تعداد نشریات | 43 |

تعداد شمارهها | 1,658 |

تعداد مقالات | 13,565 |

تعداد مشاهده مقاله | 31,197,457 |

تعداد دریافت فایل اصل مقاله | 12,287,113 |

## Prediction of Thermodynamic Properties of Helium and Neon as Working Fluids in Cryogenic Processes using Fundamental Equations of States | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

Gas Processing Journal | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

مقاله 6، دوره 6، شماره 2، دی 2018، صفحه 75-84 اصل مقاله (1.03 M)
| |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

شناسه دیجیتال (DOI): 10.22108/gpj.2019.24025 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

نویسندگان | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

Mohammad Maboudi^{1}؛ Masoud Ziabasharhagh^{1}؛ Mostafa Mafi^{*} ^{2}
| |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

^{1}Faculty of Mechanical Engineering, K. N. Toosi University of Technology, Tehran, Iran | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

^{2}Department of Mechanical Engineering, Imam Khomeini International University, Qazvin, Iran | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

چکیده | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

Design and optimization of various thermodynamic processes that are used in chemical industries such as low- temperature refrigeration and cryogenic cycles, requires computer software to simulate the thermodynamic cycle and examine the effect of various parameters on the performance of the cycle. So the existence of an equation of state to predict thermodynamic properties of working fluids in a wide range of temperatures and pressures is essential. Despite the greater complexity than the other equations, the fundamental equations of state have higher accuracy in the calculation of the thermodynamic properties and the main advantage of them is that other thermodynamic properties can be obtained with high accuracy by differentiating them. In this study, the thermodynamic properties of Helium and Neon as working fluids in cryogenic processes including density, internal energy, enthalpy, entropy, isobaric specific heat capacity, and isochoric heat capacity, have been calculated based on fundamental equations of state using a developed computer code in MATLAB software. By comparing the results with the valid reference data, a range of temperature and pressure in which the fundamental equations of state can be used with high accuracy, have been presented. In this high accuracy region, the maximum error is related to the isobaric heat capacity that is 3.37 % and 1.1 % respectively for Helium and Neon. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

کلیدواژهها | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

Fundamental equations of state؛ Thermodynamic properties؛ Cryogenic process simulation؛ Neon؛ Helium | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

