TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR

Membrane contactor is separation processing unit using membrane as a contacting device. The major advantage of membrane contactor relies on its high contact area compared to conventional <br /> scrubber. One of the important applications of membrane contactor is to reduce emission of acid ga...

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Main Author: ARYANTI, NITA
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/1665
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:1665
spelling id-itb.:16652004-07-20T10:34:41ZTWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR ARYANTI, NITA Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/1665 Membrane contactor is separation processing unit using membrane as a contacting device. The major advantage of membrane contactor relies on its high contact area compared to conventional <br /> scrubber. One of the important applications of membrane contactor is to reduce emission of acid gases. In this work, modeling of membrane contactor is conducted to describe concentration distribution along fiber length used for predicting effective fiber length by solving mass conservation equation. Solving of <br /> mass conservation equation requires information of fluid flow distribution obtained by solving continuity and momentum equations <br /> simultaneously. Furthermore, the finite volume method is used to obtain the solution. <br /> Modeling of fluid flow was carried out by adding Darcy\'s and Brinkman-Darcy flow models into Navier-Stokes equation. The momentum and continuity equations are solved for two-dimensional cylindrical coordinate, The results of velocity profile at axial direction <br /> were validated with Pangrle (1992) experimental data. The comparison shows that consideration using Brinkman-Darcy flow model give a good <br /> agreement with experimental data in which maximal axial velocity achieved is 0.047 m/s for this model and 0.05 m/s for experimental data <br /> The concentration profiles at radial direction using Darcy and Brinkman-Darcy flow models have also been investigated. Furthermore. <br /> concentration profiles at axial direction using both the two flow models indicate a decrease of concentration along fiber length. The comparison <br /> between models and experimental data by Subhakti and Irvan (1997) agree very closely to the Brinkman-Darcy flow model. The prediction of effective fiber length was conducted based on <br /> minimum economical flux of membrane contactor. The calculation obtains the effective fiber length obtained is 0.19 m at gas concentration. <br /> gas flow rate, and sorbent concentration of 0.02 mol/L, 0.8 m/s and 0.256 M respectively text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Membrane contactor is separation processing unit using membrane as a contacting device. The major advantage of membrane contactor relies on its high contact area compared to conventional <br /> scrubber. One of the important applications of membrane contactor is to reduce emission of acid gases. In this work, modeling of membrane contactor is conducted to describe concentration distribution along fiber length used for predicting effective fiber length by solving mass conservation equation. Solving of <br /> mass conservation equation requires information of fluid flow distribution obtained by solving continuity and momentum equations <br /> simultaneously. Furthermore, the finite volume method is used to obtain the solution. <br /> Modeling of fluid flow was carried out by adding Darcy\'s and Brinkman-Darcy flow models into Navier-Stokes equation. The momentum and continuity equations are solved for two-dimensional cylindrical coordinate, The results of velocity profile at axial direction <br /> were validated with Pangrle (1992) experimental data. The comparison shows that consideration using Brinkman-Darcy flow model give a good <br /> agreement with experimental data in which maximal axial velocity achieved is 0.047 m/s for this model and 0.05 m/s for experimental data <br /> The concentration profiles at radial direction using Darcy and Brinkman-Darcy flow models have also been investigated. Furthermore. <br /> concentration profiles at axial direction using both the two flow models indicate a decrease of concentration along fiber length. The comparison <br /> between models and experimental data by Subhakti and Irvan (1997) agree very closely to the Brinkman-Darcy flow model. The prediction of effective fiber length was conducted based on <br /> minimum economical flux of membrane contactor. The calculation obtains the effective fiber length obtained is 0.19 m at gas concentration. <br /> gas flow rate, and sorbent concentration of 0.02 mol/L, 0.8 m/s and 0.256 M respectively
format Theses
author ARYANTI, NITA
spellingShingle ARYANTI, NITA
TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
author_facet ARYANTI, NITA
author_sort ARYANTI, NITA
title TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
title_short TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
title_full TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
title_fullStr TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
title_full_unstemmed TWO-DIMENSIONAL NUMERICAL MODELS OF HOLLOW FIBER MEMBRANE CONTACTOR
title_sort two-dimensional numerical models of hollow fiber membrane contactor
url https://digilib.itb.ac.id/gdl/view/1665
_version_ 1820663026477432832