Andrés Melgar
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Andrés Melgar has a total of 39 co-authors. Here are the top co-authors by number of shared publications:
- Francisco V. Tinaut
University of Valladolid
16 shared publications - Juan Fernando Pérez
Grupo de Manejo Eficiente de la Energía (GIMEL), Departamento de Ingeniería Mecánica, Facultad de Ingeniería, Universidad de Antioquia, Medellín 050010, Colombia
8 shared publications B. Giménez
6 shared publications- Alfonso Horrillo
CIDAUT Foundation for Research and Development in Transport and Energy, Boecillo, Spain
5 shared publications - Miriam Reyes
Department of Energy and Fluid Mechanics Engineering, University of Valladolid, Paseo del Cauce 59, E-47011 Valladolid, Valladolid, Spain
4 shared publications - Blanca Giménez
Department of Energy and Fluid Mechanics Engineering, University of Valladolid, Paseo del Cauce 59, E-47011 Valladolid, Spain
3 shared publications
Latest Publications
- Open Access
- 21 November 2025
- Published by IOP Publishing in Measurement Science and Technology
- Vol. 36 (11) , 116122
Adaptive low-pass filter design for in-cylinder pressure signals in internal combustion engines
In-cylinder pressure is a fundamental parameter in the design and optimization of internal combustion engines. Therefore, before performing analyses it is essential to correctly obtain and process pressure measurements. However, these signals are often contaminated with high-frequency noise that can compromise combustion diagnostics, especially when cycle-to-cycle variations (CCVs) are significant. This work presents a novel adaptive methodology for filtering in-cylinder pressure signals using a frequency-domain low-pass filter. The proposed approach is able to automatically determine the filter parameters by analyzing the spectral characteristics of the signal, allowing the preservation of both cycle-averaged and CCV information. The method has been validated using pressure traces generated from engine simulations under two extreme operating conditions, with various levels of Additive White Gaussian Noise. For each scenario, the optimal filter configuration was identified by grid searching the cut-off and stopband frequencies to minimize error between the filtered and noise-free signals. The proposed method closely approaches the optimal filter configuration outperforming existing filtering strategies in both signal reconstruction and combustion diagnostics based on the rate of heat release. The results confirm that the proposed filtering strategy effectively retains both cycle-averaged features and cycle-to-cycle variability across a wide range of operating conditions and noise levels.
- 21 November 2025
- Published by IOP Publishing in Measurement Science and Technology
- Vol. 36 (11) , 116122
Open AccessAdaptive low-pass filter design for in-cylinder pressure signals in internal combustion engines
In-cylinder pressure is a fundamental parameter in the design and optimization of internal combustion engines. Therefore, before performing analyses it is essential to correctly obtain and process pressure measurements. However, these signals are often contaminated with high-frequency noise that can compromise combustion diagnostics, especially when cycle-to-cycle variations (CCVs) are significant. This work presents a novel adaptive methodology for filtering in-cylinder pressure signals using a frequency-domain low-pass filter. The proposed approach is able to automatically determine the filter parameters by analyzing the spectral characteristics of the signal, allowing the preservation of both cycle-averaged and CCV information. The method has been validated using pressure traces generated from engine simulations under two extreme operating conditions, with various levels of Additive White Gaussian Noise. For each scenario, the optimal filter configuration was identified by grid searching the cut-off and stopband frequencies to minimize error between the filtered and noise-free signals. The proposed method closely approaches the optimal filter configuration outperforming existing filtering strategies in both signal reconstruction and combustion diagnostics based on the rate of heat release. The results confirm that the proposed filtering strategy effectively retains both cycle-averaged features and cycle-to-cycle variability across a wide range of operating conditions and noise levels.
- Open Access
- 1 January 2021
- Published by Elsevier in Combustion and Flame
- Vol. 223, 15-27
A correlation for turbulent combustion speed accounting for instabilities and expansion speed in a hydrogen-natural gas spark ignition engine
- 1 January 2021
- Published by Elsevier in Combustion and Flame
- Vol. 223, 15-27
Open AccessA correlation for turbulent combustion speed accounting for instabilities and expansion speed in a hydrogen-natural gas spark ignition engine
- 1 June 2016
- Published by Elsevier in Industrial Crops and Products
- Vol. 84, 166-175
Fixed bed gasification of Jacaranda Copaia wood: Effect of packing factor and oxygen enriched air
- 1 June 2016
- Published by Elsevier in Industrial Crops and Products
- Vol. 84, 166-175
Fixed bed gasification of Jacaranda Copaia wood: Effect of packing factor and oxygen enriched air
- 8 March 2016
- Published by Taylor & Francis in International Journal of Sustainable Energy
- Vol. 36 (10) , 1010-1028
Thermodynamic methodology to support the selection of feedstocks for decentralised downdraft gasification power plants
Thermodynamic criteria as a feedstock selection tool for decentralised downdraft gasifiers coupled to spark-ignition engines are presented in this work. The methodology consists of an energy and exergy analysis of gasification process. The analysis is carried out by computational modelling of the gasification process as a function of biomass type (ultimate analysis, moisture content and heating value) and fuel/air ratio. Considering a system operating with different wood species, analysed parameters are gas heating value, energy and exergy efficiencies and engine fuel quality (EFQ). With a fixed fuel/air ratio (2.6) and moisture content (20%wt), it is highlighted that as the carbon-oxygen molar ratio of wood decreases from 2.0 to 1.78 as model input, reaction temperature increases by 9%, energy and exergy efficiencies diminish by 1.8% and 4.2%, respectively, while EFQ increases by 3.2%. Therefore, for decentralised power plants, biomass should be selected to produce higher EFQ.
