585
291. Kim HD, Park HJ, Kim TW, Jeong K-E, Chae H-J, Jeong S-Y, Lee C-H, Kim C-U (2012)
Hydrogen production through the aqueous phase reforming of ethylene glycol over supported Pt-based bimetallic catalysts. Int J Hydrog Energy 37(10):8310–8317. https://doi.
org/10.1016/j.ijhydene.2012.02.160
292. Kim HD, Park HJ, Kim TW, Jeong K-E, Chae H-J, Jeong S-Y, Lee C-H, Kim C-U (2012)
The effect of support and reaction conditions on aqueous phase reforming of polyol over
supported Pt-Re bimetallic catalysts. Catal Today 185(1):73–80. https://doi.org/10.1016/j.
cattod.2011.08.012
293. Huber GW, Shabaker JW, Evans ST, Dumesic JA (2006) Aqueous-phase reforming of ethylene glycol over supported Pt and Pd bimetallic catalysts. Appl Catal B Environ 62:226–235.
https://doi.org/10.1016/j.apcatb.2005.07.010
294. Bai Y, Lu CS, Ma L, Chen P, Zheng YF, Li XN (2006) Hydrogen production by aqueousphase reforming of ethylene glycol over Pt catalysts supported on γ-Al2O3 modified with Ce
and Mg. Chin J Catal 27(3):275–280
295. Wawrzetz A, Peng B, Hrabar A, Jentys A, Lemonidou AA, Lercher JA (2010) Towards understanding the bifunctional hydrodeoxygenation and aqueous phase reforming of glycerol. J
Catal 269(2):411–420. https://doi.org/10.1016/j.jcat.2009.11.027
296. Barbelli ML, Pompeo F, Santori GF, Nichio NN (2013) Pt catalyst supported on α-Al 2 O 3 modified with CeO 2 and ZrO 2 for aqueous-phase-reforming of glycerol. Catal Today 213:58–64.
https://doi.org/10.1016/j.cattod.2013.02.023
297. Wen G, Xu Y, Ma H, Xu Z, Tian Z (2008) Production of hydrogen by aqueous-phase
reforming of glycerol. Int J Hydrog Energy 33(22):6657–6666. https://doi.org/10.1016/j.
ijhydene.2008.07.072
298. Fasolini A, Cespi D, Tabanelli T, Cucciniello R, Cavani F (2019) Hydrogen from renewables:
a case study of glycerol reforming. Catalysts 9:722. https://doi.org/10.3390/catal9090722
299. Seretis A, Tsiakaras P (2016) Hydrogenolysis of glycerol to propylene glycol by in situ
produced hydrogen from aqueous phase reforming of glycerol over SiO 2 – Al 2 O 3 supported
nickel catalyst. Fuel Process Technol 142:135–146
300. Iriondo A, Barrio VL, Cambra JF, Arias PL, Guemez MB, Navarro RM, Sánchez-Sánchez
MC, Fierro JLG (2008) Hydrogen production from glycerol over nickel catalysts supported on Al 2 O 3 modified by Mg, Zr, Ce or La. Top Catal 49:46–58. https://doi.org/10.1007/
s11244- 008- 9060- 9
301. Haryanto A, Fernando S, Murali N, Adhikari S (2005) Current status of hydrogen production
techniques by steam reforming of ethanol: a review. Energy Fuel 19:2098–2106. https://doi.
org/10.1021/ef0500538
302. Tokarev A, Kirilin A, Murzina E, Eranen K, Mikkola JP (2010) The role of bio-ethanol in
aqueous phase reforming to sustainable hydrogen. Int J Hydrog Energy 35:12642–12649.
https://doi.org/10.1016/j.ijhydene.2010.07.118
303. Roy B, Loganathan K, Pham H, Datye AK, Leclerc CA (2010) Surface modification of solution combustion synthesized Ni/Al 2 O 3 catalyst for aqueous-phase reforming of ethanol. Int J
Hydrog Energy 35:11700–11708. https://doi.org/10.1016/j.ijhydene.2010.07.167
304. Roy B, Martinez U, Loganathan K, Datye AK, Leclerc CA (2012) Effect of preparation
methods on the performance of Ni/Al 2 O 3 catalysts for aqueous-phase reforming of ethanol: Part I catalytic activity. Int J Hydrog Energy 37:8143–8153. https://doi.org/10.1016/j.
ijhydene.2012.02.056
305. Roy B, Artyushkova K, Pham H, Li L, Leclerc CA (2012) Effect of preparation method
on the performance of the Ni/Al 2 O 3 catalysts for aqueous-phase reforming of ethanol:
Part II characterization. Int J Hydrog Energy 37:18815–18826. https://doi.org/10.1016/j.
ijhydene.2012.09.098
306. Nozawa T, Mizukoshi Y, Yoshida A, Naito S (2014) Aqueous phase reforming of ethanol and
acetic acid over TiO2 supported Ru catalysts. Appl Catal B Environ 146:221–226. https://doi.
