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Journal articles on the topic 'Advanced exergoenvironmental analysis'

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Author: Grafiati

Published: 10 December 2022

Last updated: 28 January 2023

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Tabatabaei, Meisam, and Mortaza Aghbashlo. "The critical role of advanced sustainability assessment tools in enhancing the real-world application of biofuels." Acta Innovations, no. 37 (December 1, 2020): 67–73. http://dx.doi.org/10.32933/actainnovations.37.6.

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Sustainability has become of paramount importance in the biofuel industry. Accordingly, various ‎sustainability assessment schemes such as emergy analysis, techno-economic analysis, life ‎cycle ‎assessment, energy accounting, and exergy analysis and its extensions (exergoeconomic, ‎exergoenvironmental, and ‎exergoeconoenvironmental analyses) are being employed increasingly for decision-‎making on biofuel production and consumption systems. In this opinion paper, after classifying ‎and describing biofuel generations, the developed sustainability assessment tools are critically ‎explained, and their pros and cons are discussed. Overall, among the various sustainability assessment approaches introduced so far, exergy-based methods appear to be ‎the most promising tools for developing ‎sustainable biofuel systems. This can be attributed to the fact that the exergy ‎concept is deeply ‎rooted in the well-defined principles of thermodynamics.‎

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Wang, Qingqiang, Jili Hou, Xing Wei, Nan Jin, Yue Ma, Shuyuan Li, and Yuchao Zhao. "Advanced exergoenvironmental analysis of the oil shale retorting process with SJ-type rectangular retort." Energy 260 (December 2022): 124929. http://dx.doi.org/10.1016/j.energy.2022.124929.

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Petrakopoulou, Fontina, George Tsatsaronis, and Tatiana Morosuk. "Advanced Exergoenvironmental Analysis of a Near-Zero Emission Power Plant with Chemical Looping Combustion." Environmental Science & Technology 46, no. 5 (February 22, 2012): 3001–7. http://dx.doi.org/10.1021/es203430b.

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Boyano, A., T. Morosuk, A. M. Blanco-Marigorta, and G. Tsatsaronis. "Conventional and advanced exergoenvironmental analysis of a steam methane reforming reactor for hydrogen production." Journal of Cleaner Production 20, no. 1 (January 2012): 152–60. http://dx.doi.org/10.1016/j.jclepro.2011.07.027.

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Mergenthaler, Pieter, Arndt-Peter Schinkel, and George Tsatsaronis. "Application of exergoeconomic, exergoenvironmental, and advanced exergy analyses to Carbon Black production." Energy 137 (October 2017): 898–907. http://dx.doi.org/10.1016/j.energy.2017.03.107.

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Khoshgoftar Manesh, Mohammad, Reza Ghadikolaei, Hossein Modabber, and Viviani Onishi. "Integration of a Combined Cycle Power Plant with MED-RO Desalination Based on Conventional and Advanced Exergy, Exergoeconomic, and Exergoenvironmental Analyses." Processes 9, no. 1 (December 29, 2020): 59. http://dx.doi.org/10.3390/pr9010059.

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The ever-increasing world population, change in lifestyle, and limited natural water and energy resources have made industrial seawater desalination plants the leading contenders for cost-efficient freshwater production. In this study, the integration of a combined cycle power plant (CCPP) with multi-effect distillation (MED) and reverse osmosis (RO) desalination units is investigated through comprehensive conventional and advanced exergy, exergoeconomic, and exergoenvironmental analyses. Firstly, the thermodynamic modelling of the CCPP is performed by using a mathematical programming procedure. Then, a mathematical model is developed for the integration of the existing CCPP plant with MED and RO desalination units. Finally, conventional and advanced exergy, exergoeconomic, and exergoenvironmental analyses are carried out to assess the main performance parameters of the integrated CCPP and MED-RO desalination system, as well as to identify potential technical, economic, and environmental improvements. A case study is presented based on the Shahid Salimi Neka power plant located at the north of Iran along the Caspian Sea. The mathematical modelling approach for the integrated CCPP and MED-RO desalination system is solved in MATLAB, and the results are validated via Thermoflex software. The results reveal an increase of 3.79% in fuel consumption after the integration of the CCPP with the desalination units. The exergy efficiency of the integrated system is 42.7%, and the highest cost of exergy destruction of the combustion chamber is 1.09 US$ per second. Economic and environmental analyses of the integrated system also show that gas turbines present the highest investment cost of 0.047 US$ per second. At the same time, MED exhibits the highest environmental impact rate of 0.025 points per second.

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Khoshgoftar Manesh, M. H., P. Navid, A. M. Blanco Marigorta, M. Amidpour, and M. H. Hamedi. "New procedure for optimal design and evaluation of cogeneration system based on advanced exergoeconomic and exergoenvironmental analyses." Energy 59 (September 2013): 314–33. http://dx.doi.org/10.1016/j.energy.2013.06.017.