- 8 March 2016
- Published by Taylor & Francis in International Journal of Sustainable Energy
- Vol. 36 (10) , 1010-1028
Thermodynamic methodology to support the selection of feedstocks for decentralised downdraft gasification power plants
Thermodynamic criteria as a feedstock selection tool for decentralised downdraft gasifiers coupled to spark-ignition engines are presented in this work. The methodology consists of an energy and exergy analysis of gasification process. The analysis is carried out by computational modelling of the gasification process as a function of biomass type (ultimate analysis, moisture content and heating value) and fuel/air ratio. Considering a system operating with different wood species, analysed parameters are gas heating value, energy and exergy efficiencies and engine fuel quality (EFQ). With a fixed fuel/air ratio (2.6) and moisture content (20%wt), it is highlighted that as the carbon-oxygen molar ratio of wood decreases from 2.0 to 1.78 as model input, reaction temperature increases by 9%, energy and exergy efficiencies diminish by 1.8% and 4.2%, respectively, while EFQ increases by 3.2%. Therefore, for decentralised power plants, biomass should be selected to produce higher EFQ.
- 1 January 2016
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 41 (3) , 2064-2074
Characterization of the combustion process and cycle-to-cycle variations in a spark ignition engine fuelled with natural gas/hydrogen mixtures
- 1 January 2016
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 41 (3) , 2064-2074
Characterization of the combustion process and cycle-to-cycle variations in a spark ignition engine fuelled with natural gas/hydrogen mixtures
- 1 December 2015
- Published by Elsevier in Biomass and Bioenergy
- Vol. 83, 403-421
Sensitivity analysis of a biomass gasification model in fixed bed downdraft reactors: Effect of model and process parameters on reaction front
- 1 December 2015
- Published by Elsevier in Biomass and Bioenergy
- Vol. 83, 403-421
Sensitivity analysis of a biomass gasification model in fixed bed downdraft reactors: Effect of model and process parameters on reaction front
- 1 November 2013
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 38 (35) , 15477-15487
Study of the cycle-to-cycle variations of an internal combustion engine fuelled with natural gas/hydrogen blends from the diagnosis of combustion pressure
- 1 November 2013
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 38 (35) , 15477-15487
Study of the cycle-to-cycle variations of an internal combustion engine fuelled with natural gas/hydrogen blends from the diagnosis of combustion pressure
- 20 April 2013
- Published by Hindawi Limited in International Journal of Energy Research
- Vol. 38 (3) , 319-338
Modeling of fixed bed downdraft biomass gasification: Application on lab-scale and industrial reactors
This study aimed at presenting a model to simulate downdraft biomass gasification under steady-state or unsteady-state conditions. The model takes into account several processes that are relevant to the transformation of solid biomass into fuel gas, such as drying; devolatilization; oxidation; CO2, H2O, and H2 reduction with char, pressure losses, solid and gas temperature, particle diameter, and bed void fraction evolution; and heat transfer by several mechanisms such as solid–gas convection, bed–wall convection, and radiation in the solid phase. Model validation is carried out by performing experiments in two lab-scale downdraft fixed bed reactors (unsteady-state conditions) and in a novel industrial pilot plant of 400 kWth–100 kWe (steady-state conditions). The capability of the model to predict the effect of several factors (reactor diameter, air superficial velocity, and particle size and biomass moisture) on key response variables (temperature field, maximum temperature inside the bed, flame front velocity, biomass consumption rate, and composition and calorific value of the producer gas) is evaluated. For most response variables, a good agreement between experimental and estimated values is attained, and the model is able to reproduce the trend of variation of the experimental results. In general terms, the process performance improves with higher reactor diameter and lesser air superficial velocity, particle size, and moisture content of biomass. The steady-state simulation appears to be a versatile tool for simulating different reactor configurations (preheating systems, variable geometry, and different materials). Copyright © 2013 John Wiley & Sons, Ltd.
- 20 April 2013
- Published by Hindawi Limited in International Journal of Energy Research
- Vol. 38 (3) , 319-338
Modeling of fixed bed downdraft biomass gasification: Application on lab-scale and industrial reactors
This study aimed at presenting a model to simulate downdraft biomass gasification under steady-state or unsteady-state conditions. The model takes into account several processes that are relevant to the transformation of solid biomass into fuel gas, such as drying; devolatilization; oxidation; CO2, H2O, and H2 reduction with char, pressure losses, solid and gas temperature, particle diameter, and bed void fraction evolution; and heat transfer by several mechanisms such as solid–gas convection, bed–wall convection, and radiation in the solid phase. Model validation is carried out by performing experiments in two lab-scale downdraft fixed bed reactors (unsteady-state conditions) and in a novel industrial pilot plant of 400 kWth–100 kWe (steady-state conditions). The capability of the model to predict the effect of several factors (reactor diameter, air superficial velocity, and particle size and biomass moisture) on key response variables (temperature field, maximum temperature inside the bed, flame front velocity, biomass consumption rate, and composition and calorific value of the producer gas) is evaluated. For most response variables, a good agreement between experimental and estimated values is attained, and the model is able to reproduce the trend of variation of the experimental results. In general terms, the process performance improves with higher reactor diameter and lesser air superficial velocity, particle size, and moisture content of biomass. The steady-state simulation appears to be a versatile tool for simulating different reactor configurations (preheating systems, variable geometry, and different materials). Copyright © 2013 John Wiley & Sons, Ltd.