CN113952983B - A kind of preparation method of paper-supported noble metal nanoparticle catalyst - Google Patents
A kind of preparation method of paper-supported noble metal nanoparticle catalyst Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 67
- 229910000510 noble metal Inorganic materials 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- 239000002082 metal nanoparticle Substances 0.000 title claims abstract description 10
- 238000006356 dehydrogenation reaction Methods 0.000 claims abstract description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 44
- 239000000243 solution Substances 0.000 claims description 37
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 24
- 239000010970 precious metal Substances 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 239000002253 acid Substances 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical class Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 7
- 239000003223 protective agent Substances 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 claims description 7
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical group [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 6
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims description 6
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims description 6
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims description 6
- 239000001632 sodium acetate Substances 0.000 claims description 6
- 235000017281 sodium acetate Nutrition 0.000 claims description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 5
- GBMDVOWEEQVZKZ-UHFFFAOYSA-N methanol;hydrate Chemical compound O.OC GBMDVOWEEQVZKZ-UHFFFAOYSA-N 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 4
- 239000008103 glucose Substances 0.000 claims description 4
- 239000002243 precursor Substances 0.000 claims description 4
- 238000004587 chromatography analysis Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 claims description 3
- 239000012694 precious metal precursor Substances 0.000 claims description 3
- KIDBBTHHMJOMAU-UHFFFAOYSA-N propan-1-ol;hydrate Chemical compound O.CCCO KIDBBTHHMJOMAU-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- AEDZKIACDBYJLQ-UHFFFAOYSA-N ethane-1,2-diol;hydrate Chemical compound O.OCCO AEDZKIACDBYJLQ-UHFFFAOYSA-N 0.000 claims description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052737 gold Inorganic materials 0.000 claims description 2
- 239000010931 gold Substances 0.000 claims description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 2
- 229910052741 iridium Inorganic materials 0.000 claims description 2
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 claims description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims description 2
- 229910052753 mercury Inorganic materials 0.000 claims description 2
- 229910001507 metal halide Inorganic materials 0.000 claims description 2
- 150000005309 metal halides Chemical class 0.000 claims description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N n-Butanol Substances CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 2
- 239000002105 nanoparticle Substances 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 claims description 2
- 239000010948 rhodium Substances 0.000 claims description 2
- 229910052703 rhodium Inorganic materials 0.000 claims description 2
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 2
- 239000012266 salt solution Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 229910052724 xenon Inorganic materials 0.000 claims description 2
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims 1
- 229910002651 NO3 Inorganic materials 0.000 claims 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims 1
- 159000000021 acetate salts Chemical class 0.000 claims 1
- 239000000460 chlorine Substances 0.000 claims 1
- 229910052801 chlorine Inorganic materials 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 239000002638 heterogeneous catalyst Substances 0.000 abstract description 11
- 239000002815 homogeneous catalyst Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 5
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- 238000006722 reduction reaction Methods 0.000 abstract 1
- 238000006555 catalytic reaction Methods 0.000 description 13
- 239000000084 colloidal system Substances 0.000 description 12
- 230000003197 catalytic effect Effects 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
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- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000004642 Polyimide Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000002608 ionic liquid Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 4
- 239000003960 organic solvent Substances 0.000 description 4
- 230000001699 photocatalysis Effects 0.000 description 4
- 229920001721 polyimide Polymers 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- VEUMANXWQDHAJV-UHFFFAOYSA-N 2-[2-[(2-hydroxyphenyl)methylideneamino]ethyliminomethyl]phenol Chemical compound OC1=CC=CC=C1C=NCCN=CC1=CC=CC=C1O VEUMANXWQDHAJV-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 238000007210 heterogeneous catalysis Methods 0.000 description 2
- 238000007172 homogeneous catalysis Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000007146 photocatalysis Methods 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- KTUQUZJOVNIKNZ-UHFFFAOYSA-N butan-1-ol;hydrate Chemical compound O.CCCCO KTUQUZJOVNIKNZ-UHFFFAOYSA-N 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- VZHHNBNSMNNUAD-UHFFFAOYSA-N cobalt 2-[2-[(2-hydroxyphenyl)methylideneamino]ethyliminomethyl]phenol Chemical compound [Co].OC1=CC=CC=C1C=NCCN=CC1=CC=CC=C1O VZHHNBNSMNNUAD-UHFFFAOYSA-N 0.000 description 1
- 238000000366 colloid method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
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- 238000007306 functionalization reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
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- 239000000376 reactant Substances 0.000 description 1
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- 238000013112 stability test Methods 0.000 description 1
- 238000004416 surface enhanced Raman spectroscopy Methods 0.000 description 1
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- 238000001291 vacuum drying Methods 0.000 description 1
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- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
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- 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
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- 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
- B01J35/39—Photocatalytic properties
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
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Abstract
Description
技术领域technical field
本发明属于催化剂材料的合成领域,尤其涉及一种纸负载贵金属纳米粒子催化剂的合成方法。The invention belongs to the field of synthesis of catalyst materials, in particular to a synthesis method of a paper-supported noble metal nanoparticle catalyst.
