Highly Dispersed Cu Nanoparticles Prepared Using Ammonia Evaporation Method
Source abstract
Abstract
The most common method for the synthesis of copper‐containing supported catalysts is impregnation of the support with a copper salt solution. However, calcination and reduction of the resulting materials can lead to agglomeration of copper species and a decrease in catalytic activity. The synthesis of highly dispersed copper particles on the support surface can be performed using ammonia evaporation method with a copper ammine complex as a precursor. This review considers the effect of copper loading and the support nature on the structure of the obtained catalysts with a focus on the benefits of the ammonia evaporation method for preparation of the Cu/SiO 2 catalysts compared to other methods. This review summarizes the results concerning influence of the synthesis conditions of the ammonia evaporation method on the morphology and structure of Cu‐based catalysts. The effect of ammonia evaporation temperature and solution pH on copper dispersion, copper particle size, and reducibility of the Cu‐based catalysts is also included. The morphology of the silica support and the particle size of the silica sol have impact on the formation of copper phyllosilicate in the Cu/SiO 2 catalysts.
Source: crossref · Quality: baseline
Research context
OpenAlex topics: Catalytic Processes in Materials Science · Nanomaterials for catalytic reactions · Copper-based nanomaterials and applications
SciVX discovery tags are terminology-based. OpenAlex topics are source-provided classifications.
Affiliations
Department of Fine Organic Synthesis Boreskov Institute of Catalysis Novosibirsk Russia
Funding
Ministry of Science and Higher Education of the Russian Federation
References (98)
Show source-provided references
1. 10.1016/j.mcat.2024.11413310.1016/j.mcat.2024.114133 ↗
2. 10.1002/cctc.20230049310.1002/cctc.202300493 ↗
3. 10.1039/C4CY01619J10.1039/C4CY01619J ↗
4. 10.1039/C6CY00249H10.1039/C6CY00249H ↗
5. A Review of Dry (CO2) Reforming of Methane over Noble Metal Catalysts
6. 10.1021/acs.chemrev.7b0027210.1021/acs.chemrev.7b00272 ↗
7. 10.1021/acs.chemrev.8b0054710.1021/acs.chemrev.8b00547 ↗
8. 10.1055/a-1807-318810.1055/a-1807-3188 ↗
9. 10.1021/acscatal.9b0530310.1021/acscatal.9b05303 ↗
10. 10.1016/j.apsusc.2023.15773610.1016/j.apsusc.2023.157736 ↗
11. 10.1007/s10562-016-1960-x10.1007/s10562-016-1960-x ↗
12. 10.1021/acs.chemrev.9b0072310.1021/acs.chemrev.9b00723 ↗
13. 10.1007/s11746-012-2119-610.1007/s11746-012-2119-6 ↗
14. 10.1002/cctc.20170027910.1002/cctc.201700279 ↗
15. 10.1006/jcat.2000.288310.1006/jcat.2000.2883 ↗
16. 10.1021/acs.chemrev.5b0048210.1021/acs.chemrev.5b00482 ↗
17. 10.1016/j.ijhydene.2021.11.25310.1016/j.ijhydene.2021.11.253 ↗
18. 10.1021/acs.jpcc.7b0295710.1021/acs.jpcc.7b02957 ↗
19. 10.1002/jctb.650810.1002/jctb.6508 ↗
20. 10.1039/c2gc35565e10.1039/c2gc35565e ↗
21. Highly Efficient and Robust Cu Catalyst for Non‐oxidative Dehydrogenation of Ethanol to Acetaldehyde and Hydrogen
22. 10.3389/fchem.2022.97935310.3389/fchem.2022.979353 ↗
23. 10.1246/bcsj.56.133710.1246/bcsj.56.1337 ↗
24. The Structure of CuSiO2 Catalysts Prepared by the Ion‐exchange Technique
25. Cu/SiO2 Catalysts Prepared by the Sol‐Gel Method for Hydrogenation of Dimethyl Oxalate to Ethylene Glycol
26. 10.1016/j.apcata.2011.06.02410.1016/j.apcata.2011.06.024 ↗
27. 10.3390/catal1208087810.3390/catal12080878 ↗
28. 10.1016/S0025-5408(01)00491-310.1016/S0025-5408(01)00491-3 ↗
29. 10.1016/S0166-9834(00)82204-610.1016/S0166-9834(00)82204-6 ↗
30. 10.31788/RJC.2020.131526710.31788/RJC.2020.1315267 ↗
31. 10.1016/j.apcata.2022.11855510.1016/j.apcata.2022.118555 ↗
32. 10.1016/S0166-9834(00)80699-510.1016/S0166-9834(00)80699-5 ↗
33. 10.1021/jp993399q10.1021/jp993399q ↗
34. 10.1007/s10971-010-2247-010.1007/s10971-010-2247-0 ↗