اصل مقاله | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

## 1. IntroductionUsing a suitable equation is an essential solution for predicting the thermodynamic properties of fluids in the design and simulation of thermodynamic processes. Although there are many thermodynamic tables and charts that provide detailed information on the thermodynamic properties of fluids, an accurate equation is necessary to correctly predict the thermodynamic properties of fluids in a wide range of temperature and pressure using to design and simulate the thermodynamic cycles. So far, many of equations of state were suggested such as primary simple equations with a few of parameters and modern equations that are complex but accurate. In the primary equation of state, the pressure is a function of other properties such as temperature and volume so these equations are named the pressure-explicit equation of state while new equations are explicated on Helmholtz energy. These equations that are known as the fundamental equations of state are more complex than pressure-explicit equations but have higher accuracy in the calculation of the thermodynamic properties in a wide range of temperature and pressure. The main advantage of these equations is that there is no need for integration for driving other thermodynamic properties. All required thermodynamic properties can be obtained with differentiating of Helmholtz energy with high accuracy. Due to the applicability of these equations in accurately predicting thermal-physical properties, extensive research is done on the development of these equations. Most of the works were done on this subject are about presenting a model based on Helmholtz energy or using previous models and calculating the thermodynamic properties of fluids and then comparing them with experimental data. Jacobsen et al. presented a thermodynamic property formulation for nitrogen from the freezing line to 2000 K at pressures to 1000 MPa. The given relation can be used for thermodynamic property calculation with uncertainty 0.1% for the pressure and density, 0.2% for thermal capacities and 2% for the values of speed of sound. The formulation is not recommended near the critical point (Jacobsen, Stewart, & Jahangiri, 1986). Dillon and Penoncello presented a formulation for the thermodynamic properties of ethanol (C This study aims to predict the thermodynamic properties of cryogenic refrigerants using fundamental equations of state and calculate the uncertainty in the wide range of temperature and pressure to evaluate the applicability of these equations in the prediction of thermodynamic properties of these refrigerants. Using a developed computer code based on fundamental equations of state, thermodynamic properties of Helium and Neon including density, internal energy, enthalpy, entropy, isobaric specific heat capacity, and isochoric heat capacity are calculated. By comparing the results of predictions with the valid reference data is (Jacobsen, Penoncello & Lemmon, 1997), the scope of this equation to predict the thermodynamic properties of Helium and Neon are offered. In earlier work, not only the prediction of the thermodynamic properties of cryogenic refrigerants such as Helium and Neon not considered, but also providing a diagram that easily presents the applicability of fundamental equation of state in different ranges of temperature and pressure has been neglected. In the following section, a brief description is provided of the types of equations of state. Then the fundamental equations and how to obtain thermodynamic properties have been obtained. Finally, the results of comparing the reference data and predicted thermodynamic properties using fundamental equations of state are presented.
## 2. Theory of fundamental equation of stateThe most common thermodynamic properties that are measured and used in the equations of state are pressure, temperature and specific volume (or its reverse, the density). Primary types of the equation of state make a correlation between the thermodynamic properties in which the pressure is expressed as a function of temperature and density (or specific volume). The general form of the pressure-explicit equation of state is (Jacobsen, Penoncello & Lemmon, 1997):
Virial equation of state (equation 2), cubic equations of state (equation 3) such as Van der Waals and Peng-Robinson and Lee-Kesler equations of state are the most common pressure explicit equations of state. The typical pressure explicit equation of state must be integrated for the calculation of enthalpy and entropy (Jacobsen, Penoncello & Lemmon, 1997).
In the secondary form of the equation of state, Helmholtz energy is used as a dependent variable (Jacobsen, Penoncello & Lemmon, 1997):
This form of the equation of state is named the - Pressure-explicit equations of state
- Fundamental equations of state
As mentioned, the fundamental form of the equation of state is implicit in the Helmholtz energy. This form of the equation has some advantages over other forms of the equation of state. An inherent advantage in fundamental equations of state is that all thermodynamic properties can be derived with relatively simple differentiation. Schmidt and Wagner developed a 32-term fundamental equation in 1985 (Jacobsen, Penoncello, & Lemmon, 1997). Although this form was developed for oxygen, it has been used by other investigators for correlating properties of other fluids. The equation is explicit in dimensionless Helmholtz energy. Jacobsen et al. developed a general form of the fundamental equation similar to that of Schmidt and Wagner which has been used for correlating thermodynamic properties of several cryogens. The functional form of this equation is (Jacobsen, Penoncello & Lemmon, 1997):
where , , and and are critical temperature and critical density respectively. The Helmholtz energy consists of two parts: the ideal gas contribution part ( ), and the residual part of the Helmholtz energy . The ideal gas portion is given by (Jacobsen, Penoncello & Lemmon, 1997):
where and are as defined below. Also, and are arbitrary values for enthalpy and entropy at standard temperature ( ) and pressure (
The residual part of the Helmholtz energy is given by (Jacobsen, Penoncello & Lemmon, 1997)
where for terms with ## 3. Prediction of thermodynamic properties using fundamental equation of stateAs mentioned, the fundamental equation of states allows computing other thermodynamic properties with differentiation of Helmholtz energy. Table 1 shows examples of functions for obtaining the thermodynamic properties from Helmholtz energy. These functions can be used easily in computer programs.
