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Dive into the research topics where H. Romero-Paredes is active.

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Featured researches published by H. Romero-Paredes.


Journal of Renewable and Sustainable Energy | 2012

Radiative heat transfer analysis of a directly irradiated cavity-type solar thermochemical reactor by Monte-Carlo ray tracing

H.I. Villafán-Vidales; Stéphane Abanades; C.A. Arancibia-Bulnes; David Riveros-Rosas; H. Romero-Paredes; G. Espinosa-Paredes; C.A. Estrada

Radiative heat transfer in a 1u2009kW cavity-type solar reactor devoted to the thermal reduction of compressed ZnO and SnO2 powders is analyzed by a Monte Carlo ray tracing simulation. The developed model takes into account the radiative properties of the reactant particles and of the ceramic cavity walls, as well as the angular intensity distribution of the incoming concentrated solar irradiation. The model also includes the conduction heat losses through the lateral walls and the energy consumed by the endothermic chemical reaction. It is used to predict the temperature and the absorbed flux density profiles on the inner cavity walls for different main features of the reactor, concerning the dimensions of the cavity and the type of reactant. Results show that the absorbed flux density profile and the theoretical thermochemical efficiency change with the cavity aspect ratio and with the oxide reactant. The cavity with an aspect ratio of 3 and a SnO2 pellet undergoing dissociation presents the highest thermoc...


Journal of Solar Energy Engineering-transactions of The Asme | 2011

Monte Carlo Heat Transfer Modeling of a Particle-Cloud Solar Reactor for SnO2 Thermal Reduction

H.I. Villafán-Vidales; C.A. Arancibia-Bulnes; Stéphane Abanades; David Riveros-Rosas; H. Romero-Paredes

A directly irradiated cavity solar reactor devoted to the thermal reduction of SnO 2 particle-cloud is studied numerically by using the Monte Carlo method. The steady-state model solves the radiation and convection heat transfers in the semitransparent particle suspension and the chemical reaction. It was used to predict the temperature distribution and the reaction extent inside the cavity, as well as the theoretical thermochemical efficiency for different operational conditions. The simulations assume that the reactor contains a nonuniform size suspension of radiatively participating reacting SnO 2 particles. The model takes into account the radiative characteristics of the particles, as well as the directional characteristics of the power distribution of the incoming concentrated solar energy. The particle concentration, the particle size, and the length of the reactor are varied. Results show that the particle temperature and the yield of the endothermic reaction are higher when the reactor is fed with a cloud of particles with average diameter of 20 μm. The maximal thermochemical efficiency reached is 10%, which corresponds to an optimal optical thickness of around 2.


Science and Technology of Nuclear Installations | 2012

Heat and Mass Transfer during Hydrogen Generation in an Array of Fuel Bars of a BWR Using a Periodic Unit Cell

H. Romero-Paredes; Francisco J. Valdés-Parada; G. Espinosa-Paredes

This paper presents, the numerical analysis of heat and mass transfer during hydrogen generation in an array of fuel cylinder bars, each coated with a cladding and a steam current flowing outside the cylinders. The analysis considers the fuel element without mitigation effects. The system consists of a representative periodic unit cell where the initial and boundary-value problems for heat and mass transfer were solved. In this unit cell, we considered that a fuel element is coated by a cladding with steam surrounding it as a coolant. The numerical simulations allow describing the evolution of the temperature and concentration profiles inside the nuclear reactor and could be used as a basis for hybrid upscaling simulations.


Energy Sources Part A-recovery Utilization and Environmental Effects | 2015

Exergy and Energy Efficiencies in High Temperature Gas Reactors (PBMR)

J. Valle-Hernández; Gilberto Espinosa-Paredes; Jaime B. Morales-Sandoval; H. Romero-Paredes

The aims of this work are to determine the maximum efficiency in the generation and conversion of energy to electricity, and to obtain the exergy efficiency in a pebblebBed modular reactor. The dynamics of the process of energy generation in the nuclear fuel is represented by a point reactor kinetics model, and the process of transport of this energy toward the coolant fluid was based on the conservation laws of mass, energy, and momentum. The conversion to mechanical energy in the turbo-generators, as well as the operation of the heat exchangers, was also made on the simplified models based on physical laws. The results obtained of the energy and exergy balances were applied in order to calculate the maximum efficiency considering a change in the original design and the utilization of the energy lost in the cooling process, respectively.