背景技术Background technique
催化作用与催化剂对于人类社会的发展有着举足轻重的作用。目前,超过90%以上的化学工业过程都离不开催化作用与催化剂。在催化反应中,催化剂与反应物发生作用,改变了反应途径,从而降低了反应的活化能,这是催化剂得以提高反应速率的原因。催化在世界文明发展和人类社会进步中扮演着非常关键的角色。它能够以一种高性价比、高效能、绿色和环保的方式将易得廉价的原材料经化学变化转变为具有高附加值的化工产品和高能量密度燃料等,这些材料不仅关系到人类的衣食住行等,还涉及到现代高科技高新领域,如网络技术、信息传输、生物工程及航空航天和军工等领域,因此催化被称为“现代工业的心脏”。催化剂主要分为三种:多相催化剂、均相催化剂和酶催化剂。多相催化剂由于其易分离,稳定性高等特点被广泛用于工业生产,而均相催化剂和酶催化剂由于成本高,分离困难等缺点难以在工业上得到应用,但是多相催化剂不具备均相催化剂高选择性、高活性的特点。建立多相催化与均相催化/酶催化之间的桥梁,让多相催化剂具有均相催化剂和酶催化剂的优异性能是非常具有挑战性的工作。因此,开发绿色、高效、低成本、高选择性、环保的新型多相催化剂,是化学、化工、催化等学科发展的核心。Catalysis and catalyst play a pivotal role in the development of human society. At present, more than 90% of chemical industrial processes are inseparable from catalysis and catalysts. In the catalytic reaction, the catalyst interacts with the reactants to change the reaction pathway, thereby reducing the activation energy of the reaction, which is the reason why the catalyst can increase the reaction rate. Catalysis plays a very crucial role in the development of world civilization and the progress of human society. It can chemically transform readily available and cheap raw materials into high value-added chemical products and high energy density fuels in a cost-effective, high-efficiency, green and environmentally friendly way. It also involves modern high-tech fields, such as network technology, information transmission, bioengineering, aerospace and military industries, so catalysis is called "the heart of modern industry". There are three main types of catalysts: heterogeneous catalysts, homogeneous catalysts and enzyme catalysts. Heterogeneous catalysts are widely used in industrial production due to their easy separation and high stability, while homogeneous catalysts and enzyme catalysts are difficult to be applied in industry due to their high cost and difficult separation. However, heterogeneous catalysts do not have homogeneous catalysts. High selectivity and high activity. It is very challenging to establish a bridge between heterogeneous catalysis and homogeneous catalysis/enzymatic catalysis, so that heterogeneous catalysts have the excellent performance of homogeneous catalysts and enzymatic catalysts. Therefore, the development of green, high-efficiency, low-cost, high-selectivity, and environmentally friendly new heterogeneous catalysts is the core of the development of chemistry, chemical industry, catalysis and other disciplines.
已知,贵金属催化剂在许多反应中表现出较高的催化活性和选择性。因此贵金属催化剂得到了大量的应用,寻找合适的贵金属载体使贵金属催化剂突破其原有的性能至关重要。纸催化剂可以集多相催化剂的易分离,稳定、均相催化剂的独立单一清晰的活性中心和高选择性,高活性的特点于一体。这是因为在液相化学反应体系中,纸催化剂可以通过形成纸浆的状态而具有均相催化剂的特点,在分离和回收的时候以纸张的状态存在,又能具有多相催化剂的特点。同时纸张催化剂在分离和回收的同时较传统的多相催化剂分离更为简单。因此纸催化剂的制备研究非常重要,甚至有希望建立催化大一统理论。It is known that noble metal catalysts exhibit high catalytic activity and selectivity in many reactions. Therefore, noble metal catalysts have been widely used, and it is very important to find suitable noble metal supports to make noble metal catalysts break through their original performance. Paper catalysts can integrate the characteristics of easy separation of heterogeneous catalysts, independent single clear active centers and high selectivity and high activity of stable and homogeneous catalysts. This is because in the liquid-phase chemical reaction system, the paper catalyst can have the characteristics of a homogeneous catalyst by forming the state of pulp, and exists in the state of paper during separation and recovery, and can also have the characteristics of a heterogeneous catalyst. At the same time, the separation and recovery of the paper catalyst is simpler than the traditional heterogeneous catalyst separation. Therefore, the research on the preparation of paper catalysts is very important, and it is even hopeful to establish a unified theory of catalysis.
