CN111359670A - 一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 - Google Patents
一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 Download PDFInfo
- Publication number
- CN111359670A CN111359670A CN202010161924.5A CN202010161924A CN111359670A CN 111359670 A CN111359670 A CN 111359670A CN 202010161924 A CN202010161924 A CN 202010161924A CN 111359670 A CN111359670 A CN 111359670A
- Authority
- CN
- China
- Prior art keywords
- mil
- catalyst
- reaction
- alloy
- palladium
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 52
- 229910002710 Au-Pd Inorganic materials 0.000 title claims abstract description 44
- 239000013178 MIL-101(Cr) Substances 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 13
- 239000002105 nanoparticle Substances 0.000 claims abstract description 19
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- 235000008109 Thuja occidentalis Nutrition 0.000 claims abstract description 15
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 14
- 239000000956 alloy Substances 0.000 claims abstract description 14
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 12
- 230000001699 photocatalysis Effects 0.000 claims abstract description 12
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 claims abstract description 9
- 230000003647 oxidation Effects 0.000 claims abstract description 8
- 239000007791 liquid phase Substances 0.000 claims abstract description 3
- 238000010438 heat treatment Methods 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000010931 gold Substances 0.000 claims description 17
- 241000218636 Thuja Species 0.000 claims description 14
- 229910052737 gold Inorganic materials 0.000 claims description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- 239000008367 deionised water Substances 0.000 claims description 11
- 229910021641 deionized water Inorganic materials 0.000 claims description 11
- 238000001035 drying Methods 0.000 claims description 11
- 239000012696 Pd precursors Substances 0.000 claims description 10
- 239000000284 extract Substances 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical group [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 9
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 8
- 239000002243 precursor Substances 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 7
- GPNDARIEYHPYAY-UHFFFAOYSA-N palladium(ii) nitrate Chemical compound [Pd+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O GPNDARIEYHPYAY-UHFFFAOYSA-N 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- GPNNOCMCNFXRAO-UHFFFAOYSA-N 2-aminoterephthalic acid Chemical compound NC1=CC(C(O)=O)=CC=C1C(O)=O GPNNOCMCNFXRAO-UHFFFAOYSA-N 0.000 claims description 5
