JUAN ANTONIO
LABARTA REYES
CATEDRATICO/A DE UNIVERSIDAD
Publications (141) JUAN ANTONIO LABARTA REYES publications
2025
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Optimal design of heat pump assisted thermally coupled distillation sequences
Applied Thermal Engineering, Vol. 274
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Optimizing Heat Recovery: Advanced Design of Integrated Heat Exchanger Networks with ORCs and Heat Pumps
Systems and Control Transactions
2024
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Efficient use of energy in distillation: Advancing towards the electrification of the chemical industry
Computer Aided Chemical Engineering (Elsevier B.V.), pp. 103-108
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From power to heat: Strategies for electrifying distillation for sustainable chemical processes
Applied Thermal Engineering, Vol. 257
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Graphical User Interfaces (GUIs) for Helping the Thermodynamic Analysis of Phase Equilibrium Data Correlation Results
VII Congreso de Innovación Docente en Ingeniería Química (CIDIQ 2024). Área temática: T3. Herramientas informáticas en la formación/enseñanza en Ingeniería Química (#40)
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Optimal Design of Heat Pump Assisted Distillation Sequences
Computer Aided Chemical Engineering, Vol. 53, pp. 1255-1260
2023
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Efficient use of energy in distillation sequences
Computer Aided Chemical Engineering (Elsevier B.V.), pp. 1927-1932
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Hypertensive emergency versus preeclampsia in a patient with sickle cell disease: a case report
WORLD JOURNAL OF EMERGENCY MEDICINE
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Liquid-Liquid Equilibrium Data Correlation: Predicting a robust and consistent set of initial NRTL parameters
Computer Aided Chemical Engineering (Elsevier B.V.), pp. 3459-3464
2022
- Boundaries_LL_NRTL: Graphical User Interface (GUI) for the Characterization of the NRTL Model: Binary Spinodal Surfaces (in the tau(i,j)-tau(j,i)-xi space), LLE Maps, and Miscibility Boundaries
- GMcal_TieLinesVL: Graphical User Interface (GUI) for the Topological Analysis of Experimental and Calculated GM Functions for Binary and Ternary (Isobaric or Isothermal) Vapor-Liquid Equilibrium (VLE or VLLE) Data (including Tie-Lines, Derivatives, Distillation Boundaries, LL Critical Points Location, etc.)
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Operaciones de separación de transferencia de materia
Síntesis
- ParamIni_LL_NRTL: Graphical User Interface (GUI) for the Selection of NRTL Initial Parameters for the Correlation of Ternary Liquid-Liquid Equilibrium Data (Type I, II, III and 0 (LL island), i.e. with 1, 2, 3 or 0 binary pairs partially miscible)
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What does the NRTL model look like? Determination of boundaries for different fluid phase equilibrium regions
AIChE Journal, Vol. 68, Núm. 10
2021
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Explorations of Liquid-Liquid Phase Equilibrium for the Mixture (Isopropanol + Water) with Pyridinium-Based Ionic Liquids
Journal of Chemical and Engineering Data, Vol. 66, Núm. 5, pp. 2192-2199
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Liquid-liquid equilibrium measurements and interaction explorations for separation of azeotrope n-butyl acetate and n-butanol using three ionic liquids
Journal of Chemical Thermodynamics, Vol. 155
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Structural considerations in zeotropic distillation sequences with multiple feeds
Computers and Chemical Engineering, Vol. 154
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Thermo-economic and environmental optimization of a solar-driven zero-liquid discharge system for shale gas wastewater desalination
Desalination, Vol. 511
2020
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Environmental and economic water management in shale gas extraction
Sustainability (Switzerland), Vol. 12, Núm. 4
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Liquid-Liquid Equilibrium Data Correlation Using NRTL Model for Different Types of Binary Systems: Upper Critical Solution Temperature, Lower Critical Solution Temperature, and Closed Miscibility Loops
Industrial and Engineering Chemistry Research, Vol. 59, Núm. 17, pp. 8469-8479