综上,当我们使用一些特种纸张,如多孔色谱纸,滤纸等作为催化剂载体,除了可以承载贵金属纳米粒子外,由于其表面具有丰富的羟基,无须官能团化,能够和贵金属纳米粒子良好地结合,同时便宜易得。使用纸作为催化剂载体,可以利用纸的独特相态转变特性,可以轻松且可逆地进行液相和固体相的转变。同时使用胶体法将贵金属胶体化并沉积在纸上,利用纸张表明的羟基吸附贵金属,通过调节保护剂浓度,制备胶体的反应时间等可以调节贵金属的粒径,并制得均一的贵金属纳米粒子,当贵金属/纸催化剂形成纸浆状态时,其结构与性能与均相催化剂甚至酶催化剂类似。In summary, when we use some special papers, such as porous chromatography paper, filter paper, etc., as catalyst carriers, in addition to supporting noble metal nanoparticles, due to the abundant hydroxyl groups on the surface, it does not require functionalization, and can be well combined with noble metal nanoparticles. Also cheap and easy to get. Using paper as a catalyst support can take advantage of the unique phase transition properties of paper, allowing easy and reversible transitions between liquid and solid phases. At the same time, the colloid method is used to colloid and deposit the precious metal on the paper, and the hydroxyl group indicated by the paper is used to adsorb the precious metal, and the particle size of the precious metal can be adjusted by adjusting the concentration of the protective agent and the reaction time of preparing the colloid, and uniform precious metal nanoparticles can be obtained. When the noble metal/paper catalyst is formed into pulp state, its structure and performance are similar to homogeneous catalysts or even enzyme catalysts.
目前对于纸催化剂的制备方法,都存在一些不足:At present, there are some deficiencies in the preparation methods of paper catalysts:
中国专利,申请号:CN201910955378.X,介绍一种具有催化性能和SERS性能的聚酰亚胺复合纸及其制备。使用负载金属纳米粒子的沉析纤维直接进行抄纸;或将负载金属纳米粒子的沉析纤维、聚酰亚胺短切纤维混合经抄纸得到聚酰亚胺复合纸。但是其制备条件较为繁琐,且原料较为昂贵,尤其聚酰亚胺的价格甚至达到了9000-15000元/kg,经济效益不明显。Chinese patent, application number: CN201910955378.X, introduces a polyimide composite paper with catalytic properties and SERS properties and its preparation. Use the metal nanoparticle-loaded precipitating fiber to directly make paper; or mix the metal nanoparticle-loaded precipitating fiber and the polyimide chopped fiber to make a polyimide composite paper. However, the preparation conditions are cumbersome and the raw materials are relatively expensive, especially the price of polyimide has even reached 9000-15000 yuan/kg, and the economic benefit is not obvious.
中国专利,申请号:CN201610569319.5,介绍一种离子液体中M(salen)催化纸催化液化生物质的工艺。在离子液体和M(salen)催化纸存在的条件下,对生物质化合物进行催化液化处理,因为引入了离子液体催化,离子液体难以与纸浆分离使得其催化剂难以循环使用,限制了其应用。Chinese patent, application number: CN201610569319.5, introduces a process of M(salen) catalytic paper catalyzing liquefaction of biomass in ionic liquid. In the presence of ionic liquid and M(salen) catalytic paper, the catalytic liquefaction of biomass compounds is carried out. Because of the introduction of ionic liquid catalysis, the difficult separation of ionic liquid from pulp makes its catalyst difficult to recycle, which limits its application.
中国专利,申请号:CN201510130919.7,介绍一种Co(salen)催化纸在木素氧化中的应用。该专利合成Co配合物并将其与陶瓷纤维、聚丙烯酰胺等混合经抄纸得到催化剂-陶瓷纤维-聚合物复合纸,同样具有工艺繁琐,成本高昂的问题,并且Co的形貌粒径不可控,影响了其性能。Chinese patent, application number: CN201510130919.7, introduces the application of Co(salen) catalyzed paper in lignin oxidation. This patent synthesizes Co complexes and mixes them with ceramic fibers, polyacrylamide, etc. to obtain catalyst-ceramic fiber-polymer composite paper by papermaking. It also has the problems of cumbersome process and high cost, and the morphology and particle size of Co cannot be control, affecting its performance.
