CN116786136A - Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst - Google Patents
Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst Download PDFInfo
- Publication number
- CN116786136A CN116786136A CN202310708581.3A CN202310708581A CN116786136A CN 116786136 A CN116786136 A CN 116786136A CN 202310708581 A CN202310708581 A CN 202310708581A CN 116786136 A CN116786136 A CN 116786136A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- electrolyte
- intermetallic compound
- preparation
- solution
- 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
Links
- 239000011943 nanocatalyst Substances 0.000 title claims abstract description 31
- 229910000765 intermetallic Inorganic materials 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 239000003054 catalyst Substances 0.000 claims abstract description 32
- 150000003839 salts Chemical class 0.000 claims abstract description 27
- 239000003792 electrolyte Substances 0.000 claims abstract description 26
- 229910052751 metal Inorganic materials 0.000 claims abstract description 18
- 239000002184 metal Substances 0.000 claims abstract description 17
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 16
- 239000000956 alloy Substances 0.000 claims abstract description 16
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims abstract description 16
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 15
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 13
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 13
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 230000003647 oxidation Effects 0.000 claims abstract description 11
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 11
- 239000012018 catalyst precursor Substances 0.000 claims abstract description 10
- 239000011159 matrix material Substances 0.000 claims abstract description 10
- 230000009467 reduction Effects 0.000 claims abstract description 10
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000005977 Ethylene Substances 0.000 claims abstract description 6
- 239000011259 mixed solution Substances 0.000 claims abstract description 4
- 239000012535 impurity Substances 0.000 claims abstract description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 53
- 239000010949 copper Substances 0.000 claims description 44
- 239000011777 magnesium Substances 0.000 claims description 29
- 239000000243 solution Substances 0.000 claims description 29
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 27
- 229910052749 magnesium Inorganic materials 0.000 claims description 27
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims description 18
- 239000011734 sodium Substances 0.000 claims description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 12
- 229910000365 copper sulfate Inorganic materials 0.000 claims description 12
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 12
- 229910052708 sodium Inorganic materials 0.000 claims description 12
- 239000004115 Sodium Silicate Substances 0.000 claims description 10
- 239000002105 nanoparticle Substances 0.000 claims description 10
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 10
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 6
- 239000002738 chelating agent Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000002243 precursor Substances 0.000 claims description 3
- 230000008569 process Effects 0.000 claims description 3
- 238000011068 loading method Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims 2
- 230000000536 complexating effect Effects 0.000 claims 1
- 239000008151 electrolyte solution Substances 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 11
- 238000005516 engineering process Methods 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 238000011065 in-situ storage Methods 0.000 abstract description 3
- 229910044991 metal oxide Inorganic materials 0.000 abstract description 2
- 150000004706 metal oxides Chemical class 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract 2
- 239000001995 intermetallic alloy Substances 0.000 abstract 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 27
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000011698 potassium fluoride Substances 0.000 description 13
- 235000003270 potassium fluoride Nutrition 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 9
- 238000006555 catalytic reaction Methods 0.000 description 8
- 239000013522 chelant Substances 0.000 description 8
- 230000006872 improvement Effects 0.000 description 7
- 238000005457 optimization Methods 0.000 description 7
- 229910052763 palladium Inorganic materials 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000005498 polishing Methods 0.000 description 4
- 238000004321 preservation Methods 0.000 description 4
- 244000137852 Petrea volubilis Species 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000009941 weaving Methods 0.000 description 3
- 238000000731 high angular annular dark-field scanning transmission electron microscopy Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 229910001252 Pd alloy Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000009954 braiding Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical group [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000007745 plasma electrolytic oxidation reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000010998 test method Methods 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8926—Copper and noble 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
- B01J37/18—Reducing with gases containing free hydrogen
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
- B01J37/341—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
- B01J37/347—Ionic or cathodic spraying; Electric discharge
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
- B01J37/348—Electrochemical processes, e.g. electrochemical deposition or anodisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/08—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
- C07C5/09—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds to carbon-to-carbon double bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
- C07C7/167—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Electrochemistry (AREA)
- Optics & Photonics (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Catalysts (AREA)
Abstract
The invention discloses preparation and application of a highly ordered Cu3Pd intermetallic compound nano catalyst, which mainly comprises the following preparation methods: pretreating metal matrix Mg wires; mixing alloy catalyst precursor salt mixed solution with electrolyte and carrying out microplasma electrolytic oxidation treatment; carrying out heating reduction treatment on the prepared catalyst to finally obtain the intermetallic compound nano catalyst with high order; the preparation process is simple, two metal elements can be uniformly mixed and loaded on the surface of the metal oxide carrier by a one-step method, and the in-situ preparation of the highly ordered intermetallic alloy nano-catalyst is realized; the catalyst is applied to acetylene hydrogenation reaction, is used for eliminating acetylene impurities in ethylene gas, and shows excellent catalytic selectivity; the development of the technology is beneficial to the development of the preparation of a trace noble metal alloy nano catalyst, greatly reduces the noble metal content required by acetylene hydrogenation, and is beneficial to the sustainable utilization and development of resources.
