol solution of 100mg/20mL, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 200 DEG C Lower reaction 48h, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo for 24 hours with deionized water and dehydrated alcohol, obtained hollow CoFe-PBA。
Embodiment 3
The trisodium citrate dihydrate of the cobalt acetate of 106mg and 265mg is dissolved in 20mL deionized water, is added while stirring 20mL potassium ferricyanide aqueous solution, obtains mixed solution, stands 48h, and product is centrifuged, is washed, is dried in vacuo and obtains for 24 hours CoFe-PBA。
The above-mentioned CoFe-PBA powder of 20mg is weighed, is dispersed in 20mL dehydrated alcohol, then pours into continuous stirring In the PVP ethanol solution of 200mg/20mL, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 160 DEG C Lower reaction for 24 hours, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo for 24 hours with deionized water and dehydrated alcohol, obtained hollow CoFe-PBA。
Embodiment 4
The trisodium citrate dihydrate of the cobalt chloride hexahydrate of 143mg and 265mg is dissolved in 20mL deionized water, side stirring 20mL potassium cobalticyanide aqueous solution is added in side, obtains mixed solution, stands 36h, product is centrifuged, wash, is dried in vacuo for 24 hours Obtain CoCo-PBA.
The above-mentioned CoCo-PBA powder of 20mg is weighed, is dispersed in 20mL dehydrated alcohol, then pours into continuous stirring In the PVP ethanol solution of 400mg/20mL, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 180 DEG C Lower reaction for 24 hours, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo for 24 hours with deionized water and dehydrated alcohol, obtained hollow CoCo-PBA。
Mixed solution embodiment 5
The trisodium citrate dihydrate of the cobalt chloride hexahydrate of 143mg and 265mg is dissolved in 20mL deionized water, side stirring 20mL potassium ferricyanide aqueous solution is added in side, obtains mixed solution, stands 36h, product is centrifuged, wash, is dried in vacuo for 24 hours Obtain CoFe-PBA.
The above-mentioned CoFe-PBA powder of 20mg is weighed, is dispersed in 20mL dehydrated alcohol, then pours into continuous stirring In the PVP ethanol solution of 500mg/20mL, after stirring 15min, mixed solution is transferred in 50mL water heating kettle, 200 DEG C Lower reaction 6h, is centrifuged after being cooled to room temperature, is washed, is dried in vacuo for 24 hours with deionized water and dehydrated alcohol, obtained hollow CoFe-PBA。
Finally it should be noted that: the above examples are only used to illustrate the technical scheme of the present invention rather than its limitations, to the greatest extent Pipe is described the invention in detail referring to above-described embodiment, it should be understood by those ordinary skilled in the art that: still may be used With modifications or equivalent substitutions are made to specific embodiments of the invention, and repaired without departing from any of spirit and scope of the invention Change or equivalent replacement, should all cover in present claims range.

Claims (6)

1. the preparation method of a kind of electrolysis water and electrolysis urea anode catalyst, it is characterised in that the following steps are included:
S1, PBA cube is synthesized using the precipitation method;
S2, using hydro-thermal method, PBA cube is performed etching using dehydrated alcohol, finally obtains hollow PBA cube, as Electrolysis water and electrolysis urea anode catalyst.
2. the preparation method of electrolysis water according to claim 1 and electrolysis urea anode catalyst, it is characterised in that institute Stating step S1 includes:
S11,0.5-1mmol cobalt metal salt and the dissolution of 0.5-2mmol sodium citrate dehydrate are weighed in deionized water, stirring is equal It is even to obtain mixed solution;
S12, certain density metal cyanide aqueous solutions of potassium is added in the stirring of above-mentioned mixed solution side, continues to stir 5min, stands Product is centrifuged, is washed, is dried in vacuo with deionized water and dehydrated alcohol, obtains PBA cube by 20-48h.
3. the preparation method of electrolysis water according to claim 1 and electrolysis urea anode catalyst, it is characterised in that institute Stating step S2 includes: to weigh a certain amount of PBA cube, is dispersed in dehydrated alcohol, then pours into 100- with continuous stirring It is stirred evenly in the PVP ethanol solution of 500mg/20ml, mixed solution is transferred in water heating kettle, it is anti-at 160-200 DEG C 6-48h is answered, is centrifuged after being cooled to room temperature, washed, be dried in vacuo with deionized water and dehydrated alcohol, obtain hollow PBA cubes Body.
4. the preparation method of electrolysis water according to claim 2 and electrolysis urea anode catalyst, it is characterised in that: institute Stating cobalt metal salt is one or more of nitrate, sulfate, acetate, chloride.
5. a kind of electrolysis water and electrolysis urea anode catalyst of any one of -4 method preparations according to claim 1.
6. electrolysis water according to claim 5 and electrolysis urea anode catalyst, it is characterised in that: it receives to be hollow Rice cube structure.
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CN111632624A (en) * 2020-06-22 2020-09-08 陕西科技大学 Anode catalyst for water electrolysis and preparation method thereof
CN111822054A (en) * 2020-08-14 2020-10-27 陕西科技大学 Nano porous material anode catalyst and preparation method thereof

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Publication number Priority date Publication date Assignee Title
CN111632624A (en) * 2020-06-22 2020-09-08 陕西科技大学 Anode catalyst for water electrolysis and preparation method thereof
CN111632624B (en) * 2020-06-22 2022-10-28 陕西科技大学 Anode catalyst for water electrolysis and preparation method thereof
CN111822054A (en) * 2020-08-14 2020-10-27 陕西科技大学 Nano porous material anode catalyst and preparation method thereof

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