中国专利,申请号:CN202110485155.9,介绍一种光催化纸及其制备方法。制备了一种光催化纸用于光催化,尽管其工艺简单,成本低廉,但是仅限于光催化的应用,具有局限性。Chinese patent, application number: CN202110485155.9, introduces a photocatalytic paper and its preparation method. A photocatalytic paper has been prepared for photocatalysis. Although its process is simple and low in cost, it is limited to the application of photocatalysis and has limitations.
中国专利,申请号:CN200420022026.8,介绍一种全棉印花用转移催化纸。该实用新型由纸张及染料层组成,该加工装置包括加压橡胶辊、膨胀平衡辊以及催化浸轧橡胶辊等部件,在被印纸张的表面设有隔离层,背面设有催化剂层,在隔离层上设有或涂有转移催化纸凹版印刷的染料层。是一种环保,绿色的技术,但是工艺较为繁琐,难以实现大规模生产。Chinese patent, application number: CN200420022026.8, introduces a transfer catalytic paper for cotton printing. The utility model is composed of paper and a dye layer. The processing device includes a pressure rubber roller, an expansion balance roller, a catalytic padding rubber roller and other components. An isolation layer is arranged on the surface of the printed paper, and a catalyst layer is arranged on the back. The layer is provided with or coated with a transfer catalyzed paper gravure printed dye layer. It is an environmentally friendly and green technology, but the process is cumbersome and difficult to achieve large-scale production.
发明内容SUMMARY OF THE INVENTION
本发明公开了一种纸负载贵金属纳米粒子催化剂的制备方法,属于催化剂材料的合成领域。本发明旨在提供一种新型的催化剂制备方法,以期沟通多相催化和均相催化,利用纸可以进行可逆相变的特点使其兼具易分离,高活性的特点。The invention discloses a preparation method of a paper-supported noble metal nanoparticle catalyst, which belongs to the field of synthesis of catalyst materials. The present invention aims to provide a novel catalyst preparation method, in order to communicate heterogeneous catalysis and homogeneous catalysis, and to make use of the characteristics of paper that can undergo reversible phase transition, so that it has the characteristics of easy separation and high activity.
本发明的技术方案如下:The technical scheme of the present invention is as follows:
使用水或醇类有机溶剂溶解贵金属的前体盐,得到贵金属前体盐溶液的浓度为0.001-0.1mol/L,搅拌使贵金属的前体盐完全溶解,然后加入保护剂,控制保护剂在体系中的溶度为0.01-0.1mol/L,搅拌溶解后,然后将溶液于100-140℃温度条件下加热5-120分钟,制得贵金属胶体溶液。然后将纸加入贵金属胶体溶液中,调节pH小于3再加热至100-140℃,恒温5-120分钟;此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤至中性,在60-100℃温度条件下干燥6-12小时,制得纸负载贵金属纳米粒子催化剂;其中贵金属占纸的质量百分比为0.01-10wt%。水或醇类有机溶剂,醇类有机溶剂是水-甲醇、水-乙醇、水-乙二醇、水-正丙醇或水-正丁醇,其中有机溶剂的体积分数不大于100%。所述的贵金属为铂、钯、金、铑、铱等贵金属中的一种或两种以上混合。所述的金属盐溶液是硝酸盐、氯化盐、醋酸盐、氯盐酸中的一种或两种以上混合。所述的保护剂是无机盐类如醋酸钠,聚合物如聚乙烯吡咯烷酮等。作为催化剂载体的纸是色谱纸、滤纸、复写纸等具有纤维或纸状结构的纸系材料。使用外部灯或电磁波以功率为0-2w·m-2照射纸12-100小时,还可以调节纸的理化性能。所述的外部灯源是汞灯、氙灯、金卤灯等常见灯源中的一种或两种以上组合。所述的电磁波是可见光、紫外线、红外线、X射线等不可见光的一种或两种以上组合。Use water or alcoholic organic solvent to dissolve the precursor salt of the precious metal to obtain a solution of the precious metal precursor salt with a concentration of 0.001-0.1mol/L, stir to completely dissolve the precursor salt of the precious metal, and then add a protective agent to control the protective agent in the system. The solubility of the solution is 0.01-0.1 mol/L. After stirring and dissolving, the solution is heated at a temperature of 100-140° C. for 5-120 minutes to obtain a precious metal colloid solution. Then add the paper to the precious metal colloid solution, adjust the pH to less than 3, then heat to 100-140°C, and keep the constant temperature for 5-120 minutes; at this time, the solution is in a pulp state, then cooled to room temperature, filtered and washed until neutral, at 60-100 Drying at a temperature of ℃ for 6-12 hours to prepare a paper-supported noble metal nanoparticle catalyst; wherein the weight percentage of the noble metal in the paper is 0.01-10 wt %. Water or alcohol organic solvent, alcohol organic solvent is water-methanol, water-ethanol, water-ethylene glycol, water-n-propanol or water-n-butanol, wherein the volume fraction of organic solvent is not more than 100%. The precious metal is one