- 240000002924 Platycladus orientalis Species 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 4
- 239000012265 solid product Substances 0.000 claims description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-dimethylformamide Substances CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000012295 chemical reaction liquid Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000011068 loading method Methods 0.000 claims description 3
- 229910001507 metal halide Inorganic materials 0.000 claims description 3
- 150000005309 metal halides Chemical class 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 238000013032 photocatalytic reaction Methods 0.000 claims description 3
- 239000003755 preservative agent Substances 0.000 claims description 3
- 230000002335 preservative effect Effects 0.000 claims description 3
- 238000007865 diluting Methods 0.000 claims description 2
- 239000012065 filter cake Substances 0.000 claims description 2
- 239000000706 filtrate Substances 0.000 claims description 2
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical group Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 claims description 2
- WVDDGKGOMKODPV-ZQBYOMGUSA-N phenyl(114C)methanol Chemical compound O[14CH2]C1=CC=CC=C1 WVDDGKGOMKODPV-ZQBYOMGUSA-N 0.000 claims description 2
- 239000000047 product Substances 0.000 claims description 2
- 238000010992 reflux Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims 1
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 abstract description 24
- 235000019445 benzyl alcohol Nutrition 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 7
- 238000007146 photocatalysis Methods 0.000 abstract description 3
- 240000003243 Thuja occidentalis Species 0.000 abstract 1
- 239000007864 aqueous solution Substances 0.000 description 11
- 239000000243 solution Substances 0.000 description 10
- 238000006555 catalytic reaction Methods 0.000 description 9
- 239000013177 MIL-101 Substances 0.000 description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 7
- 239000012621 metal-organic framework Substances 0.000 description 6
- 238000001291 vacuum drying Methods 0.000 description 6
- 238000011156 evaluation Methods 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- 229910052763 palladium Inorganic materials 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000002082 metal nanoparticle Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910001020 Au alloy Inorganic materials 0.000 description 1