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Oyekale, Joseph, and Eyere Emagbetere. "Comparative design-point and yearly advanced exergoenvironmental analyses of a solar-biomass organic Rankine cycle power plant." Energy Sources, Part A: Recovery, Utilization, and Environmental Effects 44, no. 4 (November 30, 2022): 10433–49. http://dx.doi.org/10.1080/15567036.2022.2150795.

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Jadidi, Esmaeil, Mohammad Hasan Khoshgoftar Manesh, Mostafa Delpisheh, and Viviani Caroline Onishi. "Advanced Exergy, Exergoeconomic, and Exergoenvironmental Analyses of Integrated Solar-Assisted Gasification Cycle for Producing Power and Steam from Heavy Refinery Fuels." Energies 14, no. 24 (December 13, 2021): 8409. http://dx.doi.org/10.3390/en14248409.

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Integrated solar-assisted gasification cycles (ISGC) have emerged as a more flexible and environmentally friendly solution for producing power, steam, and other high-valued by-products from low-cost opportunity fuels. In this light, this paper investigates a new ISGC system for converting heavy refineries fuels into power and steam utilities while enhancing energy efficiency and economic and environmental performance indicators. In this approach, a solar energy field and a two-pressure heat recovery steam generator were integrated into the ISGC system to improve overall economic and environmental plant viability. The ISGC system was modelled in MATLAB software, and the results were validated using Thermoflex software. Conventional and advanced energy, exergy, exergoeconomic, and exergoenvironmental (4E) analyses were implemented to assess the main performance parameters and identify potential system improvements. The ISGC system produced 319.92 MW of power by feeding on 15.5 kg/s of heavy refinery fuel, with a thermal efficiency of 50% and exergy efficiency of 54%. The results also revealed an investment cost of $466 million, evaluated at a system cost rate of 446 $/min and an environmental impact rate of 72,796 pts/min. The conventional and advanced 4E analyses unveiled the process economic and environmental feasibilities, particularly for oil-rich countries with high availability of solar resources.

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Nourpour, M., M. H. Khoshgoftar Manesh, A. Pirozfar, and M. Delpisheh. "Exergy, Exergoeconomic, Exergoenvironmental, Emergy-based Assessment and Advanced Exergy-based Analysis of an Integrated Solar Combined Cycle Power Plant." Energy & Environment, December 17, 2021, 0958305X2110635. http://dx.doi.org/10.1177/0958305x211063558.

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The high amount of solar energy as clean and sustainable energy has increased awareness in solar energy concentration, especially in integrated concepts. One of the best and promising hybrid configurations for converting solar energy into power is an integrated solar combined cycle system (ISCCS). In this study, conventional and advanced analysis tools for the ISCCS located in Yazd (Iran) have been investigated. In this paper, thermodynamic simulation, exergy, exergoeconomic, and exergoenvironmental analysis based on Life Cycle Assessment (LCA) have been performed. In addition, an emergy-based concept, including emergoeconomic and emergoenvironmental assessment, has been performed. In-depth analysis of exergy, exergoeconomic, and exergoenvironmental modelling, advanced exergy analysis based on endogenous/exogenous and avoidable/unavoidable parts have been done. In this regard, MATLAB code has been developed for thermodynamic simulation, exergy, exergoeconomic, exergoenvironment, emergoeconomic and emergoenvironment analysis. Furthermore, THERMOFLEX (commercial software) applied for thermodynamic simulation and verification. The Sankey diagram based on each analysis tool has been constructed. Furthermore, the priority of improvement based on each analysis has been identified. The thermal efficiency and net power generation of ISCCS are 48.25% and 419600 kW, respectively. It was obsereved that in most equipment, less than 10% of exergy destruction and cost and environmental impact rates were avoidable/endogenous.

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Petrakopoulou, Fontina, George Tsatsaronis, and Tatiana Morosuk. "Assessment of a Power Plant With CO2 Capture Using an Advanced Exergoenvironmental Analysis." Journal of Energy Resources Technology 136, no. 2 (November 26, 2013). http://dx.doi.org/10.1115/1.4025715.

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This paper presents an evaluation of the environmental performance of an advanced zero emission plant (AZEP) including CO2 capture. The evaluation is conducted with the aid of an advanced exergoenvironmental analysis. The results are compared with those of a reference combined-cycle power plant without CO2 capture. Advanced exergy-based methods are used to (a) quantify the potential for improving individual components or overall systems, and (b) reveal detailed interactions among components—two features not present in conventional analyses, but very useful, particularly when evaluating complex systems. In an advanced exergoenvironmental analysis, the environmental impacts calculated in a conventional exergoenvironmental analysis are split into avoidable/unavoidable (to evaluate the potential for component improvement) and endogenous/exogenous (to understand the interactions among components) parts. As in the reference plant, the potential for reducing the environmental impact of the AZEP has been found to be limited by the relatively low avoidable environmental impact associated with the thermodynamic inefficiencies of several of its components. However, although the environmental impacts for the majority of the components of the plant are related mainly to internal inefficiencies and component interactions are of secondary importance, there are strong interactions between the reactor and some other components.

