CN110627030A - Platinum phosphide nano-catalyst, preparation method thereof and application thereof in electrocatalytic oxygen reduction - Google Patents
Platinum phosphide nano-catalyst, preparation method thereof and application thereof in electrocatalytic oxygen reduction Download PDFInfo
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- CN110627030A CN110627030A CN201910888541.5A CN201910888541A CN110627030A CN 110627030 A CN110627030 A CN 110627030A CN 201910888541 A CN201910888541 A CN 201910888541A CN 110627030 A CN110627030 A CN 110627030A
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- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 title claims abstract description 455
- 229910052697 platinum Inorganic materials 0.000 title claims abstract description 207
- 239000011943 nanocatalyst Substances 0.000 title claims abstract description 95
- 238000002360 preparation method Methods 0.000 title claims abstract description 31
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 18
- 239000001301 oxygen Substances 0.000 title claims abstract description 18
- 230000009467 reduction Effects 0.000 title claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 112
- 239000007788 liquid Substances 0.000 claims abstract description 50
- 238000006243 chemical reaction Methods 0.000 claims abstract description 41
- 239000006185 dispersion Substances 0.000 claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 34
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 27
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000005406 washing Methods 0.000 claims abstract description 20
- 239000011574 phosphorus Substances 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 16
- 239000002904 solvent Substances 0.000 claims abstract description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 22
- 239000002245 particle Substances 0.000 claims description 19
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- QGLWBTPVKHMVHM-KTKRTIGZSA-N (z)-octadec-9-en-1-amine Chemical group CCCCCCCC\C=C/CCCCCCCCN QGLWBTPVKHMVHM-KTKRTIGZSA-N 0.000 claims description 12
- CCCMONHAUSKTEQ-UHFFFAOYSA-N octadec-1-ene Chemical compound CCCCCCCCCCCCCCCCC=C CCCMONHAUSKTEQ-UHFFFAOYSA-N 0.000 claims description 12
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 11
- 229910052763 palladium Inorganic materials 0.000 claims description 11
- 239000002159 nanocrystal Substances 0.000 claims description 10
- 229910045601 alloy Inorganic materials 0.000 claims description 8
- 239000000956 alloy Substances 0.000 claims description 8
- KZTYYGOKRVBIMI-UHFFFAOYSA-N diphenyl sulfone Chemical compound C=1C=CC=CC=1S(=O)(=O)C1=CC=CC=C1 KZTYYGOKRVBIMI-UHFFFAOYSA-N 0.000 claims description 8
- 239000002808 molecular sieve Substances 0.000 claims description 7
- 239000000377 silicon dioxide Substances 0.000 claims description 7
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 7
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 6
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 claims description 6
- 229910001260 Pt alloy Inorganic materials 0.000 claims description 6
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims description 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 claims description 6
- PCLURTMBFDTLSK-UHFFFAOYSA-N nickel platinum Chemical compound [Ni].[Pt] PCLURTMBFDTLSK-UHFFFAOYSA-N 0.000 claims description 6
- RIOQSEWOXXDEQQ-UHFFFAOYSA-N triphenylphosphine Chemical compound C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 RIOQSEWOXXDEQQ-UHFFFAOYSA-N 0.000 claims description 6
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 4
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 4
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 4
- 239000005642 Oleic acid Substances 0.000 claims description 4
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 4
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 4
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 4
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 claims description 4
- JTPNRXUCIXHOKM-UHFFFAOYSA-N 1-chloronaphthalene Chemical compound C1=CC=C2C(Cl)=CC=CC2=C1 JTPNRXUCIXHOKM-UHFFFAOYSA-N 0.000 claims description 3
- 229910019142 PO4 Inorganic materials 0.000 claims description 3
- LMHKOBXLQXJSOU-UHFFFAOYSA-N [Co].[Ni].[Pt] Chemical compound [Co].[Ni].[Pt] LMHKOBXLQXJSOU-UHFFFAOYSA-N 0.000 claims description 3
- CLBRCZAHAHECKY-UHFFFAOYSA-N [Co].[Pt] Chemical compound [Co].[Pt] CLBRCZAHAHECKY-UHFFFAOYSA-N 0.000 claims description 3
- CMHKGULXIWIGBU-UHFFFAOYSA-N [Fe].[Pt] Chemical compound [Fe].[Pt] CMHKGULXIWIGBU-UHFFFAOYSA-N 0.000 claims description 3
- GIMWDLLVKMZDMJ-UHFFFAOYSA-N [Mn].[Fe].[Pt] Chemical compound [Mn].[Fe].[Pt] GIMWDLLVKMZDMJ-UHFFFAOYSA-N 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- WBLJAACUUGHPMU-UHFFFAOYSA-N copper platinum Chemical compound [Cu].[Pt] WBLJAACUUGHPMU-UHFFFAOYSA-N 0.000 claims description 3
- JUWSSMXCCAMYGX-UHFFFAOYSA-N gold platinum Chemical compound [Pt].[Au] JUWSSMXCCAMYGX-UHFFFAOYSA-N 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 3
- 239000010452 phosphate Substances 0.000 claims description 3
- ACVYVLVWPXVTIT-UHFFFAOYSA-M phosphinate Chemical compound [O-][PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-M 0.000 claims description 3
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 claims description 3
- 229910000073 phosphorus hydride Inorganic materials 0.000 claims description 3
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 claims description 3