- 230000010718 Oxidation Activity Effects 0.000 description 1
- 229910001252 Pd alloy Inorganic materials 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 241000902900 cellular organisms Species 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000012377 drug delivery Methods 0.000 description 1
- 238000007210 heterogeneous catalysis Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000013110 organic ligand Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000002940 palladium Chemical class 0.000 description 1
- 239000013354 porous framework Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Images
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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/28—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of the platinum group metals, iron group metals or copper
-
- 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
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1691—Coordination polymers, e.g. metal-organic frameworks [MOF]
-
- 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
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
-
- 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
- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
- B01J35/23—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/37—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of >C—O—functional groups to >C=O groups
- C07C45/38—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of >C—O—functional groups to >C=O groups being a primary hydroxyl group
-
- 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
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/70—Oxidation reactions, e.g. epoxidation, (di)hydroxylation, dehydrogenation and analogues
- B01J2231/76—Dehydrogenation
- B01J2231/763—Dehydrogenation of -CH-XH (X= O, NH/N, S) to -C=X or -CX triple bond species
-
- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0213—Complexes without C-metal linkages
-
- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/60—Complexes comprising metals of Group VI (VIA or VIB) as the central metal
- B01J2531/62—Chromium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明提供了一种Au‑Pd/NH2‑MIL‑101(Cr)催化剂及其制备方法,以及在光催化苯甲醇无溶剂液相氧化制备苯甲醛的反应中的应用;本发明首次将侧柏还原制备的Au‑Pd合金纳米颗粒负载于NH2‑MIL‑101(Cr)材料上,成功制备出Au‑Pd合金负载型NH2‑MIL‑101(Cr)催化剂,与现有技术相比,本发明制备的催化剂表现出更优异的光催化稳定性能。
Description
技术领域
本发明涉及一种Au-Pd合金催化剂,尤其是涉及一种用于光催化苯甲醇氧化制备苯甲醛的 Au-Pd/NH2-MIL-101(Cr)催化剂及其制备方法。
背景技术
