2014
DOI: 10.1016/j.fuel.2013.11.026
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Experimental and modeling study of pinewood char gasification with CO2

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Cited by 67 publications
(43 citation statements)
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“…Mentioned disadvantages can be eliminated by a heat processing of raw materials into energy products of acceptable quality, such as solid composite [8][9][10][11][12], liquid [13][14][15] or gaseous fuels [16][17][18]. Given the advantages of the gaseous fuels energy use (possibility of combustion process automating, ecological compatibility, low abrasive deterioration of heating surfaces and intensive heat transfer due to higher flow velocities available), the authors examined processing of low-grade raw material to a gaseous fuel.…”
Section: Discussionmentioning
confidence: 99%
“…Mentioned disadvantages can be eliminated by a heat processing of raw materials into energy products of acceptable quality, such as solid composite [8][9][10][11][12], liquid [13][14][15] or gaseous fuels [16][17][18]. Given the advantages of the gaseous fuels energy use (possibility of combustion process automating, ecological compatibility, low abrasive deterioration of heating surfaces and intensive heat transfer due to higher flow velocities available), the authors examined processing of low-grade raw material to a gaseous fuel.…”
Section: Discussionmentioning
confidence: 99%
“…It is thought that the gasification of solid fuel is actual and perspective direction of research, given that this technology is allows to use low grade fuels with producing of high quality gas and solid products [4][5][6]. The developments, reduced heat consumption for own needs by autothermal mode of gasification, are exist.…”
Section: The Gasification Rolementioning
confidence: 99%
“…(35) with (32) Sircar et al (2014) have highlighted that the structural parameter (ψ in Eq. (36)) of the random pore model increases with gasification temperature in many studies on biomass char gasification Consequently based on the relation (36) the activation energy of k 2 should be higher than the activation energy of k 1 .…”
Section: Effect Of Steam Gasification Temperature On Gasification Ratementioning
confidence: 99%
“…k 2 (mol m À 3 ) À 1 s À 1 2.98*10 À 5 5.285*10 À 5 K (mol m À 3 ) À 1 0.264 0.0357 σ 0 (m 2 kg À 1 ) 200000 200000 (Sircar et al, 2014) τ 5 5 Assumed based on (Satterfield, 1970) ψ 5.5 5.5 (Sircar et al, 2014) D m (m 2 s À 1 ) 9.94*10 À 5 1.596*10 À 4 (Perry and Green, 1999) Table 3 External convective transfer coefficient and Biot number as functions of reactant gas and particle size (calculated for the conditions in Table 2). …”
Section: Reactant Gas Co 2 H 2 O Referencementioning
confidence: 99%