Roghayeh Ghasempour

Dr. Roghayeh Ghasempour

orcid

Research Focus & Metrics

Academic Career Length

10Years (2017-Present)

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

Representative Publications

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1 January 2020 in Energy
Verified
Journal Article
Closed access
MRMohammad Amin Vaziri Rad
Mohammad Amin Vaziri Rad
RGRoghayeh Ghasempour
Roghayeh Ghasempour
PRParisa Rahdan
Parisa Rahdan
SMSoroush Mousavi
Soroush Mousavi
MAMehrdad Arastounia
Mehrdad Arastounia

3 June 2020 in International Journal of Energy Research
Verified
Journal Article
Closed access
PDF file
MMMohammad Dehghani madvar
Mohammad Dehghani madvar
RSReza Shirmohammadi
Reza Shirmohammadi
MSMilad Sadeghzadeh
Milad Sadeghzadeh
AAAlireza Aslani
Alireza Aslani
RGRoghayeh Ghasempour
Roghayeh Ghasempour

13 September 2020 in Processes
Verified
Journal Article
Open access
PDF file
RSReza Shirmohammadi
Reza Shirmohammadi
AAAlireza Aslani
Alireza Aslani
RGRoghayeh Ghasempour
Roghayeh Ghasempour
LRLuis M Romeo
Luis M Romeo
Carbon capture and utilization (CCU) may offer a response to climate change mitigation from major industrial emitters. CCU can turn waste CO2 emissions into valuable products such as chemicals and fuels. Consequently, attention has been paid to petrochemical industries as one of the best options for CCU. The largest industrial CO2 removal monoethanol amine-based plant in Iran has been simulated with the aid of a chemical process simulator, i.e., Aspen HYSYS® v.10. The thermodynamic properties are calculated with the acid gas property package models, which are available in Aspen HYSYS®. The results of simulation are validated by the actual data provided by Kermanshah Petrochemical Industries Co. Results show that there is a good agreement between simulated results and real performance of the plant under different operational conditions. The main parameters such as capture efficiency in percent, the heat consumption in MJ/kg CO2 removed, and the working capacity of the plant are calculated as a function of inlet pressure and temperature of absorber column. The best case occurred at the approximate temperature of 40 to 42 °C and atmospheric pressure with CO2 removal of 80.8 to 81.2%; working capacity of 0.232 to 0.233; and heat consumption of 4.78 MJ/kg CO2.

1 June 2018 in Thermal Science and Engineering Progress
Verified
Journal Article
Closed access
MAMilad Ashouri
Milad Ashouri
MAMohammad Hossein Ahmadi
Mohammad Hossein Ahmadi
SPS. Mohsen Pourkiaei
S. Mohsen Pourkiaei
FAFatemeh Razi Astaraei
Fatemeh Razi Astaraei
RGRoghayeh Ghasempour
Roghayeh Ghasempour
JHJavid Haj Hemati
Javid Haj Hemati

23 May 2019 in Journal of Thermal Analysis and Calorimetry
Verified
Journal Article
Closed access
PDF file
AAAmir Abdollahpour
Amir Abdollahpour
RGRoghayeh Ghasempour
Roghayeh Ghasempour
AKAlibakhsh Kasaeian
Alibakhsh Kasaeian
MAMohammad H. Ahmadi
Mohammad H. Ahmadi

8 August 2019 in Journal of Thermal Analysis and Calorimetry
Verified
Journal Article
Closed access
PDF file
MAMohammad Hossein Ahmadi
Mohammad Hossein Ahmadi
ABAlireza Baghban
Alireza Baghban
MGMahyar Ghazvini
Mahyar Ghazvini
MHMasoud Hadipoor
Masoud Hadipoor
RGRoghayeh Ghasempour
Roghayeh Ghasempour
MNMohammad Reza Nazemzadegan
Mohammad Reza Nazemzadegan