“…The preceding char gasification behavior in MFBRA exhibited an obvious difference with those from the literature reports using TGA [26][27][28][29]. The latter reported usually that the reaction rate at the beginning was very low, and the peak reaction rate appears in the conversion range of 0.3-0.7.…”
Section: Char Gasification Behavior In Mfbracontrasting
“…The preceding char gasification behavior in MFBRA exhibited an obvious difference with those from the literature reports using TGA [26][27][28][29]. The latter reported usually that the reaction rate at the beginning was very low, and the peak reaction rate appears in the conversion range of 0.3-0.7.…”
Section: Char Gasification Behavior In Mfbracontrasting
“…Chemical composition of coal: Volatile matter, moisture and ash content have the primary effect on gasification reaction [16][17][18][19] . Several studies have been published on coal analysis (see for example refs 20, 21).…”
Section: Key Factors Influencing Ucgmentioning
confidence: 99%
“…Studies considering the reaction kinetics and source terms while dealing with the seam as porous media using a single-step decomposition method and analysing the role of frequency factors and activation energies of several reactions have been undertaken 26,27 . Recently even the pyrolysis and the use of CO 2 as a gasifying agent have been tested in sub-bituminous coal as well as lignite [28][29][30][31] . Even the modelling of species diffusion for CO 2 gasification in the UCG context, for single particle basis using TGA study of CO 2 gasification has been studied and reported 32 .…”
Section: Modelling Of Ucg For Successful Deployment: Status In Indiamentioning
Globally, the sheen of coal-based energy production is slowly wearing, with few exceptions of developing novel technologies that aid in coal gasification and gas clean-up
“…[42] A coke mass of 50 mg was used in each test with a size below 90 lm, a particle size which has been considered safe for coal gasification to rule out intra-particle diffusion. [43] Inter-particle diffusion control was ruled out by performing tests at 1050°C with 50, 100, and 150 mg of material with both H 2 O and CO 2 , in which no difference in conversion rate was observed compared to from sample mass. The carbon conversion curves are depicted in Figure 6.…”
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