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Esmaeilzadehazimi, Mohammadamin, Mohammad Hasan Khoshgoftar Manesh, M. Majidi, and Mohsen Nourpour. "Evaluation of a Novel Quadruple Combined Cycle with the Magnetohydrodynamic Generator based on 6E Analysis." Journal of Energy Resources Technology, December 26, 2020, 1–28. http://dx.doi.org/10.1115/1.4049461.

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Abstract The generation of the electric power through magnetohydrodynamic is one of the most advanced high -temperature energy conversions as it directly turns the heat into electricity. In this study, a quadruple cycle with magnetohydrodynamic generator was considered as the upstream cycle and a Brayton cycle was taken as the middle cycle through heating and an organic Rankine cycle and steam cycle were regarded as the downstream cycles using the heat loss of the magnetohydrodynamic generator and gas turbine, respectively. Energy, exergy, exergoeconomic, exergoenvironmental, emergoeconomic, and emergoenvironmental (6E) analyses were done in the proposed system simultaneously for the first time. In addition, advanced exergy, exergoeconomic, and exergoenvironmental analyses were performed for the proposed system to show the effect of irreversibility accurately and deeply. Despite the slight difference between the results of the emergoeconomic and emergoenvironmental sector with the exergoeconomic and exergoenvironmental sector, the obtained qualitative results were very similar showing that the emergoeconomic and emergoenvironmental analyses can be proper alternatives to the conventional exergoeconomic and exergoenvironmental analyses. The temperature of the heat source is one of the most important criteria for fluid selection in the organic Rankin cycles. Five organic fluids were selected and evaluated according to the desired hot source temperature for the Rankin organic cycle (262 °C). The results showed that the R141b with energy and efficiency of 15.25 and 58.05%, respectively had the best thermodynamic and exergy performance with the least amount of total costs using this fluid.

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Khoshgoftar Manesh, Mohammad Hasan, Mohammad Abdolmaleki, Hossein Vazini Modabber, and Marc A. Rosen. "Dynamic Advanced Exergetic, Exergoeconomic and Environmental Analyses of a Hybrid Solar City Gate Station." Journal of Energy Resources Technology, December 24, 2020, 1–19. http://dx.doi.org/10.1115/1.4049459.

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Abstract The use of solar energy to preheat natural gas before a city gate station (CGS) for reducing fuel consumption and environmental emissions is investigated in a real CGS. All analyses are conducted with a one-hour time step throughout the entire year so that seasonal climate changes are accounted for precisely. A thermodynamic analysis of the hybrid system is performed with TRNSYS and verified with THERMOFLEX to ensure reliability. In addition, dynamic exergetic, exergoeconomic, and exergoenvironmental evaluation for the integrated system are performed. A life cycle assessment based on Eco-indicator 99 is performed using SIMA PRO to compute the environmental impacts for each component of the system. The exergetic, exergoeconomic, and environmental analyses are performed in EES. To perform the transient exergetic, exergoeconomic, and environmental analyses, the results of the thermodynamic analysis from TRNSYS are automatically imported into the EES code. The advanced exergetic, exergoeconomic and exergoenvironmental evaluation are done to better determine components that have high potentials for improving the system; potentials are considered based on the exergy destruction, exergetic cost of destruction, and environmental impacts associated with exergy destruction.

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Khoshgoftar Manesh, Mohammad Hasan, and Esmaeil Jadidi. "Conventional and advanced exergy, exergoeconomic and exergoenvironmental analysis of a biomass integrated gasification combined cycle plant." Energy Sources, Part A: Recovery, Utilization, and Environmental Effects, April 21, 2020, 1–22. http://dx.doi.org/10.1080/15567036.2020.1752856.

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Miar Naeimi, Masoud, Mohammad Eftekhari Yazdi, and Gholam Reza Salehi. "Advanced Exergy, Exergoeconomic, Exergoenvironmental Evaluation of a Solar Hybrid Trigeneration System Based on Solar Gas Turbine for an Office Building." Journal of Energy Resources Technology 143, no. 2 (August 3, 2020). http://dx.doi.org/10.1115/1.4047756.

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Abstract In this article, optimal design and advanced exergetic, exergoeconomic, and exergoenvironmental analyses of a trigeneration system for an office building based on integration flat plate solar collector and gas turbine have been performed. The proposed system includes a heat recovery steam generator, a steam turbine, a solar plate collector, and an absorption chiller. The transient simulation for solar calculation has been done using transys software. In addition, a computer code was built to compute conventional and advanced exergy, exergoeconomic, and exergoenvironmental evaluation dynamically. Furthermore, multiobjective optimization by NSGA-II and cuckoo Search algorithm with maximum exergetic efficiency, minimum total exergetic cost, and minimum exergetic environmental impacts has been carried out simultaneously. The results demonstrate that the three objective parameters have been enhanced. Also, the endogenous, exogenous, available, and unavailable parts of exergy destruction have been determined.

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