- ZMBHCYHQLYEYDV-UHFFFAOYSA-N trioctylphosphine oxide Chemical compound CCCCCCCCP(=O)(CCCCCCCC)CCCCCCCC ZMBHCYHQLYEYDV-UHFFFAOYSA-N 0.000 claims description 3
- 238000006722 reduction reaction Methods 0.000 abstract description 15
- 230000003197 catalytic effect Effects 0.000 abstract description 14
- 125000004437 phosphorous atom Chemical group 0.000 abstract description 12
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000006479 redox reaction Methods 0.000 abstract 1
- 239000002243 precursor Substances 0.000 description 30
- 239000000243 solution Substances 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 16
- RMZAYIKUYWXQPB-UHFFFAOYSA-N trioctylphosphane Chemical compound CCCCCCCCP(CCCCCCCC)CCCCCCCC RMZAYIKUYWXQPB-UHFFFAOYSA-N 0.000 description 14
- 239000002105 nanoparticle Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- 229910052723 transition metal Inorganic materials 0.000 description 6
- 150000003624 transition metals Chemical class 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 229910001252 Pd alloy Inorganic materials 0.000 description 4
- 238000002441 X-ray diffraction Methods 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- 229910000990 Ni alloy Inorganic materials 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000010941 cobalt Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 239000010948 rhodium Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910001096 P alloy Inorganic materials 0.000 description 2
- 238000003917 TEM image Methods 0.000 description 2
- 238000005275 alloying Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 238000002484 cyclic voltammetry Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- -1 gold and silver) Chemical class 0.000 description 2
- 238000002173 high-resolution transmission electron microscopy Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000000543 intermediate Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052755 nonmetal Inorganic materials 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 229910052703 rhodium Inorganic materials 0.000 description 2
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 238000013112 stability test Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- KWSLGOVYXMQPPX-UHFFFAOYSA-N 5-[3-(trifluoromethyl)phenyl]-2h-tetrazole Chemical compound FC(F)(F)C1=CC=CC(C2=NNN=N2)=C1 KWSLGOVYXMQPPX-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- 238000001016 Ostwald ripening Methods 0.000 description 1
- 229910002844 PtNi Inorganic materials 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- JTLNYVRJWSILIT-UHFFFAOYSA-N [P].[Au].[Pt] Chemical compound [P].[Au].[Pt] JTLNYVRJWSILIT-UHFFFAOYSA-N 0.000 description 1
- PFZHNAXLNCTMNS-UHFFFAOYSA-N [P].[Ni].[Pt] Chemical compound [P].[Ni].[Pt] PFZHNAXLNCTMNS-UHFFFAOYSA-N 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 229910002056 binary alloy Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 229910021397 glassy carbon Inorganic materials 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- VAKIVKMUBMZANL-UHFFFAOYSA-N iron phosphide Chemical compound P.[Fe].[Fe].[Fe] VAKIVKMUBMZANL-UHFFFAOYSA-N 0.000 description 1
- 239000003273 ketjen black Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000004502 linear sweep voltammetry Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002843 nonmetals Chemical group 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 229910003446 platinum oxide Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
- 229910001379 sodium hypophosphite Inorganic materials 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910002058 ternary alloy Inorganic materials 0.000 description 1
- 238000004832 voltammetry Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/185—Phosphorus; Compounds thereof with iron group metals or platinum group metals
- B01J27/1856—Phosphorus; Compounds thereof with iron group metals or platinum group metals with platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/33—Electric or magnetic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y40/00—Manufacture or treatment of nanostructures
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/08—Other phosphides
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Nanotechnology (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Composite Materials (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Catalysts (AREA)
Abstract
The invention provides a platinum phosphide nano-catalyst, a preparation method thereof and application thereof in electrocatalytic oxygen reduction, comprising the following steps: 1) dispersing a platinum catalyst in a solvent, and uniformly stirring to obtain a platinum catalyst dispersion liquid; 2) adding a phosphorus source into the platinum catalyst dispersion liquid, uniformly mixing, reacting at a certain temperature, and centrifuging and washing after the reaction is finished to obtain the platinum phosphide nano-catalyst. The method synthesizes the platinum phosphide nano-catalyst with a specific electronic structure by diffusing phosphorus atoms generated by decomposing a phosphorus source into the platinum catalyst at a certain temperature. The preparation method has the advantages of simple flow, low cost, good repeatability, no environmental pollution and convenient mass preparation, and the prepared platinum phosphide nano-catalyst shows far higher catalytic activity and stability than a commercial platinum/carbon catalyst in an electrocatalytic oxidation-reduction reaction, thereby having good application prospect.