## 4. Prediction of thermodynamic properties of Helium and NeonTo calculate the thermodynamic properties of Helium and Neon, coefficients and parameters reported by Jacobsen et al. were used (Jacobsen, Penoncello, & Lemmon, 1997). Thermodynamic properties were calculated at pressures 0.1, 0.2, 0.5, 1, 2, 5, 10, 20, 50, and 100 MPa with temperature step of 10 °C at low temperatures and 100 °C at high temperatures from saturated point up to 1500 °C for Helium and 650 °C for Neon, using a developed computer code in MATLAB software. Since in the fundamental equations of state, Helmholtz energy has been explicit in terms of temperature and density, the equation should be solved numerically to obtain thermodynamic properties at a given temperature and pressure. Therefore, at a given temperature, the Newton-Raphson method was used to achieve the corresponding density to the desired pressure with an approximation of 0.000001 MPa.
## 5. Result and discussionUsing a developed computational code based on fundamental equation of state, thermodynamic properties of gases Helium and Neon were calculated as two cryogenic refrigerants. By comparison, these calculated properties with reference (Jacobsen, Penoncello & Lemmon, 1997), the applicability diagrams of the fundamental equation of state were provided for these two refrigerants. Also, forecast errors of thermodynamic properties inside the applicability region are presented. The thermodynamic properties were calculated for pressures up to 100 MPa and in the temperature range 10 to 1500 K and 30 to 650 K, respectively for Helium and Neon. A standard reverse-Brayton cryocooler cycle for long-length High-Temperature Superconducting cable systems is one of the most application of the range studied in this investigation (Hou, Zhao, Chen, & Xiong, 2006) and (Maboudi & Zia Bashrhagh, 2015).
As an example, Table 2 shows a part of the thermodynamic property table obtained for Helium using the fundamental equation of state. Figure 1 shows a comparison between the entropy of Helium gas calculated using the fundamental equations of state and reference data (Jacobsen, Penoncello & Lemmon, 1997) in various temperatures and pressures. As can be seen in this figure, the difference between the results obtained from the fundamental equations of state and the reference data is negligible, which indicates the capability of the fundamental equations of states in the calculation of the thermodynamic properties of gases. These comparisons were done about other thermodynamic properties of Helium and adaptation of results with reference data was investigated. In Figure 2, the applicability region of the fundamental equation of state for predicting the thermodynamic properties of Helium can be seen on the temperature-entropy graph for different pressures. Forecast errors of thermodynamic properties of Helium in high accuracy region are presented in Table 3.
Figure 3 shows the relative error percentage of the results on the boundary of the applicability area of the fundamental equation of states (the line between the green and brown areas in Figure 2) in predicting the thermodynamic properties of Helium. According to the graph, it is shown that relative error of density, unlike other thermodynamic properties, decreases with increasing pressure. The maximum error is related to the isobaric heat capacity and isochoric heat capacity which is 3.37% and 0.94% respectively. The relative error of other thermodynamic properties on the boundary between high and low accuracy areas does not exceed 0.6%. The relative error in the low accuracy area shown in Figure 2, is above 5%.
Table 4 shows a selection of thermodynamic properties of Neon that were calculated using the fundamental equation of state. Figure 4 compares the entropy of Neon gas calculated using the fundamental equations of state with entropy obtained from reference data(Jacobsen, Penoncello & Lemmon, 1997) in various temperatures and pressures. As can be seen in this figure, the difference between the results calculated using the fundamental equations of state and the reference data is negligible. These comparisons were done for other thermodynamic properties of Neon and adaptation of results with reference data was investigated.Figure 5 shows the areas with acceptable and high accuracy of the fundamental equations of state to predict the thermodynamic properties of Neon gas. The relative error of calculating the thermodynamic properties in the area with high accuracy can be seen in Table 5. For Neon in the acceptable accuracy area of the fundamental equations of state, the maximum error in the calculation of the thermodynamic properties was 5.42 %, which is related to the isobaric heat capacity. Figure 6 shows the relative error percentage of the results on the boundary of the applicability area of the fundamental equation of states (the line between the green and yellow areas shown in Figure 5) in predicting the thermodynamic properties of Neon. According to the graph, the relative error percentage of thermodynamic properties on the boundary between high and acceptable accuracy areas of the fundamental equation of states does not exceed 1% except density that its relative error percentage is little more than 1 %. The relative error of all thermodynamic properties in acceptable accuracy area in figure 5 is in the range of 1% to 5%, except isobaric heat capacity that its relative error percentage is little more than 5 %. The relative error in the low accuracy area, shown in Figure 5, is above 5%.
## 6. ConclusionUsing a developed computational code based on the fundamental equation of state, the thermodynamic properties of two refrigerants Helium and Neon were predicted. By comparison, the results with reference data (Jacobsen, Penoncello & Lemmon, 1997), the pressure and temperature area in which the fundamental equation of state can be applied with high accuracy, were presented. Due to error of computation the thermodynamic properties in these areas, the accuracy of equations to predict thermodynamic properties of the cryogenic refrigerants in a wide range of temperature and pressure were approved. Most of the equations are effective only for certain areas of temperature and pressure however the fundamental equations of state can meet this problem greatly. In the applicability area of the fundamental equations of state with high accuracy area, the average relative errors of predicting thermodynamic properties of Helium is about 0.54, 0.01, and 0.05 percent respectively for density, enthalpy, and entropy. These errors for Neon are about 0.24, 0.15, and 0.02 percent respectively for density, enthalpy, and entropy. Due to the small amount of error in the calculation of the thermodynamic properties, these equations can be used for computer simulation of thermodynamic cycles in the gaseous phase. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

