Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure
This study explored Fischer–Tropsch synthesis (FTS) by combining a non-thermal plasma (NTP), generated by an arc discharge reactor at pressures >> 1 MPa, coupled with a mullite-coated 2 wt%-Co/5 wt%-Al<sub>2</sub>O<sub>3</sub> catalyst. The FTS product yields and electr...
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doaj-237e957423cc42449b140a14071556602021-02-26T00:01:00ZengMDPI AGCatalysts2073-43442021-02-011129729710.3390/catal11030297Plasma-Catalytic Fischer–Tropsch Synthesis at Very High PressureByron Bradley Govender0Samuel Ayodele Iwarere1Deresh Ramjugernath2Thermodynamics Research Unit, Howard College Campus, School of Engineering, College of Agriculture, Engineering and Science, University of KwaZulu-Natal, Durban 4041, South AfricaThermodynamics Research Unit, Howard College Campus, School of Engineering, College of Agriculture, Engineering and Science, University of KwaZulu-Natal, Durban 4041, South AfricaThermodynamics Research Unit, Howard College Campus, School of Engineering, College of Agriculture, Engineering and Science, University of KwaZulu-Natal, Durban 4041, South AfricaThis study explored Fischer–Tropsch synthesis (FTS) by combining a non-thermal plasma (NTP), generated by an arc discharge reactor at pressures >> 1 MPa, coupled with a mullite-coated 2 wt%-Co/5 wt%-Al<sub>2</sub>O<sub>3</sub> catalyst. The FTS product yields and electrical energy consumption for the pure plasma (no catalyst) and plasma-catalytic FTS processes were compared under the scope of various reactor operating parameters, namely, pressure (0.5 to 10 MPa), current (250 to 450 mA) and inter-electrode gap (0.5 to 2 mm). The major products, obtained in low concentrations for both processes, were gaseous C<sub>1</sub>–C<sub>3</sub> hydrocarbons, synthesised in the order: methane >> ethane > ethylene > propane. The hydrocarbon product yields were observed to increase, while the specific required energy generally decreased with increasing pressure, decreasing current and increasing inter-electrode gap. Plasma-catalysis improved the FTS performance, with the optimum conditions as: (i) 10 MPa at 10 s and 2 MPa at 60 s for the pressure variation study with the longer treatment time producing higher yields; (ii) 250 mA for the current variation study; (iii) 2 mm for the inter-electrode gap variation study. Plasma-catalysis at a gap of 2 mm yielded the highest concentrations of methane (15,202 ppm), ethane (352 ppm), ethylene (121 ppm) and propane (20 ppm), thereby indicating the inter-electrode gap as the most influential parameter.https://www.mdpi.com/2073-4344/11/3/297non-thermal plasmahigh pressurearc dischargeFischer–Tropsch synthesiscobalt catalyst |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Byron Bradley Govender Samuel Ayodele Iwarere Deresh Ramjugernath |
spellingShingle |
Byron Bradley Govender Samuel Ayodele Iwarere Deresh Ramjugernath Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure Catalysts non-thermal plasma high pressure arc discharge Fischer–Tropsch synthesis cobalt catalyst |
author_facet |
Byron Bradley Govender Samuel Ayodele Iwarere Deresh Ramjugernath |
author_sort |
Byron Bradley Govender |
title |
Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure |
title_short |
Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure |
title_full |
Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure |
title_fullStr |
Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure |
title_full_unstemmed |
Plasma-Catalytic Fischer–Tropsch Synthesis at Very High Pressure |
title_sort |
plasma-catalytic fischer–tropsch synthesis at very high pressure |
publisher |
MDPI AG |
series |
Catalysts |
issn |
2073-4344 |
publishDate |
2021-02-01 |
description |
This study explored Fischer–Tropsch synthesis (FTS) by combining a non-thermal plasma (NTP), generated by an arc discharge reactor at pressures >> 1 MPa, coupled with a mullite-coated 2 wt%-Co/5 wt%-Al<sub>2</sub>O<sub>3</sub> catalyst. The FTS product yields and electrical energy consumption for the pure plasma (no catalyst) and plasma-catalytic FTS processes were compared under the scope of various reactor operating parameters, namely, pressure (0.5 to 10 MPa), current (250 to 450 mA) and inter-electrode gap (0.5 to 2 mm). The major products, obtained in low concentrations for both processes, were gaseous C<sub>1</sub>–C<sub>3</sub> hydrocarbons, synthesised in the order: methane >> ethane > ethylene > propane. The hydrocarbon product yields were observed to increase, while the specific required energy generally decreased with increasing pressure, decreasing current and increasing inter-electrode gap. Plasma-catalysis improved the FTS performance, with the optimum conditions as: (i) 10 MPa at 10 s and 2 MPa at 60 s for the pressure variation study with the longer treatment time producing higher yields; (ii) 250 mA for the current variation study; (iii) 2 mm for the inter-electrode gap variation study. Plasma-catalysis at a gap of 2 mm yielded the highest concentrations of methane (15,202 ppm), ethane (352 ppm), ethylene (121 ppm) and propane (20 ppm), thereby indicating the inter-electrode gap as the most influential parameter. |
topic |
non-thermal plasma high pressure arc discharge Fischer–Tropsch synthesis cobalt catalyst |
url |
https://www.mdpi.com/2073-4344/11/3/297 |
work_keys_str_mv |
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