or a mixture of two or more precious metals such as platinum, palladium, gold, rhodium and iridium. The metal salt solution is a mixture of one or more of nitrates, chlorides, acetates and chlorohydrochloric acid. The protective agents are inorganic salts such as sodium acetate, polymers such as polyvinylpyrrolidone and the like. The paper used as the catalyst carrier is a paper-based material having a fibrous or paper-like structure, such as chromatography paper, filter paper, and carbon paper. The physical and chemical properties of the paper can also be adjusted by irradiating the paper with an external lamp or electromagnetic wave at a power of 0-2w·m -2 for 12-100 hours. The external light source is one or a combination of two or more common light sources such as mercury lamps, xenon lamps, and metal halide lamps. The electromagnetic wave is one or more combinations of visible light, ultraviolet light, infrared light, X-ray and other invisible light.
本发明与已知的纸催化剂制备技术相比,具有以下优点:Compared with the known paper catalyst preparation technology, the present invention has the following advantages:
1、无须使用陶瓷纤维,大量高分子聚合物等昂贵的材料,成本低廉。1. There is no need to use ceramic fibers, a large number of high molecular polymers and other expensive materials, and the cost is low.
2、无须进行抄纸等繁琐的纸张工艺技术。2. There is no need to carry out tedious paper technology such as paper making.
3、不局限于光电催化,可用于热催化领域,具有潜在的工业应用前景。3. Not limited to photoelectric catalysis, it can be used in the field of thermal catalysis and has potential industrial application prospects.
4、进行催化反应时,催化剂在溶液中以纸浆的状态存在,使得其活性中心均一,理论上其催化性能可以媲美均相催化剂甚至酶催化剂。反应后催化剂可以通过简单的分离手段重新形成纸张,具有多相催化剂可循环的特点。4. During the catalytic reaction, the catalyst exists in the state of pulp in the solution, so that its active center is uniform. In theory, its catalytic performance can be comparable to that of a homogeneous catalyst or even an enzyme catalyst. After the reaction, the catalyst can be re-formed into paper by a simple separation method, and the heterogeneous catalyst can be recycled.
5、廉价易得,同时由于其表面富含的羟基,无须进行载体预处理。兼具均相催化剂,多相催化剂的优势,甚至有希望建立催化大一统理论。5. It is cheap and easy to obtain, and at the same time, due to the abundant hydroxyl groups on its surface, no carrier pretreatment is required. It combines the advantages of homogeneous catalysts and heterogeneous catalysts, and even has the hope of establishing a unified theory of catalysis.
具体实施方式Detailed ways
为了进一步说明本发明,列举以下实施例,但它并不限制各附加权利要求所定义的发明范围。In order to further illustrate the present invention, the following examples are given without limiting the scope of the invention as defined by the appended claims.
实施例1:取一定量氯铂酸溶解于10mL乙二醇溶液中,使其浓度为0.0025mol/L,充分搅拌至完全溶解,然后加入一定量醋酸钠,使醋酸钠的浓度为0.04mol/L,搅拌溶解后于120度下加热20分钟,制得Pt胶体溶液。然后将8张色谱纸(1cm×1cm,97.5mg)加入胶体溶液,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤5次,在80度下干燥12小时,制得Pt/纸催化剂,其中贵金属占载体的质量百分比为5wt%。Embodiment 1: get a certain amount of chloroplatinic acid and dissolve it in 10mL ethylene glycol solution, make its concentration be 0.0025mol/L, fully stir until completely dissolved, then add a certain amount of sodium acetate, so that the concentration of sodium acetate is 0.04mol/L. L. After stirring and dissolving, heat at 120 degrees for 20 minutes to obtain a Pt colloidal solution. Then, 8 sheets of chromatographic paper (1cm×1cm, 97.5mg) were added to the colloid solution, and the acid-base environment was adjusted with dilute hydrochloric acid to make the pH less than 3, and then heated to 120 degrees and kept at a constant temperature for 60 minutes. At this time, the solution was in pulp state, then cooled to room temperature, filtered and washed for 5 times, and dried at 80 degrees for 12 hours to obtain a Pt/paper catalyst, wherein the mass percentage of noble metal in the carrier was 5wt%.