Description
Technical Field
The invention belongs to the field of nano science, and particularly relates to a platinum phosphide nano catalyst, a preparation method thereof and application thereof in electrocatalytic oxygen reduction.
Background
The platinum catalyst shows excellent catalytic performance in the fields of energy, chemistry and petrochemical industry, and particularly plays a role in fuel cells, automobile exhaust purification, hydrogenation, dehydrogenation and other industrial catalytic reactions. However, due to the scarcity of platinum resources and the concentration in a few countries and regions, the price of platinum is expensive and the use cost is extremely high, which seriously hinders the large-scale application of platinum in modern industries. Therefore, the method for improving the catalytic performance of the platinum catalyst and reducing the platinum dosage becomes a great research hotspot of energy science at present, and has great significance for promoting economic development and saving resources.
Alloying platinum by introducing a second phase transition metal (such as palladium, gold, cobalt, nickel, copper, iron, lead, etc.) is a strategy for effectively improving the performance of the platinum catalyst. The method mainly improves the number of surface active sites of platinum or changes the binding energy of platinum with reactants, reactant intermediates and products by changing the electronic structure (5d empty rail) of platinum, thereby achieving the purposes of improving the catalytic activity of platinum and reducing the platinum dosage. However, the second phase transition metal component in the catalyst is easy to undergo corrosion dissolution and Ostwald ripening process (Nano Energy 2019,60,111-118) under the conditions of low pH value, high oxygen concentration, high humidity, different potentials and the like, so that the activity of the catalyst is damaged in the using process, the service life is shortened, and the process of commercial scale application of the catalyst is hindered. In addition, the platinum alloying technology is limited by its complicated preparation method and the use of expensive transition metals (such as gold and silver), so that it is not feasible to develop conditions in industry.
Recent research results show that compared with the modification of a platinum catalyst by adding a second phase metal element, the addition of a non-metal atom (such as H, B, N, C or P) into the metal catalyst has a larger influence on the electronic structure (nat. Comm.2014,5,5787, J.Mater. chem.A 2019,7,4714.), and further has better improvement on the catalytic performance. However, due to the strong bonding energy between platinum atoms and the large bonding energy (306.7 kJ/mol) (CRC press,2007), doping non-metal atoms into a platinum lattice to form PtX (X ═ H, B, N, C, P, or the like) remains a great challenge.
