Conversion of Syngas to LPG and Aromatics over Commercial Fischer-Tropsch Catalyst and HZSM-5 in Dual Bed Reactor

Result code in IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F61989100%3A27230%2F14%3A86086565" target="_blank" >RIV/61989100:27230/14:86086565 - isvavai.cz</a>
Alternative codes found
RIV/61989100:27730/14:86086565
Result on the web
<a href="http://dx.doi.org/10.1080/10916466.2013.845574" target="_blank" >http://dx.doi.org/10.1080/10916466.2013.845574</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1080/10916466.2013.845574" target="_blank" >10.1080/10916466.2013.845574</a>

Result language
angličtina
Original language name
Conversion of Syngas to LPG and Aromatics over Commercial Fischer-Tropsch Catalyst and HZSM-5 in Dual Bed Reactor
Original language description
The commercial Co-based Fischer-Tropsch (FT) catalyst and HZSM-5 were tested in a single reactor process. FT catalyst was evaluated at 463 K, whereas HZSM-5 was evaluated at various temperatures (523, 573, and 623 K). The effect of syngas flow rate, HZSM-5 temperature and loading on liquefied petroleum gas (LPG) and aromatics selectivities were investigated. HZSM-5 addition suppressed the formation of CO2 and CH4, and remarkably enhanced the simultaneous formation of LPG and aromatics. The optimal operating conditions were identified as: THZM-5 = 623 K, HZSM-5 loading = 2.5 g, and GHSV = 4.8 Lsyngas/(gcat h).
Czech name
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Czech description
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Type
J<sub>x</sub> - Unclassified - Peer-reviewed scientific article (Jimp, Jsc and Jost)
CEP classification
CC - Organic chemistry
OECD FORD branch
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Publication year
2014
Confidentiality
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

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