金属有机骨架材料(MOFs)是一种由金属离子和有机配体组成的新型多孔骨架材料。金属有机骨架(MOF)复合材料作为一种新型功能材料正在迅速发展,广泛应用于气体吸附、分离与储存、催化、气体传感、药物转运等领域(Journal of Chromatography A,2018,1574)。MOF材料种类繁多,而MIL-101(Cr)在催化氧化反应中表现出优异的性能。具有比表面积大、孔隙率高、热稳定性好、水稳定性好、有机溶剂稳定性好等优点。这些优异的性能使其在多相催化领域具有良好的应用前景,并得到了广泛的研究。
而贵金属Au和Pd拥有着的特殊的物理化学性质,使其在石化工业中起到有效的催化氧化作用(Journal of Physical Chemistry C,2010,13362)。随着MOFs的发展,Au和Pd的纳米粒子因为具有较高的表面积,而被证明其有着很好的氧化活性,使得负载Au/Pd催化剂成为催化领域研究的重点。
目前贵金属负载型催化剂在制备过程中,贵金属纳米颗粒容易发生团聚而导致催化剂失去催化性能,其次催化剂在使用过程中贵金属纳米颗粒可能容易脱落,而导致催化剂的稳定性能下降。本发明将Au、Pd合金纳米颗粒负载于MIL-101(Cr)材料内,并用于光催化苯甲醇氧化。MIL-101(Cr) 材料可以提供有限的孔道空间,防止在催化剂的制备过程中金属颗粒的团聚,以及催化剂在使用过程中阻止贵金属纳米颗粒的流失。
发明内容
本发明旨在提供一种用于光催化苯甲醇氧化制备苯甲醛的Au-Pd/NH2-MIL-101(Cr)催化剂及其制备方法。
本发明的技术方案如下:
一种Au-Pd/NH2-MIL-101(Cr)催化剂,按如下方法制备得到:
(1)NH2-MIL-101(Cr)的制备:将Cr(NO)3·9H2O、2-氨基对苯二甲酸、碱液混合均匀,升温至100~200℃反应10~24h,之后反应液经后处理,得到NH2-MIL-101(Cr);
所述Cr(NO)3·9H2O和2-氨基对苯二甲酸的质量比为1:0.3~3;
所述碱液由碱性物质溶于水而得,所述碱性物质例如氢氧化钠,所述碱液的浓度为0.1~1M,碱液的体积用量以Cr(NO)3·9H2O的质量计为15~20mL/g;
所述后处理的方法为:反应结束后,待反应液冷却至室温(20~30℃),离心(7000rpm)收集固体产物,分别用水、DMF、甲醇洗涤,100℃下干燥过夜,得到NH2-MIL-101(Cr);
(2)Au-Pd双金属纳米颗粒的制备:将侧柏(学名:Platycladus orientalis)提取液用去离子水稀释后,加入钯前驱体溶液和金前驱体溶液,升温至60~90℃反应0.5~4h,得到Au-Pd双金属纳米颗粒溶胶;
所述侧柏提取液的制备方法为:取侧柏粉按料液质量比1:100与去离子水混合均匀,用保鲜膜密封,于30~100℃下搅拌0.5~4h,之后过滤,收集滤液即为侧柏提取液;
所述钯前驱体与金前驱体的物质的量之比为1:0.1~10,优选1:0.5~1,所述钯前驱体溶液的浓度为0.01~0.5M,所述金前驱体溶液的浓度为0.01~0.5M,所述钯前驱体为可溶性钯盐,例如氯化钯、硝酸钯等,所述金前驱体例如氯金酸等;
所述侧柏提取液的体积用量以钯前驱体的物质的量计为500~2500mL/mmol;
(3)Au-Pd/NH2-MIL-101(Cr)催化剂的制备:将步骤(1)制备的NH2-MIL-101(Cr)加入步骤(2) 制备的Au-Pd双金属纳米颗粒溶胶中,于60~90℃下搅拌0.5~4h,之后过滤,滤饼于60~100℃下真空干燥,得到粉末状的Au-Pd/NH2-MIL-101(Cr)催化剂;
本发明制备的催化剂中Au-Pd双金属纳米颗粒的负载量在0.05~6wt%,优选2~4wt%。
本发明所述Au-Pd/NH2-MIL-101(Cr)催化剂可用于光催化苯甲醇无溶剂液相氧化制备苯甲醛的反应中,具体应用的方法为:
将所述催化剂加入装有苯甲醇的反应瓶中,90℃下预热5min并回流,以90mL/min的速度通入氧气,打开150W的金卤灯光源照射反应瓶进行光催化反应,反应结束后,获得含苯甲醛的反应液,经分离纯化,获得氧化产物苯甲醛。
本发明首次将侧柏还原制备的Au-Pd合金纳米颗粒负载于NH2-MIL-101(Cr)材料上,成功制备出Au-Pd合金负载型NH2-MIL-101(Cr)催化剂。与现有技术相比,本发明制备的催化剂表现出更优异的光催化稳定性能。
附图说明
图1为实施例3制备的Au-Pd/NH2-MIL-101(Cr)催化剂的TEM图。
具体实施方式
下面通过具体实施例对本发明作进一步说明,但本发明的保护范围并不仅限于此。
实施例1
将3.2g Cr(NO)3·9H2O和1.44g 2-氨基对苯二甲酸缓慢加入到60mL含有0.8克NaOH的水溶液中。然后将在室温下搅拌30min的混合物转移到100mL水热反应釜中并在150℃下保持12h。自然冷却后,通过在7000rpm下离心收集所得混合物。将得到的绿色粉末分别用水,DMF和甲醇洗涤数次,并在100℃下干燥过夜。获得活化的NH2-MIL-101(Cr)。
取侧柏粉2g,去离子水200mL,置于250mL锥形瓶中,用保鲜膜封好,置于30℃油浴中加热搅拌。充分搅拌2小时后,停止加热搅拌,取出锥形烧瓶,用循环水多用途真空泵对溶液进行真空过滤得到透明土黄色侧柏提取液。取30mL的去离子水和30mL的侧柏提取液混合,然后加入190微升浓度为0.075M的硝酸钯水溶液和156微升浓度为0.049M的氯金酸水溶液,置于油浴90℃加热和搅拌,1h后即可得到Au-Pd双金属纳米颗粒溶胶。
向Au-Pd双金属纳米颗粒溶胶中加入0.3g已制备好的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Au-Pd/MIL-101催化剂A。
催化剂A用于光催化苯甲醇氧化反应,50mL三口烧瓶中加入0.1g催化剂A,并加入10mL苯甲醇,之后将三口烧瓶置于90℃油浴锅中预热5min并回流,之后通入90mL/min的氧气,打开150W的金卤灯光源开始光催化反应,反应4h后,取样分析。催化反应结果见表1。
实施例2