In recent years, transition metal phosphides (e.g., phosphorous compounds) have been usedNickel phosphide, cobalt phosphide, iron phosphide, rhodium phosphide, ruthenium phosphide and the like) has the advantages of low raw material cost (avoiding the use of second-phase transition metal), various preparation modes, high catalytic activity and stability and the like, and is widely applied to the research of electrocatalysis, energy storage, photocatalysis, chemical catalysis and the like. The porous surface oxidized cobalt phosphide nano-catalyst is reported to have good electrocatalytic oxygen reduction performance (J.Power Sources,2017,363,87-94), and the rhodium phosphide nano-catalyst shows high catalytic activity and stability in both electrocatalytic hydrogen evolution and oxygen evolution reactions (J.Am.chem.Soc.,2017,139, 5494-. The surface of the palladium catalyst can be rapidly modified by adding a phosphorus source to improve the selectivity of the palladium catalyst in the carbon monoxide catalytic reaction (patent CN107413359A), but the prepared catalyst is palladium-palladium phosphide with a core-shell structure, wherein the palladium phosphide is in an amorphous state, and the structure cannot be stably maintained in the catalytic reaction. In addition, although there have been many studies on metal phosphide, few studies on platinum phosphide nano-catalyst have been reported at present due to the limitations of difficult synthesis of platinum phosphide nano-crystal, harsh production conditions, complex preparation and few controllable factors. Such as PtP formation on a platinum catalyst core by Cramerikawa et al2A surface layer and is applied to a fuel cell (patent CN 102365775B). However, the catalyst prepared by the method can only be synthesized on a carrier material, has no universality, needs vacuum and high-temperature calcination and other conditions, has high process cost, and is not beneficial to industrial large-scale production. Therefore, developing a low-cost and efficient way to obtain a platinum phosphide nano-catalyst with excellent catalytic activity and stability is a great challenge while having great significance.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides a platinum phosphide nano-catalyst, a preparation method thereof and application thereof in electrocatalytic oxygen reduction.
The invention is realized by the following technical scheme:
a preparation method of a platinum phosphide nano-catalyst comprises the following steps:
step 1, dispersing a platinum catalyst in a solvent to obtain a platinum catalyst dispersion liquid;
and 2, adding a phosphorus source into the platinum catalyst dispersion liquid obtained in the step 1, uniformly stirring, reacting at the temperature of 200-360 ℃ for 1-20h, and centrifuging and washing after the reaction is finished to obtain the platinum phosphide nano-catalyst.
Preferably, in step 1, the platinum catalyst is a platinum nanocrystal, a platinum-based alloy or a supported platinum-based catalyst.
Furthermore, the particle size of the platinum nanocrystal is 2-8 nm.
Further, the platinum-based alloy is an alloy of platinum cobalt, platinum nickel, platinum iron, platinum copper, platinum gold, platinum palladium, platinum cobalt nickel, platinum rhodium palladium or platinum iron manganese.
Further, the supported platinum-based catalyst is commercial platinum/carbon, platinum/alumina, platinum/silica, platinum/titania or platinum-supported molecular sieve.
Preferably, in step 1, the solvent is oleylamine, oleic acid, 1-octadecene, glycerol, formamide, quinoline, 1-chloronaphthalene, sulfolane, diphenyl ether or diphenyl sulfone.
Preferably, in step 2, the phosphorus source is white phosphorus, red phosphorus, phosphine, phosphate, phosphite, hypophosphite, tri-n-octylphosphine oxide or triphenylphosphine.
Preferably, in the step 1, the concentration of platinum in the platinum catalyst dispersion liquid is 0.01-10 mg/mL; the concentration of the amount of phosphorus species in the phosphorus source used in step 2 is lower than the concentration of the amount of platinum species in the platinum catalyst.
The platinum phosphide nano-catalyst prepared by the preparation method.
The application of the platinum phosphide nano-catalyst in electrocatalytic oxygen reduction is provided.
Compared with the prior art, the invention has the following beneficial technical effects:
in the invention, phosphorus atoms generated by decomposing a phosphorus source are diffused into the platinum catalyst lattice to prepare pure-phase platinum phosphide (with the molecular formula of Pt)2P) nanocrystalline catalysts, specific forThe determined electronic structure weakens the binding energy of the catalyst to the intermediate of the oxygen reduction reaction, and shows excellent activity of the electrocatalytic oxygen reduction reaction. Meanwhile, the surface of the catalyst is rich in stacking fault defects, and the catalyst has a large number of dangling bonds and rich platinum reaction active sites, so that the electrocatalysis performance is further improved. More importantly, the platinum phosphide nano-catalyst has a good crystal structure (face-centered cubic structure) and is a pure phase, so that the catalyst has structural stability superior to other amorphous structures or heterogeneous catalysts, shows excellent catalytic stability in electrocatalysis reaction, avoids great reduction of catalyst activity in the catalytic process, and has great application potential in the field of electrocatalysis.
In addition, the invention avoids the use of transition metal in the conventional platinum-based alloy catalyst, greatly reduces the manufacturing cost of the catalyst and further meets the requirement of industrial mass production. Compared with the existing platinum-based catalyst, the preparation method provided by the invention is simple, the raw materials are cheap, the production cost is low, and no environmental pollution is caused.
