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Issue Info: 
  • Year: 

    2024
  • Volume: 

    14
  • Issue: 

    3
  • Pages: 

    96-109
Measures: 
  • Citations: 

    0
  • Views: 

    3
  • Downloads: 

    0
Abstract: 

In this study, weather conditions such as air humidity, temperature air, and wind speed were investigated in relation to wind turbine efficiency with the approach of an Exergy study. In this study, the wind speed has been investigated in two different climatic regions of Iran with an approximate distance of 1200 km, in the names of Ardabil and Marvast. The amount of wind density of Ardabil is equal to 66 (kW/m2) and Marvast is equal to 123 (kW/m2). Power production using a 10 (Kw) wind turbine in the Ardabil region is 2.3 (MWh) and in the Marvast region is 3.2 (MWh) per year. The highest wind turbine Exergy efficiency is 0.48 in the Ardabil region, and the highest Exergy efficiency in the Marvast region is 0.18. The amount of reduction of CO2 gas production, using wind turbines in comparison to gas and diesel power plants in Ardabil, are 1.1 and 2.1 tons and in Marvast are 1.5 and 2.9 tons per year. This reduction in CO2 greenhouse gas per year is equal to using a forest region of 1000 (m2) to 3000 (m2). The use of wind turbines reduces the fuel consumption of diesel power plants in the Ardabil region for the amount of 797.4 liters and in the Marvast region for the amount of 1244 liters of diesel per year. According to this review, it can be concluded that in addition to wind speed, air humidity plays a significant role in the selection, installation, and commissioning of wind turbines in the region. According to this survey, it can be seen that in the Ardabil region, the wind speed of the wind turbine has a higher Exergy efficiency than in the Marvast region, and it can be concluded that the wind turbine has performed better in the Ardabil region.

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Issue Info: 
  • Year: 

    2018
  • Volume: 

    6
  • Issue: 

    2
  • Pages: 

    131-141
Measures: 
  • Citations: 

    0
  • Views: 

    155
  • Downloads: 

    52
Abstract: 

In this case study, Exergy analysis is applied to a mini two-shaft gas turbine which is located in Islamic Azad University Khomeini Shahr Branch`s Thermodynamics laboratory and a proposal presented to make Exergy destruction less using a Heat Recovery Water Heater (HRWH). Calculations were done for N2=20000 (rpm) constant and various N1 and after that for N1=60000 (rpm) constant and various N2. Results revealed that the highest Exergy destruction rate occurs in combustion chamber in all conditions and a huge part of Exergy destruction through the turbine exhaust. Increase in N1 leads to increases in all component Exergy destruction rates. On the other hand, power turbine is the only component which is affected by changes in N2 and the Exergy destruction rate increases with increase in N2. Moreover, Exergy gained rate within HRWH increased with increase in N1 and is almost constant with changes in N2. In the same vein, exergetic efficiency of HRWH and Exergy gained rate within HRWH are increased with decrease in water outlet temperature of HRWH.

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Issue Info: 
  • Year: 

    2014
  • Volume: 

    8
Measures: 
  • Views: 

    160
  • Downloads: 

    65
Abstract: 

IN THIS PAPER, THE Exergy ANALYSIS IN PNEUMATIC DRYING PROCESS, AIMS TO INCREASE Exergy EFFICIENCY BY IDENTIFYING BOTTLENECKS IN THE DRIER SYSTEM. Exergy ANALYSIS IS PERFORMED BY MODELING OF THE MASS, ENERGY, MOMENTUM AND Exergy BALANCE AROUND THE SYSTEM. MODEL IS SOLVED BY FORWARD DIFFERENCE METHOD FOR NUMERICAL CALCULATION. THE EFFECTS OF INLET TEMPERATURE, MASS FLOW RATE AND THE AMOUNT OF MOISTURE IN THE DRYING AIR ARE INVESTIGATED ON THE THERMODYNAMIC EFFICIENCY OF Exergy. THE RESULTS SHOW THAT IN THE DRYER WITH THE AIR MASS AMOUNT OF 1 KG/S AT 550 °K AND THE DRYING MATERIAL OF MASS FLOW RATE EQUIVALENT TO 0.6 KG/S, THE INPUT Exergy IS EQUAL TO 93.43 KJ/S AND THE EXERGETIC AVERAGE EFFICIENCY AND MAXIMUM AMOUNT OF Exergy DESTRUCTION ARE 32.7% AND 62.87 KJ/S, RESPECTIVELY.