Description
Technical Field
The invention belongs to the field of catalyst preparation and hydrogenation application, and mainly relates to Cu 3 A preparation method and application of Pd/MgO catalyst.
Background
The catalyst is used as an important composition distribution for social and economic development, and has been widely applied to various fields of society, including agriculture, industry, aerospace and the like. At present, for a common catalyst, noble metals are mainly selected as main raw materials to construct a catalytic material; noble metals such as Pd, pt, etc., exhibit excellent catalytic activity in various catalytic reactions due to their unique electronic structures. However, the use of such metals in the catalytic field is severely inhibited by their relatively low content in the earth, which is relatively expensive. The non-noble metal is doped into the noble metal to form the alloy nano catalyst (comprising intermetallic compound), and the electronic structure of the alloy particles is regulated and controlled, so that the reduction of the consumption of the noble metal is realized while the catalytic performance is maintained or improved, and the method is a feasible and potential development mode. At present, the preparation of the alloy nano-catalyst is mainly carried out by a wet chemical method, the method needs more steps, and the selection of alloy elements has certain limitation; on the other hand, the alloy particles prepared by the methods generally have no strict ordering among alloy elements, and in the catalytic reaction, the selectivity of the catalytic reaction, such as hydrogenation of acetylene, for preparing ethylene, is adversely affected. Therefore, developing a new preparation method of the ordered alloy nano catalyst simplifies the preparation steps, reduces the consumption of noble metals, improves the catalytic reaction performance and is a problem which needs to be solved urgently at present.
Disclosure of Invention
In view of the above problems, the present invention employs a micro-scalePreparation of highly ordered Cu by plasma electrolytic oxidation technology 3 Pd/MgO intermetallic compound nano catalyst; microplasma electrolytic oxidation is a high-temperature high-pressure plasma effect technology which occurs at a metal interface, and a metal matrix can be oxidized in situ on the metal surface to generate a metal oxide to form a catalyst carrier; meanwhile, the plasma effect can decompose catalyst precursor salt, such as chelated Cu salt and chelated Pd salt, near the metal matrix Mg wire to form Cu and Pd alloy nano particles; because the precursor salt is uniformly mixed in the solution near the Mg wire, cu and Pd in the prepared alloy particles are also uniformly distributed; the prepared CuPd alloy nano particles are heated and reduced for 2 hours in a hydrogen atmosphere, cu atoms and Pd atoms are rearranged under the thermal effect, and finally the highly ordered Cu is prepared 3 Pd intermetallic compound nano-catalyst.
The invention can be realized by the following technical scheme:
highly ordered Cu 3 The preparation method of the Pd intermetallic compound nano catalyst comprises the following steps: mixing copper sulfate and sodium chloropalladate with EDTA chelating agent, respectively, and mixing the two mixtures with electrolyte to obtain copper element and palladium element with concentration of 2×10 respectively -3 -5×10 -3 mol/L,3×10 -4 -8×10 -4 The mol/L and the temperature of electrolyte are kept between 5 ℃ and 25 ℃, metal magnesium wires are used as anodes, microplasma electrolytic oxidation is carried out, the CuPd alloy nano-catalyst is prepared, and the Cu is finally prepared by carrying out thermal reduction treatment in hydrogen atmosphere 3 Pd intermetallic compound nano-catalyst.
