Papa M. Ndiaye

ORCID: 0000-0003-4961-7768
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Research Areas
  • Phase Equilibria and Thermodynamics
  • Thermodynamic properties of mixtures
  • Chemical Thermodynamics and Molecular Structure
  • Process Optimization and Integration
  • Petroleum Processing and Analysis
  • Biodiesel Production and Applications
  • Material Dynamics and Properties
  • Hydrocarbon exploration and reservoir analysis
  • Biofuel production and bioconversion
  • Polymer Foaming and Composites
  • Sugarcane Cultivation and Processing
  • Advanced Combustion Engine Technologies
  • Adsorption, diffusion, and thermodynamic properties of materials
  • Thermal and Kinetic Analysis
  • biodegradable polymer synthesis and properties
  • Natural Products and Biological Research
  • Theoretical and Computational Physics
  • Carbon Dioxide Capture Technologies
  • Essential Oils and Antimicrobial Activity
  • Ginger and Zingiberaceae research
  • Catalysis and Oxidation Reactions
  • Piperaceae Chemical and Biological Studies
  • Enhanced Oil Recovery Techniques
  • NMR spectroscopy and applications
  • Aerogels and thermal insulation

Universidade Federal do Rio de Janeiro
2005-2024

Universidade Federal do Paraná
2009-2014

Institut national de recherche en informatique et en automatique
2002

The aim of this work is to report the experimental data and thermodynamic modeling phase equilibrium binary systems containing soybean olive oils with propane n-butane. Phase experiments were carried out using static synthetic method in a high-pressure variable-volume view cell temperature range from 30 70ºC varying solvent overall composition 5 98 wt%. Vapor-liquid, liquid-liquid vapor-liquid-liquid transitions observed at relatively low pressures. Peng-Robinson SAFT equations state without...

10.1590/s0104-66322006000300014 article EN Brazilian Journal of Chemical Engineering 2006-09-01

This work reports new vapor pressure data of soybean oil, castor and their fatty acid ethyl ester mixtures (FAEE) obtained from an enzyme-catalyzed reaction. Vapor measurements were carried out in a temperature range (290 to 355 K) using static method having differential transducer with precision 5 Pa. Degassing was performed inside the equilibrium cell by freezing thawing samples under moderate vacuum (about 50 kPa). For vegetable oils, values varied (0.19 2.16) kPa, whereas for FAEE...

10.1021/je049898o article EN Journal of Chemical & Engineering Data 2005-02-01

Summary This paper reports a study of sugar cane juice carbonation and the evaluation variables effects such as pH, time temperature on industrially relevant parameters for quality juice. Three different batches were evaluated using complete two‐level factorial design with central point performed in triplicate. From results this work, it can be seen that higher sucrose concentrations lower percentage total soluble solids reducing sugars obtained clarified juices maximum values reaction (9.5,...

10.1111/j.1365-2621.2011.02857.x article EN International Journal of Food Science & Technology 2011-11-28

This work reports experimental phase equilibrium data for the ternary system involving ε-caprolactone, carbon dioxide, and dichloromethane. Such provide fundamental information to conduct polymerization reactions in supercritical dioxide medium. The experiments were performed using a variable-volume view cell over temperature range from 323.15 353.15 K different mass ratios of dichloromethane ε-caprolactone (0.5:1, 1:1, 2:1). Phase transitions vapor–liquid at bubble point (VLE-PB),...

10.1021/acs.jced.8b01017 article EN Journal of Chemical & Engineering Data 2019-03-20
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