Further, the components of the catalyst can be regulated and controlled through reaction time, and the size of the catalyst can be accurately controlled through regulating and controlling the size of the original platinum catalyst.
The platinum phosphide nano-catalyst prepared by the invention is applied to electrocatalytic oxygen reduction reaction, has excellent catalytic activity and stability due to the characteristics of specific electronic structure, surface rich defect, stable structure in the reaction, good dispersibility and the like, and can meet the requirement of higher industrial application.
Drawings
FIG. 1 is a TEM photograph of Pt phosphide nanocatalyst prepared in the first example of the present invention, wherein the inset is an enlarged photograph of a single nanoparticle.
FIG. 2 is a TEM photograph of Pt phosphide nanocatalyst prepared in example II of the present invention, wherein the inset is an enlarged photograph of a single nanoparticle.
FIG. 3 is a TEM photograph of Pt phosphide nanocatalyst prepared in example III of the present invention, wherein the inset is an enlarged photograph of a single nanoparticle.
FIG. 4 is a TEM photograph of Pt phosphide nanocatalyst prepared in example IV of the present invention, wherein the inset is an enlarged photograph of a single nanoparticle.
FIG. 5 is a TEM photograph of Pt phosphide nanocatalyst prepared in example V of the present invention, wherein the inset is an enlarged photograph of a single nanoparticle.
FIG. 6 is a high-resolution TEM image of Pt phosphide nanocatalyst prepared in example V of the present invention, and the corresponding Fourier transform image is shown in the inset.
FIG. 7 is an X-ray diffraction spectrum of a platinum phosphide nanocatalyst prepared in example five of the present invention.
FIG. 8 is a TEM photograph of Pt phosphide nanocatalyst prepared in example six of the present invention.
FIG. 9 is a graph comparing the X-ray diffraction spectra of the Pt phosphide nano-catalyst prepared in example six and the Pt nano-particles as the raw material.
FIG. 10 is a TEM photograph of commercial carbon black loaded with Pt nano-catalyst prepared in example six of the present invention.
FIG. 11 is a graph comparing the electrocatalytic oxygen reduction reaction activity of the platinum phosphide nanocatalyst prepared in example six of the present invention and a commercial platinum/carbon catalyst.
FIG. 12 is a graph comparing the stability of electrocatalytic oxygen reduction reaction of the platinum phosphide nanocatalyst prepared in example six of the present invention and a commercial platinum/carbon catalyst.
Detailed Description
The present invention will now be described in further detail with reference to specific examples, which are intended to be illustrative, but not limiting, of the invention.
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
step 1, dispersing a platinum catalyst in a solvent to obtain a platinum catalyst dispersion liquid;
and 2, adding a phosphorus source into the platinum catalyst dispersion liquid obtained in the step 1, uniformly stirring, heating for reaction, and centrifuging and washing after the reaction is finished to obtain the platinum phosphide nano-catalyst.
In step 1, the platinum catalyst is platinum nanocrystal, platinum-based alloy or a supported platinum-based catalyst. The platinum-based alloy is a platinum-based binary alloy such as platinum cobalt, platinum nickel, platinum iron, platinum copper, platinum gold, platinum palladium, etc., a platinum-based ternary alloy such as platinum cobalt nickel, platinum rhodium palladium, platinum iron manganese, etc., a platinum-based multicomponent alloy, etc. The supported platinum-based catalysts are commercial platinum/carbon, platinum/alumina, platinum/silica, platinum/titania or platinum-supported molecular sieves.
In the step 1, the solvent is oleylamine, oleic acid, 1-octadecene, glycerol, formamide, quinoline, 1-chloronaphthalene, sulfolane, diphenyl ether or diphenyl sulfone.
In step 2, the phosphorus source is a simple substance of phosphorus element and compounds with various valence states (inorganic substances of phosphorus such as white phosphorus, red phosphorus, phosphine, phosphate, phosphite, hypophosphite and the like, and organic phosphorus reagents such as tri-n-octylphosphine, tri-n-octylphosphine oxide, triphenylphosphine and the like).
In the step 1, the concentration of platinum in the platinum catalyst dispersion liquid is 0.01-10 mg/mL; the concentration of the amount of phosphorus species in the phosphorus source used in step 2 is lower than the concentration of the amount of platinum species in the platinum catalyst.