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Issue Info: 
  • Year: 

    0
  • Volume: 

    20
  • Issue: 

    5
  • Pages: 

    110-119
Measures: 
  • Citations: 

    0
  • Views: 

    428
  • Downloads: 

    0
Abstract: 

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Author(s): 

PALAZZO PIERFRANCESCO

Issue Info: 
  • Year: 

    2011
  • Volume: 

    2
  • Issue: 

    4
  • Pages: 

    57-70
Measures: 
  • Citations: 

    0
  • Views: 

    291
  • Downloads: 

    127
Abstract: 

The mechanical aspect of entropy-Exergy relationship, together with the thermal aspect usually considered, leads to an extended formulation of physical Exergy based on both maximum useful work and maximum useful heat that are the outcome of available energy of a thermodynamic system.This approach suggests that a mechanical entropy can be studied, in addition to the already used thermal entropy, with respect to work interaction due to volume variation. The mechanical entropy is related to energy transfer by means of work and it is complementary to the thermal entropy that accounts energy transfer by means of heat. Furthermore, the paper proposes a definition of Exergy based on Carnot cycle that is reconsidered in the case the inverse cycle is adopted and, as a consequence, the concept that work depends on pressure similarly as heat depends on temperature, is pointed out. Then, the logical sequence to get mechanical Exergy expression to evaluate work withdrawn from available energy is demonstrated. On the basis of the mechanical Exergy, the mechanical entropy set forth is deduced in a general form valid for any process.Finally, the extended formulation of physical Exergy is proposed, that summarizes the contribution of either heat and work interactions and related thermal Exergy as well as mechanical Exergy that both result as the outcome from the available energy of the system interacting with an external reference environment (reservoir). The extended formulation contains an additional term that takes into account the volume, and consequently the pressure, that allows to evaluate Exergy with respect to the reservoir characterized by constant pressure other than constant temperature. The conclusion is that the extended physical Exergy takes into account the equality of pressure, other than equality of temperature, as a further condition of mutual stable equilibrium state between system and reservoir.

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Author(s): 

KAHROBAEIAN A.

Journal: 

Issue Info: 
  • Year: 

    2008
  • Volume: 

    42
  • Issue: 

    1 (111)
  • Pages: 

    131-144
Measures: 
  • Citations: 

    0
  • Views: 

    1832
  • Downloads: 

    272
Abstract: 

A new method of optimization on linear parabolic solar collectors using Exergy analysis is presented. A comprehensive mathematical modeling of thermal and optical performance is simulated and geometrical and thermodynamic parameters were assumed as optimization variables. By applying a derived expression for Exergy efficiency, Exergy losses were generated and the optimum design and operating conditions were investigated. The objective function (Exergy efficiency) along with constraint equations constitutes a four-degree freedom optimization problem. Using Lagrange multipliers method, the optimization procedure was applied to a typical collector and the optimum design point was extracted. The optimum values of collector inlet temperature, oil mass flow rate, concentration ratio and glass envelope diameter are calculated simultaneously by numerical solution of a highly non-linear equations system. To study the effect of changes in optimization variables on the collected Exergy, the sensitivity of optimization to changes in collector parameters and operating conditions is evaluated and variation of Exergy fractions at this point are studied.

