Abstract:LignocellulosicPellet durability Storage a b s t r a c tThe goal of the study was to evaluate and compare the physical properties of control, pretreated and densified corn stover, switchgrass, and prairie cord grass samples.Ammonia Fiber Expansion (AFEX) pretreated switchgrass, corn stover, and prairie cord grass samples were densified by using the comPAKco device developed by Federal Machine Company of Fargo, ND. The densified biomass were referred as "PAKs" in this study. All feedstocks were ground into thre… Show more
“…These improvements will make biomass meet the specifications in terms of density, particle size, ash composition, and carbohydrate content for both biochemical and thermochemical conversion applications. Various thermal methods, such as dry and wet torrefaction (hydrothermal carbonization) and steam explosion, as well as chemical pretreatment techniques, such as ionic, acid, alkali, and ammonia fiber expansion, were investigated to understand how they improve the biomass specifications for biofuels production [8,9,10,11,12,13]. Recent studies by Sarkar et al .…”
Deep drying and torrefaction compose a thermal pretreatment method where biomass is heated in the temperature range of 150–300 °C in an inert or reduced environment. The process parameters, like torrefaction temperature and residence time, have a significant impact on the proximate, ultimate, and energy properties. In this study, torrefaction experiments were conducted on 2-mm ground lodgepole pine (Pinus contorta) using a thermogravimetric analyzer. Both deep drying and torrefaction temperature (160–270 °C) and time (15–120 min) were selected. Torrefied samples were analyzed for the proximate, ultimate, and higher heating value. The results indicate that moisture content decreases with increases in torrefaction temperature and time, where at 270 °C and 120 min, the moisture content is found to be 1.15% (w.b.). Volatile content in the lodgepole pine decreased from about 80% to about 45%, and ash content increased from 0.77% to about 1.91% at 270 °C and 120 min. The hydrogen, oxygen, and sulfur content decreased to 3%, 28.24%, and 0.01%, whereas the carbon content and higher heating value increased to 68.86% and 23.67 MJ/kg at 270 °C and 120 min. Elemental ratio of hydrogen to carbon and oxygen to carbon (H/C and O/C) calculated at 270 °C and a 120-min residence time were about 0.56 and 0.47. Based on this study, it can be concluded that higher torrefaction temperatures ≥230 °C and residence time ≥15 min influence the proximate, ultimate, and energy properties of ground lodgepole pine.
“…These improvements will make biomass meet the specifications in terms of density, particle size, ash composition, and carbohydrate content for both biochemical and thermochemical conversion applications. Various thermal methods, such as dry and wet torrefaction (hydrothermal carbonization) and steam explosion, as well as chemical pretreatment techniques, such as ionic, acid, alkali, and ammonia fiber expansion, were investigated to understand how they improve the biomass specifications for biofuels production [8,9,10,11,12,13]. Recent studies by Sarkar et al .…”
Deep drying and torrefaction compose a thermal pretreatment method where biomass is heated in the temperature range of 150–300 °C in an inert or reduced environment. The process parameters, like torrefaction temperature and residence time, have a significant impact on the proximate, ultimate, and energy properties. In this study, torrefaction experiments were conducted on 2-mm ground lodgepole pine (Pinus contorta) using a thermogravimetric analyzer. Both deep drying and torrefaction temperature (160–270 °C) and time (15–120 min) were selected. Torrefied samples were analyzed for the proximate, ultimate, and higher heating value. The results indicate that moisture content decreases with increases in torrefaction temperature and time, where at 270 °C and 120 min, the moisture content is found to be 1.15% (w.b.). Volatile content in the lodgepole pine decreased from about 80% to about 45%, and ash content increased from 0.77% to about 1.91% at 270 °C and 120 min. The hydrogen, oxygen, and sulfur content decreased to 3%, 28.24%, and 0.01%, whereas the carbon content and higher heating value increased to 68.86% and 23.67 MJ/kg at 270 °C and 120 min. Elemental ratio of hydrogen to carbon and oxygen to carbon (H/C and O/C) calculated at 270 °C and a 120-min residence time were about 0.56 and 0.47. Based on this study, it can be concluded that higher torrefaction temperatures ≥230 °C and residence time ≥15 min influence the proximate, ultimate, and energy properties of ground lodgepole pine.
