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Journal of Water Process Engineering
journal homepage: www.elsevier.com/locate/jwpe
Global velocity gradient evaluation: An innovative approach using CFD
modeling applied to water and wastewater treatment plants
Danieli Soares de Oliveira
a,
⁎
, Clainer Bravin Donadel
b
a
Department of Production Engineering, Federal Institute of Espírito Santo – campus Cariacica, Rodovia G. José Sette, 184, Itacibá, Cariacica-ES, 29150-410, Brazil
b
Department of Electrical Engineering, Federal Institute of Espírito Santo – campus Vitória, Av. Vitória, 1729, Jucutuquara, Vitória-ES, 29078-040, Brazil
ARTICLEINFO
Keywords:
CFD modeling
Global velocity gradient
Helically coiled tube flocculators
Hydrodynamics
Water and wastewater treatment
ABSTRACT
ThispaperproposesanalternativeapproachforestimatingtheGlobalVelocityGradientparameter( G)through
hydrodynamic characteristics using Computational Fluid Dynamics Modeling (CFD). In the design of water and
wastewatertreatmentplants,severalhydraulicandgeometricparametersareneededtoguaranteetheefficiency
ofthetreatmentprocesses.Amongtheseparameters, G isestimatedusingempiricalequationsorprototypes.The
use of empirical equations is a simple and fast way to estimate G but they are often incompatible with the
geometryoftheunit,leadingtoahighnumberoferrors.Ontheotherhand,theuseofprototypesleadstohigher
accuracy,buttheirconstructionistimeconsumingandcanbeverycostly.Thus,anin-depthanalysisofthebasic
equations for obtaining G and of CFD modeling aspects can assist in obtaining this parameter without using
empirical equations or prototypes. The proposed approach was tested in six flocculation units based on helical
geometry (called Helically Coiled Tube Flocculators -HCTFs). As a result, a high correlation between G ob-
tained from prototypes (used as reference) and G obtained from the corresponding CFD modeling results was
verified(withadeterminationcoefficienthigherthan0.9995),indicatingthatthisapproachcanbeapromising
tool for designing new water and wastewater treatment units and the improvement of existing ones.
1. Introduction
The Global Velocity Gradient ( G),definedinCampandStein[1]as
ametricoftheagitationdegreeoftheliquidmassinsideareactor,isan
important design parameter in water and wastewater treatment units
(especiallyinflocculators).Inthesecases,theagitationmustbeenough
topromoteaninteractionbetweenvariousparticlestoformlargerflocs
for later removal by sedimentation/flotation; and the agitation cannot
promotethedisintegrationoftheflocspreviouslyformed,whichwould
undermine the efficiency of the process.
Two different methodologies were used to evaluate G: empirical
equations and prototyping. Empirical equations are developed for
standardized configurations such as straight tubes and helically coiled
tubes.Asanexample,VigneswaranandSetiadi[2]andAl-Hashimiand
Ashjyan [3] present G prediction models based on experimental results
intheirstudies.Theuseofempiricalequationsisastraightforwardand
fast way to estimate G, but they are frequently incompatible with the
unit geometry, leading to a high number of errors.
The use of prototypes to evaluate G is widespread due to its high
accuracy. However, their construction requires a considerable amount
of time and can be very costly, especially when units with several
geometrical characteristics are built. As an example, Oliveira and
Teixeira[4]built30differenthelicalflocculationunitstoobtain G with
distinct reactor lengths, winding diameter and tube diameter.
In the literature, Computational Fluid Dynamics (CFD) modeling
has been applied to improve the water and wastewater treatment pro-
cess [5–7]. In this way, the use of CFD modeling to evaluate G is a
promising tool for the design and improvement of new and existing
units since it is unnecessary to build prototypes and several different
configurationscanbetestedwithminimaleffort.Thispaperproposesa
novel approach for estimating G through hydrodynamic characteristics
using CFD.
The remainder of this paper is organized as follows: Section 2 pre-
sentsaliteraturereviewconcerningthemainaspectsof G evaluation;in
Section 3, the proposed methodology is presented; in Section 4, nu-
merical results are presented and the results obtained through the ap-
plication of the proposed methodology are discussed in detail. The
conclusions to this are presented in Section 5.
2. Literature review
Thepioneeringworkinthestudyof G wascarriedoutbyCampand
https://doi.org/10.1016/j.jwpe.2018.12.009
Received 2 July 2018; Received in revised form 2 December 2018; Accepted 27 December 2018
⁎
Corresponding author.
E-mail addresses: danieli@ifes.edu.br (D.S.d. Oliveira), cdonadel@ifes.edu.br (C.B. Donadel).
Journal of Water Process Engineering 28 (2019) 21–27
2214-7144/ © 2019 Elsevier Ltd. All rights reserved.
T