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Author(s): 

FEYZI VAFA | BEHESHTI MASOUD

Journal: 

GAS PROCESSING

Issue Info: 
  • Year: 

    2015
  • Volume: 

    3
  • Issue: 

    1
  • Pages: 

    51-66
Measures: 
  • Citations: 

    0
  • Views: 

    246
  • Downloads: 

    111
Abstract: 

Exergy analysis and response surface methodology (RSM) is applied to reduce the Exergy loss and improve energy and Exergy efficiency of acetic acid production plant. Exergy analysis is run as a thermodynamic tool to assess Exergy loss in reactor and towers of acetic acid production process. The process is simulated in Aspen Plus (v.8.4) simulator and the necessary thermodynamics data for calculating Exergy of the streams is extracted from the simulation. By applying Exergy balance on each one of the equipment, Exergy losses are calculated. Response Surface Methodology (RSM) is a well-known statistical optimization method adopted in optimizing and modeling chemical processes, and operational parameters in reactor and towers. In this optimization framework the objective is to minimize Exergy loss as objective function, subject to engineering and operational constraints. One of the modifications made on the reaction section is consumption of hot effluent stream from the reactor to produce steam. This modification prevents wasting the generated heat in the reactor and leads to improving Exergy efficiency in reactor. All tunable operation parameters regarding reactor and towers and their upper and lower limits are specified and optimized through the RSM method. As a result, by optimization, Exergy loss is reduced by 11365.8 Mj/hr and 2496.1Mj/hr in reactor and towers, respectively.

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Issue Info: 
  • Year: 

    621
  • Volume: 

    10
  • Issue: 

    2
  • Pages: 

    254-267
Measures: 
  • Citations: 

    0
  • Views: 

    16
  • Downloads: 

    10
Abstract: 

In this research, using Harris Hawks optimization method, the gasket- plate heat exchangers is studied with an Exergy- economic approach. Six parameters of hot fluid inlet temperature, cold fluid inlet temperature, hot fluid mass flow rate, cold fluid mass flow rate, port diameter and the number of plates were selected as design variables. The ratio of hot fluid mass flow rate to cold fluid mass flow rate, λ, is introduced to the analysis of Exergy loss. The results showed that using Harris Hawks optimization method, Exergy loss and total cost can be reduced by 70% and 81%, respectively. The optimization results showed that minimizing the Exergy loss, the efficiency of the gasket- plate heat exchanger increases by 30%. It is also found that for λ>1, with the increase of cold fluid mass flow rate, the Exergy loss number decreases and for λ<1, with the increase of cold fluid mass flow rate, the Exergy loss number increases.

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Journal: 

GAS PROCESSING

Issue Info: 
  • Year: 

    2015
  • Volume: 

    3
  • Issue: 

    1
  • Pages: 

    11-18
Measures: 
  • Citations: 

    0
  • Views: 

    297
  • Downloads: 

    99
Abstract: 

The Exergy analysis is a proper method for performance evaluation of industrial systems. A generic and detailed analysis of the GPCSs on the second gas pipeline of Iran is made by the means of Exergy. The two main improvement measures of fuel pre-heating and steam injection technologies are presented for the current conventional stations. Steady state equations regarding the second law of thermodynamics and the chemical and physical Exergy analysis are presented as well. The results indicate that the improved cycle is a more energy saving one, with an overall efficiency and net output power. The exegetic efficiency of every gas turbine of the improved station is increased by 31% in average and their Exergy destruction is decreased by 84%. The amount of total Exergy saving for the case study would be 552 MW. A higher overall efficiency can be achieved by an increase in both the turbine inlet temperature (TIT) and steam mass flow (SMF).

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Issue Info: 
  • Year: 

    2006
  • Volume: 

    -
  • Issue: 

    -
  • Pages: 

    5-10
Measures: 
  • Citations: 

    1
  • Views: 

    145
  • Downloads: 

    0
Keywords: 
Abstract: 

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