Hussain, M. and Zabiri, H. and Uddin, F. and Yusup, S. and Tufa, L.D. (2023) Pilot-scale biomass gasification system for hydrogen production from palm kernel shell (part A): steady-state simulation. Biomass Conversion and Biorefinery, 13 (5). pp. 3849-3862.
Full text not available from this repository.Abstract
Hydrogen (H2) production via biomass gasification has demonstrated to be a viable method to obtain environmental-friendly fuel. In this paper, steady-state modeling of palm kernel shell (PKS) steam gasification pilot-plant is developed and validated using experimental data. The process optimization study for the gasification of PKS utilizing the coal bottom ash as a catalyst is conducted in the continuous advanced fluidized bed technology pilot-scale gasification plant to determine the optimum conditions to produce maximum H2 and syngas composition. The optimum conditions for maximum H2 and syngas composition are a temperature of 625 °C, PKS particle size of 1�2 mm, and coal bottom ash to PKS percentage of 7.5 . The optimum operating condition results are then validated in the pilot-scale gasification system. Steady-state simulation of the pilot scale biomass gasification plant is then developed using Aspen Plus® and validated using the experimental data. © 2021, The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature.
Item Type: | Article |
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Additional Information: | cited By 6 |
Uncontrolled Keywords: | Ash handling; Ashes; Biomass; Computer software; Fluidized beds; Gasification; Hydrogen production; Optimization; Particle size; Pilot plants; Synthesis gas, ASPEN PLUS; Aspen plus®; Bottom ash; Coal bottom ash; Optimum conditions; Palm kernel shells; Pilot scale; Steady-state simulations; Syngas composition, Coal |
Depositing User: | Mr Ahmad Suhairi UTP |
Date Deposited: | 04 Jun 2024 14:11 |
Last Modified: | 04 Jun 2024 14:11 |
URI: | https://khub.utp.edu.my/scholars/id/eprint/18692 |