org/10.1016/j.apcatb.2013.06.017
Catalytic Conversion of Alcohols into Value-Added Products
291. Kim HD, Park HJ, Kim TW, Jeong K-E, Chae H-J, Jeong S-Y, Lee C-H, Kim C-U (2012)
Hydrogen production through the aqueous phase reforming of ethylene glycol over supported Pt-based bimetallic catalysts. Int J Hydrog Energy 37(10):8310–8317. https://doi.
org/10.1016/j.ijhydene.2012.02.160
292. Kim HD, Park HJ, Kim TW, Jeong K-E, Chae H-J, Jeong S-Y, Lee C-H, Kim C-U (2012)
The effect of support and reaction conditions on aqueous phase reforming of polyol over
supported Pt-Re bimetallic catalysts. Catal Today 185(1):73–80. https://doi.org/10.1016/j.
cattod.2011.08.012
293. Huber GW, Shabaker JW, Evans ST, Dumesic JA (2006) Aqueous-phase reforming of ethylene glycol over supported Pt and Pd bimetallic catalysts. Appl Catal B Environ 62:226–235.
https://doi.org/10.1016/j.apcatb.2005.07.010
294. Bai Y, Lu CS, Ma L, Chen P, Zheng YF, Li XN (2006) Hydrogen production by aqueousphase reforming of ethylene glycol over Pt catalysts supported on γ-Al2O3 modified with Ce
and Mg. Chin J Catal 27(3):275–280
295. Wawrzetz A, Peng B, Hrabar A, Jentys A, Lemonidou AA, Lercher JA (2010) Towards understanding the bifunctional hydrodeoxygenation and aqueous phase reforming of glycerol. J
Catal 269(2):411–420. https://doi.org/10.1016/j.jcat.2009.11.027
296. Barbelli ML, Pompeo F, Santori GF, Nichio NN (2013) Pt catalyst supported on α-Al 2 O 3 modified with CeO 2 and ZrO 2 for aqueous-phase-reforming of glycerol. Catal Today 213:58–64.
https://doi.org/10.1016/j.cattod.2013.02.023
297. Wen G, Xu Y, Ma H, Xu Z, Tian Z (2008) Production of hydrogen by aqueous-phase
reforming of glycerol. Int J Hydrog Energy 33(22):6657–6666. https://doi.org/10.1016/j.
ijhydene.2008.07.072
298. Fasolini A, Cespi D, Tabanelli T, Cucciniello R, Cavani F (2019) Hydrogen from renewables:
a case study of glycerol reforming. Catalysts 9:722. https://doi.org/10.3390/catal9090722
299. Seretis A, Tsiakaras P (2016) Hydrogenolysis of glycerol to propylene glycol by in situ
produced hydrogen from aqueous phase reforming of glycerol over SiO 2 – Al 2 O 3 supported
nickel catalyst. Fuel Process Technol 142:135–146
300. Iriondo A, Barrio VL, Cambra JF, Arias PL, Guemez MB, Navarro RM, Sánchez-Sánchez
MC, Fierro JLG (2008) Hydrogen production from glycerol over nickel catalysts supported on Al 2 O 3 modified by Mg, Zr, Ce or La. Top Catal 49:46–58. https://doi.org/10.1007/
s11244- 008- 9060- 9
301. Haryanto A, Fernando S, Murali N, Adhikari S (2005) Current status of hydrogen production
techniques by steam reforming of ethanol: a review. Energy Fuel 19:2098–2106. https://doi.
org/10.1021/ef0500538
302. Tokarev A, Kirilin A, Murzina E, Eranen K, Mikkola JP (2010) The role of bio-ethanol in
aqueous phase reforming to sustainable hydrogen. Int J Hydrog Energy 35:12642–12649.
https://doi.org/10.1016/j.ijhydene.2010.07.118
303. Roy B, Loganathan K, Pham H, Datye AK, Leclerc CA (2010) Surface modification of solution combustion synthesized Ni/Al 2 O 3 catalyst for aqueous-phase reforming of ethanol. Int J
Hydrog Energy 35:11700–11708. https://doi.org/10.1016/j.ijhydene.2010.07.167
304. Roy B, Martinez U, Loganathan K, Datye AK, Leclerc CA (2012) Effect of preparation
methods on the performance of Ni/Al 2 O 3 catalysts for aqueous-phase reforming of ethanol: Part I catalytic activity. Int J Hydrog Energy 37:8143–8153. https://doi.org/10.1016/j.
ijhydene.2012.02.056
305. Roy B, Artyushkova K, Pham H, Li L, Leclerc CA (2012) Effect of preparation method
on the performance of the Ni/Al 2 O 3 catalysts for aqueous-phase reforming of ethanol:
Part II characterization. Int J Hydrog Energy 37:18815–18826. https://doi.org/10.1016/j.
ijhydene.2012.09.098
306. Nozawa T, Mizukoshi Y, Yoshida A, Naito S (2014) Aqueous phase reforming of ethanol and
acetic acid over TiO2 supported Ru catalysts. Appl Catal B Environ 146:221–226. https://doi.
org/10.1016/j.apcatb.2013.06.017
Catalytic Conversion of Alcohols into Value-Added Products