Exergoeconomic and exergoenvironmental evaluation of Integration of desalinations with a total site utility system

Janalizadeh, H.; Manesh, Mohammad Hasan Khoshgoftar; Amidpour, Majid

doi:10.1007/s10098-014-0765-0

Cited by 14 publications

(2 citation statements)

References 24 publications

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“…Several reviews of relevant publications on heat exchange synthesis and process integration have been published [35,36]. Recent studies have introduced an optimal design approach and multi-objective optimization methods of cogeneration systems based on exergo-economic and exergo-environmental parameters [37,38]. The goal of this study is to develop an approach to maximize energy efficiency of an industrial zone through waste heat recovery and reuse, via indirect heat integration.…”

Section: Liew Et Al Developed An Extended Methodology Tsmentioning

confidence: 99%

Targeting heat recovery and reuse in industrial zone

Zaric¹,

Stijepović²,

Linke

et al. 2017

CI&CEQ

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Section: Liew Et Al Developed An Extended Methodology Tsmentioning

confidence: 99%

Targeting heat recovery and reuse in industrial zone

Zaric¹,

Stijepović²,

Linke

et al. 2017

CI&CEQ

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“…Due to the exclusive conceptual characteristics of the exergy analysis, such methodology has been largely applied to analyze and optimize several energy systems such as thermoelectrical plants [7], vapor compression refrigeration systems [23], distillation columns [30], multicrystalline solar photovoltaic systems [18], supercritical thermoelectric coal plants assisted by solar concentrator [23], active solar distillation systems integrated with solar ponds [22], cogeneration with LNG [11] and desalination plants [9].…”

Section: Introductionmentioning

confidence: 99%

Exergy efficiency of thermochemical syngas-to-ethanol production plants

Silva

Miranda

2021

SN Appl. Sci.

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This work presents exergy analyses applied in four different conceptual second-generation ethanol production processes through a thermochemical route using catalysts based on Molybdenum (P-1), Copper (P-2), and Rhodium (P-3 and P-4), aiming to assess their exergetic efficiencies. The results show that the conceptual processes have satisfactory exergy efficiencies in both cases, when compared among themselves and when compared with other processes reported in literature. The processes’ efficiency for P-1, P-2, P-3 and P-4 were, respectively, 52.4%, 41.4%, 43.7% and 48.9%. The reactors were the sections in which exergy destruction was more significant, due to the exothermic reactions and mixing points (where streams with different temperatures were mixed). Such results show the potential of thermochemical ethanol production, besides opening the possibilities of process improvement. Graphic abstract

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