Marcelo H. Garcia

Marcelo H. Garcia


Research Focus & Metrics

Academic Career Length

25Years (2002-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 July 2018 in Advances in Water Resources
Verified
Journal Article
Closed access
HLHao Luo
Hao Luo
Dimitrios K. FytanidisDimitrios K. Fytanidis
Dimitrios K. Fytanidis
ASArthur R. Schmidt
Arthur R. Schmidt
MGMarcelo H. Garcia
Marcelo H. Garcia

1 February 2010 in Journal of Hydraulic Research
Verified
Journal Article
Open access
ALArturo S. Leon
Arturo S. Leon
MGMohamed S. Ghidaoui
Mohamed S. Ghidaoui
ASArthur R. Schmidt
Arthur R. Schmidt
MGMarcelo H. Garcia
Marcelo H. Garcia
A finite-volume model was built upon earlier work with the aim of simulating free surface flows, pressurized flows and their simultaneous occurrence (mixed flows) in single-liquid and two-phase flow conditions (entrapment and release of air pockets). The model presented herein is based on a two-governing equation model. Three main contributions are presented herein, namely (1) the ability of the proposed model to simulate mixed flows without restriction of the flow type in the free surface region (e.g. supercritical flow), (2) extension of our single-phase flow model for simulating the entrapment and release of air pockets and (3) formulation of an approach for handling numerical instabilities that may occur during numerical pressurization of the flow. The model presented herein is robust and simulates any transient-mixed flow condition for realistic pressure wave celerities.

23 May 2012 in Environmental Fluid Mechanics
Verified
Journal Article
Closed access
PDF file
SSS. Sinha
S. Sinha
XLX. Liu
X. Liu
MGMarcelo H. Garcia
Marcelo H. Garcia

1 March 2011 in Journal of Hydraulic Engineering
Verified
Journal Article
Closed access
XLXiaofeng Liu
Xiaofeng Liu
MGMarcelo H. Garcia
Marcelo H. Garcia
Settling tanks are used to remove solids at wastewater treatment plants. Many numerical models have been proposed to simulate the settling process and to improve tank efficiency. In this research, a three-dimensional (3D) numerical model is developed to simulate large primary settling tanks. In the proposed model, the non-Newtonian properties of the sludge flow in the settling tank are described by a Bingham plastic rheological model. To eliminate the singularity inherited in the rheological model, a modified constitutive relation is used in both the yielded and unyielded regions. Hindered settling of particles in the settling tank is also modeled. Tracer study, where a massless scalar is injected and transported, is done to investigate the tank’s residence time. This numerical model is used to improve the design of the primary settling tanks, which will be built in Chicago. The Metropolitan Water Reclamation District of Greater Chicago (MWRDGC) is in the process of building new preliminary treatment faci...

25 June 2013 in Earth Surface Processes and Landforms
Verified
Journal Article
Closed access
PDF file
Jorge D AbadJorge D Abad
Jorge D Abad
CFChristian E. Frias
Christian E. Frias
GBGustavo C. Buscaglia
Gustavo C. Buscaglia
MGMarcelo H. Garcia
Marcelo H. Garcia

1 October 2010 in Journal of Hydraulic Engineering
Verified
Journal Article
Closed access
ALArturo S. León
Arturo S. León
XLXiaofeng Liu
Xiaofeng Liu
MGMohamed S. Ghidaoui
Mohamed S. Ghidaoui
ASArthur R. Schmidt
Arthur R. Schmidt
MGMarcelo H. Garcia
Marcelo H. Garcia
A junction and drop-shaft boundary conditions (BCs) for one-dimensional modeling of transient flows in single-phase conditions (pure liquid) are formulated, implemented and their accuracy are evaluated using two computational fluid dynamics (CFD) models. The BCs are formulated in the case when mixed flows are simulated using two sets of governing equations, the Saint-Venant equations for the free-surface regions and the compressible water hammer equations for the pressurized regions. The proposed BCs handle all possible flow regimes and their combinations. The flow in each pipe can range from free surface to pressurized flow and the water depth at the junction or drop shaft can take on all possible levels. The BCs are applied to the following three cases: (1) a three-way merging flow; (2) a three-way dividing flow; and (3) a drop shaft connected to a single-horizontal pipe subjected to a rapid variation of the water surface level in the drop shaft. The flow regime for the first two cases range from free s...