H-ZSM-11 and Zn-ZSM-11 zeolites and their applications in the catalytic transformation of LDPE

被引:63
作者
Renzini, Maria S. [2 ]
Sedran, Ulises [1 ]
Pierella, Liliana B. [2 ]
机构
[1] UNL CONICET, FIQ, INCAPE, Santa Fe, Argentina
[2] Univ Tecnol Nacl, Fac Cordoba, Grp Zeolitas, CITeQ, Cordoba, Argentina
关键词
LDPE; Thermal and catalytic degradation; ZSM-11; Aromatics; SOLID ACID CATALYSTS; CRACKING CATALYSTS; PLASTIC WASTES; POLYETHYLENE; DEGRADATION; FUEL; HYDROCARBONS; PYROLYSIS; DENSITY; BLENDS;
D O I
10.1016/j.jaap.2009.06.008
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Low density polyethylene was converted into hydrocarbons over Zn- and H-ZSM-11 zeolite catalysts in a fixed-bed reactor during 20 and 60 min reaction time, 0.5 and 2.0 polymer to catalyst mass ratio at 500 degrees C. The zeolites were synthesized by conventional techniques and characterized by XRD, pyridine FTIR and N-2 adsorption. The adsorbed pyridine spectra demonstrated that new Lewis sites were formed after Zn exchange, and that the relationship between Lewis and Bronsted sites in the Zn-ZSM-11 zeolite (3.53) was much higher than that in the H-ZSM-11 zeolite (0.09). Thermal analyses confirmed that the temperature of decomposition of the polymer can be decreased in as much as about 145 degrees C when the catalysts were added. As compared to the thermal degradation, the catalytic conversion produced less solid residues and much higher amounts of gas and liquid hydrocarbons. The catalysts showed different yield profiles: the H-ZSM-11 zeolite yielded more gases, while the Zn-ZSM-11 zeolite yielded more liquid products. Notably over Zn-ZSM-11 zeolite, these liquid products were mainly aromatic, and depending on experimental conditions (higher temperature, longer reaction time, smaller polymer/catalyst relationship), aromatic selectivity could be increased to almost 100%. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:215 / 220
页数:6
相关论文
共 33 条
[1]   ROLES OF BRONSTED AND LEWIS SITES DURING CRACKING OF N-OCTANE ON H-MORDENITE [J].
ABBOT, J ;
GUERZONI, FN .
APPLIED CATALYSIS A-GENERAL, 1992, 85 (02) :173-188
[2]  
AGUADO J, 1999, RSC CLEAN TECHNOLOGY
[3]   Catalytic degradation of plastic waste to liquid fuel over commercial cracking catalysts - Effect of polymer to catalyst ratio/acidity content [J].
Akpanudoh, NS ;
Gobin, K ;
Manos, G .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2005, 235 (1-2) :67-73
[4]  
[Anonymous], 1999, POLYM DATA HDB
[5]   Catalytic activity of ZSM-11 zeolites modified with metal cations for the ethane conversion [J].
Anunziata, OA ;
Eimer, GA ;
Pierella, LB .
CATALYSIS LETTERS, 2001, 75 (1-2) :93-97
[6]   NATURE OF THE ACTIVE-SITES IN H-ZSM-11 ZEOLITE MODIFIED WITH ZN(2+) AND GA(3+) [J].
ANUNZIATA, OA ;
PIERELLA, LB .
CATALYSIS LETTERS, 1993, 19 (2-3) :143-151
[7]  
*APME ASS PLAST MA, 2004, SUMM REP AN PLAST CO
[8]  
AYAME A, 1979, JAPAN PETROL I, V5, P280
[9]   Catalytic pyrolysis of polyethylene [J].
Bagri, R ;
Williams, PT .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2002, 63 (01) :29-41
[10]   Structure and density of active Zn species in Zn/H-ZSM5 propane aromatization catalysts [J].
Biscardi, JA ;
Meitzner, GD ;
Iglesia, E .
JOURNAL OF CATALYSIS, 1998, 179 (01) :192-202