پیوندهای مفید
اخبار و اعلانات
آمار
| تعداد نشریات | 162 |
| تعداد شماره‌ها | 6,623 |
| تعداد مقالات | 71,546 |
| تعداد مشاهده مقاله | 126,903,188 |
| تعداد دریافت فایل اصل مقاله | 99,953,092 |
تحلیل انرژی، اگزرژی و اقتصادی سیستم تولید چند‌گانۀ نوین مبتنی بر منبع زمین‌گرمایی برای تولید توان، حرارت، سرمایش و هیدروژن مایع به روش آبشاری | ||
| فصلنامه سیستم های انرژی پایدار | ||
| دوره 4، شماره 1، دی 1403، صفحه 83-105 اصل مقاله (1.27 M) | ||
| نوع مقاله: مقاله پژوهشی | ||
| شناسه دیجیتال (DOI): 10.22059/ses.2025.386772.1108 | ||
| نویسندگان | ||
| علی عیوضی* 1؛ مهران عامری2؛ محمد شفیعی دهج3؛ هادی غائبی4 | ||
| 1دانشجوی دکتری، گروه مهندسی مکانیک، دانشکدۀ فنی و مهندسی، دانشگاه ولی عصر(عج) رفسنجان، رفسنجان، ایران | ||
| 2استاد، گروه مهندسی مکانیک، دانشکدۀ فنی و مهندسی، دانشگاه شهید باهنر کرمان، کرمان، ایران | ||
| 3دانشیار، گروه مهندسی مکانیک، دانشکدۀ فنی و مهندسی، دانشگاه ولی عصر(عج) رفسنجان، رفسنجان، ایران | ||
| 4استاد، گروه مهندسی مکانیک، دانشکدۀ فنی و مهندسی، دانشگاه محقق اردبیلی، اردبیل، ایران | ||
| چکیده | ||
| در مطالعۀ حاضر سیستم جدید تولید چندگانه با استفاده از منبع زمین‌گرمایی به عنوان منبع تأمین انرژی برای تولید الکتریسیته، حرارت، سرما و هیدروژن مایع توسعه داده شده است. سیستم پیشنهادی متشکل از چرخۀ رانکین آلی ترکیب‌شده با مبدل حرارتی داخلی و گرم‌کن آب تغذیه، چرخۀ سرمایش جذبی دو اثره، واحد الکترولایزر غشای تبادل پروتون، منبع زمین‌گرمایی فلش دوگانه و چرخۀ نوین آبشاری مایع‌سازی است. در این مطالعه روش جدید مایع‌سازی آبشاری با دو دمای متغیر به کار گرفته شده است که به صورت مستقل نیتروژن مایع تولید می‌کند و هم‌زمان نیتروژن مایع تولید‌شده در مبدل حرارتی با هیدروژن غوطه‌ور می‌شود. تحلیل ترمودینامیکی و اقتصادی کاملی روی سیستم مورد مطالعه صورت گرفته است. به‌علاوه، مطالعۀ پارامتریک برای ارزیابی تأثیر تغییرات پارامتر‌های کلیدی روی کارایی سیستم در شرایط کاری مختلف انجام شده است. آرایش جدید توسعه‌داده‌شده در مطالعۀ حاضر هماهنگی مناسبی با همدیگر دارد و نتایج نشان می‌دهد عملکرد ترمودینامیکی مطلوبی را از سیستم پیشنهادی شاهد هستیم به صورتی که بازده انرژی 43 درصد و بازده اگزرژی 56 درصد حاصل می‌شود. برای رشد کارایی اقتصادی سیستم پیشنهادی توابع هزینۀ اجزای سیستم به همراه متغیر‌های اقتصادی مورد تجزیه‌وتحلیل قرار می‌گیرند و هزینۀ کل سیستم 37/0 دلار بر گیگاژول محاسبه می‌شود. چرخۀ نوین مایع‌سازی مدل‌سازی‌شده در این مطالعه دارای ضریب عملکرد 36 درصد بوده و بازده اگزرژی این واحد 39 درصد محاسبه می‌شود. | ||
| کلیدواژه‌ها | ||
| سیستم تولید چندگانه؛ چرخه مایع سازی آبشاری؛ انرژی زمین گرمایی؛ تحلیل اقتصادی | ||
| عنوان مقاله [English] | ||
| Energy, Exergy and Economic Analysis of a New Geothermal Resource-Based Multigeneration System For Power, Heat, Cooling and Liquid Hydrogen Production by Cascade Method | ||
| نویسندگان [English] | ||
| Ali Eyvazi1؛ Mehran Ameri2؛ Mohammad Shafiey Dehaj3؛ Hadi Ghaebi4 | ||
| 1Department of Mechanical Engineering, Faculty of Engineering, Vali-e-Asr University of Rafsanjan, Rafsanjan, Iran | ||
| 2Department of Mechanical Engineering, Faculty of Engineering, Shahid bahonar University of Kerman, Kerman, Iran | ||
| 3Department of Mechanical Engineering, Faculty of Engineering, Vali-e-Asr University of Rafsanjan, Rafsanjan, Iran | ||
| 4Department of Mechanical Engineering, Faculty of Engineering, University of Mohaghegh Ardabili, Ardabi, Iran | ||
| چکیده [English] | ||
| In the present study, a new multi-generation system using geothermal energy as an energy source for the production of electricity, heat, cold and liquid hydrogen has been developed. The proposed system consists of an organic Rankine cycle combined with an internal heat exchanger and feed water heater, a double-effect absorption refrigeration cycle, a proton exchange membrane electrolyzer unit, a dual flash geothermal source and a novel cascade liquefaction cycle. In this study, a new cascade liquefaction method with two variable temperatures has been used, which independently produces liquid nitrogen and simultaneously the produced liquid nitrogen is immersed