Computational fluid dynamics simulation of an Inert Particles Spouted Bed Reactor (IPSBR) system

Author:

Mohammad Ameera F.1,Mourad Aya A-H. I.12,Mustafa Jawad1,Al-Marzouqi Ali H.1,El-Naas Muftah H.3,Al-Marzouqi Mohamed H.1,Alnaimat Fadi1,Suleiman Mabruk I.4,Al Musharfy Mohamed4,Firmansyah Tommy4

Affiliation:

1. College of Engineering, UAE University, Al Ain, United Arab Emirates

2. Academic Support Department, Abu Dhabi Polytechnic, Institute of Applied Technology, Abu Dhabi, United Arab Emirates

3. Gas Processing Center, College of Engineering, Qatar University, Doha, Qatar

4. Research Centre Division, ADNOC Refining, Abu Dhabi, United Arab Emirates

Abstract

AbstractA novel system for contacting gases and liquids, suitable for many applications involving gas–liquid contact such as CO2 capture and brine desalination, has been simulated and experimentally validated. The system comprises a vertical vessel with gas and liquid ports and inert particles that enhance mixing and provide a high gas–liquid interfacial area. A low gas flow rate was statistically demonstrated and experimentally verified to be the optimum condition for CO2 capture and brine desalination; however, the gas velocity can have a considerable effect on the motion of inert particles inside the reactor. Uniform particles motion ensures good mixing within the reactor and hence efficient absorption and stripping process. A computational fluid dynamics (CFD) model, namely Eulerian model, presented in this paper, will help demonstrate the effect of mixing particles at specific conditions on the gas and liquid velocities inside the reactor, gas and liquid volume distribution through reactor, and eddy viscosities stresses of the mixing particles. A mesh-independent study was conducted to demonstrate the independency of mesh structure and size on the output responses. A quasi-steady state was attained to ensure the stability and feasibility of the selected model. The assembled model exhibits remarkable applicability in determining the optimum mixing particles densities, volume ratios, and sizes to ensure best velocity distribution and gas spreading inside the reactor and accordingly enhance the associated chemical reactions.

Publisher

Walter de Gruyter GmbH

Subject

General Chemical Engineering

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