Yolanda Vásquez

Dr. Yolanda Vásquez

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Research Focus & Metrics

Academic Career Length

7Years (2020-Present)

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

Representative Publications

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15 April 2020 in Water Science & Technology
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Journal Article
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RBRaimund Bürger
Raimund Bürger
SDStefan Diehl
Stefan Diehl
MMMaría Carmen Martí
María Carmen Martí
YVYolanda Vásquez
Yolanda Vásquez
Flotation is a separation process where particles or droplets are removed from a suspension with the aid of floating gas bubbles. Applications include dissolved air flotation (DAF) in industrial wastewater treatment and column froth flotation (CFF) in wastewater treatment and mineral processing. One-dimensional models of flotation have been limited to steady-state situations for half a century by means of the drift-flux theory. A newly developed dynamic one-dimensional model formulated in terms of partial differential equations can be used to predict the process of simultaneous flotation of bubbles and sedimentation of particles that are not attached to bubbles. The governing model is a pair of first-order conservation laws for the aggregate and solids volume fractions as functions of height and time. An analysis of nonlinear ingredients of the governing equations helps to identify desired steady-state operating conditions. These can be chosen by means of operating charts, which are diagrams that visualize regions of admissible values of the volumetric flows of the feed input and underflow outlet. This is detailed for the DAF thickening process. Dynamic simulations are obtained with a recently developed numerical method. Responses to control actions are demonstrated with scenarios in CFF and DAF.

1 January 2022 in Networks and Heterogeneous Media
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Journal Article
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RBRaimund Bürger
Raimund Bürger
SDStefan Diehl
Stefan Diehl
MMM. Carmen Martí
M. Carmen Martí
YVYolanda Vásquez
Yolanda Vásquez
A triangular system of conservation laws with discontinuous flux that models the one-dimensional flow of two disperse phases through a continuous one is formulated. The triangularity arises from the distinction between a primary and a secondary disperse phase, where the movement of the primary disperse phase does not depend on the local volume fraction of the secondary one. A particular application is the movement of aggregate bubbles and solid particles in flotation columns under feed and discharge operations. This model is formulated under the assumption of a variable cross-sectional area. A monotone numerical scheme to approximate solutions to this model is presented. The scheme is supported by three partial theoretical arguments. Firstly, it is proved that it satisfies an invariant-region property, i.e., the approximate volume fractions of the three phases, and their sum, stay between zero and one. Secondly, under the assumption of flow in a column with constant cross-sectional area it is shown that the scheme for the primary disperse phase converges to a suitably defined entropy solution. Thirdly, under the additional assumption of absence of flux discontinuities it is further demonstrated, by invoking arguments of compensated compactness, that the scheme for the secondary disperse phase converges to a weak solution of the corresponding conservation law. Numerical examples along with estimations of numerical error and convergence rates are presented for counter-current and co-current flows of the two disperse phases.

20 December 2022 in IMA Journal of Applied Mathematics
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Journal Article
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RBRaimund Bürger
Raimund Bürger
SDStefan Diehl
Stefan Diehl
MMM Carmen Martí
M Carmen Martí
YVYolanda Vásquez
Yolanda Vásquez
Froth flotation is a common unit operation used in mineral processing. It serves to separate valuable mineral particles from worthless gangue particles in finely ground ores. The valuable mineral particles are hydrophobic and attach to bubbles of air injected into the pulp. This creates bubble-particle aggregates that rise to the top of the flotation column where they accumulate to a froth or foam layer that is removed through a launder for further processing. At the same time, the hydrophilic gangue particles settle and are removed continuously. The drainage of liquid due to capillarity is essential for the formation of a stable froth layer. This effect is included into a previously formulated hyperbolic system of partial differential equations that models the volume fractions of floating aggregates and settling hydrophilic solids [R. Bürger, S. Diehl and M.C. Martí, IMA J. Appl. Math. 84 (2019) 930–973]. The construction of desired steady-state solutions with a froth layer is detailed and feasibility conditions on the feed volume fractions and the volumetric flows of feed, underflow and wash water are visualized in so-called operating charts. A monotone numerical scheme is derived and employed to simulate the dynamic behaviour of a flotation column. It is also proven that, under a suitable Courant-Friedrichs-Lewy (CFL) condition, the approximate volume fractions are bounded between zero and one when the initial data are.

1 October 2020 in Minerals Engineering
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Journal Article
Closed access
RBRaimund Bürger
Raimund Bürger
SDStefan Diehl
Stefan Diehl
CMCarmen Marti
Carmen Marti
YVYolanda Vásquez
Yolanda Vásquez

28 February 2023 in Minerals
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Journal Article
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FBFernando Betancourt
Fernando Betancourt
RBRaimund Bürger
Raimund Bürger
SDStefan Diehl
Stefan Diehl
Leopoldo GutierrezLeopoldo Gutierrez
Leopoldo Gutierrez
CMCarmen Marti
Carmen Marti
YVYolanda Vásquez
Yolanda Vásquez
The operation of a froth flotation column can be described by a nonlinear convection–diffusion partial differential equation that incorporates the solids–flux and drift–flux theories as well as a model of foam drainage. The resulting model predicts the bubble and (gangue) particle volume fractions as functions of height and time. The steady-state (time-independent) version of the model defines so-called operating charts that map conditions on the gas and pulp feed rates that allow for operation with a stationary froth layer. Operating charts for a suitably adapted version of the model are compared with experimental results obtained with a laboratory flotation column. Experiments were conducted with a two-phase liquid–bubble flow. The results indicate good agreement between the predicted and measured conditions for steady states. Numerical simulations for transient operation, in part for the addition of solid particles, are presented.

22 October 2025
Verified
Conference Paper
Closed access
JRJavier Rivas
Javier Rivas
YVYolanda Vásquez
Yolanda Vásquez
MAMatías Alvarado
Matías Alvarado
Breast cancer is one of the major challenges in public health, with high incidence and mortality rates among women worldwide. Immunotherapy treatment has emerged as an alternative for successful breast cancer treatment with variable effectiveness however. This highlights the need for predictive models that can optimize the selection of patients who are more likely to benefit from immunotherapy treatments. This paper advances the development of machine learning classification for predicting immune response to immune checkpoint inhibitor therapy in breast cancer patients. One random forest (RF) method is trained using single-cell RNA sequencing (scRNAseq) data to identify gene expression patterns associated with successful PD-1 and PD-L1 immunotherapy treatment. Test and validation is with data from GEO after the need preprocessing and normalization of gene expression matrices. Results from the RF classification show good performance.