2018
DOI: 10.1016/j.biortech.2017.11.012
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Pyrolysis/gasification of pine sawdust biomass briquettes under carbon dioxide atmosphere: Study on carbon dioxide reduction (utilization) and biochar briquettes physicochemical properties

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Cited by 73 publications
(18 citation statements)
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“…Apart from the conventional two-step physical activation (carbonization/activation), the one-step gasification in an oxidizing gas by heating a precursor from room temperature to the desired activation temperature can also be utilized for the production of activated carbon. As an example, Liu et al [ 33 ] synthesized activated char briquette from the pine sawdust briquette at the maximum gasification temperature of 800 °C under 100% CO 2 using the one-step heating that produced the activated biochar with reasonable BET surface area of around 478 m 2 /g. However, the application of the two-step activation is more advantageous for the reason that it could effectively remove tarry materials during the first carbonization step, giving better quality char for the following activation step.…”
Section: Resultsmentioning
confidence: 99%
“…Apart from the conventional two-step physical activation (carbonization/activation), the one-step gasification in an oxidizing gas by heating a precursor from room temperature to the desired activation temperature can also be utilized for the production of activated carbon. As an example, Liu et al [ 33 ] synthesized activated char briquette from the pine sawdust briquette at the maximum gasification temperature of 800 °C under 100% CO 2 using the one-step heating that produced the activated biochar with reasonable BET surface area of around 478 m 2 /g. However, the application of the two-step activation is more advantageous for the reason that it could effectively remove tarry materials during the first carbonization step, giving better quality char for the following activation step.…”
Section: Resultsmentioning
confidence: 99%
“…Generally, the high heating values (HHV) of chars make them attractive sources for clean energy production instead of fossil-based solid fuels [26,27]. HHVs reported in literature for chars produced from biomass vary between 10 MJ/kg (as for seaweed derived chars [28]) and 9 33 MJ/kg (for pinewood derived chars [29]), while the HHV for coal vary between 14 and 35 MJ/kg [30].…”
Section: Energy Contents and Chemical Compositionmentioning
confidence: 99%
“…23,67 This is due to the combination of CO 2 and steam, promoting the cracking of tar via steam and dry reforming reactions. 39 Moreover, an enhancement in char properties (high porosity; 618 m 2 /g) results from the presence of CO 2 during pyrolysis compared to 98.4 m 2 /g in a N 2 atmosphere (Table 4) and also promotes the tar cracking/reforming process by adsorbing along the pores distributed at the surface of the char. 53,68 At a fixed S/C molar ratio of 3.4, the tar gradually decreased with the increasing CO 2 percentage in the carrier gas, i.e., from 18.3 g/Nm 3 at a CO 2 /N 2 ratio of 1:5 to 12.6 g/Nm 3 at a CO 2 /N 2 ratio of 1:1 and 11.9 g/Nm 3 at a CO 2 /N 2 ratio of 5:1, respectively (Table 8), which is similar to what is reported in the literature.…”
Section: Effect Of Comentioning
confidence: 99%
“…Recently, CO 2 has been considered as an oxidizing agent for biomass gasification to obtain high-quality syngas/H 2 production. , A number of studies were carried out using a computational model, focusing on the effects of operating conditions in the CO 2 -assisted biomass steam gasification, e.g., CO 2 concentration in the carrier gas, CO 2 pressure, CO 2 /H 2 O ratio, and CO 2 /C ratio , on the reaction rate, syngas properties, and process efficiency, including model validating using experimental data. However, in previous experimental studies, workers only focused on the effect of CO 2 as a single step either pyrolysis of biomass , or biomass char gasification , without providing any systematic effects and interactions among CO 2 concentration in the carrier gas, steam, and catalyst on H 2 /syngas production and gasification performance in the entire biomass gasification process. Therefore, in this study, the synergetic effect of CO 2 (CO 2 concentration), steam (steam to carbon in the feedstock molar ratio), and incorporation of catalysts (Ni/RM, Ni/HZSM-5, and Ni/Al 2 O 3 ) with a tight control of the gasification process on the properties of the product gas composition and process efficiency was investigated via two-stage gasification in which feedstock was decomposed into intermediate products (eq ) at the first stage and subsequently gasified (eqs –) at the second stage of the gasifier. …”
Section: Introductionmentioning
confidence: 99%