مراجع | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

Bücker, D., & Wagner, W. (2006). A reference equation of state for the thermodynamic properties of ethane for temperatures from the melting line to 675 K and pressures up to 900 MPa. Dillon, H., & Penoncello, S. (2004). A fundamental equation for calculation of the thermodynamic properties of ethanol. Estela-Uribe, J. F. (2013a). An improved Helmholtz energy model for non-polar fluids and their mixtures. Part 1: Application to non-polar pure fluids. Estela-Uribe, J. F. (2013b). An improved Helmholtz energy model for non-polar fluids and their mixtures. Part 2: Application to mixtures of non-polar fluids. Estela-Uribe, J. F. (2013c). An improved Helmholtz energy model for non-polar fluids and their mixtures. Part 3: Application to natural gases and related systems. Estela-Uribe, J. F. (2014). Helmholtz energy and extended corresponding states model for the prediction of thermodynamic properties of refrigerants. Gernert, J., & Span, R. (2016). EOS–CG: A Helmholtz energy mixture model for humid gases and CCS mixtures. Grigoriev, B., Alexandrov, A. & Gerasimov, A. (2018). Application of multiparameter fundamental equations of state to predict the thermodynamic properties and phase equilibria of technological oil fractions. Hou, Y., Zhao, H. L., Chen, C. Z., & Xiong, L. Y. (2006). Developments in reverse Brayton cycle cryocooler in China. Jacobsen, R., Stewart, R., & Jahangiri, M. (1986). A thermodynamic property formulation for nitrogen from the freezing line to 2000 K at pressures to 1000 MPa. Jacobsen, R. T., Penoncello, S. G., & Lemmon, E. W. (1997). Kunz, O., & Wagner, W. (2012). The GERG-2008 wide-range equation of state for natural gases and other mixtures: an expansion of GERG-2004. Leachman, J. W., Jacobsen, R. T., Penoncello, S., & Lemmon, E. (2009). Fundamental equations of state for parahydrogen, normal hydrogen, and orthohydrogen. Maboudi, M., & Zia Bashrhagh, M. (2015). Applicability of fundamental equations of state in Simulation of Cryogenic Systems; Case Study: Reverse Brayton cryocooler for HTS cable. Thol, M., Dubberke, F., Rutkai, G., Windmann, T., Köster, A., Span, R., & Vrabec, J. (2015). Fundamental equation of state correlation for hexamethyldisiloxane based on experimental and molecular simulation data. Thol, M., Rutkai, G., Köster, A., Kortmann, M., Span, R., & Vrabec, J. (2015). Fundamental equation of state for ethylene oxide based on a hybrid dataset. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||

آمار تعداد مشاهده مقاله: 822 تعداد دریافت فایل اصل مقاله: 330 |