Investigation of Nickel as a Metal Substitute of Palladium Supported on HBeta Zeolite for Waste Tire Pyrolysis
Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 32799
Investigation of Nickel as a Metal Substitute of Palladium Supported on HBeta Zeolite for Waste Tire Pyrolysis

Authors: Lalita Saeaeh, Sirirat Jitkarnka

Abstract:

Pyrolysis of waste tire is one of alternative technique to produce petrochemicals, such as light olefins, mixed C4, and monoaromatics. Noble metals supported on acid zeolite catalysts were reported as potential catalysts to produce the high valuable products from waste tire pyrolysis. Especially, Pd supported on HBeta gave a high yield of olefins, mixed C4, and mono-aromatics. Due to the high prices of noble metals, the objective of this work was to investigate whether or not a non-noble Ni metal can be used as a substitute of a noble metal, Pd, supported on HBeta as a catalyst for waste tire pyrolysis. Ni metal was selected in this work because Ni has high activity in cracking, isomerization, hydrogenation and the ring opening of hydrocarbons Moreover, Ni is an element in the same group as Pd noble metal, which is VIIIB group, aiming to produce high valuable products similarly obtained from Pd. The amount of Ni was varied as 5, 10, and 20% by weight, for comparison with a fixed 1 wt% Pd, using incipient wetness impregnation. The results showed that as a petrochemical-producing catalyst, 10%Ni/HBeta performed better than 1%Pd/HBeta because it did not only produce the highest yield of olefins and cooking gases, but the yields were also higher than 1%Pd/HBeta. 5%Ni/HBeta can be used as a substitute of 1%Pd/HBeta for similar crude production because its crude contains the similar amounts of naphtha and saturated HCs, although it gave no concentration of light mono-aromatics (C6-C11) in the oil. Additionally, 10%Ni/HBeta that gave high olefins and cooking gases was found to give a fairly high concentration of the light mono-aromatics in the oil.

Keywords: Catalytic pyrolysis; Waste tire; Pd; Ni; HBeta

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1077966

Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 1800

References:


[1] Chang, Y.M., (1996). On pyrolysis of waste tire: degradation rate and product yields. Resources, Consevation and Recycling, 17, 125-139
[2] Díez, C., Martínez, O., Calvo, L.F., Cara, J., and Morán, A.,(2004). Pyrolysis of tyres. Influence of the final temperature of the process on emissions and the calorific value of the products recovered. Waste Management, 24, 463-469
[3] Williams, P.T. and Taylor, D.T., (1993). Aromatization of type pyrolysis oil to yield polycyclic aromatic hydrocarbons. Fuel, 72, 1469-1474
[4] Williams, P.T., Serpil Besler., and Taylor, D.T., (1990). The pyrolysis of scrap automotive tyres The influence of temperature and heating rate on product composition. Fuel, 69, 1474-1482
[5] D┼®ng, N.A., Tanglumlert, W., and Jitkarnka, S., (2008). Effects of pyrolysis temperature and Pt-loaded catalysts on polar-aromatic content in tire-derived oil. Applied Catalysis B: Environmental, 91, 300-307
[6] Ishihara, A., Dumeignil, F., Lee, J., Mitsuhashi, K., Qian, E.W., and Kabe, T., (2005). Hydrodesulfurization of sulfur-containing polyaromatic compounds in light gas oil using noble metal catalysts. Applied Catalysis A: General, 289, 163-173
[7] Tang, T., Yin, C., Wang, L., Ji, Y., and Xiao, F-S.(2008). Good sulfur tolerance of a mesoporous Beta zeolite-supported palladium catalyst in the deep hydrogenation of aromatics: Journal of catalysis, 257, 125-133
[8] Loiha, S., Föttinger, K., Zorn, K., Klysubun, W., Rupprechter, G., and Wittayakun, J., (2009). Catalytic enhancement of platinum supported on zeolite beta for toluene hydrogenation by addition of palladium. Journal of Industrial and Engineering Chemistry, 15, 819-823
[9] Casta├▒o, P., Pawelec, B., Fierro, J.L.G., Arandes, J.M., and Bilbal, J.,(2007). Enhancement of pyrolysis gasoline hydrogenation over Pdpromoted Ni/Si02-Al2O3 catalysts: Feul, 86, 2264-2274
[10] Choosuton, A., (2007). Development of Waste Tire Pyrolysis for the Production of Commercial Fuels: Effect of Noble Metals and Supports. M.S. Thesis, The Petroleum and Petrochemical College, Chulalongkorn University, Bangkok, Thailand.
[11] Fúnez, A., Lucas, A.D., Sánchez, P., Ramos, M.J., and Valverde, J.L., (2008) Hydroisomerization in liquid phase of a refinery naphtha stream over Pt-Ni/H-beta zeolite catalysts. Chemical Engineering Journal, 136, 267-275
[12] Cańizares, P., De Lucas, A., Dorado, F., Dur├ín, and A., Asencio, I., (1998) Characterization of Ni and Pd supported on H-mordenite catalysts: Infuence of the metal loading method. Applied Catalysis A: General 169, 137-150
[13] Jao, R.M, Lin, T.B, and Chang, J.R., (1996) Light Naphtha Isomerization over Mordenite-Supported Ni-Pt Catalysts:Effects of Ni on the Catalytic Performance for Pure Feed and Sulfur-Containing Feed JOURNAL OF CATALYSIS 161, 222-229 (1996).
[14] Sebor.G, Blazek.J, and Nemer.M.F., (1999) Optimization of the preparative separation of petroleum maltenes by liquid adsorption chromatography. Journal of Chromatography A, 847, 323-330.
[15] Eswaramoorthi, L., Bhavani, A.G., and Lingappan, N., (2003). Activity, selectivity and stability of Ni-Pt loaded zeolite-β and mordenite catalysts for hydroisomerisation of n-heptane. Applied Catalysis A: General, 253, 469-486