Hafiza Shukor

Dr. Hafiza Shukor

Faculty of Chemical Engineering and Technology, Universiti Malaysia Perlis (UniMAP), Kangar, Perlis, Malaysia
orcid
Biofuels, Biomass, Biosorbents, Membrane Fabrication

Research Focus & Metrics

Academic Career Length

13Years (2014-Present)

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

Representative Publications

View All Publications
1 August 2014 in International Journal of Hydrogen Energy
Verified
Journal Article
Closed access
PAPeyman Abdeshahian
Peyman Abdeshahian
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
NSNoura K.M. Salih
Noura K.M. Salih
Hafiza ShukorHafiza Shukor
Hafiza Shukor
AKAbudukeremu Kadier
Abudukeremu Kadier
MKMohd Sahaid Kalil
Mohd Sahaid Kalil

1 October 2014 in Bioresource Technology
Verified
Journal Article
Closed access
Hafiza ShukorHafiza Shukor
Hafiza Shukor
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
Peyman AbdeshahianPeyman Abdeshahian
Peyman Abdeshahian
AHAidil Abdul Hamid
Aidil Abdul Hamid
NANurina Anuar
Nurina Anuar
MKMohd Sahaid Kalil
Mohd Sahaid Kalil

1 November 2018 in Saudi Journal of Biological Sciences
Verified
Journal Article
Open access
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
Hafiza ShukorHafiza Shukor
Hafiza Shukor
PAPeyman Abdeshahian
Peyman Abdeshahian
MKMohd Sahaid Kalil
Mohd Sahaid Kalil
WYWan Mohtar Wan Yusoff
Wan Mohtar Wan Yusoff
AHAidil Abdul Hamid
Aidil Abdul Hamid
A new isolate of the solvent-producing Clostridium acetobutylicum YM1 was used to produce butanol in batch culture fermentation. The effects of glucose concentration, butyric acid addition and C/N ratio were studied conventionally (one-factor-at-a-time). Moreover, the interactions between glucose concentration, butyric acid addition and C/N ratio were further investigated to optimize butanol production using response surface methodology (RSM). A central composite design was applied, and a polynomial regression model with a quadratic term was used to analyze the experimental data using analysis of variance (ANOVA). ANOVA revealed that the model was highly significant (p < 0.0001) and the effects of the glucose and butyric acid concentrations on butanol production were significant. The model validation experiment showed 13.82 g/L butanol was produced under optimum conditions. Scale up fermentation in optimized medium resulted in 17 g/L of butanol and 21.71 g/L of ABE. The experimental data of scale up in 5 L bioreactor and flask scale were fitted to kinetic mathematical models published in the literature to estimate the kinetic parameters of the fermentation. The models used gave the best fit for butanol production, biomass and glucose consumption for both flask scale and bioreactor scale up.

1 October 2016 in Bioresource Technology
Verified
Journal Article
Closed access
Hafiza ShukorHafiza Shukor
Hafiza Shukor
PAPeyman Abdeshahian
Peyman Abdeshahian
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
AHAidil Abdul Hamid
Aidil Abdul Hamid
NRNorliza A. Rahman
Norliza A. Rahman
MKMohd Sahaid Kalil
Mohd Sahaid Kalil

1 April 2015 in Biocatalysis and Agricultural Biotechnology
Verified
Journal Article
Closed access
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
Hafiza ShukorHafiza Shukor
Hafiza Shukor
PAPeyman Abdeshahian
Peyman Abdeshahian
YNYusuf Nazir
Yusuf Nazir
MKMohd Sahaid Kalil
Mohd Sahaid Kalil
WYWan Mohtar Wan Yusoff
Wan Mohtar Wan Yusoff

1 February 2016 in Bioresource Technology
Verified
Journal Article
Closed access
Hafiza ShukorHafiza Shukor
Hafiza Shukor
PAPeyman Abdeshahian
Peyman Abdeshahian
NANajeeb Kaid Nasser Al-Shorgani
Najeeb Kaid Nasser Al-Shorgani
AHAidil Abdul Hamid
Aidil Abdul Hamid
NRNorliza A. Rahman
Norliza A. Rahman
MKMohd Sahaid Kalil
Mohd Sahaid Kalil