35. 10.1016/j.cattod.2011.08.03810.1016/j.cattod.2011.08.038 ↗
36. 10.1016/j.apcata.2015.07.02610.1016/j.apcata.2015.07.026 ↗
37. 10.1021/ja303415310.1021/ja3034153 ↗
38. 10.1039/C4CY01148A10.1039/C4CY01148A ↗
39. 10.1002/cctc.20200052310.1002/cctc.202000523 ↗
40. 10.3390/catal1203027610.3390/catal12030276 ↗
41. 10.3390/catal1102025510.3390/catal11020255 ↗
42. 10.1039/C5CY01965F10.1039/C5CY01965F ↗
43. 10.1016/j.fuproc.2019.05.00310.1016/j.fuproc.2019.05.003 ↗
44. 10.3390/nano906084210.3390/nano9060842 ↗
45. 10.1021/jp013153x10.1021/jp013153x ↗
46. 10.1007/BF0190964710.1007/BF01909647 ↗
47. 10.1007/BF0197939010.1007/BF01979390 ↗
48. 10.1021/cs400574v10.1021/cs400574v ↗
49. 10.1021/acscatal.5b0068210.1021/acscatal.5b00682 ↗
50. 10.1016/j.ijhydene.2020.07.05410.1016/j.ijhydene.2020.07.054 ↗
51. 10.1016/0022-3093(89)90461-410.1016/0022-3093(89)90461-4 ↗
52. 10.1149/2162-8777/ac757e10.1149/2162-8777/ac757e ↗
53. 10.1021/jp056604c10.1021/jp056604c ↗
54. Cu/SiO2 Catalysts Prepared by the Ammonia‐Evaporation Method: Texture, Structure, and Catalytic Performance in Hydrogenation of Dimethyl Oxalate to Ethylene Glycol
55. 10.1016/0926-860X(96)00087-710.1016/0926-860X(96)00087-7 ↗
56. 10.1016/j.apcata.2006.02.01710.1016/j.apcata.2006.02.017 ↗
57. 10.1016/j.catcom.2010.10.03010.1016/j.catcom.2010.10.030 ↗
58. 10.1016/j.cclet.2014.05.05010.1016/j.cclet.2014.05.050 ↗
59. 10.1002/cctc.20090024410.1002/cctc.200900244 ↗
60. 10.1016/0040-6031(90)87011-Z10.1016/0040-6031(90)87011-Z ↗
61. 10.1016/j.apcata.2017.04.00110.1016/j.apcata.2017.04.001 ↗
62. 10.1016/j.jcat.2019.12.01610.1016/j.jcat.2019.12.016 ↗
63. 10.1021/jp902688b10.1021/jp902688b ↗
64. 10.1016/S0926-860X(97)00207-X10.1016/S0926-860X(97)00207-X ↗
65. Influence of Ni Species on the Structural Evolution of Cu/SiO2 Catalyst for the Chemoselective Hydrogenation of Dimethyl Oxalate
66. Highly Active and Stable ZrO2 ‐SiO 2‐Supported Cu–Catalysts for the Hydrogenation of Dimethyl Oxalate to Methyl Glycolate
67. 10.1016/j.apcata.2018.02.02010.1016/j.apcata.2018.02.020 ↗
68. 10.1039/C6RA06464G10.1039/C6RA06464G ↗
69. 10.1039/C5GC00810G10.1039/C5GC00810G ↗
70. 10.1007/s12039-014-0659-z10.1007/s12039-014-0659-z ↗
71. 10.1021/acscatal.5b0167810.1021/acscatal.5b01678 ↗
72. 10.1039/C5CY00857C10.1039/C5CY00857C ↗
73. Highly Active Cu/SiO2 Catalysts for Hydrogenation of Diethylmalonate to 1,3‐Propanediol
74. 10.3390/catal703007510.3390/catal7030075 ↗
75. 10.1016/j.cattod.2019.06.03110.1016/j.cattod.2019.06.031 ↗
76. 10.17586/2220-8054-2020-11-5-601-60710.17586/2220-8054-2020-11-5-601-607 ↗
77. 10.1016/j.ijhydene.2016.09.06410.1016/j.ijhydene.2016.09.064 ↗
78. 10.1016/j.catcom.2011.04.01910.1016/j.catcom.2011.04.019 ↗
79. 10.1039/D4CY00675E10.1039/D4CY00675E ↗
80. 10.1016/j.apsusc.2023.15777410.1016/j.apsusc.2023.157774 ↗
81. 10.3390/catal1304073710.3390/catal13040737 ↗
82. 10.1002/aic.1399810.1002/aic.13998 ↗
83. 10.1016/j.jcou.2018.06.02310.1016/j.jcou.2018.06.023 ↗
84. 10.1016/j.jcou.2016.11.01510.1016/j.jcou.2016.11.015 ↗
85. 10.1021/es301809410.1021/es3018094 ↗
86. 10.1016/j.jssc.2018.10.01810.1016/j.jssc.2018.10.018 ↗
87. 10.1021/acs.inorgchem.9b0136510.1021/acs.inorgchem.9b01365 ↗
88. 10.1002/chem.20130259910.1002/chem.201302599 ↗
89. 10.1021/cm902916510.1021/cm9029165 ↗
90. 10.1021/ie500288g10.1021/ie500288g ↗
91. 10.1002/cctc.20210048910.1002/cctc.202100489 ↗
92. Gas‐Phase Carbonylation of Methanol to Dimethyl Carbonate on Chloride‐Free Cu‐Precipitated Zeolite Y at Normal Pressure
93. 10.1021/jp993893u10.1021/jp993893u ↗
94. 10.1039/C9RA10501H10.1039/C9RA10501H ↗
95. 10.1016/0144-2449(94)90134-110.1016/0144-2449(94)90134-1 ↗
96. 10.1021/acsomega.3c0884510.1021/acsomega.3c08845 ↗
97. 10.1016/j.apcata.2013.03.02110.1016/j.apcata.2013.03.021 ↗
98. 10.1016/j.apcata.2015.10.02210.1016/j.apcata.2015.10.022 ↗