取30mL的去离子水和30mL实施例1中制备的侧柏提取液混合,然后加入380微升浓度为0.075 M的硝酸钯水溶液和312微升浓度为0.049M的氯金酸水溶液,置于油浴90℃加热和搅拌,1h后即可得到Au-Pd双金属纳米颗粒溶胶。
向溶胶中加入放入0.3g实施例1中制备的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Au-Pd/MIL-101催化剂B。催化剂评价条件同实施例1,催化反应结果见表1。
实施例3
取30mL的去离子水和30mL实施例1中制备的侧柏提取液混合,然后加入570微升浓度为0.075 M的硝酸钯水溶液和468微升浓度为0.049M的氯金酸水溶液,置于油浴90℃加热和搅拌,1h后即可得到Au-Pd双金属纳米颗粒溶胶。
向溶胶中加入放入0.3g实施例1中制备的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Au-Pd/MIL-101催化剂C。催化剂评价条件同实施例1,催化反应结果见表1。
实施例4
取30mL的去离子水和30mL实施例1中制备的侧柏提取液混合,然后加入760微升浓度为0.075 M的硝酸钯水溶液和624微升浓度为0.049M的氯金酸水溶液,置于油浴90℃加热和搅拌,1h后即可得到Au-Pd双金属纳米颗粒溶胶。
向溶胶中加入放入0.3g实施例1中制备的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Au-Pd/MIL-101催化剂D。催化剂评价条件同实施例1,催化反应结果见表1。
实施例5
取30mL的去离子水和30mL实施例1中制备的侧柏提取液混合,然后加入312微升浓度为0.049 M的氯金酸水溶液,置于油浴90℃加热和搅拌,1h后即可得到Au纳米颗粒溶胶。
向溶胶中加入放入0.3g实施例1中制备的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Au/MIL-101催化剂E。催化剂评价条件同实施例1,催化反应结果见表1。
实施例6
取30mL的去离子水和30mL实施例1中制备的侧柏提取液混合,然后加入380微升浓度为0.075 M的硝酸钯水溶液,置在油浴90℃加热和搅拌,1h后即可得到Pd纳米颗粒溶胶。
向溶胶中加入放入0.3g实施例1中制备的NH2-MIL-101(Cr)载体,继续加热搅拌1小时,过滤,并置于60℃真空干燥箱内烘干。即可得到粉末状的Pd/MIL-101催化剂E。催化剂评价条件同实施例1,催化反应结果见表1。
表1 Au-Pd/MIL-101催化剂光催化苯甲醇氧化反应性能
结论:相比较单金属Au和Pd催化剂,Au-Pd合金双金属催化的光催化性能得到显著提升,其中Au和Pd负载量都为1.5wt%,合金催化剂达到最佳的光催化性能。
Claims (9)
1.一种Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,按如下方法制备得到:
(1)NH2-MIL-101(Cr)的制备:将Cr(NO)3·9H2O、2-氨基对苯二甲酸、碱液混合均匀,升温至100~200℃反应10~24h,之后反应液经后处理,得到NH2-MIL-101(Cr);
所述Cr(NO)3·9H2O和2-氨基对苯二甲酸的质量比为1:0.3~3;
(2)Au-Pd双金属纳米颗粒的制备:将侧柏提取液用去离子水稀释后,加入钯前驱体溶液和金前驱体溶液,升温至60~90℃反应0.5~4h,得到Au-Pd双金属纳米颗粒溶胶;
所述钯前驱体与金前驱体的物质的量之比为1:0.1~10;
(3)Au-Pd/NH2-MIL-101(Cr)催化剂的制备:将步骤(1)制备的NH2-MIL-101(Cr)加入步骤(2)制备的Au-Pd双金属纳米颗粒溶胶中,于60~90℃下搅拌0.5~4h,之后过滤,滤饼于60~100℃下真空干燥,得到粉末状的Au-Pd/NH2-MIL-101(Cr)催化剂。
2.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(1)中,所述碱液由碱性物质溶于水而得,所述碱性物质为氢氧化钠,所述碱液的浓度为0.1~1M,碱液的体积用量以Cr(NO)3·9H2O的质量计为15~20mL/g。
3.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(1)中,所述后处理的方法为:反应结束后,待反应液冷却至室温,离心收集固体产物,分别用水、DMF、甲醇洗涤,100℃下干燥过夜,得到NH2-MIL-101(Cr)。
4.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(2)中,所述侧柏提取液的制备方法为:取侧柏粉按料液质量比1:100与去离子水混合均匀,用保鲜膜密封,于30~100℃下搅拌0.5~4h,之后过滤,收集滤液即为侧柏提取液。
5.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(2)中,所述钯前驱体溶液的浓度为0.01~0.5M,所述金前驱体溶液的浓度为0.01~0.5M,所述钯前驱体为氯化钯或硝酸钯,所述金前驱体为氯金酸。
6.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(2)中,所述侧柏提取液的体积用量以钯前驱体的物质的量计为500~2500mL/mmol。
7.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂,其特征在于,步骤(3)中,所得催化剂中Au-Pd双金属纳米颗粒的负载量在0.05~6wt%。
8.如权利要求1所述Au-Pd/NH2-MIL-101(Cr)催化剂在光催化苯甲醇无溶剂液相氧化制备苯甲醛的反应中的应用。
9.如权利要求8所述的应用,其特征在于,所述应用的方法为:
