© The Institution of Engineering and Technology
A series of CuO/SiO2 catalysts containing different modifiers were prepared via co-precipitation and used for glycerol hydrogenolysis. CuO–CeO2/SiO2 gave the best glycerol conversion rate (100%) and highest selectivity for 1,2-propanediol (up to 95%). Reactions were carried out under the following conditions: temperature, 220°C; H2 pressure, 0.5 MPa; glycerol concentration, 100 wt.%; and H2/glycerol molar ratio, 35:1. The catalysts were characterised by X-ray diffraction, NH3 temperature-programmed desorption, N2 adsorption, and scanning electron microscopy. The CuO–CeO2/SiO2 catalyst had smaller particle sizes, better dispersion, and greater specific surface area than the CuO/SiO2, CuO–phosphotungstic acid (PTA)/SiO2, and CuO–CeO2–PTA/SiO2 catalysts.
References
-
-
1)
-
12. Feng, J., Wang, J., Zhou, Y., et al: ‘ChemInform abstract: effect of base additives on the selective hydrogenolysis of glycerol over Ru/TiO2 catalyst’, ChemInform, 2008, 39, (9), pp. 1274–1275 (doi: 10.1002/chin.200809066).
-
2)
-
3. Huber, G.W., Dumesic, J.A.: ‘Production of liquid alkanes by aqueous-phase processing of biomass-derived carbohydrates’, Science, 2005, 308, (5727), pp. 1446–1450 (doi: 10.1126/science.1111166).
-
3)
-
7. Feng, Y., Yin, H., Wang, A., et al: ‘Gas phase hydrogenolysis of glycerol catalyzed by Cu/ZnO/MOx (MOx=Al2O3, TiO2, and ZrO2) catalysts’, Midwifery, 2011, 168, (1), pp. 403–412.
-
4)
-
13. Vasiliadou, E.S., Heracleous, E., Vasalos, I.A., et al: ‘Ru-based catalysts for glycerol hydrogenolysis – effect of support and metal precursor’, Appl. Catal. B, Environ., 2009, 92, (1-2), pp. 90–99 (doi: 10.1016/j.apcatb.2009.07.018).
-
5)
-
21. Nakagawa, Y., Shinmi, Y., Koso, S., et al: ‘Direct hydrogenolysis of glycerol into 1,3-propanediol over rhenium-modified iridium catalyst’, J. Catal., 2010, 272, (2), pp. 191–194 (doi: 10.1016/j.jcat.2010.04.009).
-
6)
-
19. Guo, X., Li, Y., Shi, R., et al: ‘Co/MgO catalysts for hydrogenolysis of glycerol to 1, 2-propanediol’, Appl. Catal. A, Gen., 2009, 371, (1), pp. 108–113 (doi: 10.1016/j.apcata.2009.09.037).
-
7)
-
9. Schmidt, S.R., Tanielyan, S.K., Marin, N., et al: ‘Selective conversion of glycerol to propylene glycol over fixed bed Raney® Cu catalysts’, Top. Catal., 2010, 53, (53), pp. 1214–1216 (doi: 10.1007/s11244-010-9565-x).
-
8)
-
10. Vasiliadou, E.S., Lemonidou, A.A.: ‘Investigating the performance and deactivation behaviour of silica-supported copper catalysts in glycerol hydrogenolysis’, Appl. Catal. A, Gen., 2011, 396, (1-2), pp. 177–185 (doi: 10.1016/j.apcata.2011.02.014).
-
9)
-
18. Zhu, S., Zhu, Y., Hao, S., et al: ‘Aqueous-phase hydrogenolysis of glycerol to 1,3-propanediol over Pt-H4SiW12O40/SiO2’, Catal. Lett., 2012, 142, (2), pp. 267–274 (doi: 10.1007/s10562-011-0757-1).
-
10)
-
16. Shinmi, Y., Koso, S., Kubota, T., et al: ‘Modification of Rh/SiO2 catalyst for the hydrogenolysis of glycerol in water’, Appl. Catal. B, Environ., 2010, 94, (3), pp. 318–326 (doi: 10.1016/j.apcatb.2009.11.021).
