TY - JOUR
T1 - Synthesis and Characterization ZSM-5 Based on Kaolin as a Catalyst for Catalytic Cracking of Heavy Distillate
AU - Ulfiati, Ratu
AU - Dhaneswara, Donanta
AU - Harjanto, Sri
AU - Fatriansyah, Jaka Fajar
N1 - Funding Information:
The research was funded by a Research Grant from Penelitian Disertasi Doktor Kementerian Riset dan Teknologi/Badan Riset dan Inovasi Nasional Tahun Anggaran 2021 Nomor: NKB-328/UN2.RST/HKP.05.00/2021. The authors would also like to acknowledge the technical assistance provided by the Universitas Indonesia Advanced Materials Laboratory and the PPPTMGB "LEMIGAS" Catalyst Laboratory
Publisher Copyright:
© 2022, International Journal of Technology.All Rights Reserved.
PY - 2022
Y1 - 2022
N2 - This article describes the study of synthesis of ZSM-5 Zeolite based on kaolin as catalysts for catalytic cracking of heavy distillate. There are five types of formulas A, B, C, D, and E synthesized with varying the molar ratios of SiO2/Al2O3, SiO2/Na2O, and H2O/SiO2 and characterized by chemical compound, microstructure and catalytic performance. Three methods conducted the catalytic cracking of heavy distillate such as without catalyst, Ni-Mo commercial catalyst, and bifunctional catalyst ZSM-5 from Formula E, which was impregnated with transition metals (Ni, Mo) to be Ni-Mo/HZSM-5. The catalytical performance test result shows that, under operational conditions (~350 °C, 1 MPa), middle distillate hydrocarbon is obtained by the catalytic cracking of heavy distillate using Ni-Mo commercial catalyst and Ni-Mo/HZSM-5 Formula E catalyst.
AB - This article describes the study of synthesis of ZSM-5 Zeolite based on kaolin as catalysts for catalytic cracking of heavy distillate. There are five types of formulas A, B, C, D, and E synthesized with varying the molar ratios of SiO2/Al2O3, SiO2/Na2O, and H2O/SiO2 and characterized by chemical compound, microstructure and catalytic performance. Three methods conducted the catalytic cracking of heavy distillate such as without catalyst, Ni-Mo commercial catalyst, and bifunctional catalyst ZSM-5 from Formula E, which was impregnated with transition metals (Ni, Mo) to be Ni-Mo/HZSM-5. The catalytical performance test result shows that, under operational conditions (~350 °C, 1 MPa), middle distillate hydrocarbon is obtained by the catalytic cracking of heavy distillate using Ni-Mo commercial catalyst and Ni-Mo/HZSM-5 Formula E catalyst.
KW - Catalytic cracking
KW - Formulation
KW - Heavy distillate
KW - Zeolite
UR - http://www.scopus.com/inward/record.url?scp=85140019614&partnerID=8YFLogxK
U2 - 10.14716/ijtech.v13i4.5150
DO - 10.14716/ijtech.v13i4.5150
M3 - Article
AN - SCOPUS:85140019614
SN - 2086-9614
VL - 13
SP - 860
EP - 869
JO - International Journal of Technology
JF - International Journal of Technology
IS - 4
ER -