in a heat exchanger with hydrogen. A complete thermodynamic and economic analysis has been carried out on the studied system. In addition, a parametric study has been carried out to evaluate the effect of changes in key parameters on the efficiency of the system under different operating conditions. The new arrangement developed in the present study has a good coordination with each other and the results show that we witness a desirable thermodynamic performance from the proposed system, such that an energy efficiency of 43% and an exergy efficiency of 56% are achieved. To increase the economic efficiency of the proposed system, the cost functions of the system components are analyzed along with economic variables and the total system cost is calculated to be $0.37/GJ. The new liquefaction cycle modeled in this study has a performance factor of 36% and the exergy efficiency of this unit is calculated to be 39%. | ||
| کلیدواژه‌ها [English] | ||
| Multigeneration system, cascade liquefaction cycle, geothermal energy, economic analysis | ||
| مراجع | ||
|
[1] Ifaei P, Nazari-Heris M, Charmchi AS, Asadi S, Yoo C. Sustainable energies and machine learning: An organized review of recent applications and challenges. Energy. 2023 Mar 1;266:126432.
[2] Shinde TU, Dalvi VH, Patil RG, Mathpati CS, Panse SV, Joshi JB. Thermal performance analysis of novel receiver for parabolic trough solar collector. Energy. 2022 Sep 1;254:124343.
[3] Dan M, He A, Ren Q, Li W, Huang K, Wang X, Feng B, Sardari F. Multi-aspect evaluation of a novel double-flash geothermally-powered integrated multigeneration system for generating power, cooling, and liquefied Hydrogen. Energy. 2024 Feb 15;289:129900.
[4] Guzović Z, Duić N, Piacentino A, Markovska N, Mathiesen BV, Lund H. Paving the way for the Paris Agreement: Contributions of SDEWES science. Energy. 2023 Jan 15;263:125617.
[5] Li P, Lin H, Li J, Cao Q, Wang Y, Pei G, Jie D, Zhao Z. Analysis of a direct vapor generation system using cascade steam-organic Rankine cycle and two-tank oil storage. Energy. 2022 Oct 15;257:124776.
[6] Chen C, Witte F, Tuschy I, Kolditz O, Shao H. Parametric optimization and comparative study of an organic Rankine cycle power plant for two-phase geothermal sources. Energy. 2022 Aug 1;252:123910.
[7] Karayel GK, Javani N, Dincer I. Effective use of geothermal energy for hydrogen production: a comprehensive application. Energy. 2022 Jun 15;249:123597.
[8] Arslan O, Arslan AE. Multi-criteria optimization of a new geothermal driven integrated power and hydrogen production system via a new Index: Economic sustainability (EcoSI). Fuel. 2024 Feb 15;358:130160.
[9] Naquash A, Qyyum MA, Islam M, Sial NR, Min S, Lee S, Lee M. Performance enhancement of hydrogen liquefaction process via absorption refrigeration and organic Rankine cycle-assisted liquid air energy system. Energy Conversion and Management. 2022 Feb 15;254:115200.
[10] Riaz A, Qyyum MA, Min S, Lee S, Lee M. Performance improvement potential of harnessing LNG regasification for hydrogen liquefaction process: Energy and exergy perspectives. Applied Energy. 2021 Nov 1;301:117471.
[11] Nabat MH, Zeynalian M, Razmi AR, Arabkoohsar A, Soltani M. Energy, exergy, and economic analyses of an innovative energy storage system; liquid air energy storage (LAES) combined with high-temperature thermal energy storage (HTES). Energy Conversion and Management. 2020 Dec 15;226:113486.
[12] Manesh MH, Ghorbani B. Energy and exergy analyses of an innovative energy storage configuration using liquid air integrated with Linde-Hampson liquefaction system, molten carbonate fuel cell, and organic Rankine cycle. Journal of Energy Storage. 2022 Mar 1;47:103676.
[13] Koc M, Yuksel YE, Ozturk M. Thermodynamic assessment of a novel multigenerational power system for liquid hydrogen production. International Journal of Hydrogen Energy. 2022 Aug 29;47(74):31806-20.
