2020
DOI: 10.1016/j.biteb.2020.100479
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Kinetics of co-gasification of rice husk biomass and high sulphur petroleum coke with oxygen as gasifying medium via TGA

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Cited by 55 publications
(12 citation statements)
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“…5,54−58 Due to the low conductivity property of biomass, it has been reported that there is a limitation in the transference of heat from the heating source of the torrefier to the biomass sample. 59,60 As a result of this limitation, higher temperatures will be required to ensure uniform decomposition of the lignocellulosic components throughout the biomass sample, translating into an increase in the HHV. This phenomenon is responsible for increasing HHV and EEF as the mass feed reduces (i.e., an increase in NSR).…”
Section: Comparative Analysis Of the Effect Of Process Conditions On ...mentioning
confidence: 99%
“…5,54−58 Due to the low conductivity property of biomass, it has been reported that there is a limitation in the transference of heat from the heating source of the torrefier to the biomass sample. 59,60 As a result of this limitation, higher temperatures will be required to ensure uniform decomposition of the lignocellulosic components throughout the biomass sample, translating into an increase in the HHV. This phenomenon is responsible for increasing HHV and EEF as the mass feed reduces (i.e., an increase in NSR).…”
Section: Comparative Analysis Of the Effect Of Process Conditions On ...mentioning
confidence: 99%
“…temperature and time) increased. This continuous mass loss as the severity of the process increases was also reported in investigations done by Anca-Couce et al and Gajera et al on the thermal degradation of biomass using a thermogravimetric analyzer. Furthermore, it can be observed that there was a drastic mass loss when the temperature was increased to 300 °C.…”
Section: Resultsmentioning
confidence: 99%
“…The producer gas was cleaned to remove tar at an efficiency of 98%, which enabled the cleaned producer gas to be used for a 400 kW e gas engine. Gajera et al [ 149 ] investigated the kinetics of co-gasification of RH and petroleum coke, using a thermogravimetric analyser at three different heating rates (10, 20, and 30 °C/min). The co-gasification process improved the reactivity of petroleum coke, as the activation energy of 126 kJ/mol for gasification of petroleum coke alone was lowered to 86 kJ/mol for the co-gasification of a 3:1 mixture of RH and petroleum coke.…”
Section: Valorization Of Rice Residuesmentioning
confidence: 99%