Further improvement and optimization of the technical proposal, the electrolyte main salt is sodium silicate Na 2 SjO 3 ·9H 2 O, the concentration is 4g/L-9g/L; other components comprise KF and KOH, the concentrations of which are 5-9g/L and 5-8g/L respectively, and the total volume of the electrolyte is 500mL.
Further improvement and optimization of the technical scheme, and parameters of the microplasma electrolytic oxidation process: pulse number 250-400Hz, pulse width 50-80 μs, constant current mode, current setting 0.5-2A/cm 2 The action time is 1-2min.
According to the technical scheme, the catalyst precursor salt is prepared by respectively coordinating 0.1mol/L of copper sulfate solution and 0.01mol/L of sodium chloropalladate solution with EDTA chelating agent, then respectively taking a certain amount of chelated solution, adding the chelated solution into electrolyte, and uniformly stirring for 5 minutes to complete the mixing of the precursor salt in the electrolyte.
Further improvement and optimization of the technical proposal, the concentrations of the copper element and the palladium element of the catalyst precursor in the mixed solution are respectively 2 multiplied by 10 -3 ,3×10 -4 。
Further improvement and optimization of the technical scheme are that the temperature of the mixed solution is kept at 10-25 ℃, and liquid nitrogen is used for cooling.
Further improvement and optimization of the technical scheme are that the metal magnesium wire is sanded for 3 times, braided into a spiral shape, ultrasonically cleaned in ethanol for 15min, dried and stored.
Further improvement and optimization of the technical scheme, wherein the chelating agent EDTA concentration is 4 multiplied by 10 -3 -9×10 -3 mol/L。
Further improvement and optimization of the technical scheme, wherein the catalyst is heated (350-420 ℃) in a hydrogen atmosphere for reduction for 2 hours, and is stored in a sealing bag after completion;
the catalyst takes metal magnesium wires as a matrix, and a layer of three-dimensional porous MgO and Cu are attached to the surfaces of the wires 3 Pd nano particles are uniformly loaded on the MgO surface and in the pore canal, and the loading amount of noble metal Pd is 100mg/kg.
Another object of the present invention is to provide a Cu 3 The use of a Pd/MgO intermetallic catalyst in the hydrogenation of acetylene, said catalyst being used to convert acetylene impurities in ethylene to ethylene.
Further, the conversion rate of the catalyst in the acetylene hydrogenation reaction is 70-80%, the selectivity of the catalyst is 95% -96%, and the whole service life can reach 125 hours.
The invention utilizes microplasma electrolytic oxidation technology and combines the thermal reduction process to prepare MgO-loaded Cu on the metal magnesium wire substrate in situ 3 Pd intermetallic compound nanoparticles; compared with other methodsThe technical process is simple, and the designed technology is simpler and more convenient; prepared Cu 3 Pd intermetallic compound, cu atoms and Pd atoms of which are arranged in a highly ordered manner in nano particles, provide a uniform catalytic environment, show excellent catalytic performance in acetylene hydrogenation reaction, and have selectivity to ethylene up to 95% at 80% conversion; importantly, the intermetallic compound nano catalyst greatly reduces the dosage of noble metal Pd, the load of the noble metal Pd is only 100-360mg/kg, and the equivalent or synergistic decrement of the noble metal catalyst is realized. In addition, the catalyst also has excellent catalytic stability, and can keep stable aging for 125 hours under the condition of 95% selectivity. The catalyst preparation technology disclosed by the invention can be used for conveniently and efficiently preparing the acetylene hydrogenation catalyst, and greatly promotes the development and application of the metal catalyst.
Drawings
FIG. 1 shows Cu in example 1 of the present invention 3 Physical diagram of Pd/MgO catalyst.
FIG. 2 is a diagram showing Cu in example 1 of the present invention 3 Spherical aberration electron microscope (HAADF-STEM) diagram of Pd/MgO catalyst.
FIG. 3 is a diagram showing Cu in example 1 of the present invention 3 Pd/MgO catalyst catalytic conversion acetylene hydrogenation conversion rate diagram.
FIG. 4 shows Cu in example 1 of the present invention 3 Pd/MgO catalyst for catalyzing hydrogenation stabilization of acetylene.
Detailed Description
The following non-limiting examples will enable those of ordinary skill in the art to more fully understand the invention and are not intended to limit the invention in any way.