将所述催化剂加入装有苯甲醇的反应瓶中,90℃下预热5min并回流,以90mL/min的速度通入氧气,打开150W的金卤灯光源照射反应瓶进行光催化反应,反应结束后,获得含苯甲醛的反应液,经分离纯化,获得氧化产物苯甲醛。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010161924.5A CN111359670A (zh) | 2020-03-10 | 2020-03-10 | 一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010161924.5A CN111359670A (zh) | 2020-03-10 | 2020-03-10 | 一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN111359670A true CN111359670A (zh) | 2020-07-03 |
Family
ID=71200425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010161924.5A Pending CN111359670A (zh) | 2020-03-10 | 2020-03-10 | 一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111359670A (zh) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113731502A (zh) * | 2021-08-20 | 2021-12-03 | 华南理工大学 | 一种共掺杂负载纳米钯颗粒的Cr基MOF碳材料催化剂及其制备与在甲酸制氢中的应用 |
CN114471724A (zh) * | 2022-01-17 | 2022-05-13 | 华中师范大学 | Au-Pd NPs@NMOF-Ni超薄纳米片复合材料及其制备方法和应用 |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104525264A (zh) * | 2014-12-16 | 2015-04-22 | 中国科学院宁波材料技术与工程研究所 | 包含活性金属组分的氨基金属有机骨架材料、其制备方法及应用 |
CN105521766A (zh) * | 2015-08-28 | 2016-04-27 | 浙江理工大学 | 金钯修饰的mil-101及其制备方法 |
US20160185806A1 (en) * | 2014-12-17 | 2016-06-30 | Instituto Mexicano Del Petróleo | PROCESS FOR OBTAINING METAL-ORGANIC MATERIALS WITH STRUCTURE TYPE MIL-101 (Cr) AND MIL-101-Cr-Mx+ |
CN107442180A (zh) * | 2017-08-15 | 2017-12-08 | 汕头大学 | 一种MOFs‑rGO负载的Pd纳米催化剂及其制备与应用 |
CN107497488A (zh) * | 2017-09-11 | 2017-12-22 | 大连理工大学 | 一种高加氢选择性Au‑Pd单原子合金催化剂的制备方法及应用 |
CN109331822A (zh) * | 2018-11-16 | 2019-02-15 | 浙江工业大学 | 一种光催化苯甲醇氧化Au-Pd合金催化剂及其制备方法与应用 |
CN110124717A (zh) * | 2019-05-13 | 2019-08-16 | 浙江师范大学 | 一种用于苯甲醇转化为苯甲醛的催化剂及其制备方法 |
CN110420662A (zh) * | 2019-08-15 | 2019-11-08 | 山东大学 | 一种可在低温下高效降解秸秆纤维素的复合催化材料及其制备方法与应用 |
-
2020
- 2020-03-10 CN CN202010161924.5A patent/CN111359670A/zh active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104525264A (zh) * | 2014-12-16 | 2015-04-22 | 中国科学院宁波材料技术与工程研究所 | 包含活性金属组分的氨基金属有机骨架材料、其制备方法及应用 |
US20160185806A1 (en) * | 2014-12-17 | 2016-06-30 | Instituto Mexicano Del Petróleo | PROCESS FOR OBTAINING METAL-ORGANIC MATERIALS WITH STRUCTURE TYPE MIL-101 (Cr) AND MIL-101-Cr-Mx+ |
CN105521766A (zh) * | 2015-08-28 | 2016-04-27 | 浙江理工大学 | 金钯修饰的mil-101及其制备方法 |
CN107442180A (zh) * | 2017-08-15 | 2017-12-08 | 汕头大学 | 一种MOFs‑rGO负载的Pd纳米催化剂及其制备与应用 |
CN107497488A (zh) * | 2017-09-11 | 2017-12-22 | 大连理工大学 | 一种高加氢选择性Au‑Pd单原子合金催化剂的制备方法及应用 |
CN109331822A (zh) * | 2018-11-16 | 2019-02-15 | 浙江工业大学 | 一种光催化苯甲醇氧化Au-Pd合金催化剂及其制备方法与应用 |
CN110124717A (zh) * | 2019-05-13 | 2019-08-16 | 浙江师范大学 | 一种用于苯甲醇转化为苯甲醛的催化剂及其制备方法 |
CN110420662A (zh) * | 2019-08-15 | 2019-11-08 | 山东大学 | 一种可在低温下高效降解秸秆纤维素的复合催化材料及其制备方法与应用 |
