Valorization of the blends polystyrene/light cycle oil and polystyrene-butadiene/light cycle oil over HZSM-5 zeolites

被引:11
作者
Arandes, JM
Ereña, J
Bilbao, J
López-Valerio, D
de la Puente, G
机构
[1] Univ Basque Country, Dept Ingn Quim, E-48080 Bilbao, Spain
[2] Univ Nacl Ingn, Fac Ingn Quim, Managua, Nicaragua
[3] UNL, CONICET, FIQ, INCAPE,Inst Invest Catalisis & Petroquim, RA-3000 Santa Fe, Argentina
关键词
D O I
10.1021/ie030045j
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The conversions and yields of the fractions of gases (C-1, C-2) LPG (C-3, C-4), gasoline (C-5-C-12), and coke and their compositions have been studied in the catalytic cracking of blends made up of polystyrene and polystyrene-butadiene with a LCO (light cycle oil, which is a secondary refinery product) used as the solvent. The catalysts were prepared from HZSM-5 zeolites of different total acidities. The reaction was carried out in the 450-550 degreesC range and under the standard conditions of FCC units. The important effects both of the total acidity of the zeolite and of the temperature on the conversion and yield of styrene are demonstrated. Total recovery of the monomer styrene is attained at 550 degreesC. Likewise, the LCO is valorized, as high yields of both the C-5-C-12 aromatic fraction and LPG (olefinic) are obtained with low yields of gases (C-1, C-2) and coke.
引用
收藏
页码:3700 / 3710
页数:11
相关论文
共 49 条
[1]   Kinetics of polystyrene pyrolysis in a conical spouted bed reactor [J].
Aguado, R ;
Olazar, M ;
Gaisán, B ;
Prieto, R ;
Bilbao, J .
CHEMICAL ENGINEERING JOURNAL, 2003, 92 (1-3) :91-99
[2]   ISOTHERMS OF CHEMICAL ADSORPTION OF BASES ON SOLID CATALYSTS FOR ACIDITY MEASUREMENT [J].
AGUAYO, AT ;
GAYUBO, AG ;
ERENA, J ;
OLAZAR, M ;
ARANDES, JM ;
BILBAO, J .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 1994, 60 (02) :141-146
[3]  
AGUAYO AT, 1994, STUD SURF SCI CATAL, V88, P567
[4]   Transformation of several plastic wastes into fuels by catalytic cracking [J].
Arandes, JM ;
Abajo, I ;
LopezValerio, D ;
Fernandez, I ;
Azkoiti, MJ ;
Olazar, M ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (11) :4523-4529
[5]   Effect of HZSM-5 zeolite addition to a fluid catalytic cracking catalyst.: Study in a laboratory reactor operating under industrial conditions [J].
Arandes, JM ;
Abajo, I ;
Fernández, I ;
Azkoiti, MJ ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (06) :1917-1924
[6]   Consistency of the ten-lump kinetic model for cracking: Study in a laboratory reactor and use for simulation of an FCCU [J].
Arandes, JM ;
Bilbao, J ;
Aokziti, J ;
De Lasa, HI .
CHEMICAL ENGINEERING COMMUNICATIONS, 2003, 190 (02) :254-284
[7]  
ARANDES JM, IN PRESS J ANAL APPL
[8]  
ARANDES JM, IN PRESS IND ENG CHE
[9]  
Argauer R.J., 1972, US Pat., Patent No. [3702886, US3702886A]
[10]   CATALYTIC DEGRADATION OF POLYMERS .3. DEGRADATION OF POLYSTYRENE [J].
AUDISIO, G ;
BERTINI, F ;
BELTRAME, PL ;
CARNITI, P .
POLYMER DEGRADATION AND STABILITY, 1990, 29 (02) :191-200