The test methods described in the following examples, unless otherwise specified, are all conventional; the reagents and materials, unless otherwise specified, are commercially available.
Example 1
Highly ordered Cu 3 The preparation method of the Pd intermetallic compound nano catalyst mainly comprises the following steps:
(1) braiding 1m long metal magnesium wires into a spiral shape, sequentially polishing with 1000# and 3000#, ultrasonically cleaning in ethanol for 15min, and drying and preserving;
(2) preparing electrolyte, namely adding sodium silicate, potassium fluoride and potassium hydroxide into 500ml of water respectively, and dissolving; the concentration of the potassium fluoride is 4g/L of sodium silicate, 5g/L of potassium fluoride and 6g/L of potassium hydroxide respectively;
(3) dissolving copper sulfate in water to prepare a copper sulfate solution with the concentration of 0.1 mol/L; dissolving sodium chloropalladate in water to prepare 0.01mol/L sodium chloropalladate solution; EDTA is dissolved in water to prepare 0.5mol/L EDTA solution; respectively adding a proper amount of EDTA into the catalyst precursor salt to form chelate salts of Cu and Pd;
(4) adding a proper amount of the chelate solution prepared in the step (3) into an electrolyte, and uniformly mixing, wherein the final concentrations of Cu salt and Pd salt in the electrolyte are respectively 2 multiplied by 10 -3 mol/L,3×10 -4 mol/L;
(5) Performing liquid nitrogen cooling treatment on the solution obtained in the step (4) to keep the temperature between 5 and 10 ℃;
(6) the spiral metal magnesium wire is used as anode to carry out microplasma electrolytic oxidation treatment, the pulse width is 80 mu s, the pulse number is 250Hz, and the pulse current density is 0.5A/cm 2 The action time is 2min;
(7) and (3) carrying out thermal reduction treatment on the prepared CuPd/MgO catalyst under the hydrogen atmosphere, wherein the heating temperature is 350 ℃, the time is 2 hours, and then sealing the bag for preservation after the completion.
For the spiral magnesium wire prepared in the example as a matrix, mgO is loaded with Cu 3 Pd intermetallic compound nano-catalyst, the entity of which is shown in figure 1: cu with gray color uniformly distributed on magnesium wire surface 3 Pd nanoparticle catalyst.
For the Cu prepared in this example and using spiral magnesium wire as matrix, mgO is loaded 3 The Pd intermetallic compound nano-catalyst and the ICP result show that the Pd content of the prepared catalyst is 100mg/kg.
For the Cu prepared in this example and using spiral magnesium wire as matrix, mgO is loaded 3 Pd intermetallic compound nano-catalyst, HAADF-STEM electron microscope thereof is shown in figure 2: cu (Cu) 3 Pd nano particles are uniformly distributed on the surface of the carrier and in the pore canal, and Cu atoms and Pd atoms are in a highly ordered arrangement state in the nano particles, so that the nano particles have a tetragonal structure.
For the Cu prepared in this example and using spiral magnesium wire as matrix, mgO is loaded 3 Pd intermetallic compound nano-catalyst, the acetylene hydrogenation conversion rate of which is shown in figure 3; with the increase of the catalytic reaction temperature, the conversion rate of acetylene gradually increases and finally reaches 100%.
For the Cu prepared in this example and using spiral magnesium wire as matrix, mgO is loaded 3 Pd intermetallic compound nano catalyst, is used for detecting the catalytic stability of acetylene hydrogenation reaction; placing the catalyst in a glass tube reactor for catalytic reaction, and monitoring in real time by using gas chromatography; the reaction process is detected every 25 hours, the stability of the catalytic reaction is detected, and the experimental result is shown in fig. 4: after 125h reaction, the catalyst has no obvious change in catalytic reaction selectivity and conversion rate, and has excellent catalytic stability.
