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Glycerol reforming

Current biodiesel can not be considered as a 100% biomass-based fuel as long as methanol is derived from petrochemical resources. A clean way to solve the biorelated problem is the conversion of glycerol waste from the transesterification process into syngas. In this context, glycerol reforming is a suitable target reaction worthy of study. [Pg.249]

Chen, H., Ding, Y., Cong, N. T., Don, B., Dupont, V., Ghadiri, M., et al. (2011). A comparative study on hydrogen production from steam-glycerol reforming thermodynamics and experimental. Ren Energy, 36, 779—788. [Pg.264]

Two-bed membrane reactor for integrated process involving aqueous-phase glycerol reforming to synthesis gas coupled with DME synthesis process combines two physically separated enclosures (Figure 5.13). The first unit is a tube-in-tube fixed-bed water perm-selective membrane reactor for DME synthesis process. The reaction-side compartment (outer tube) is packed with bifunctional catalytic particles for DME synthesis, whereas the permeate-side compartment (inner tube) is an empty... [Pg.121]

Figure 5.13 Schematic diagram of two-bed reactor system for DME production from glycerol via an integrated process involving aqueous-phase glycerol reforming coupled with DME synthesis process. Figure 5.13 Schematic diagram of two-bed reactor system for DME production from glycerol via an integrated process involving aqueous-phase glycerol reforming coupled with DME synthesis process.
Figure 5.14 Steady-state axial profiles of the volumetric gas flow rate (a) and temperature (b) for aqueous-phase glycerol reforming and DME synthesis without in situ H2O removal. Figure 5.14 Steady-state axial profiles of the volumetric gas flow rate (a) and temperature (b) for aqueous-phase glycerol reforming and DME synthesis without in situ H2O removal.
With in situ H2O removal, the exothermic reactions in DME synthesis unit make possible the endothermic aqueous-phase glycerol reforming process, and the aqueous-phase glycerol reforming process produces the synthesis gas appropriate for DME synthesis process (Figure 5.15). Simulations surest that allothermal operation could be achieved the overall energy balance is favorable, and the synthesis gas produced in... [Pg.125]

CO = 0.5% Aqueous-phase glycerol reforming unit-trickle-bed reactor ... [Pg.125]

Diuta I, Iliuta MC, Fongarland P, Larachi F. Integrated aqueous glycerol reforming to dimethyl ether synthesis—a novel allother-mal dual bed membrane reactor concept Chem. Eng. J. 2012b 187 311... [Pg.131]

Authayamun S, Maunlouk M, Scott K et ad (2013) Comparison of high-temperature amd low-temperature polymer electrolyte membrane fuel cell systems with glycerol reforming process for stationary applications. Appl Energy 109 192-201... [Pg.418]

Wu, G., Li, S., Zhang, C, Wang, T., and Gong, J. (2014) Glycerol reforming over perovskite-derived nickel-based catalysts. Appl Catal B 144, 277-285. [Pg.556]

Ni/Si02 fiber catalyst prepared by electrospinning technique for glycerol reforming to synthesis gas... [Pg.689]

Keywords Ni/Si02, fiber catalyst, electrospinning, glycerol, reforming... [Pg.689]


See other pages where Glycerol reforming is mentioned: [Pg.242]    [Pg.249]    [Pg.249]    [Pg.249]    [Pg.250]    [Pg.435]    [Pg.220]    [Pg.88]    [Pg.97]    [Pg.98]    [Pg.110]    [Pg.121]    [Pg.121]    [Pg.123]    [Pg.125]    [Pg.125]    [Pg.125]    [Pg.126]    [Pg.126]    [Pg.127]    [Pg.128]    [Pg.390]    [Pg.554]   
See also in sourсe #XX -- [ Pg.219 , Pg.249 ]




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Glycerol steam reforming

Glycerol steam reforming hydrogen production

Glycerol steam reforming reactions

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