实施例2:取一定量氯铂酸溶解于10mL乙二醇溶液中,使其浓度为0.0025mol/L,充分搅拌至完全溶解,然后加入一定量醋酸钠,使醋酸钠的浓度为0.04mol/L,搅拌溶解后于120度下加热20分钟,制得Pt胶体溶液。然后将97.5mg活性炭加入胶体,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。过滤并洗涤5次,在80度下干燥12小时制得Pt/活性炭催化剂,其中贵金属占载体的质量百分比为5wt%。Embodiment 2: get a certain amount of chloroplatinic acid and dissolve it in 10mL of ethylene glycol solution, make its concentration be 0.0025mol/L, fully stir until completely dissolved, then add a certain amount of sodium acetate, so that the concentration of sodium acetate is 0.04mol/L. L. After stirring and dissolving, heat at 120 degrees for 20 minutes to obtain a Pt colloidal solution. Then, 97.5 mg of activated carbon was added to the colloid, and the acid-base environment was adjusted to pH less than 3 with dilute hydrochloric acid, and then heated to 120 degrees for 60 minutes at a constant temperature. Filtration and washing 5 times, drying at 80 degrees for 12 hours to obtain a Pt/activated carbon catalyst, wherein the mass percentage of noble metal in the carrier is 5 wt%.
实施例3:使用紫外光照射色谱纸:采用UVA-340型紫外灯管,紫外光波长选择340nm;辐照度为0.76w·m-2;温度为(30±3)℃;湿度不控制;直接照射纸张正面12小时后照射纸张背面12小时。随后按照实施例1的方法制备催化剂。记为Pt/L纸催化剂。Embodiment 3: use ultraviolet light to irradiate chromatographic paper: use UVA-340 type ultraviolet lamp tube, ultraviolet light wavelength selection 340nm; irradiance is 0.76w m -2 ; temperature is (30 ± 3) ℃; humidity is not controlled; Directly irradiate the front of the paper for 12 hours and then irradiate the back of the paper for 12 hours. The catalyst was then prepared according to the method of Example 1. Denoted as Pt/L paper catalyst.
实施例4:取50mL甲醇-水溶液,其中醇与水的比例为1:1,加入0.15g聚乙烯吡咯烷酮,加入一定量氯铂酸,使氯铂酸浓度为0.0005ml/L,搅拌溶解后于120度下加热180分钟,制得Pt胶体溶液。然后将8张色谱纸(1cm×1cm,97.5mg)加入胶体溶液,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤5次,在80度下干燥12小时,制得Pt/纸催化剂-4,其中贵金属占载体的质量百分比为5wt%。Example 4: take 50mL methanol-water solution, wherein the ratio of alcohol to water is 1:1, add 0.15g polyvinylpyrrolidone, add a certain amount of chloroplatinic acid, make the concentration of chloroplatinic acid 0.0005ml/L, stir and dissolve in Heating at 120 degrees for 180 minutes to obtain a Pt colloidal solution. Then, 8 sheets of chromatographic paper (1cm×1cm, 97.5mg) were added to the colloid solution, and the acid-base environment was adjusted with dilute hydrochloric acid to make the pH less than 3, and then heated to 120 degrees and kept at a constant temperature for 60 minutes. At this time, the solution was in pulp state, then cooled to room temperature, filtered and washed for 5 times, and dried at 80 degrees for 12 hours to obtain Pt/paper catalyst-4, in which the mass percentage of precious metals in the carrier was 5wt%.
