Saidu Waziri Mohammed
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Research Interests
Saidu Waziri Mohammed has a total of 28 co-authors. Here are the top co-authors by number of shared publications:
- Abdulkarim S. Ahmed
Department of Chemical Engineering, Ahmadu Bello University, Zaria, Nigeria
3 shared publications - Ala’a H. Al-Muhtaseb
Department of Petroleum and Chemical Engineering, College of Engineering, Sultan Qaboos University, Muscat 123, Oman
3 shared publications - Abdullah Mohammed Aitani
Interdisciplinary Research Center for Refining and Advanced Chemicals, King Fahd University of Petroleum & Minerals, Dhahran, Saudi Arabia
2 shared publications Baba Y. Jibril
2 shared publicationsEsam Z. Hamad
Center for Refining and Petrochemicals, Research Institute, King Fahd University of Petroleum & Minerals, 31261 Dhahran, Saudi Arabia, and Research & Development Center, Saudi Aramco, 31311 Dhahran, Saudi Arabia
2 shared publicationsMohammed Dauda
2 shared publications
Latest Publications
- 27 October 2021
- Published by Springer Nature in Reaction Kinetics, Mechanisms and Catalysis
- Vol. 134 (2) , 727-742
Kinetic modeling of CuO/CeO2 and CuO/Nb2O5 as oxygen carriers in the production of syngas
- 27 October 2021
- Published by Springer Nature in Reaction Kinetics, Mechanisms and Catalysis
- Vol. 134 (2) , 727-742
Kinetic modeling of CuO/CeO2 and CuO/Nb2O5 as oxygen carriers in the production of syngas
- 1 June 2017
- Published by Elsevier in Renewable Energy Focus
- Vol. 19-20, 38-48
Techno-economic analysis of polymer electrolyte membrane fuel cell system configurations
- 1 June 2017
- Published by Elsevier in Renewable Energy Focus
- Vol. 19-20, 38-48
Techno-economic analysis of polymer electrolyte membrane fuel cell system configurations
- 1 August 2015
- Published by Elsevier in Powder Technology
- Vol. 280, 266-272
Synthesis, characterization and adsorption study of nano-sized activated alumina synthesized from kaolin using novel method
- 1 August 2015
- Published by Elsevier in Powder Technology
- Vol. 280, 266-272
Synthesis, characterization and adsorption study of nano-sized activated alumina synthesized from kaolin using novel method
- Open Access
- 1 June 2015
- Published by Sultan Qaboos University in The Journal of Engineering Research
- Vol. 12 (1) , 44-52
Microwave-Assisted Adsorptive Desulfurization of Model Diesel Fuel Using Synthesized Microporous Rare Earth Metal-Doped Zeolite Y
The microwave-assisted adsorptive desulfurization of model fuel (thiophene in n-heptane) was investigated using a synthesized rare earth metal-doped zeolite Y (RE Y). Crystallinity of the synthesized zeolite was 89.5%, the silicon/aluminium (Si/Al) molar ratio was 5.2, the Brunauer–Emmett–Teller (BET) surface area was 980.9 m2/g, and the pore volume and diameter was 0.3494 cm3/g and 1.425 nm, respectively. The results showed that the microwave reactor could be used to enhance the adsorptive desulfurization process with best efficiency of 75% at reaction conditions of 100 °C and 15 minutes. The high desulfurization effect was likely due to the higher efficiency impact of microwave energy in the interaction between sulfur in thiophene and HO-La(OSiAl).
- 1 June 2015
- Published by Sultan Qaboos University in The Journal of Engineering Research
- Vol. 12 (1) , 44-52
Open AccessMicrowave-Assisted Adsorptive Desulfurization of Model Diesel Fuel Using Synthesized Microporous Rare Earth Metal-Doped Zeolite Y
The microwave-assisted adsorptive desulfurization of model fuel (thiophene in n-heptane) was investigated using a synthesized rare earth metal-doped zeolite Y (RE Y). Crystallinity of the synthesized zeolite was 89.5%, the silicon/aluminium (Si/Al) molar ratio was 5.2, the Brunauer–Emmett–Teller (BET) surface area was 980.9 m2/g, and the pore volume and diameter was 0.3494 cm3/g and 1.425 nm, respectively. The results showed that the microwave reactor could be used to enhance the adsorptive desulfurization process with best efficiency of 75% at reaction conditions of 100 °C and 15 minutes. The high desulfurization effect was likely due to the higher efficiency impact of microwave energy in the interaction between sulfur in thiophene and HO-La(OSiAl).
