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A generic input-output approach in developing and optimizing an Aspen plus steam-gasification model for biomass
Sk Arafat Zaman1, Sudip Ghosh1
1Department of Mechanical Engineering, Indian Institute of Engineering Science and Technology, Shibpur, Howrah 711103, West Bengal, India.
Bioresource Technology
|June 24, 2021
Summary
This study optimizes steam-gasification for higher hydrogen production. The best results for cold gas efficiency and lower heating value were achieved at a steam-to-biomass ratio of 0.7 and temperatures between 780-790°C.
Area of Science:
- Chemical Engineering
- Renewable Energy
- Biomass Conversion
Background:
- Steam-gasification is a key process for producing hydrogen-rich syngas.
- Optimizing steam-gasification is crucial for maximizing energy recovery and efficiency from biomass.
Purpose of the Study:
- To develop and present an equilibrium steam-gasification model in Aspen Plus.
- To investigate the effects of input variables on cold gas efficiency (CGE) and lower heating value (LHV).
- To optimize the steam-gasification process for various biomass types using Response Surface Methodology (RSM).
Main Methods:
- Development of an equilibrium steam-gasification model using Aspen Plus.
- Application of Response Surface Methodology (RSM) for process optimization.
- Analysis of synchronized effects of input variables on CGE and LHV.
Main Results:
- Identified optimal operating conditions for steam-gasification: steam to biomass ratio of 0.7 and gasification temperature between 780-790°C.
- Achieved nearly 100% desirability (D) for the optimized process.
- Framed generic relations to estimate CGE and LHV for different biomass feeds at optimum conditions.
Conclusions:
- The developed model and optimization strategy effectively enhance steam-gasification performance.
- Optimal conditions significantly improve cold gas efficiency and lower heating value.
- The study provides a framework for efficient biomass-to-syngas conversion.

