Zobrazeno 1 - 10
of 23
pro vyhledávání: '"Giuseppe Diglio"'
Publikováno v:
Renewable Energy. 143:488-500
A novel energy index to assess plants capable of producing electricity from a renewable source is introduced in this paper. This index allows to evaluate the bidirectional energy flows on the external power grid, due the electricity exported to the g
Autor:
Vasilije Manovic, Piero Bareschino, Giuseppe Diglio, Erasmo Mancusi, Dawid P. Hanak, Fabio Montagnaro, Francesco Pepe
Publikováno v:
Applied Energy. 230:241-256
In this article, a process for sorption-enhanced steam methane reforming in an adiabatic fixed-bed reactor coupled with a solid oxide fuel cell (SOFC) is evaluated using a 1D numerical reactor model combined with a simplified fuel cell simulation. A
Publikováno v:
Industrial & Engineering Chemistry Research. 57:11299-11311
This paper reports the techno-economic analysis of a small-scale power generation unit integrating chemical looping combustion (CLC) with inherent CO2 capture and power sections. In the CLC section four adiabatic fixed beds are operated using Cu as a
Publikováno v:
Geothermics. 72:112-123
This paper presents numerical study on the use of nanofluids to replace conventional ethylene glycol/water mixture as heat carrier in a BoreHole Heat Exchanger. Nanofluids contain suspended metallic nanoparticles: increasing their concentration, in c
Autor:
Giuseppe Diglio, Francesco Pepe, Vasilije Manovic, Piero Bareschino, Dawid P. Hanak, Fabio Montagnaro
Publikováno v:
Applied Energy. 210:1-15
In this study sorption-enhanced steam methane reforming (SE-SMR) in fixed beds is investigated by means of 1D numerical modelling, and the model is validated with the data reported in the literature. Isothermal conditions (973 K) are considered, and
Autor:
Giuseppe Diglio, Dawid P. Hanak, Fabio Montagnaro, Erasmo Mancusi, Vasilije Manovic, Francesco Pepe, Piero Bareschino
Publikováno v:
Journal of Power Sources. 364:41-51
Sorption-enhanced steam methane reforming (SE-SMR) is a promising alternative for H 2 production with inherent CO 2 capture. This study evaluates the techno-economic performance of SE-SMR in a network of fixed beds and its integration with a solid ox
Autor:
Carlo Roselli, Giuseppe Diglio, Piero Bareschino, Giovanni Angrisani, Maurizio Sasso, Francesco Pepe
Publikováno v:
Applied Thermal Engineering. 124:641-651
The use of a MIL101@GO-6 (MILGO) based Desiccant Wheel in a desiccant cooling system for air conditioning has been numerically studied. MILGO is a novel composite material, consisting of 6% w/w graphite oxide dispersed in the MIL101 metal organic fra
Autor:
Giuseppe Diglio, Roberto Solimene, Piero Bareschino, Piero Salatino, Francesco Pepe, Erasmo Mancusi
Publikováno v:
Powder technology
316 (2017): 614–627. doi:10.1016/j.powtec.2016.12.051
info:cnr-pdr/source/autori:Diglio, Giuseppe; Bareschino, Piero; Solimene, Roberto; Mancusi, Erasmo; Pepe, Francesco; Salatino, Piero/titolo:Numerical simulation of hydrogen production by chemical looping reforming in a dual fluidized bed reactor/doi:10.1016%2Fj.powtec.2016.12.051/rivista:Powder technology (Print)/anno:2017/pagina_da:614/pagina_a:627/intervallo_pagine:614–627/volume:316
316 (2017): 614–627. doi:10.1016/j.powtec.2016.12.051
info:cnr-pdr/source/autori:Diglio, Giuseppe; Bareschino, Piero; Solimene, Roberto; Mancusi, Erasmo; Pepe, Francesco; Salatino, Piero/titolo:Numerical simulation of hydrogen production by chemical looping reforming in a dual fluidized bed reactor/doi:10.1016%2Fj.powtec.2016.12.051/rivista:Powder technology (Print)/anno:2017/pagina_da:614/pagina_a:627/intervallo_pagine:614–627/volume:316
Although exploitation of Dual Fluidized Bed systems (DFB) is currently being explored in various fields, DFBs present some criticalities, mainly related to effective control of solids recirculation and to avoidance of gas leakage between the beds, ex
Publikováno v:
Advanced Science Letters. 23:6002-6006
Publikováno v:
International Journal of Hydrogen Energy. 42:15010-15023
This paper presents a novel quasi -autothermal hydrogen production process. The proposed layout couples a Chemical Looping Combustion (CLC) section and a Steam Methane Reforming (SMR) one. In CLC section, four packed-beds are operated using Ni as oxy