实施例5:取50mL乙醇-水溶液,其中醇与水的比例为1:1,加入0.15g聚乙烯吡咯烷酮,加入一定量氯铂酸,使氯铂酸浓度为0.0005ml/L,搅拌溶解后于120度下加热120分钟,制得Pt胶体溶液。然后将8张色谱纸(1cm×1cm,97.5mg)加入胶体溶液,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤5次,在80度下干燥12小时,制得Pt/纸催化剂-5,其中贵金属占载体的质量百分比为5wt%。Embodiment 5: take 50mL ethanol-water solution, wherein the ratio of alcohol and water is 1:1, add 0.15g polyvinylpyrrolidone, add a certain amount of chloroplatinic acid, make the concentration of chloroplatinic acid be 0.0005ml/L, stir and dissolve in Heat at 120 degrees for 120 minutes to obtain a Pt colloidal solution. Then, 8 sheets of chromatographic paper (1cm×1cm, 97.5mg) were added to the colloid solution, and the acid-base environment was adjusted with dilute hydrochloric acid to make the pH less than 3, and then heated to 120 degrees and kept at a constant temperature for 60 minutes. At this time, the solution was in pulp state, then cooled to room temperature, filtered and washed for 5 times, and dried at 80 degrees for 12 hours to obtain Pt/paper catalyst-5, wherein the mass percentage of noble metal in the carrier was 5wt%.
实施例6:取50mL正丙醇-水溶液,其中醇与水的比例为1:1,加入0.146g聚乙烯吡咯烷酮,加入一定量氯铂酸,使氯铂酸浓度为0.0005ml/L,搅拌溶解后于120度下加热120分钟,制得Pt胶体溶液。然后将8张色谱纸(1cm×1cm,97.5mg)加入胶体溶液,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤5次,在80度下干燥12小时,制得Pt/纸催化剂-6,其中贵金属占载体的质量百分比为5wt%。Embodiment 6: take 50mL n-propanol-water solution, wherein the ratio of alcohol to water is 1:1, add 0.146g polyvinylpyrrolidone, add a certain amount of chloroplatinic acid, make the concentration of chloroplatinic acid be 0.0005ml/L, stir and dissolve After heating at 120 degrees for 120 minutes, a Pt colloid solution was obtained. Then, 8 sheets of chromatographic paper (1cm×1cm, 97.5mg) were added to the colloid solution, and the acid-base environment was adjusted with dilute hydrochloric acid to make the pH less than 3, and then heated to 120 degrees and kept at a constant temperature for 60 minutes. At this time, the solution was in pulp state, then cooled to room temperature, filtered and washed for 5 times, and dried at 80 degrees for 12 hours to obtain Pt/paper catalyst-6, wherein the mass percentage of noble metal in the carrier was 5wt%.
实施例7:取50mL正丁醇-水溶液,其中醇与水的比例为1:1,加入0.15g聚乙烯吡咯烷酮,加入一定量氯铂酸,使氯铂酸浓度为0.0005ml/L,搅拌溶解后于120度下加热120分钟,制得Pt胶体溶液。然后将8张色谱纸(1cm×1cm,97.5mg)加入胶体溶液,使用稀盐酸调节酸碱环境至pH小于3,再加热至120度,恒温60分钟。此时溶液为纸浆状态,之后冷却至室温,过滤并洗涤5次,在80度下干燥12小时,制得Pt/纸催化剂-7,其中贵金属占载体的质量百分比为5wt%。Embodiment 7: take 50mL n-butanol-water solution, wherein the ratio of alcohol and water is 1:1, add 0.15g polyvinylpyrrolidone, add a certain amount of chloroplatinic acid, make the concentration of chloroplatinic acid be 0.0005ml/L, stir and dissolve After heating at 120 degrees for 120 minutes, a Pt colloid solution was obtained. Then, 8 sheets of chromatographic paper (1cm×1cm, 97.5mg) were added to the colloid solution, and the acid-base environment was adjusted with dilute hydrochloric acid to make the pH less than 3, and then heated to 120 degrees and kept at a constant temperature for 60 minutes. At this time, the solution was in pulp state, then cooled to room temperature, filtered and washed for 5 times, and dried at 80 degrees for 12 hours to obtain Pt/paper catalyst-7, wherein the mass percentage of precious metals in the carrier was 5wt%.
实施例8:对比Pt/纸催化剂与Pt/活性炭催化剂的性能。将实施例1-实施例3制备的催化剂用于催化脱氢氧化葡萄糖反应。首先将0.4324g葡萄糖溶解于40mL水-甲醇溶液中,水的体积分数为40%,加入0.7405gKOH,用Ar气氛置换反应器中的气体,反应温度30℃,反应压力为常压,脱氢氧化催化剂为Pt/活性炭,Pt/纸,Pt/L纸催化剂,收集产物气体使用气相色谱分析,检测器为热导检测器,色谱柱为TDX-01,气相色谱显示氢气的产生,反应结果见表1。Example 8: Comparison of the performance of Pt/paper catalyst and Pt/activated carbon catalyst. The catalysts prepared in Example 1-Example 3 were used to catalyze the reaction of dehydrogenation of glucose. Firstly, 0.4324g glucose was dissolved in 40mL water-methanol solution, the volume fraction of water was 40%, 0.7405g KOH was added, the gas in the reactor was replaced with Ar atmosphere, the reaction temperature was 30℃, the reaction pressure was normal pressure, and the dehydrogenation was carried out. The catalyst is Pt/activated carbon, Pt/paper, Pt/L paper catalyst, the product gas is collected and analyzed by gas chromatography, the detector is a thermal conductivity detector, the chromatographic column is TDX-01, the gas chromatography shows the generation of hydrogen, and the reaction results are shown in the table 1.
