Abstract:In this study, a novel solar energy assisted multigeneration energy plant by using the solar radiation as a renewable energy resource is designed to produce some useful products, such as electricity, heating-cooling, and hydrogen, and modelled to increase the system performance. This designed multigeneration energy system consists of the solar power tower, steam Rankine cycles, absorption heating-cooling system, Cu-Cl thermochemical cycle, and hydrogen liquefaction unit. A thermodynamic assessment is developed… Show more
“…Hall et al examined the electrolysis step by investigating the efficiency and thermodynamics of a Cu–Cl electrolyzer. Integration of the Brayton cycle with three-, four-, and five-step variants of the Cu–Cl cycle and their thermodynamic assessment was conducted by Wu et al A conceptual multi-generation system incorporating the Cu–Cl cycle for hydrogen production was modeled and investigated by Corumlu and Ozturk . Comprehensive energy and exergy analyses and thermal management of a four-step integrated Cu–Cl cycle at the Ontario Tech University have been conducted by Razi et al.…”
Section: Introductionmentioning
confidence: 99%
“…Integration of the Brayton cycle with three-, four-, and five-step variants of the Cu−Cl cycle and their thermodynamic assessment was conducted by Wu et al 14 A conceptual multi-generation system incorporating the Cu−Cl cycle for hydrogen production was modeled and investigated by Corumlu and Ozturk. 15 Comprehensive energy and exergy analyses and thermal management of a four-step integrated Cu− Cl cycle at the Ontario Tech University have been conducted by Razi et al in refs 16 and 17, respectively, by modeling every component of the integrated cycle in Aspen-plus.…”
In
this paper, we perform detailed energy and exergy analyses of
a four-step integrated copper–chlorine cycle for hydrogen production.
In this regard, we consider the incorporation of the flash vaporization
technique as a novel approach to the anolyte separation process in
the cycle. The flash vaporization process is most commonly used commercially
for the desalination of seawater. However, there are no studies in
the literature that consider the application of this technique for
a themochemical process in general and for the anolyte separation
purposes in a copper–chlorine cycle in particular. The rationale
for the need for an alternate anolyte separation technique is based
on our previously published results considering the energy and exergy
analyses of the Cu–Cl cycle in the Clean Energy Research Laboratory
(CERL) at the Ontario Tech University, where it is reported that the
current anolyte separation approach is relatively energy-intensive.
The purpose of this modification is to perform the partial separation
of the oxidized anolyte at a reduced temperature by realizing the
separation process under vacuum conditions. In this regard, the results
of the energy and exergy analyses of the integrated cycle conceptually
modified with flash vaporization process are compared to those of
the original integrated cycle in terms of the total exergy destruction,
overall heat input and rejection rates, overall energy and exergy
efficiencies, and heat input and exergy destruction of the anolyte
separation step. According to the energy and exergy analyses, the
modified cycle results in relatively lower exergy destruction (with
196.6 MW) compared to the original cycle (with 209.2 MW) and relatively
higher overall energy (7.2% compared to 6.6%) and exergy (11% compared
to 10.2%) efficiencies.
“…Hall et al examined the electrolysis step by investigating the efficiency and thermodynamics of a Cu–Cl electrolyzer. Integration of the Brayton cycle with three-, four-, and five-step variants of the Cu–Cl cycle and their thermodynamic assessment was conducted by Wu et al A conceptual multi-generation system incorporating the Cu–Cl cycle for hydrogen production was modeled and investigated by Corumlu and Ozturk . Comprehensive energy and exergy analyses and thermal management of a four-step integrated Cu–Cl cycle at the Ontario Tech University have been conducted by Razi et al.…”
Section: Introductionmentioning
confidence: 99%
“…Integration of the Brayton cycle with three-, four-, and five-step variants of the Cu−Cl cycle and their thermodynamic assessment was conducted by Wu et al 14 A conceptual multi-generation system incorporating the Cu−Cl cycle for hydrogen production was modeled and investigated by Corumlu and Ozturk. 15 Comprehensive energy and exergy analyses and thermal management of a four-step integrated Cu− Cl cycle at the Ontario Tech University have been conducted by Razi et al in refs 16 and 17, respectively, by modeling every component of the integrated cycle in Aspen-plus.…”
In
this paper, we perform detailed energy and exergy analyses of
a four-step integrated copper–chlorine cycle for hydrogen production.
In this regard, we consider the incorporation of the flash vaporization
technique as a novel approach to the anolyte separation process in
the cycle. The flash vaporization process is most commonly used commercially
for the desalination of seawater. However, there are no studies in
the literature that consider the application of this technique for
a themochemical process in general and for the anolyte separation
purposes in a copper–chlorine cycle in particular. The rationale
for the need for an alternate anolyte separation technique is based
on our previously published results considering the energy and exergy
analyses of the Cu–Cl cycle in the Clean Energy Research Laboratory
(CERL) at the Ontario Tech University, where it is reported that the
current anolyte separation approach is relatively energy-intensive.
The purpose of this modification is to perform the partial separation
of the oxidized anolyte at a reduced temperature by realizing the
separation process under vacuum conditions. In this regard, the results
of the energy and exergy analyses of the integrated cycle conceptually
modified with flash vaporization process are compared to those of
the original integrated cycle in terms of the total exergy destruction,
overall heat input and rejection rates, overall energy and exergy
efficiencies, and heat input and exergy destruction of the anolyte
separation step. According to the energy and exergy analyses, the
modified cycle results in relatively lower exergy destruction (with
196.6 MW) compared to the original cycle (with 209.2 MW) and relatively
higher overall energy (7.2% compared to 6.6%) and exergy (11% compared
to 10.2%) efficiencies.
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