Non-Patent Citations (3)
Title |
---|
ANDREA SANTIAGO-PORTILLO ET AL.: ""Tuning the Microenvironment of Gold Nanoparticles Encapsulated within MIL-101(Cr) for the Selective Oxidation of Alcohols with O2: Influence of the Amino Terephthalate Linker"", 《CHEM. EUR. J.》 * |
YONG LIU ET AL.: ""Synthesis of highly dispersed metallic nanoparticles inside the pores of MIL-101(Cr) via the new double solvent method"", 《CATALYSIS COMMUNICATIONS》 * |
周凌云 等著: "《功能化介孔材料 捕集CO2研究》", 31 March 2019, 中国科学技术出版社 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113731502A (zh) * | 2021-08-20 | 2021-12-03 | 华南理工大学 | 一种共掺杂负载纳米钯颗粒的Cr基MOF碳材料催化剂及其制备与在甲酸制氢中的应用 |
CN113731502B (zh) * | 2021-08-20 | 2023-09-26 | 华南理工大学 | 一种共掺杂负载纳米钯颗粒的Cr基MOF碳材料催化剂及其制备与在甲酸制氢中的应用 |
CN114471724A (zh) * | 2022-01-17 | 2022-05-13 | 华中师范大学 | Au-Pd NPs@NMOF-Ni超薄纳米片复合材料及其制备方法和应用 |
CN114471724B (zh) * | 2022-01-17 | 2023-05-26 | 华中师范大学 | Au-Pd NPs@NMOF-Ni超薄纳米片复合材料及其制备方法和应用 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110270348B (zh) | 一种贵金属单原子催化剂及其制备和应用 | |
CN111054443B (zh) | 一种负载双活性位点的锆基mof催化剂及其制备方法与应用 | |
CN104549368B (zh) | 一种负载双金属型Cu‑Pt/TiO2‑NBs催化剂的制备方法与应用 | |
CN107890867B (zh) | 一种灰色Pd/TiO2纳米线光催化剂及其制备方法和应用 | |
CN109999915B (zh) | 一种用于co2环化催化反应的卟啉基金属有机骨架材料及其制备方法 | |
CN109794294B (zh) | 一种磺化金属酞菁@zif-8的光催化剂及其制备方法和应用 | |
CN108212217B (zh) | 一种降解氯酚类污染物的催化剂、制备方法和应用 | |
CN111359670A (zh) | 一种Au-Pd/NH2-MIL-101(Cr)催化剂及其制备与应用 | |
CN108355716B (zh) | 一种Cu-BTC组装纳米金属催化剂、制备及用于CO2的甲酰化反应 | |
CN110227553B (zh) | 一种具有CUS的MIL-101(Cr)组装双金属催化剂、制备及应用 | |
CN114805449B (zh) | 一种水溶性Pd(II)配合物及其合成方法和作为催化前驱体的用途 | |
Tosun et al. | A synergistic catalyst based on a multivalence monodisperse-porous microspheres with oxygen vacancies for benzyl alcohol oxidation | |
JP2005509515A (ja) | 金属塗布ナノ粒子の凝集体を構成する不均質触媒 | |
CN107694563A (zh) | 钯炭催化剂及其制备方法和应用 | |
CN107670697B (zh) | 可见光催化环己烷选择性氧化的催化剂及其制备方法 | |
CN115814859A (zh) | 一种新型光催化剂、制备方法及应用 | |
CN114247479B (zh) | 一种双金属Pt-Co/UiO-66催化剂及其制备方法和应用 | |
CN102909034A (zh) | 一种担载型金镍合金纳米催化剂的制备 | |
Li et al. | An amino functionalized zirconium metal organic framework as a catalyst for oxidative desulfurization | |
CN109331819B (zh) | 二氧化钛负载型Pt-Pd双金属光催化剂及其制备方法与应用 | |
CN108889342B (zh) | 用于丁腈橡胶非均相加氢催化剂的再生及回收再利用方法 | |
CN109621953A (zh) | 一种高效光催化氧化苯甲醇的三维有序大孔钒酸铋负载钌催化剂 | |
CN112898514B (zh) | 一种烯胺酮共价有机聚合物及其制备方法和应用 | |
CN110090648B (zh) | 一种还原氧化石墨烯负载的铜钯氧化物纳米颗粒及其制备方法和应用 | |
CN114917905A (zh) | 一种高性能双铜结构复合纳米催化材料的制备与应用 |
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 | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200703 |