In the step 2, the reaction temperature is 200-.
Example one
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nanocubes (with the average particle size of 8nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 1h, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 4%, the morphology is still maintained as a nanocube, and the size is not obviously changed.
Example two
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nanocubes (with the average particle size of 8nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 1.5h, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 10%, and the shape gradually changes into a chamfered cube.
EXAMPLE III
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nanocubes (with the average particle size of 8nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 2 hours, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The content of phosphorus atoms in the catalyst is 16%, the catalyst particles become gradually round, and the corners disappear gradually.
Example four
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nanocubes (with the average particle size of 8nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 2.5h, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 21 percent, the morphology of the catalyst is changed into a nearly spherical shape, and the size of the catalyst is not obviously changed.
EXAMPLE five
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nanocubes (with the average particle size of 8nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 3 hours, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 33.3%, the particle morphology further becomes spherical, and the particle size is increased to 9.5 nm.
EXAMPLE six
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nano particles (with the average particle size of 5nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 3 hours, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 33.3%, the particle appearance is quasi-sphere, and the particle size is 6.2 nm.
EXAMPLE seven
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 3.76mg of platinum nano particles (with the average particle size of 2nm) in 10mL of oleylamine to obtain a stable platinum catalyst dispersion liquid, wherein the concentration of platinum is 0.376 mg/mL;
2) adding 1.6mL of tri-n-octylphosphine into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 300 ℃, reacting for 1.5h, centrifuging and washing to obtain the platinum phosphide nano-catalyst. The phosphorus atom content in the catalyst is 33.3%, the particle appearance is quasi-sphere, and the particle size is 2.5 nm.
Example eight
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 3.71mg of a platinum-nickel alloy (composition PtNi)3) The nano catalyst is ultrasonically dispersed in 10mL of oleylamine to obtain stable platinum-nickel alloy nano catalyst dispersion liquid. Wherein the concentration of platinum atoms is 0.195 mg/mL;
2) adding 3mL of tri-n-octylphosphine into the platinum-nickel alloy catalyst dispersion liquid in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 200 ℃, reacting for 20 hours, centrifuging and washing to obtain the platinum-nickel-phosphorus alloy nano catalyst.
Example nine
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 5mg of a platinum alloy (composition: Pt)50Au50) The nano catalyst is ultrasonically dispersed in 10mL of oleic acid to obtain stable platinum alloy nano catalyst dispersion liquid. Wherein the concentration of platinum atoms is 0.249 mg/mL;
2) adding 5.4mL of tri-n-octylphosphine into the platinum alloy catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 290 ℃, reacting for 8.5h, centrifuging and washing to obtain the platinum-gold-phosphorus alloy nano catalyst.
Example ten
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 17mg of a platinum rhodium palladium alloy (composition: Pt)47Rh33Pd20) The nano catalyst is ultrasonically dispersed in 10mL of 1-octadecene to obtain stable platinum-rhodium-palladium alloy nano catalyst dispersion liquid. It is composed ofThe concentration of the platinum atom in the platinum alloy is 1.06 mg/mL;
2) adding 5mL of tri-n-octylphosphine into the platinum-rhodium-palladium alloy catalyst dispersion liquid in the step 1), and uniformly stirring to obtain reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 280 ℃, reacting for 3.5h, centrifuging and washing to obtain the platinum-rhodium-palladium alloy nano catalyst.
EXAMPLE eleven
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 50mg of a commercial platinum/carbon catalyst (loading 10%) was ultrasonically dispersed in 10mL of 1-octadecene to obtain a stable platinum/carbon catalyst dispersion. Wherein the concentration of platinum atoms is 0.5 mg/mL;
2) adding 2mL of tri-n-octylphosphine into the platinum/carbon catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 250 ℃, reacting for 6 hours, centrifuging and washing to obtain the platinum phosphide/carbon nano-catalyst.
Example twelve
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 100mg of a commercial platinum/silica catalyst (loading 5%) was ultrasonically dispersed in 10mL of 1-octadecene to give a stable platinum/silica catalyst dispersion. Wherein the concentration of platinum atoms is 0.5 mg/mL;
2) adding 2mL of tri-n-octylphosphine into the platinum/silicon dioxide catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 260 ℃, reacting for 5 hours, centrifuging and washing to obtain the platinum phosphide/silicon dioxide nano catalyst.
