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High-purity dichlorosilane (DCS) is an important raw material for thin film deposition in the semiconductor industry, such as epitaxial silicon, which is mainly produced by trichlorosilane (TCS) catalytic decomposition in a fixed-bed reactor. The productivity of DCS is strongly dependent on the controlling of the TCS decomposition reaction process, associated with the cost in practical application. In this study, we have performed computational fluid dynamics (CFD) simulation on the TCS decomposition reaction kinetics in a cylindrical fixed-bed reactor, in which the effects of catalyst bed height, feed temperature, and feed flow rate are stressed to predict the conversion rate of TCS and the generation rate of DCS. This indicates that the increase of bed height helps the reaction to proceed adequately, but too large a bed height does not improve the DCS generation rate. Meanwhile, the feed temperature and reactor temperature have important effects on the DCS generation rate. However, it is found that changing the feed flow rate and L/D ratio cannot effectively improve the DCS generation rate while the bed volume remains constant. Furthermore, we have designed a fixed-bed reactor to verify the simulation results, which are in good agreement with each other. These results are of significance for the practical industrial production of high-purity DCS in a fixed-bed reactor.
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http://dx.doi.org/10.1021/acsomega.4c07049 | DOI Listing |
Nat Commun
August 2025
School of Environmental Science and Engineering, Guangdong Provincial Key Laboratory of Environmental Pollution Control and Remediation Technology, Sun Yat-sen University, Guangzhou, China.
Heterogeneous catalytic ozonation shows promise in destroying organic pollutants in water, yet developing catalysts with both high activity and stability remains challenging. In this study, we propose a catalyst design strategy involving the anchoring of electron-sharing sites near single-atom sites to construct bidirectional electron transfer interaction tunnels. The developed catalyst (MnN-Fe@FeN) features Fe@FeN atomic clusters as electron-sharing sites, coordinated Mn single-atom centers through shared nitrogen bridges, successfully establishing a synergistic system.
View Article and Find Full Text PDFACS Omega
August 2025
Department of Chemical Technology, Faculty of Science, Chulalongkorn University, Phayathai Road, Bangkok 10330, Thailand.
This study investigated the catalytic performance of Ni-based catalysts supported on micromesoporous composites derived from the incorporation of SBA-15 with USY-(SBA-15-xUSY) or Hbeta-(SBA-15-xHbeta) zeolites (where x is wt percentage of zeolite fraction in the composite) for palm oil hydroisomerization to produce biojet fuel range. The hydroisomerization was conducted in a fixed-bed reactor under 25 bar of H pressure at 40 mL/min, 425 °C, 0.1 mL/min palm oil feed rate, and 5 g of catalyst.
View Article and Find Full Text PDFWater Res
August 2025
School of Environmental Science and Engineering, Sun Yat-sen University, Guangzhou 510006, PR China; Guangdong Provincial Key Laboratory of Environmental Pollution Control and Remediation Technology, Sun Yat-sen University, Guangzhou 510275, China. Electronic address:
Nitrate contamination in saline wastewater poses significant environmental risks, including eutrophication and groundwater contamination. Targeted nitrate removal from saline wastewater is of critical importance for environmental sustainability. In this study, we explored the response of microbial denitrification to varying salinity levels using a fixed-bed biofilm reactor (FBBR) operated under freshwater (0 g NaCl/L), mesosaline (50 g NaCl/L), and hypersaline (100 g NaCl/L) conditions.
View Article and Find Full Text PDFMolecules
August 2025
Institute of Organic Chemistry, Catalysis and Petrochemistry, Slovak University of Technology, Radlinského 9, 812 37 Bratislava, Slovakia.
This review outlines a comprehensive methodology for the research and development of heterogeneous catalytic technologies (R&D_HeCaTe). Emphasis is placed on the fundamental interactions between reactants, solvents, and heterogeneous catalysts-specifically the roles of catalytic centers and support materials (e.g.
View Article and Find Full Text PDFBioresour Technol
December 2025
Biotechnology Process Engineering Center, KRIBB, 30 Yeongudanji-ro, Ochang-eup, Cheongwon-gu, Cheongju-si 28116, Republic of Korea; Bioprocess Department, University of Science and Technology, 217 Gajeong-ro, Yuseong-gu, Daejeon 34113, Republic of Korea. Electronic address:
The convergence of chemical and biological technologies offers unprecedented opportunities for sustainable chemical production. Oxygenated oil-based biomass requires a chemical process to refine it into less-toxic hydrocarbons to be used for microbial biotransformation to produce value-added chemicals. This study demonstrates the transformation of hydrotreated vegetable oils, specifically coconut oil, into α,ω-diacids (DCAs), which are essential for bio-based polymer production.
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