“…The AFEX during A-NaOH pretreatment did not have a large effect on the lignin removal rate, but it could redistribute the lignin on the cell wall and form a highly porous structure, thus improving the enzymatic efficiency of lignocellulose. 33 Additionally, AFEX reduces the adverse effect of lignin on cellulase. 34 This alkaline treatment exposes more lignin; since the lignin removal rate affects the enzymatic efficiency, the poor lignin removal rate will adversely affect the enzymatic digestion of lignin.…”
The most essential
issue facing the world today is the provision
of energy and sustainable consumption of natural resources. Pretreatment
is an essential step to produce biofuels from lignocellulosic biomass.
In this study, ammonia fiber explosion (AFEX) combined with NaOH (A-NaOH)
pretreatment effects on the characteristics of
Pennisetum
sinese
(herbaceous), oak (hardwood), and camphor wood (softwood)
were assessed using enzymatic efficiency analysis, thereby identifying
the composition properties of subsequent bio-H
2
production.
The results show that the lignin removal (84.2%, 59.7%, and 36.7%,
respectively) at 5%A-NaOH conditions and enzymatic efficiency (36.2%,
9.7%, and 6.5%, respectively) of
Pennisetum sinese
(
P. sinese
), oak, and camphor wood were significantly
increased under 4% A-NaOH conditions. Further A-NaOH pretreatment
significantly promoted dark fermentation bio-H
2
production
(152.3, 99.1, and 76.9 mL/g TS, respectively) and volatile acid production
(4660.2, 3720.2, and 3496.2 mg/L, respectively) of
P. sinese
, oak, and camphor wood. These findings show that A-NaOH pretreatment
is an effective means of utilization of lignocellulose resources.
“…Thermal conductivity governs the rate of heat dissipation in the corn stover storage (Karki et al, 2015). Heat transport by conduction was experimentally performed with a feedback loop through a water jacket in the corn stover storage reactor, as described in section "Corn Stover Storage Reactor Experiments" Conductive heat transfer (Q k ) is modeled as a function of the thermal conductivity (K), the characteristic length (L), the heat flux area (A), and the net temperature difference between the corn stover and water jacket (T 2 − T 1 ) following Eq.…”
Section: Conductive Heat Transfermentioning
confidence: 99%
“…Corn stover density at sieve materials sizes of 2 mm, 4 mm, and 8 mm are reported at 942, 954, and 832 kg.m −3 , respectively (Karki et al, 2015). The uncertainty of density is assumed negligible in the model.…”
Corn stover dry matter loss effects variability for biofuel conversion facility and technology sustainability. This research seeks to understand the dynamic mechanisms of the thermal system, organic matter loss, and microbial heat generation in corn stover storage operations through system dynamics, a mathematical modeling approach, and response analysis to improve the system performance. This study considers epistemic uncertainties including cardinal temperatures of microbial respiratory activity, specific degradation rate, heat evolution per unit substrate degraded, and thermal conductivity in corn stover storage reactors. These uncertainties were managed through calibration, a process of improving the agreement between the computational and benchmark experimental results by adjusting the parameters of the model. Model calibration successfully predicted the temperature of the system as quantified by the mean absolute error, 0.6 • C, relative to the experimental work. The model and experimental dry matter loss after 30 days of storage were 5.1% and 4.9 ± 0.28%. The model was further validated using additional experimental results to ensure that the model accurately represented the system. Model validation obtained a temperature mean absolute relative error of 0.9 ± 0.3 • C and dry matter loss relative error of 3.1 ± 1.5%. This study presents a robust prediction of corn stover storage temperature and demonstrates that an understanding of carbon sources, microbial communities, and lag-phase evolution in bi-phasic growth are essential for the prediction of organic matter preservation in corn stover storage systems under environment's variation.
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