Validation of wax deposition models with recent laboratory scale flow loop experimental data

2017 ◽  
Vol 149 ◽  
pp. 351-366 ◽  
Author(s):  
Auzan A. Soedarmo ◽  
Nagu Daraboina ◽  
Cem Sarica
AIChE Journal ◽  
2016 ◽  
Vol 62 (11) ◽  
pp. 4131-4139 ◽  
Author(s):  
Yuandao Chi ◽  
Nagu Daraboina ◽  
Cem Sarica

Author(s):  
Wesam Taha ◽  
Fadi Al-Zir ◽  
Mohamed Abou-Khousa ◽  
Ahmed Al-Durra ◽  
Khaled Al-Wahedi ◽  
...  

2021 ◽  
pp. 13-23
Author(s):  
M.R. Manafov ◽  
◽  
G.S. Aliyev ◽  
A.I. Rustamova ◽  
V.I. Kerimli ◽  
...  

The mechanism of paraffin formation in transport pipes is briefly discussed. A kinetic model of the formation and wax deposition from oil is proposed. Comparison of the model with the available experimental data gave satisfactory results. The review considers software tools for modeling the wax deposition process. It is noted that the simulation results are not always applicable to real field cases. For a more reliable interpretation, the scaling effect must be taken into account. In the work various technologies for wax removal are considered


2019 ◽  
Author(s):  
Jatin R. Agarwal ◽  
Simran Dhingra ◽  
Neel Shah ◽  
Subhash N. Shah

Energies ◽  
2020 ◽  
Vol 13 (24) ◽  
pp. 6556
Author(s):  
Sumit Sood ◽  
Om Prakash ◽  
Mahdi Boukerdja ◽  
Jean-Yves Dieulot ◽  
Belkacem Ould-Bouamama ◽  
...  

Proton Exchange Membrane (PEM) water electrolysis system is one of the promising technologies to produce green hydrogen from renewable energy sources (wind and solar). However, performance and dynamic analysis of PEM water electrolysis systems are challenging due to the intermittent nature of such sources and involved multi-physical behaviour of the components and subsystems. This study proposes a generic dynamical model of the PEM electrolysis system represented in a modular fashion using Bond Graph (BG) as a unified modelling approach. Causal and functional properties of the BG facilitate the formal PEM electrolyser model to adapt and to fit the different configurations of the electrolyser ranging from laboratory scale to industrial scale. The system-specific key parameter values are identified optimally for a laboratory-scale electrolyser system running on a multi-source energy platform using experimental data. The mean absolute percentage error between simulation and experimental data is found to be less than 5%. The performance characteristic curves of the electrolyser are predicted at different operating temperatures using the identified key parameters. The predicted performance is in good agreement with the expected behaviour of the electrolyser found in the literature. The model also estimates the different energy losses and the real-time efficiency of the system under dynamic inputs. With these capabilities, the developed model provides an economical mean for design, control, and diagnosis development of such systems.


2008 ◽  
Author(s):  
Benallal Amine ◽  
Philippe Maurel ◽  
Jean Francois Agassant ◽  
Myriam Darbouret ◽  
Guillaume Avril ◽  
...  

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