SOLARPACES 2016: International Conference on Concentrating Solar Power and Chemical Energy Systems | 2017

Modeling of the steam hydrolysis in a two-step process for hydrogen production by solar concentrated energy

Julio Valle-Hernández; H. Romero-Paredes; Alejandro Pacheco-Reyes

In this paper the simulation of the steam hydrolysis for hydrogen production through the decomposition of cerium oxide is presented. The thermochemical cycle for hydrogen production consists of the endothermic reduction of CeO2 to lower-valence cerium oxide, at high temperature, where concentrated solar energy is used as a source of heat; and of the subsequent steam hydrolysis of the resulting cerium oxide to produce hydrogen. The modeling of endothermic reduction step was presented at the Solar Paces 2015. This work shows the modeling of the exothermic step; the hydrolysis of the cerium oxide (III) to form H2 and the corresponding initial cerium oxide made at lower temperature inside the solar reactor. For this model, three sections of the pipe where the reaction occurs were considered; the steam water inlet, the porous medium and the hydrogen outlet produced. The mathematical model describes the fluid mechanics; mass and energy transfer occurring therein inside the tungsten pipe. Thermochemical process ...


SOLARPACES 2015: International Conference on Concentrating Solar Power and Chemical Energy Systems | 2016

Modeling of a CeO2 thermochemistry reduction process for hydrogen production by solar concentrated energy

Julio Valle-Hernández; H. Romero-Paredes; C.A. Arancibia-Bulnes; H.I. Villafán-Vidales; Gilberto Espinosa-Paredes

In this paper the simulation of the thermal reduction for hydrogen production through the decomposition of cerium oxide is presented. The thermochemical cycle for hydrogen production consists of the endothermic reduction of CeO2 at high temperature, where concentrated solar energy is used as a source of heat; and of the subsequent steam hydrolysis of the resulting cerium oxide to produce hydrogen. For the thermochemical process, a solar reactor prototype is proposed; consisting of a cubic receptacle made of graphite fiber thermally insulated. Inside the reactor a pyramidal arrangement with nine tungsten pipes is housed. The pyramidal arrangement is made respect to the focal point where the reflected energy is concentrated. The solar energy is concentrated through the solar furnace of high radiative flux. The endothermic step is the reduction of the cerium oxide to lower-valence cerium oxide, at very high temperature. The exothermic step is the hydrolysis of the cerium oxide (III) to form H2 and the corres...


Applied Thermal Engineering | 2011

Heat transfer simulation in a thermochemical solar reactor based on a volumetric porous receiver

H.I. Villafán-Vidales; Stéphane Abanades; Cyril Caliot; H. Romero-Paredes


International Journal of Hydrogen Energy | 2009

Monte Carlo radiative transfer simulation of a cavity solar reactor for the reduction of cerium oxide

H.I. Villafán-Vidales; C.A. Arancibia-Bulnes; U. Dehesa-Carrasco; H. Romero-Paredes


Renewable & Sustainable Energy Reviews | 2017

An overview of the solar thermochemical processes for hydrogen and syngas production: Reactors, and facilities

H.I. Villafán-Vidales; C.A. Arancibia-Bulnes; David Riveros-Rosas; H. Romero-Paredes; C.A. Estrada


Chemical Engineering Research & Design | 2015

Transient heat transfer simulation of a 1 kWth moving front solar thermochemical reactor for thermal dissociation of compressed ZnO

H.I. Villafán-Vidales; Stéphane Abanades; M. Montiel-González; H. Romero-Paredes; C.A. Arancibia-Bulnes; C.A. Estrada

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C.A. Arancibia-Bulnes

National Autonomous University of Mexico

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H.I. Villafán-Vidales

National Autonomous University of Mexico

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David Riveros-Rosas

National Autonomous University of Mexico

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C.A. Estrada

National Autonomous University of Mexico

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Stéphane Abanades

Centre national de la recherche scientifique

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Francisco J. Valdés-Parada

Universidad Autónoma Metropolitana

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Patricio J. Valadés-Pelayo

National Autonomous University of Mexico

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G. Espinosa-Paredes

Universidad Autónoma Metropolitana

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Gilberto Espinosa-Paredes

Universidad Autónoma Metropolitana

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Julio Valle-Hernández

National Autonomous University of Mexico

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