Example 2
Highly ordered Cu 3 The preparation method of the Pd intermetallic compound nano catalyst mainly comprises the following steps:
(1) weaving magnesium wires with the diameter of 500 mu m and the length of 1m into a spiral shape, polishing the magnesium wires by using sand paper, ultrasonically cleaning the magnesium wires in ethanol for 20min, and drying and preserving the magnesium wires in an oven;
(2) preparing electrolyte, namely adding sodium silicate, potassium fluoride and potassium hydroxide into 500ml of water respectively, and dissolving; the concentration of the potassium fluoride is 6g/L of sodium silicate, 7g/L of potassium fluoride and 8g/L of potassium hydroxide respectively;
(3) dissolving copper sulfate in water to prepare a copper sulfate solution with the concentration of 0.1 mol/L; dissolving sodium chloropalladate in water to obtain
Forming 0.01mol/L sodium chloropalladate solution; EDTA is dissolved in water to prepare 0.5mol/L EDTA solution; respectively adding a proper amount of EDTA into the catalyst precursor salt to form chelate salts of Cu and Pd;
(4) adding a proper amount of the chelate solution prepared in the step (3) into an electrolyte, and uniformly mixing, wherein the final concentrations of Cu salt and Pd salt in the electrolyte are respectively 4 multiplied by 10 -3 mol/L,6×10 -4 mol/L;
(5) Performing liquid nitrogen cooling treatment on the solution obtained in the step (4) to keep the temperature between 10 and 15 ℃;
(6) the spiral metal magnesium wire is used as anode to carry out microplasma electrolytic oxidation treatment, the pulse width is 50 mu s, the pulse number is 400Hz, and the pulse current density is 1A/cm 2 The action time is 1min;
(7) and (3) carrying out thermal reduction treatment on the prepared CuPd/MgO alloy nano catalyst under the hydrogen atmosphere, wherein the heating temperature is 380 ℃, the time is 2 hours, and then sealing the bag for preservation after the completion.
Example 3
The preparation method of the highly ordered Cu3Pd intermetallic compound nano-catalyst mainly comprises the following steps:
(1) weaving magnesium wires with the diameter of 500 mu m and the length of 1.5m into a spiral shape, polishing the magnesium wires by using sand paper, ultrasonically cleaning the magnesium wires in ethanol for 25min, and drying and preserving the magnesium wires in an oven;
(2) preparing electrolyte, namely adding sodium silicate, potassium fluoride and potassium hydroxide into 500ml of water respectively, and dissolving; the concentration of the potassium fluoride is 8g/L of sodium silicate, 8g/L of potassium fluoride and 5g/L of potassium hydroxide respectively;
(3) dissolving copper sulfate in water to prepare a copper sulfate solution with the concentration of 0.1 mol/L; dissolving sodium chloropalladate in water to prepare 0.01mol/L sodium chloropalladate solution; EDTA is dissolved in water to prepare 0.5mol/L EDTA solution; respectively adding a proper amount of EDTA into the catalyst precursor salt to form chelate salts of Cu and Pd;
(4) adding a proper amount of the chelate solution prepared in the step (3) into an electrolyte, and uniformly mixing, wherein the final concentrations of Cu salt and Pd salt in the electrolyte are 5 multiplied by 10 respectively -3 mol/L,8×10 -4 mol/L;
(5) Performing liquid nitrogen cooling treatment on the solution obtained in the step (4) to keep the temperature of the electrolyte between 15 and 25 ℃;
(6) the spiral magnesium wire is used as an anode to carry out microplasma electrolytic oxidation treatment, the pulse width is 60 mu s, the pulse number is 335Hz, the pulse current density is 2A/cm < 2 >, and the action time is 1.5min;
(7) and (3) carrying out thermal reduction treatment on the prepared CuPd/MgO alloy nano catalyst under the hydrogen atmosphere, wherein the heating temperature is 400 ℃, the time is 2 hours, and then sealing the bag for preservation after the completion.