EXAMPLE thirteen
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) ultrasonically dispersing 10mg of platinum-loaded molecular sieve catalyst (the loading amount is 1%) in 10mL of oleylamine to obtain a stable platinum-loaded molecular sieve catalyst dispersion liquid. Wherein the concentration of platinum atoms is 0.01 mg/mL;
2) adding 5mL of tri-n-octylphosphine into the platinum-loaded molecular sieve catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 320 ℃, reacting for 10 hours, centrifuging and washing to obtain the nano catalyst of the phosphorized platinum-loaded molecular sieve.
Example fourteen
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 10mg of platinum nanoparticles (average particle size 5nm) were homogeneously mixed with 20mg of diphenyl sulfone;
2) adding 6mg of white phosphorus simple substance (dissolved in carbon disulfide) into the step 1), and uniformly stirring to obtain a reaction precursor;
3) heating and stirring the reaction precursor at 360 ℃, reacting for 4 hours, centrifuging and washing to obtain the platinum phosphide nano-catalyst.
Example fifteen
The preparation method of the platinum phosphide nano-catalyst comprises the following steps:
1) 100mg of platinum nanoparticles (average particle size of 5nm) were ultrasonically dispersed in 10mL of glycerin to obtain a stable platinum catalyst dispersion. Wherein the concentration of platinum atoms is 10 mg/mL;
2) adding 72mg of sodium hypophosphite into the platinum catalyst dispersion liquid obtained in the step 1), and uniformly stirring to obtain a reaction precursor liquid;
3) heating and stirring the reaction precursor solution at 260 ℃, reacting for 8.5h, centrifuging and washing to obtain the platinum phosphide nano-catalyst.
Application example
0.6mg of the platinum phosphide nanocatalyst prepared in example six was uniformly loaded on the surface of a commercial carbon material (Ketjen Black EC-300J, platinum loading 20%). Dispersing the loaded catalyst in 5mL of acetic acid, keeping the temperature at 70 ℃ for 12h to clean the surface of the catalyst, centrifuging, washing twice with an ethanol solution, drying in a 60 ℃ oven for 12h, and ultrasonically dispersing the catalyst in 2mL of a mixed solution (volume ratio is 4:1:0.02) of water, isopropanol and 5% nafion solution. 10 μ L (containing 3 μ g of platinum) of the dispersion was dropped on a glassy carbon electrode (area: 0.196 cm)2) And after being dried in the air, carrying out an electrocatalytic oxygen reduction reaction performance test on an Autolab PGSTAT302N electrochemical workstation. The test temperature is 25 ℃, a three-electrode system is adopted, and the reference electrode and the counter electrode are respectively Ag/AgCl and Pt foil electrodes. Cyclic voltammogram at N2Saturated 0.1M HClO4Obtained in solution with a sweep rate of 50 mV/s. Linear sweep voltammetry at O2The sweeping speed is 10mV/s, and the electrode rotating speed is 1600 rpm. Catalyst stability test at O2Saturated 0.1M HClO4The scanning is carried out in solution, the scanning cycle range is 0.6-1.1V (relative to the standard hydrogen electrode potential), the scanning speed is 100mV/s, and cyclic voltammetry and linear scanning voltammetry curves are recorded after the stability test.
Fig. 1-5 are transmission electron micrographs of the platinum phosphide nanocatalysts prepared in examples one-five, respectively, and show that as the reaction time increases, phosphorus atoms diffuse uniformly into the platinum catalyst lattice and the nanocrystal size increases. The appearance of the catalyst gradually evolves from a cube of the original platinum nano catalyst to be nearly spherical, and further proves that the platinum nano crystal evolves to the platinum phosphide nano crystal along with the diffusion of phosphorus atoms. Meanwhile, as the reaction proceeds, the content of phosphorus atoms in the platinum phosphide gradually increases, which also shows that the components of the platinum phosphide catalyst can be accurately controlled by regulating and controlling the reaction time.
FIG. 6 is a high resolution TEM image of the Pt phosphide nanocatalyst prepared in example five and its corresponding Fourier transform image, which shows that the Pt phosphide nanocatalyst is rich in a large number of stacking fault defects.
FIG. 7 is an X-ray diffraction pattern of the platinum phosphide nanocatalyst prepared in example five, and pure-phase platinum phosphide (molecular formula is Pt) can be determined by analyzing the diffraction pattern2P) generation of nanocrystals.