-
11)
-
23. Zhou, J., Zhang, J., Guo, X., et al: ‘Ag/Al2O3 for glycerol hydrogenolysis to 1,2-propanediol: activity, selectivity and deactivation’, Green Chem., 2012, 14, (14), pp. 156–163 (doi: 10.1039/C1GC15918F).
-
12)
-
11. Alhanash, A., Kozhevnikova, E.F., Kozhevnikov, I.V.: ‘Hydrogenolysis of glycerol to propanediol over Ru: polyoxometalate bifunctional catalyst’, Catal. Lett., 2008, 120, (120), pp. 307–311 (doi: 10.1007/s10562-007-9286-3).
-
13)
-
14. Furikado, I., Miyazawa, T., Koso, S., et al: ‘Catalytic performance of Rh/SiO2 in glycerol reaction under hydrogen’, Green Chem., 2007, 9, (6), pp. 582–588 (doi: 10.1039/b614253b).
-
14)
-
22. Wen, G., Xu, Y., Liu, Q., et al: ‘Preparation of Ce-modified Raney Ni catalysts and their application in aqueous-phase reforming of cellulose’, Catal. Lett., 2011, 141, (12), pp. 1851–1858 (doi: 10.1007/s10562-011-0712-1).
-
15)
-
8. Huang, L., Zhu, Y., Zheng, H., et al: ‘Direct conversion of glycerol into 1,3-propanediol over Cu-H4 SiW12O40/SiO2 in vapor phase’, Catal. Lett., 2009, 131, (1), pp. 312–320 (doi: 10.1007/s10562-009-9914-1).
-
16)
-
1. Hoekman, S.K.: ‘Biofuels in the U.S. – challenges and opportunities’, Renew. Energy, 2009, 34, (1), pp. 14–22 (doi: 10.1016/j.renene.2008.04.030).
-
17)
-
17. Yuan, Z., Wu, P., Gao, J., et al: ‘Pt/solid-base: a predominant catalyst for glycerol hydrogenolysis in a base-free aqueous solution’, Catal. Lett., 2009, 130, (1), pp. 261–265 (doi: 10.1007/s10562-009-9879-0).
-
18)
-
5. Balaraju, M., Rekha, V., Prasad, P.S.S., et al: ‘Selective hydrogenolysis of glycerol to 1, 2 propanediol over Cu–ZnO catalysts’, Catal. Lett., 2008, 126, (126), pp. 119–124 (doi: 10.1007/s10562-008-9590-6).
-
19)
-
6. Dasari, M.A., Kiatsimkul, P.P., Sutterlin, W.R., et al: ‘Low-pressure hydrogenolysis of glycerol to propylene glycol’, Appl. Catal. A, Gen., 2005, 281, (1-2), pp. 225–231 (doi: 10.1016/j.apcata.2004.11.033).
-
20)
-
20. Liu, Q., Guo, X., Chen, J., et al: ‘Cobalt nanowires prepared by heterogeneous nucleation in propanediol and their catalytic properties’, Nanotechnology, 2008, 19, (36), pp. 2618–2624 (doi: 10.1088/0957-4484/19/36/365608).
-
21)
-
4. Song, R., Qian, R., Li, C., et al: ‘Advances in new usage of glycerol’, China Oils Fats, 2008, 05, pp. 40–44.
-
22)
-
2. Manaţe, D., Cuzman, I., Fărcaş, P.: ‘Renewables energies industry in the current investment context’, Timisoara J. Econ., 2011, 4, (2(14)), pp. 97–103.
-
23)
-
15. Nakagawa, Y., Tomishige, K.: ‘Catalyst development for the hydrogenolysis of biomass-derived chemicals to value-added ones’, Catal. Surv. Asia, 2011, 15, (2), pp. 111–116 (doi: 10.1007/s10563-011-9114-z).
http://iet.metastore.ingenta.com/content/journals/10.1049/mnl.2016.0710
Related content
content/journals/10.1049/mnl.2016.0710
pub_keyword,iet_inspecKeyword,pub_concept
6
6