Maham Hussain

Dr. Maham Hussain

chemical and bioprocess Engineering, University College Dublin, Dublin, Ireland
orcid
Post Doctrate researcher

Research Focus & Metrics

Academic Career Length

11Years (2016-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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27 September 2021 in Water Environment Research
Verified
Journal Article
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AMAhmed Malik
Ahmed Malik
MHMaham Hussain
Maham Hussain
FUFahim Uddin
Fahim Uddin
WRWaseem Raza
Waseem Raza
SHSadiq Hussain
Sadiq Hussain
ZAZeeshan Ajmal
Zeeshan Ajmal

4 August 2023 in RSC Advances
Verified
Journal Article
Open access
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MHMaham Hussain
Maham Hussain
OAOmer Ali
Omer Ali
NRNadeem Raza
Nadeem Raza
HZHaslinda Zabiri
Haslinda Zabiri
AAAshfaq Ahmed
Ashfaq Ahmed
IAImtiaz Ali
Imtiaz Ali
Modeling strategies via Aspen Plus® for biomass gasification were assessed. Dynamic modeling can be essential in aiding control studies of biomass gasification process using Aspen Dynamics. Model predictive control is a widely recognized optimal controller for biomass gasification.

24 July 2019 in Biofuels
Verified
Journal Article
Closed access
MHMaham Hussain
Maham Hussain
HZHaslinda Zabiri
Haslinda Zabiri
LTLemma Dendena Tufa
Lemma Dendena Tufa
SYSuzana Yusup
Suzana Yusup
IAImtiaz Ali
Imtiaz Ali
The thermal decomposition behaviours of palm kernel shells (PKS) under non-isothermal conditions were investigated using the thermogravimetric analyser. A comparison of model-free and model-fitting methods for PKS decomposition was performed. Differential and integral methods used showed an increase in apparent activation energy with the conversion. Besides that, the global single reaction mechanism was evaluated using the reaction order and Sestak-Berggren models. Curve fitting results showed that Sestak-Berggren’s model demonstrated that the PKS pyrolysis mechanism was better than the reaction order model. The components, namely moisture, hemicellulose, cellulose, and lignin were found to decompose simultaneously. From Kissinger’s method, the average activation energy for devolatilisation, cellulose, and hemicellulose were 24.65 kJ mol−1, 78.98 kJ mol−1, and 183.07 kJ mol−1 , respectively. The decomposition of lignin occurred slowly, with a slower conversion rate in contrast to the hemicellulose and cellulose components.

1 January 2019 in Materials Today: Proceedings
Verified
Journal Article
Closed access
MHMaham Hussain
Maham Hussain
LTLemma Dendena Tufa
Lemma Dendena Tufa
SYSuzana Yusup
Suzana Yusup
HZHaslinda Zabiri
Haslinda Zabiri

1 January 2019 in Materials Today: Proceedings
Verified
Journal Article
Closed access
MHMaham Hussain
Maham Hussain
LTLemma Dendena Tuf
Lemma Dendena Tuf
SYSuzana Yusup
Suzana Yusup
HZHaslinda Zabiri
Haslinda Zabiri

1 January 2016 in Procedia Engineering
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Journal Article
Open access
MHMaham Hussain
Maham Hussain
LTLemma Dendena Tufa
Lemma Dendena Tufa
RARaja Nur Ariana Bt Raja Azlan
Raja Nur Ariana Bt Raja Azlan
SYSuzana Yusup
Suzana Yusup
HZHaslinda Zabiri
Haslinda Zabiri
In biomass gasification, the appropriate prediction of gasification products is one of the most important issues. In this work, a steady state equilibrium model for the pilot -scale circulating fluidized bed by using Aspen Plus is developed. The model is capable of predicting the composition of synthesis gas. The process is simulated in accordance with the fluidized bed gasifier assembly. The simulation represents entire unit operations involve, to process palm kernel shell followed by a series of equilibrium air and steam gasification reactions to obtain adequate Synthesis gas yield. The temperature is varied from 600°C to 700°C while for steam to biomass ratio, it is manipulated from 1.5wt/wt. to 2.5wt/wt. The optimum temperature and steam to biomass ratio is determined in this study