Thermo-economic-environmental analysis of a sustainable heat integration design for biomass-fueled power plant using integration of CCHP and sweater desalination application

被引:10
作者
Nutakki, Tirumala Uday Kumar [1 ]
Agrawal, Manoj Kumar [2 ]
Chauhdary, Sohaib Tahir [3 ]
Ahmad, Sayed Fayaz [4 ]
Ayadi, Mohamed [5 ]
Hedi, Elmonser [5 ]
Muhammad, Taseer [6 ]
Xiao, Fuxin [7 ]
机构
[1] American Univ Ras Al Khaimah, RAK Res & Innovat Ctr, Ras Al Khaymah, U Arab Emirates
[2] GLA Univ, Dept Mech Engn, Mathura 281406, Uttar Pradesh, India
[3] Dhofar Univ, Coll Engn, Dept Elect & Comp Engn, Salalah 211, Oman
[4] Inst Business Management, Dept Engn Management, Karachi, Pakistan
[5] Majmaah Univ, Coll Sci, Dept Math, Majmaah 11952, Saudi Arabia
[6] King Khalid Univ, Coll Sci, Dept Math, Abha 61413, Saudi Arabia
[7] Ton Duc Thang Univ, Sustainable Management Nat Resources, Ho Chi Minh City, Vietnam
关键词
Biomass fuel; Sustainable heat integration; Combined cooling heating and power; Multi-effect desalination; Environmental analysis; Economic analysis; MULTIGENERATION ENERGY SYSTEM; THERMOECONOMIC ANALYSIS; PERFORMANCE ANALYSIS; EXERGY ANALYSES; OPTIMIZATION; ABSORPTION; CYCLE; ASSESSMENTS; HYDROGEN; DRIVEN;
D O I
10.1016/j.desal.2024.117404
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The sustainable heat integration method proves to be a highly effective approach in reducing energy consumption and addressing greenhouse gas emissions while optimizing overall system performance. This study introduces a novel integrated system that combines cooling, heating, power generation, and desalination and is specifically designed for a biomass -based gas turbine cycle. This system consists of a biomass combustion unit, a gas turbine cycle, an organic Rankine cycle, an absorption chiller, and a multi -effect desalination unit. This model, which is proposed for the first time and embraces an innovative thermal matching process, is simulated by the Aspen HYSYS software. Subsequently, a comprehensive evaluation employing a thorough multi -criteria analysis is conducted, examining the process from multiple perspectives, including energy, exergy, environment, and economics under different operational scenarios. The results indicate that the overall procedure can produce power output of 20,150 kW, chilled water at a rate of 188 kg/s, hot water at a rate of 27.87 kg/s, steam at a rate of 4.28 kg/s, and fresh water at a rate of 0.07 kg/s. From a thermodynamic perspective, considering the entire system, the current process yielded energy and exergy efficiencies of 54.26 % and 29.14 %, respectively. In addition, the environmental assessment exhibits that the determined carbon dioxide emission for the developed system amounts to 0.6544 kgCO2/kWh. In the context of the entire operational mode, it is observed that the total unit exergy cost amounted to 10.28 $/GJ. This outcome illustrates a significant reduction of 33.46 % compared to the single -generation mode.
引用
收藏
页数:24
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