- 1 March 2015
- Published by Elsevier in Applied Clay Science
- Vol. 105-106, 170-177
Synthesis of gamma alumina from Kankara kaolin using a novel technique
- 1 March 2015
- Published by Elsevier in Applied Clay Science
- Vol. 105-106, 170-177
Synthesis of gamma alumina from Kankara kaolin using a novel technique
- Open Access
- 4 December 2014
- Published by International Centre for Applied Thermodynamics (ICAT) in International Journal of Thermodynamics
- Vol. 17 (4) , 221-231
Exergetic and Economic Assessment of Distillation Hybrid Configurations for Bioethanol Refining
Thermo-economics analysis was used to identify the most economic distillation hybrid configuration to dehydrate bioethanol mash (12 wt%) to fuel grade (99.5 wt%) based on economic objective of minimization of operating cost in this work. Three different hybrids of THIDC with azeotropic and, extractive distillation units were assessed using similar feed and product specifications of 1200 kmol/h (12 % by weight ethanol) and 55 kmol/h (99.5 % by weight ethanol) respectively . The six hybrid configurations were simulated using Aspen Plus ®. The hybrid of THIDC with conventional extractive distillation (THEX1) was shown to have the lowest irreversibility rate (lost work) and highest exergetic efficiency followed by the hybrid containing thermally extractive sequence (THEX3). The latter also has the lowest energy consumption. However, economic evaluation showed that thermally coupled extractive distillation hybrid (with THIDC) is the most attractive hybrid configuration dehydrating bioethanol to fuel grade at commercial scale with the highest return on investment (ROI) and the least annual product cost. This indicates its economic attractiveness when compared with the other hybrids considered in this work. The trade-off existing between economic and exergy efficiency favours the selection of THEX3 as the preferred choice for bioethanol refining among all the six hybrids investigated.
- 4 December 2014
- Published by International Centre for Applied Thermodynamics (ICAT) in International Journal of Thermodynamics
- Vol. 17 (4) , 221-231
Open AccessExergetic and Economic Assessment of Distillation Hybrid Configurations for Bioethanol Refining
Thermo-economics analysis was used to identify the most economic distillation hybrid configuration to dehydrate bioethanol mash (12 wt%) to fuel grade (99.5 wt%) based on economic objective of minimization of operating cost in this work. Three different hybrids of THIDC with azeotropic and, extractive distillation units were assessed using similar feed and product specifications of 1200 kmol/h (12 % by weight ethanol) and 55 kmol/h (99.5 % by weight ethanol) respectively . The six hybrid configurations were simulated using Aspen Plus ®. The hybrid of THIDC with conventional extractive distillation (THEX1) was shown to have the lowest irreversibility rate (lost work) and highest exergetic efficiency followed by the hybrid containing thermally extractive sequence (THEX3). The latter also has the lowest energy consumption. However, economic evaluation showed that thermally coupled extractive distillation hybrid (with THIDC) is the most attractive hybrid configuration dehydrating bioethanol to fuel grade at commercial scale with the highest return on investment (ROI) and the least annual product cost. This indicates its economic attractiveness when compared with the other hybrids considered in this work. The trade-off existing between economic and exergy efficiency favours the selection of THEX3 as the preferred choice for bioethanol refining among all the six hybrids investigated.
- 18 June 2010
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 49 (14) , 6376-6387
Transformation of Toluene and 1,2,4-Trimethylbenzene over ZSM-5 and Mordenite Catalysts: A Comprehensive Kinetic Model with Reversibility
- 18 June 2010
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 49 (14) , 6376-6387
Transformation of Toluene and 1,2,4-Trimethylbenzene over ZSM-5 and Mordenite Catalysts: A Comprehensive Kinetic Model with Reversibility
- 9 June 2010
- Published by Wiley in Chemical Engineering & Technology
- Vol. 33 (7) , 1193-1202
Production of Xylenes from Toluene and 1,2,4-Trimethylbenzene over ZSM-5 and Mordenite Catalysts in a Fluidized-Bed Reactor
- 9 June 2010
- Published by Wiley in Chemical Engineering & Technology
- Vol. 33 (7) , 1193-1202
Production of Xylenes from Toluene and 1,2,4-Trimethylbenzene over ZSM-5 and Mordenite Catalysts in a Fluidized-Bed Reactor
- 19 August 2009
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 48 (18) , 8341-8348
Kinetics of Ethylbenzene Ethylation with Ethanol over a ZSM-5-Based Catalyst in a Riser Simulator
- 19 August 2009
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 48 (18) , 8341-8348
Kinetics of Ethylbenzene Ethylation with Ethanol over a ZSM-5-Based Catalyst in a Riser Simulator
- 31 October 2008
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 47 (23) , 9658-9662
Volume-Explicit Equation of State for Fused Hard Sphere Chain Fluids
- 31 October 2008
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 47 (23) , 9658-9662
Volume-Explicit Equation of State for Fused Hard Sphere Chain Fluids