FIGS. 8 and 9 are a transmission electron micrograph and an X-ray diffraction spectrum, respectively, of a platinum phosphide nanocatalyst prepared in example six, having a catalyst particle size of 6.2nm, demonstrating small-sized pure-phase platinum phosphide (molecular formula Pt)2P) formation of nanocatalyst, indicating that the size of the platinum phosphide catalyst can beAnd (4) regulating and controlling the size of the platinum catalyst in the step one.
FIG. 10 is a TEM photograph of a small-sized Pt phosphide nanocatalyst prepared in example six and supported on commercial carbon black. It can be seen that the platinum phosphide nanoparticles are easy to uniformly load, and the catalytic performance research in subsequent application examples is facilitated.
Fig. 11 is a graph comparing the performance of the electrocatalytic oxygen reduction reaction of the platinum phosphide nanocatalyst of fig. 9 with that of the platinum catalyst before the phosphide. From the data in the figure, the area activity of the platinum phosphide nano-catalyst is 10.2 times that of the platinum catalyst, and the mass activity of the platinum phosphide nano-catalyst is 10.3 times that of the platinum catalyst, which shows that the platinum phosphide nano-catalyst has excellent catalytic activity.
FIG. 12 is a graph comparing the stability of electrocatalytic oxygen reduction reaction of the platinum phosphide nanocatalyst prepared in example six of the present invention and a commercial platinum/carbon catalyst. According to the data calculation in the figure, after 10,000 times and 30,000 times of cycle tests, the mass activity of the platinum phosphide nano-catalyst is respectively reduced by 6.8% and 9.1%. By way of comparison, the mass activity of the commercial platinum/carbon catalyst decreased by 22% and 55% after the same number of cycles. The loss of activity of the platinum phosphide nanocatalyst is far lower than that of the commercial platinum/carbon catalyst, which indicates that the catalyst has excellent catalytic stability.
Claims (10)
1. A preparation method of a platinum phosphide nano-catalyst is characterized by comprising the following steps:
step 1, dispersing a platinum catalyst in a solvent to obtain a platinum catalyst dispersion liquid;
and 2, adding a phosphorus source into the platinum catalyst dispersion liquid obtained in the step 1, uniformly stirring, reacting at the temperature of 200-360 ℃ for 1-20h, and centrifuging and washing after the reaction is finished to obtain the platinum phosphide nano-catalyst.
2. The method for preparing a platinum phosphide nano-catalyst according to claim 1, wherein in the step 1, the platinum catalyst is a platinum nanocrystal, a platinum-based alloy or a supported platinum-based catalyst.
3. The method of preparing a platinum phosphide nanocatalyst according to claim 2, wherein the particle size of the platinum nanocrystals is 2 to 8 nm.
4. The method for preparing a platinum phosphide nano-catalyst according to claim 2, wherein the platinum-based alloy is an alloy of platinum cobalt, platinum nickel, platinum iron, platinum copper, platinum gold, platinum palladium, platinum cobalt nickel, platinum rhodium palladium or platinum iron manganese.
5. The method of preparing a platinum phosphide nanocatalyst according to claim 2, wherein the supported platinum-based catalyst is commercial platinum/carbon, platinum/alumina, platinum/silica, platinum/titania or platinum-supported molecular sieve.
6. The method for preparing the platinum phosphide nanocatalyst according to claim 1, wherein in the step 1, the solvent is oleylamine, oleic acid, 1-octadecene, glycerol, formamide, quinoline, 1-chloronaphthalene, sulfolane, diphenyl ether or diphenyl sulfone.
7. The method for preparing a platinum phosphide nano-catalyst according to claim 1, wherein in the step 2, the phosphorus source is white phosphorus, red phosphorus, phosphine, phosphate, phosphite, hypophosphite, tri-n-octylphosphine oxide or triphenylphosphine.
8. The method for preparing a platinum phosphide nanocatalyst according to claim 1, wherein in the step 1, the concentration of platinum in the platinum catalyst dispersion liquid is 0.01-10 mg/mL; the concentration of the amount of phosphorus species in the phosphorus source used in step 2 is lower than the concentration of the amount of platinum species in the platinum catalyst.
9. The platinum phosphide nano-catalyst prepared by the preparation method of any one of claims 1 to 8.
10. Use of the platinum phosphide nanocatalyst of claim 9 in electrocatalytic oxygen reduction.
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Application publication date: 20191231 |