Example 4
Highly ordered Cu 3 The preparation method of the Pd intermetallic compound nano catalyst mainly comprises the following steps:
(1) weaving 500 μm diameter magnesium wire with length of 2m into spiral shape, polishing with sand paper, ultrasonically cleaning in ethanol for 30min, and drying in oven; the method comprises the steps of carrying out a first treatment on the surface of the
(2) Preparing electrolyte, namely adding sodium silicate, potassium fluoride and potassium hydroxide into 500ml of water respectively, and dissolving; the concentration of the potassium fluoride is 9g/L of sodium silicate, 9g/L of potassium fluoride and 8g/L of potassium hydroxide respectively;
(3) dissolving copper sulfate in water to prepare a copper sulfate solution with the concentration of 0.1 mol/L; dissolving sodium chloropalladate in water to prepare 0.01mol/L sodium chloropalladate solution; EDTA is dissolved in water to prepare 0.5mol/L EDTA solution; respectively adding a proper amount of EDTA into the catalyst precursor salt to form chelate salts of Cu and Pd;
(4) adding a proper amount of the chelate solution prepared in the step (3) into an electrolyte, and uniformly mixing, wherein the final concentrations of Cu salt and Pd salt in the electrolyte are respectively 4 multiplied by 10 -3 mol/L,7×10 -4 mol/L;
(5) Performing liquid nitrogen cooling treatment on the solution obtained in the step (4) to keep the temperature of the electrolyte between 15 and 25 ℃;
(6) the spiral magnesium wire is used as an anode to carry out microplasma electrolytic oxidation treatment, the pulse width is 70 mu s, the pulse number is 285Hz, the pulse current density is 2A/cm < 2 >, and the action time is 1.5min;
(7) and (3) carrying out thermal reduction treatment on the prepared CuPd/MgO alloy nano catalyst under the hydrogen atmosphere, wherein the heating temperature is 420 ℃, the time is 2 hours, and then sealing the bag for preservation after the completion.
Claims (10)
1. Highly ordered Cu 3 The preparation method of the Pd intermetallic compound nano catalyst is characterized by comprising the following steps: mixing copper sulfate and sodium chloropalladate with EDTA chelating agent, respectively, and mixing the two mixtures with electrolyte to obtain copper element and palladium element with concentration of 2×10 respectively -3 -5×10 -3 mol/L,3×10 -4 -8×10 -4 mol/L,The temperature of the electrolyte is kept between 5 ℃ and 25 ℃, metal magnesium wires are used as anodes, microplasma electrolytic oxidation is carried out, the CuPd alloy nano-catalyst is prepared, and the Cu is finally prepared by carrying out thermal reduction treatment in hydrogen atmosphere 3 Pd intermetallic compound nano-catalyst.
2. A highly ordered Cu according to claim 1 3 The preparation process of nanometer Pd intermetallic compound catalyst features that the electrolyte solution is sodium silicate Na as main salt 2 SiO 3 ·9H 2 0, the concentration is 4g/L-9g/L; other components comprise KF and KOH, the concentrations of which are 5-9g/L and 5-8g/L respectively, and the total volume of the electrolyte is 500mL.
3. A highly ordered Cu according to claim 2 3 The preparation method of the Pd intermetallic compound nano catalyst is characterized in that the parameters of the microplasma electrolytic oxidation process are as follows: pulse number 250-400Hz, pulse width 50-80 μs, constant current mode, current setting 0.5-2A/cm 2 The action time is 1-2min.
4. The method according to claim 3, wherein the catalyst precursor salt is prepared by respectively complexing 0.1mol/L of copper sulfate solution and 0.01mol/L of sodium chloropalladate solution with EDTA chelating agent, respectively taking a certain amount of chelated solution, adding the chelated solution into the electrolyte, and uniformly stirring for 5 minutes to complete the mixing of the precursor salt in the electrolyte.
5. The method according to any one of claims 1 to 4, wherein the concentrations of copper element and palladium element in the catalyst precursor in the mixed solution are 2X 10, respectively -3 ,3×10 -4 。
6. The method according to any one of claims 1 to 4, wherein the temperature of the mixed liquor is maintained at 10 to 25 ℃, and the temperature is reduced by using liquid nitrogen.
7. The method according to any one of claims 1 to 4, wherein the metal magnesium wire is sanded 3 times, braided in a spiral shape, and ultrasonically washed in ethanol for 15min, and dried and stored.
8. The method according to any one of claims 1 to 4, wherein the chelating agent EDTA is used at a concentration of 4X 10 -3 -9×10 -3 mol/L。
9. The method according to any one of claims 1 to 4, wherein the catalyst is heated in a hydrogen atmosphere (350 ℃ to 420 ℃) for 2 hours of reduction and is kept in a sealed bag after completion;
the catalyst takes metal magnesium wires as a matrix, and a layer of three-dimensional porous MgO and Cu are attached to the surfaces of the wires 3 Pd nano particles are uniformly loaded on the MgO surface and in the pore canal, and the loading amount of noble metal Pd is 100mg/kg.
