Effect of different catalyst on the co-cracking of Jatropha oil, vacuum residue and high density polyethylene

被引:26
作者
Biswas, Shelly [1 ,3 ]
Majhi, Sachchit [2 ]
Mohanty, Pravakar [2 ]
Pant, K. K. [2 ]
Sharma, D. K. [1 ]
机构
[1] Indian Inst Technol Delhi, Ctr Energy Studies, New Delhi 110016, India
[2] Indian Inst Technol Delhi, Dept Chem Engn, New Delhi 110016, India
[3] Vel Tech Dr RR & Dr SR Tech Univ, Dept Chem, Madras 600062, Tamil Nadu, India
关键词
Co-cracking; Vacuum residue; Jatropha oil; HDPE; Catalyst; GAS OIL; H-1-NMR SPECTROSCOPY; FUEL PRODUCTION; WASTE PLASTICS; NI-MO; LIQUID; HYDROTREATMENT; HYDROCRACKING; PYROLYSIS; GASOLINE;
D O I
10.1016/j.fuel.2014.04.082
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Co-processing of Jatropha oil (JO), vacuum residue (VR) and high density polyethylene (HDPE) were investigated to determine the behavior of the individual and blended mixture under atmospheric pressure and thermal heating conditions. A fixed bed tubular batch reactor was used for the experimental study under nitrogen atmosphere. The activity of the four catalysts CAT-A (Ni-Mo/SiAl), CAT-R (ZSM-5 + SiAl), CAT-Z (ZSM-5) and FCC catalyst CAT-N on the co-cracking of binary and ternary mixture has been studied. CAT-R was the best catalyst used for JO + HDPE co-cracking as it leads to the formation of 45%, gasoline range hydrocarbons (C-7-C-11) and 49% diesel range hydrocarbons in the cracked liquid. CAT-Z was the best catalyst for VR + HDPE co-cracking as it lead to the formation of 33% olefins which were absent in the thermally cracked liquid. In case of JO + VR co-cracking CAT-Z was found to show increase in the liquid yield and it also lead to the formation of 37% gasoline range hydrocarbons and 35% diesel range hydrocarbons. It was also observed that the use of catalyst had a positive effect on the pH content of the catalytically cracked liquid products. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:96 / 105
页数:10
相关论文
共 35 条
[21]   Liquid fuel production from syngas using bifunctional CuO-CoO-Cr2O3 catalyst mixed with MFI zeolite [J].
Mohanty, Pravakar ;
Pant, K. K. ;
Parikh, J. ;
Sharma, D. K. .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (03) :600-608
[22]   Pyrolysis of soybean oil with H-ZSM5 (Proton-exchange of Zeolite Socony Mobil #5) and MCM41 (Mobil Composition of Matter No. 41) catalysts in a fixed-bed reactor [J].
Ngo, Thanh-An ;
Kim, Jinsoo ;
Kim, Sun Kul ;
Kim, Seung-Soo .
ENERGY, 2010, 35 (06) :2723-2728
[23]   Hydrodesulfurization and hydrocracking of Maya crude with P-modified NiMo/Al2O3 catalysts [J].
Rayo, Patricia ;
Ramirez, Jorge ;
Torres-Mancera, Pablo ;
Marroquin, Gustavo ;
Maity, Samir K. ;
Ancheyta, Jorge .
FUEL, 2012, 100 :34-42
[24]   Hydroprocessing of sunflower oil-gas oil blends over sulfided Ni-Mo-Al-zeolite beta composites [J].
Sankaranarayanan, T. M. ;
Banu, M. ;
Pandurangan, A. ;
Sivasanker, S. .
BIORESOURCE TECHNOLOGY, 2011, 102 (22) :10717-10723
[25]   PONA analyses of cracked gasoline by 1H NMR spectroscopy.: Part II [J].
Sarpal, AS ;
Kapur, GS ;
Mukherjee, S ;
Tiwari, AK .
FUEL, 2001, 80 (04) :521-528
[26]   Study of kinetics of co-pyrolysis of coal and waste LDPE blends under argon atmosphere [J].
Sharma, Sumedha ;
Ghoshal, Aloke K. .
FUEL, 2010, 89 (12) :3943-3951
[27]   Catalytic coprocessing of waste plastics and petroleum residue into liquid fuel oils [J].
Siddiqui, Mohammad Nahid ;
Redhwi, Halim Hamid .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2009, 86 (01) :141-147
[28]   Hydrocracking of petroleum vacuum distillate containing rapeseed oil: Evaluation of diesel fuel [J].
Simacek, Pavel ;
Kubicka, David .
FUEL, 2010, 89 (07) :1508-1513
[29]   Hydroprocessed rapeseed oil as a source of hydrocarbon-based biodiesel [J].
Simacek, Pavel ;
Kubicka, David ;
Sebor, Gustav ;
Pospisil, Milan .
FUEL, 2009, 88 (03) :456-460
[30]  
Sinhamahapatra PK, 1987, J CHEM TECHNOL BIOT, V28, P740