实施例9:对比不同溶剂制备的Pt/纸催化剂性能。将实施例4-实施例7制备的催化剂用于硝基苯还原加氢反应。首先将5mmol硝基苯溶解于20mL环己烷溶液中,加氢还原催化剂为Pd/纸催化剂4-7,催化剂加入量为20mg,随后将溶液转移到釜式反应器中。使用氢气将反应器内空气置换5次,将反应器在700rpm转速下加热到60度,然后充入设定压力为1Mpa的氢气。用气相色谱分析产物组成成分,反应结果见表2。Example 9: Comparison of the performance of Pt/paper catalysts prepared with different solvents. The catalysts prepared in Examples 4 to 7 were used in the reductive hydrogenation of nitrobenzene. First, 5 mmol of nitrobenzene was dissolved in 20 mL of cyclohexane solution, the hydrogenation reduction catalyst was Pd/paper catalyst 4-7, and the amount of catalyst added was 20 mg, and then the solution was transferred to a tank reactor. The air in the reactor was replaced 5 times with hydrogen, and the reactor was heated to 60 degrees at 700 rpm, and then filled with hydrogen with a set pressure of 1 Mpa. The product composition was analyzed by gas chromatography, and the reaction results were shown in Table 2.
实施例10:催化剂循环利用的考评。将实施例8中,反应4h后的三个催化剂离心,真空干燥回收。将0.4324g葡萄糖溶解于40mL水-甲醇溶液中,水的体积分数为40%,加入0.7405gKOH,用Ar气氛置换反应器中的气体,反应温度30℃,反应压力为常压,脱氢氧化催化剂为Pt/活性炭,Pt/纸,Pt/L纸催化剂,收集产物气体使用气相色谱分析,检测器为热导检测器,色谱柱为TDX-01,气相色谱显示氢气的产生,反应结果见表1。催化剂循环利用5次,反应结果见表3。Example 10: Evaluation of catalyst recycling. In Example 8, the three catalysts after the reaction for 4 h were centrifuged and recovered by vacuum drying. Dissolve 0.4324g glucose in 40mL water-methanol solution, the volume fraction of water is 40%, add 0.7405g KOH, replace the gas in the reactor with Ar atmosphere, the reaction temperature is 30 ℃, the reaction pressure is normal pressure, deoxidation catalyst It is Pt/activated carbon, Pt/paper, and Pt/L paper catalyst. The product gas is collected and analyzed by gas chromatography. The detector is a thermal conductivity detector, and the chromatographic column is TDX-01. The gas chromatography shows the generation of hydrogen. The reaction results are shown in Table 1. . The catalyst was recycled 5 times, and the reaction results are shown in Table 3.
表1实施例1-3催化剂的性能评价Table 1 Performance Evaluation of Catalysts of Examples 1-3
表2实施例4-7催化剂的性能评价Table 2 Performance Evaluation of Catalysts of Examples 4-7
表3催化剂稳定性测试Table 3 Catalyst stability test
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CN1864854A (en) * | 2006-06-12 | 2006-11-22 | 贵研铂业股份有限公司 | Synthesis of nano noble metal hydrosol and preparation of carbon supported noble metal catalyst |
CN100428989C (en) * | 2006-09-06 | 2008-10-29 | 大连理工大学 | A method for preparing supported nanometer Pd/C catalyst by colloidal solution |
CN105457629A (en) * | 2015-12-11 | 2016-04-06 | 上海源由纳米科技有限公司 | Load type nano precious metal catalyst and preparation method and application thereof |
US11788228B2 (en) * | 2017-02-13 | 2023-10-17 | Cmblu Energy Ag | Methods for processing lignocellulosic material |
CN107011150B (en) * | 2017-05-08 | 2020-09-11 | 大连理工大学 | Method for preparing gluconic acid/gluconate and hydrogen by catalytic dehydrogenation of glucose under mild condition |
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