10. A Cu as claimed in any one of claims 1 to 4 3 The application of Pd/MgO catalyst in acetylene hydrogenation is characterized in that the catalyst is applied to eliminating acetylene impurity gas in ethylene gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310708581.3A CN116786136A (en) | 2023-06-15 | 2023-06-15 | Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310708581.3A CN116786136A (en) | 2023-06-15 | 2023-06-15 | Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst |
Publications (1)
Publication Number | Publication Date |
---|---|
CN116786136A true CN116786136A (en) | 2023-09-22 |
Family
ID=88039103
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202310708581.3A Pending CN116786136A (en) | 2023-06-15 | 2023-06-15 | Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN116786136A (en) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001000866A (en) * | 1999-06-22 | 2001-01-09 | Asahi Chem Ind Co Ltd | Water treating catalyst composition and water treatment using the catalyst |
US20050178664A1 (en) * | 2004-02-18 | 2005-08-18 | Ilya Ostrovsky | Method of anodizing metallic surfaces and compositions therefore |
JP2013119634A (en) * | 2011-12-06 | 2013-06-17 | Ulvac Japan Ltd | Method of forming oxide film, and oxide film |
WO2018179005A1 (en) * | 2017-03-25 | 2018-10-04 | Jawaharlal Nehru Centre For Advanced Scientific Research | Shape tailored ordered pdcu3 nanoparticle surpassing the activity of state-of-the-art fuel cell catalyst |
CN109289846A (en) * | 2018-10-26 | 2019-02-01 | 东北大学 | A kind of Ru/MgO catalyst and its preparation method and application |
CN111013603A (en) * | 2019-11-11 | 2020-04-17 | 中国科学院金属研究所 | Supported PdCu bimetallic catalyst for acetylene selective hydrogenation reaction and preparation method thereof |
CN113426460A (en) * | 2021-06-23 | 2021-09-24 | 中国科学技术大学 | The structure is carbon-loaded PdCu3Intermetallic compound and preparation method and application thereof |
CN115430429A (en) * | 2022-09-30 | 2022-12-06 | 四川轻化工大学 | Supported efficient ozone oxidation catalytic material and preparation method and application thereof |
CN115532269A (en) * | 2022-10-17 | 2022-12-30 | 北京化工大学 | PdM monatomic alloy catalyst for acetylene selective hydrogenation reaction and preparation method thereof |
-
2023
- 2023-06-15 CN CN202310708581.3A patent/CN116786136A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001000866A (en) * | 1999-06-22 | 2001-01-09 | Asahi Chem Ind Co Ltd | Water treating catalyst composition and water treatment using the catalyst |
US20050178664A1 (en) * | 2004-02-18 | 2005-08-18 | Ilya Ostrovsky | Method of anodizing metallic surfaces and compositions therefore |
JP2013119634A (en) * | 2011-12-06 | 2013-06-17 | Ulvac Japan Ltd | Method of forming oxide film, and oxide film |
WO2018179005A1 (en) * | 2017-03-25 | 2018-10-04 | Jawaharlal Nehru Centre For Advanced Scientific Research | Shape tailored ordered pdcu3 nanoparticle surpassing the activity of state-of-the-art fuel cell catalyst |
CN109289846A (en) * | 2018-10-26 | 2019-02-01 | 东北大学 | A kind of Ru/MgO catalyst and its preparation method and application |
CN111013603A (en) * | 2019-11-11 | 2020-04-17 | 中国科学院金属研究所 | Supported PdCu bimetallic catalyst for acetylene selective hydrogenation reaction and preparation method thereof |
CN113426460A (en) * | 2021-06-23 | 2021-09-24 | 中国科学技术大学 | The structure is carbon-loaded PdCu3Intermetallic compound and preparation method and application thereof |
CN115430429A (en) * | 2022-09-30 | 2022-12-06 | 四川轻化工大学 | Supported efficient ozone oxidation catalytic material and preparation method and application thereof |
CN115532269A (en) * | 2022-10-17 | 2022-12-30 | 北京化工大学 | PdM monatomic alloy catalyst for acetylene selective hydrogenation reaction and preparation method thereof |
Non-Patent Citations (4)
Title |
---|
