Mónica Faria

Dr. Mónica Faria

Chemical Engineering, Instituto Superior Técnico, Lisbon, Lisboa, Portugal
orcid

Research Focus & Metrics

Academic Career Length

16Years (2011-Present)

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

Representative Publications

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1 June 2018 in Carbohydrate Polymers
Verified
Journal Article
Closed access
GMGonçalo Mendes
Gonçalo Mendes
Mónica FariaMónica Faria
Mónica Faria
ACAlexandra Carvalho
Alexandra Carvalho
Maria Clara GonçalvesMaria Clara Gonçalves
Maria Clara Gonçalves
Maria Norberta De PinhoMaria Norberta De Pinho
Maria Norberta De Pinho


10 February 2020 in Cellulose
Verified
Journal Article
Closed access
PDF file
Mónica FariaMónica Faria
Mónica Faria
CMCíntia Moreira
Cíntia Moreira
TETiago Eusébio
Tiago Eusébio
PBPedro Brogueira
Pedro Brogueira
Maria Norberta De PinhoMaria Norberta De Pinho
Maria Norberta De Pinho

28 January 2023 in Toxins
Verified
Journal Article
Open access
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Flávia S. C. RodriguesFlávia S. C. Rodrigues
Flávia S. C. Rodrigues
Mónica FariaMónica Faria
Mónica Faria
End-stage renal disease (ESRD) patients rely on renal replacement therapies to survive. Hemodialysis (HD), the most widely applied treatment, is responsible for the removal of excess fluid and uremic toxins (UTs) from blood, particularly those with low molecular weight (MW < 500 Da). The development of high-flux membranes and more efficient treatment modes, such as hemodiafiltration, have resulted in improved removal rates of UTs in the middle molecular weight range. However, the concentrations of protein-bound uremic toxins (PBUTs) remain essentially untouched. Due to the high binding affinity to large proteins, such as albumin, PBUTs form large complexes (MW > 66 kDa) which are not removed during HD and their accumulation has been strongly associated with the increased morbidity and mortality of patients with ESRD. In this review, we describe adsorption- and displacement-based approaches currently being studied to enhance the removal of PBUTs. The development of mixed matrix membranes (MMMs) with selective adsorption properties, infusion of compounds capable of displacing UTs from their binding site on albumin, and competitive binding membranes show promising results, but the road to clinical application is still long, and further investigation is required.


24 August 2022 in Membranes
Verified
Journal Article
Open access
PDF file
Inês CoelhoInês Coelho
Inês Coelho
Rita PiresRita Pires
Rita Pires
SGSérgio B. B. Gonçalves
Sérgio B. B. Gonçalves
Vasco BonifácioVasco Bonifácio
Vasco Bonifácio
Mónica FariaMónica Faria
Mónica Faria
The production of medical devices follows strict guidelines where bio- and hemocompatibility, mechanical strength, and tear resistance are important features. Segmented polyurethanes (PUs) are an important class of polymers that fulfill many of these requirements, thus justifying the investigation of novel derivatives with enhanced properties, such as modulated carbon dioxide and oxygen permeability. In this work, three segmented polyurethane-based membranes, containing blocks of hard segments (HSs) dispersed in a matrix of soft segment (SS) blocks, were prepared by reacting a PU prepolymer (PUR) with tris(hydroxymethyl)aminomethane (TRIS), Congo red (CR) and methyl-β-cyclodextrin (MBCD), rendering PU/TRIS, PU/CR and PU/MBCD membranes. The pure (control) PU membrane exhibited the highest degree of phase segregation between HSs and SSs followed by PU/TRIS and PU/MBCD membranes, and the PU/CR membrane displayed the highest degree of mixing. Pure PU and PU/CR membranes exhibited the highest and lowest values of Young’s modulus, tangent moduli and ultimate tensile strength, respectively, suggesting that the introduction of CR increases molecular mobility, thus reducing stiffness. The CO2 permeability was highest for the PU/CR membrane, 347 Barrer, and lowest for the pure PU membrane, 278 Barrer, suggesting that a higher degree of mixing between HSs and SSs leads to higher CO2 permeation rates. The permeability of O2 was similar for all membranes, but ca. 10-fold lower than the CO2 permeability.