[14] Bi Y, Yin L, He T, Ju Y. Optimization and analysis of a novel hydrogen liquefaction process for circulating hydrogen refrigeration. international journal of hydrogen energy. 2022 Jan 1;47(1):348-64.
[15] Ding GC, Peng JI, Mei-Yun GE. Technical assessment of Multi-generation energy system driven by integrated renewable energy Sources: Energetic, exergetic and optimization approaches. Fuel. 2023 Jan 1;331:125689.
[16] Shakibi H, Faal MY, Assareh E, Agarwal N, Yari M, Latifi SA, Ghodrat M, Lee M. Design and multi-objective optimization of a multi-generation system based on PEM electrolyzer, RO unit, absorption cooling system, and ORC utilizing machine learning approaches; a case study of Australia. Energy. 2023 Sep 1;278:127796.
[17] Sun J, Yan G, Abed AM, Sharma A, Gangadevi R, Eldin SM, Taghavi M. Evaluation and optimization of a new energy cycle based on geothermal wells, liquefied natural gas and solar thermal energy. Process Safety and Environmental Protection. 2022 Dec 1;168:544-57.
[18] Zhang S, Liu G. Design and performance analysis of a hydrogen liquefaction process. Clean Technologies and Environmental Policy. 2022 Jan 1:1-5.
[19] Faramarzi S, Nainiyan SM, Mafi M, Ghasemiasl R. A novel hydrogen liquefaction process based on LNG cold energy and mixed refrigerant cycle. International Journal of Refrigeration. 2021 Nov 1;131:263-74.
[20] Ebrahimi A, Saharkhiz MH, Ghorbani B. Thermodynamic investigation of a novel hydrogen liquefaction process using thermo-electrochemical water splitting cycle and solar collectors. Energy Conversion and Management. 2021 Aug 15;242:114318.
[21] Liu X, Hu G, Zeng Z. Performance characterization and multi-objective optimization of integrating a biomass-fueled brayton cycle, a kalina cycle, and an organic rankine cycle with a claude hydrogen liquefaction cycle. Energy. 2023 Jan 15;263:125535.
[22] Valero A. The thermodynamic process of cost formation. Exergy, energy system analysis and optimization. 2009 May 13;2:35.
[23] Yilmaz C, Kanoglu M, Abusoglu A. Exergetic cost evaluation of hydrogen production powered by combined flash-binary geothermal power plant. International journal of hydrogen energy. 2015 Oct 26;40(40):14021-30.
[24] Boyaghchi FA, Chavoshi M, Sabeti V. Multi-generation system incorporated with PEM electrolyzer and dual ORC based on biomass gasification waste heat recovery: Exergetic, economic and environmental impact optimizations. Energy. 2018 Feb 15;145:38-51.
[25] Kianfard H, Khalilarya S, Jafarmadar S. Exergy and exergoeconomic evaluation of hydrogen and distilled water production via combination of PEM electrolyzer, RO desalination unit and geothermal driven dual fluid ORC. Energy conversion and management. 2018 Dec 1;177:339-49.
[26] Turton R, Bailie RC, Whiting WB, Shaeiwitz JA, Bhattacharyya D. Analysis, Synthesis and Design of Chemical Processes: Analy Synth Desig Chemi Pr_4. Prentice Hall; 2012 Jun 22.
[27] Valero, A., & Torres, C. Relative free energy function and structural 846 theory of thermoeconomics. In Proceedings (Vol. 58, No. 1, p. 28). MDPI. 2020, September.
[28] Razmi AR, Janbaz M. Exergoeconomic assessment with reliability consideration of a green cogeneration system based on compressed air energy storage (CAES). Energy Conversion and Management. 2020 Jan 15;204:112320.
[29] Sayyaadi H. Multi-objective approach in thermoenvironomic optimization of a benchmark cogeneration system. Applied Energy. 2009 Jun 1;86(6):867-79.
[30] Wang L, Bu X, Wang H, Ma Z, Ma W, Li H. Thermoeconomic evaluation and optimization of LiBr-H2O double absorption heat transformer driven by flat plate collector. Energy Conversion and Management. 2018 Apr 15;162:66-76.
[31] Taghavi M, Salarian H, Ghorbani B. Economic evaluation of a hybrid hydrogen liquefaction system utilizing liquid air cold recovery and renewable energies. Renewable Energy Research and Applications. 2023 Jan 1;4(1):125-43.
[32] Akrami E, Chitsaz A, Nami H, Mahmoudi SMS. Energetic and exergoeconomic assessment of a multi-generation energy system based on indirect use of geothermal energy. Energy 2017;124:625–39.
[33] Shah ZA, Zheng Q, Mehdi G, Ahmad N, Waleed R, Rehman AU, Raza A. The Theoretical Framework of the Modified Organic Rankine Cycles for Improved Energy and Exergy Performances. Int Energy J. 2020 May 25;20:169-80. | ||
|
آمار تعداد مشاهده مقاله: 62 تعداد دریافت فایل اصل مقاله: 39 |
||
سامانه مدیریت نشریات علمی. قدرت گرفته از سیناوب