Bioethanol 2012
DOI: 10.5772/21008
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Bioethanol Production from Steam Explosion Pretreated Straw

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Cited by 7 publications
(4 citation statements)
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“…All the parameters used for energy balance analysis are summarized in the Supporting Information (Table S2). The energy consumption and production were estimated according to the following equations where E in,HTT (MJ) is the heat consumption for HTT, m r (t) the disposal capacity of rice straw, m w (t) the water usage, γ w (kJ/kg °C) the specific heat capacity of water (4.18 kJ/kg °C), γ r (kJ/kg °C) the specific heat capacity of rice straw (1.67 kJ/kg °C), T p (°C) the hydrothermal pretreatment temperature (150 or 210 °C), T a the ambient temperature (25 °C in this study), T d (°C) the temperature for AD (35 °C in this study), and ϕ (%) the heat recovery efficiency (assumed at 85%). Because a short holding time (0–30 min) was applied and the out wall of the HTT reactor would be equipped with thermal insulation material when being utilized in practice, heat loss through the reactor wall during the HTT process was not accounted for in this work. where E in, AD (MJ) is the heat consumption for AD, m (t) the digestate weight, γ (kJ/kg °C) the specific heat capacity of digestate and estimated to be the same as water (4.18 kJ/kg °C) in this study, T d (°C) the AD temperature (35 °C), and T a (°C) the ambient temperature (25 °C in this study).…”
Section: Methodsmentioning
confidence: 99%
“…All the parameters used for energy balance analysis are summarized in the Supporting Information (Table S2). The energy consumption and production were estimated according to the following equations where E in,HTT (MJ) is the heat consumption for HTT, m r (t) the disposal capacity of rice straw, m w (t) the water usage, γ w (kJ/kg °C) the specific heat capacity of water (4.18 kJ/kg °C), γ r (kJ/kg °C) the specific heat capacity of rice straw (1.67 kJ/kg °C), T p (°C) the hydrothermal pretreatment temperature (150 or 210 °C), T a the ambient temperature (25 °C in this study), T d (°C) the temperature for AD (35 °C in this study), and ϕ (%) the heat recovery efficiency (assumed at 85%). Because a short holding time (0–30 min) was applied and the out wall of the HTT reactor would be equipped with thermal insulation material when being utilized in practice, heat loss through the reactor wall during the HTT process was not accounted for in this work. where E in, AD (MJ) is the heat consumption for AD, m (t) the digestate weight, γ (kJ/kg °C) the specific heat capacity of digestate and estimated to be the same as water (4.18 kJ/kg °C) in this study, T d (°C) the AD temperature (35 °C), and T a (°C) the ambient temperature (25 °C in this study).…”
Section: Methodsmentioning
confidence: 99%
“…During the laboratory tests for the thermal characterisation of AGROTESs samples, it was not possible to deduce their specific heat capacity, so the relative data for each raw material used for samples production, were retrieved from literature (Verma & Prasad 2000;Kahr et al 2012;Liuzzi et al 2020) and web databases (Greenspec.co.uk; Engineeringtoolbox). The tentative specific heat capacity of each AGROTESs samples was obtained from the weighted average of the specific heat capacities of each of the raw materials used in the panels and are reported in Table 4.…”
Section: Applications Of Agrotess Panels In Buildingsmentioning
confidence: 99%
“…Tentatively calculated heat capacity of AGROTESs samplesReferences: data retrieved fromVerma & Prasad 2000;Kahr et al 2012;Liuzzi et al 2020 …”
mentioning
confidence: 99%
“…Debido al alto consumo de energía durante esta etapa, se están buscando alternativas más sostenibles a la deshidratación convecional (Kreis y Gorak, 2006;del Pozo-Gómez et al, 2007;Bakhsni et al, 2008). No obstante, en la actualidad la destilación azeotrópica sigue siendo la más empleada a nivel industrial (Kahr et al, 2012).…”
Section: Fermentación De La Biomasa Lignocelulósicaunclassified