eprintid: 7494
rev_number: 2
eprint_status: archive
userid: 1
dir: disk0/00/00/74/94
datestamp: 2023-11-09 16:19:18
lastmod: 2023-11-09 16:19:18
status_changed: 2023-11-09 16:09:33
type: conference_item
metadata_visibility: show
creators_name: Kashif, S.B.
creators_name: Abdullah, M.Z.
creators_name: Kushaari, K.
title: CFD Modeling of N2/H2 Gaseous Flow with Geometric Variations in a Monolithic Channel
ispublished: pub
keywords: Flow of fluids; Geometry; Hydrogen; Mixing; Nitrogen; Process engineering; Reynolds number; Wire, Channel length; Favorable conditions; Flow dynamics; Geometric variations; Lateral movement; Low Reynolds number flow; Parametric study; Two-component, Computational fluid dynamics
note: cited By 1; Conference of 4th International Conference on Process Engineering and Advanced Materials, ICPEAM 2016 ; Conference Date: 15 August 2016 Through 17 August 2016; Conference Code:131138
abstract: Geometric variations by means of orientation of obstructions to the fluid flow can have a significant effect on the flow dynamics of gases in pursuit of maintaining required mixing in a low Reynolds number flow for a prospective reaction between the two gases. In this study, the effect of placing the obstructions parallel and perpendicular to the N2 and H2 flow was observed initially. Parallel placement resulted in favorable conditions in maintaining the desired ratio of the two components giving more than 90 mixing index throughout the channel length while perpendicular placement signaled better lateral movement on encountering the obstruction. Taking a cue from this, geometries having a combination of parallel and perpendicular obstructions were proposed based on results of parametric study on number of wires and spacing between them. Increasing perpendicular obstruction sets beyond 5 took the mixing index down to as low as 60. Increasing spacing from 1.5 mm to 2 mm deteriorated mixing index further but reducing perpendicular sets from 5 to 3 with 2 mm spacing resulted in 90 mixing index throughout the channel and benchmark observed in axial-only configuration was regained. Also, increasing number of axial wires on a given perpendicular set or reducing their spacing did not alter desired mixing index to a great extent. © 2016 The Authors. Published by Elsevier Ltd.
date: 2016
publisher: Elsevier Ltd
official_url: https://www.scopus.com/inward/record.uri?eid=2-s2.0-85013891460&doi=10.1016%2fj.proeng.2016.06.436&partnerID=40&md5=965c2617f2a60dce68293a3a70f7317b
id_number: 10.1016/j.proeng.2016.06.436
full_text_status: none
publication: Procedia Engineering
volume: 148
pagerange: 1266-1273
refereed: TRUE
issn: 18777058
citation:   Kashif, S.B. and Abdullah, M.Z. and Kushaari, K.  (2016) CFD Modeling of N2/H2 Gaseous Flow with Geometric Variations in a Monolithic Channel.  In: UNSPECIFIED.