DINGWANG YUAN等: "Selective hydrogenation of acetylene on Cu–Pd intermetallic compounds and Pd atoms substituted Cu(111) surfaces", 《PHYS. CHEM. CHEM. PHYS.》, vol. 23, no. 14, 9 May 2021 (2021-05-09), pages 8653 - 8660 * |
姚建华等: "《多能场激光复合表面改性技术及其应用》", 30 November 2021, 北京:机械工业出版社, pages: 328 * |
张谷令等: "《应用等离子体物理学》", 30 September 2008, 北京:首都师范大学出版社, pages: 219 * |
郑文娟: "Cu基和Pd基合金催化剂组分及结构对乙炔选择性加氢反应催化性能的影响", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》, no. 02, 15 February 2022 (2022-02-15), pages 016 - 190 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Zhang et al. | Carbon-based material-supported single-atom catalysts for energy conversion | |
Salonen et al. | Sustainable catalysts for water electrolysis: Selected strategies for reduction and replacement of platinum-group metals | |
KR102173226B1 (en) | Catalytic materials and electrodes for oxygen evolution, and systems for electrochemical reaction | |
Yang et al. | TePbPt alloy nanotube as electrocatalyst with enhanced performance towards methanol oxidation reaction | |
Boukil et al. | Enhanced electrocatalytic activity and selectivity of glycerol oxidation triggered by nanoalloyed silver–gold nanocages directly grown on gas diffusion electrodes | |
CN108191009A (en) | The Ag-Pd bimetallic composite electro catalytic cathodes and preparation method and application of polypyrrole modifying | |
JP5664370B2 (en) | Method for producing catalyst fine particles | |
CN112090436B (en) | Nickel-based catalyst, preparation method and application | |
Qiao et al. | Active-site engineering in dealloyed nanoporous catalysts for electrocatalytic water splitting | |
CN109994742B (en) | Ordered porous metal catalyst layer, preparation method thereof and fuel cell | |
Deng et al. | Pt modified NiMoO4-GO/NF nanorods with strong metal-support interaction as efficient bifunctional catalysts for overall water splitting | |
Zheng et al. | Robust FeCoP nanoparticles grown on a rGO-coated Ni foam as an efficient oxygen evolution catalyst for excellent alkaline and seawater electrolysis | |
Xie et al. | Facile surface reconstructions of cobalt–copper phosphide heterostructures enable efficient electrocatalytic glycerol oxidation for energy-saving hydrogen evolution | |
Zhou et al. | Fabrication of amorphous FeCoNiCuMnPx high-entropy phosphide/carbon composites with a heterostructured fusiform morphology for efficient oxygen evolution reaction | |
Liu et al. | Highly dispersed copper-iron nanoalloy enhanced electrocatalytic reduction coupled with plasma oxidation for ammonia synthesis from ubiquitous air and water | |
JP2012035178A (en) | Method for manufacturing catalyst, and catalyst | |
Wen et al. | Reconstruction of FeNi layered dihydroxides by cobalt doping to improve the electrocatalytic activity of oxygen evolution reaction | |
Chen et al. | Constructing abundant interfaces by decorating MoP quantum dots on CoP nanowires to induce electronic structure modulation for enhanced hydrogen evolution reaction | |
Fan et al. | The Promising Seesaw Relationship Between Activity and Stability of Ru‐Based Electrocatalysts for Acid Oxygen Evolution and Proton Exchange Membrane Water Electrolysis | |
CN116786136A (en) | Highly ordered Cu 3 Preparation and application of Pd intermetallic compound nano-catalyst | |
Gao et al. | OER catalyst fabricated with ZIF-67 derived carbon and selectively exsolvated perovskite oxide | |
CN113233514B (en) | Preparation method and application of vesicle phosphate ion functionalized cobalt oxide nano material | |
JP6403046B2 (en) | Method for producing catalyst for fuel cell, catalyst using the same and fuel cell | |
Jiao et al. | On-demand continuous H 2 release by methanol dehydrogenation and reforming via photocatalysis in a membrane reactor | |
Guo et al. | Electrochemical tuning of a Cu 3 P/Ni 2 P hybrid for a promoted hydrogen evolution reaction |
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 |