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Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate
In this paper, the mesoporous molecular sieve SBA-16 with good dispersion was prepared by hydrothermal method. Under the condition of Si/Mo= 1.0, MoO(3)/SBA-16 catalysts were prepared by iso-dipping method at 550 °C, 650 °C and 750 °C calcination temperature, which for the synthesis of diphenyl carb...
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Formato: | Online Artículo Texto |
Lenguaje: | English |
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Scientific and Technological Research Council of Turkey (TUBITAK)
2022
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10446925/ https://www.ncbi.nlm.nih.gov/pubmed/37621350 http://dx.doi.org/10.55730/1300-0527.3492 |
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author | YING, Li SHUNWU, He |
author_facet | YING, Li SHUNWU, He |
author_sort | YING, Li |
collection | PubMed |
description | In this paper, the mesoporous molecular sieve SBA-16 with good dispersion was prepared by hydrothermal method. Under the condition of Si/Mo= 1.0, MoO(3)/SBA-16 catalysts were prepared by iso-dipping method at 550 °C, 650 °C and 750 °C calcination temperature, which for the synthesis of diphenyl carbonate (DPC) from dimethyl carbonate (DMC) and phenyl acetate (PA) was used, and the uncalcined MoO(3)/SBA-16 was used as a reference. XRD, TG-DTA, XPS, ICP-MS, FT-IR, BET, SEM and TEM characterization. The effects of calcination temperature and reaction conditions on the catalytic performance of MoO(3)/SBA-16 in transesterification of DMC and PA were investigated. The results show that the MoO(3)/SBA-16 catalyst prepared at 550 °C has the best catalytic performance in the reaction of DMC and PA ester exchange, and the catalyst has the best catalytic performance in the appropriate reaction strip (n(PA) = 1.0 mol; n (PA)/n (DMC) = 2.0; m (MoO(3)/SBA-16) = 6.0g; t = 5.0 h; T = 180 °C), the DMC conversion is 78.5%, and the selectivity of methyl phenyl carbonate (MPC) and DPC is 51.1% and 46.5%, respectively. After five cycles, the catalyst activity decreased and the conversion of DMC decreased from 78.5% to 15.8%. However, its crystal structure remained unchanged. The used catalyst can be easily regenerated by calcination in air at 550 °C for 5 h. The catalytic performance of the regenerated catalyst was almost as high as that of the fresh one. |
format | Online Article Text |
id | pubmed-10446925 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | Scientific and Technological Research Council of Turkey (TUBITAK) |
record_format | MEDLINE/PubMed |
spelling | pubmed-104469252023-08-24 Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate YING, Li SHUNWU, He Turk J Chem Research Article In this paper, the mesoporous molecular sieve SBA-16 with good dispersion was prepared by hydrothermal method. Under the condition of Si/Mo= 1.0, MoO(3)/SBA-16 catalysts were prepared by iso-dipping method at 550 °C, 650 °C and 750 °C calcination temperature, which for the synthesis of diphenyl carbonate (DPC) from dimethyl carbonate (DMC) and phenyl acetate (PA) was used, and the uncalcined MoO(3)/SBA-16 was used as a reference. XRD, TG-DTA, XPS, ICP-MS, FT-IR, BET, SEM and TEM characterization. The effects of calcination temperature and reaction conditions on the catalytic performance of MoO(3)/SBA-16 in transesterification of DMC and PA were investigated. The results show that the MoO(3)/SBA-16 catalyst prepared at 550 °C has the best catalytic performance in the reaction of DMC and PA ester exchange, and the catalyst has the best catalytic performance in the appropriate reaction strip (n(PA) = 1.0 mol; n (PA)/n (DMC) = 2.0; m (MoO(3)/SBA-16) = 6.0g; t = 5.0 h; T = 180 °C), the DMC conversion is 78.5%, and the selectivity of methyl phenyl carbonate (MPC) and DPC is 51.1% and 46.5%, respectively. After five cycles, the catalyst activity decreased and the conversion of DMC decreased from 78.5% to 15.8%. However, its crystal structure remained unchanged. The used catalyst can be easily regenerated by calcination in air at 550 °C for 5 h. The catalytic performance of the regenerated catalyst was almost as high as that of the fresh one. Scientific and Technological Research Council of Turkey (TUBITAK) 2022-08-10 /pmc/articles/PMC10446925/ /pubmed/37621350 http://dx.doi.org/10.55730/1300-0527.3492 Text en © TÜBİTAK https://creativecommons.org/licenses/by/4.0/This work is licensed under a Creative Commons Attribution 4.0 International License. |
spellingShingle | Research Article YING, Li SHUNWU, He Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title | Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title_full | Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title_fullStr | Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title_full_unstemmed | Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title_short | Study on MoO(3)/SBA-16 catalyzed transesterification to synthesize diphenyl carbonate |
title_sort | study on moo(3)/sba-16 catalyzed transesterification to synthesize diphenyl carbonate |
topic | Research Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10446925/ https://www.ncbi.nlm.nih.gov/pubmed/37621350 http://dx.doi.org/10.55730/1300-0527.3492 |
work_keys_str_mv | AT yingli studyonmoo3sba16catalyzedtransesterificationtosynthesizediphenylcarbonate AT shunwuhe studyonmoo3sba16catalyzedtransesterificationtosynthesizediphenylcarbonate |