首页> 外文会议>International Mechanical Engineering Congress and Exposition 2007 >SUPPLEMENTARY BACKWARD EQUATIONS FOR THE INDUSTRIAL FORMULATION IAPWS-IF97 OF WATER AND STEAM FOR FAST CALCULATIONS OF HEAT CYCLES, BOILERS, AND STEAM TURBINES
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SUPPLEMENTARY BACKWARD EQUATIONS FOR THE INDUSTRIAL FORMULATION IAPWS-IF97 OF WATER AND STEAM FOR FAST CALCULATIONS OF HEAT CYCLES, BOILERS, AND STEAM TURBINES

机译:水和蒸汽工业配方IAPWS-IF97的补充向后方程式,用于快速计算热循环,锅炉和蒸汽轮机

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In 1997, the International Association for the Properties of Water and Steam (IAPWS) adopted the "IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam" (IAPWS-IF97) [1,2]. The IAPWS-IF97 contains fundamental equations g(p,T) for liquid region 1, vapor region 2 and high-temperature region 5, a fundamental equation f(v,T) for the critical and supercritical regions (region 3) and an equation pair for saturation pressure p_(sat)(T) and for saturation temperature T_(sat)(p); see Fig. 1. Using the fundamental equations, all thermodynamic properties can be calculated from a given pressure and temperature in regions 1, 2, 5, or from a given specific volume and temperature in region 3. In addition, the IAPWS-IF97 contains "backward" equations for the most used implicit functions T(p,h) and T(p,s) in regions 1 and 2 for fast calculations in thermodynamic process modeling. Further dependencies must be calculated iteratively from the fundamental equations. Thus, one- and two-dimensional iterations are necessary for determining certain thermodynamic properties in process modeling. Over the past 6 years, IAPWS has established a task group and developed further backward equations for water and steam supplementing the IAPWS Industrial Formulation 1997. First, backward equations p(h,s) for the liquid and vapor regions were developed and adopted as a supplementary release by IAPWS in 2001 (IAPWS-IF97-S01) [3,4]; see Fig. 1. An international survey of the power industry revealed that backward equations in the critical and supercritical regions were also required in process modeling. Thus the backward equations T(p,h), v(p,h), T(p,s), and v(p,s) were developed for region 3 and adopted as a supplementary release in 2003 and revised in 2004 (IAPWS-IF97-S03rev) [5,6]. Backward equations p(h,s) developed for the critical and supercritical regions were then adopted by IAPWS in 2004 (IAPWS-IF97-S04) [7,8]. This supplementary release also contains a backward equation for the saturation temperature T_(sat)(h,s) in the part of the two-phase region important for steam-turbine calculations. Finally, backward equations v(p,T) for the critical and supercritical regions (region 3) were published in a supplementary release in 2005 (IAPWS-IF97-S05) [9,10]; see Fig.1. In order to determine whether a given state point is located in one of the single-phase regions or in the two-phase region, iterations are necessary for the backward functions of the given properties (p,h), (p,s) or (h,s). To avoid these iterations, special region-boundary equations were developed and adopted as a part of the supplementary releases IAPWS-IF97-03rev and IAPWS-IF97-S04. In conclusion, using the equations of IAPWS-IF97, the supplementary backward equations, and the region-boundary equations, all thermodynamic properties can be calculated without iteration from the input variables (p,T), (p,h), (p,s) and (h,s) in the entire range of validity of IAPWS-IF97, including determination of the region (except for the high-temperature region 5). The numerical consistencies of the backward and region-boundary equations are sufficient for most heat-cycle, boiler, and steam-turbine calculations. For users not satisfied with the
机译:1997年,国际水和蒸汽特性协会(IAPWS)通过了“ IAPWS 1997工业配方水和蒸汽的热力学特性”(IAPWS-IF97)[1,2]。 IAPWS-IF97包含液体区域1,蒸气区域2和高温区域5的基本方程g(p,T),临界和超临界区域(区域3)的基本方程f(v,T)以及方程饱和压力p_(sat)(T)和饱和温度T_(sat)(p)的一对;参见图1。使用基本方程式,可以根据区域1、2、5中的给定压力和温度,或者区域3中的给定比体积和温度,计算所有热力学性质。此外,IAPWS-IF97还包含对于热力学过程建模中的快速计算,区域1和2中最常用的隐式函数T(p,h)和T(p,s)的“向后”方程式。必须从基本方程式迭代计算出更多的依存关系。因此,一维和二维迭代对于确定过程建模中的某些热力学特性是必要的。在过去的6年中,IAPWS建立了一个任务组,并进一步补充了1997年IAPWS工业配方的水和蒸汽后向方程。首先,开发了液体和蒸汽区域的后向方程p(h,s)并将其用作IAPWS在2001年的补充发布(IAPWS-IF97-S01)[3,4];见图1。对电力行业的一项国际调查显示,在过程建模中还需要在临界和超临界区域中建立后向方程。因此,针对区域3开发了后向方程T(p,h),v(p,h),T(p,s)和v(p,s),并在2003年作为补充发布并于2004年进行了修订( IAPWS-IF97-S03rev)[5,6]。然后,IAPWS在2004年采用了针对临界和超临界区域的后向方程p(h,s)(IAPWS-IF97-S04)[7,8]。该补充版本还包含一个对汽轮机计算重要的两相区域部分中的饱和温度T_(sat)(h,s)的反向方程。最后,关键和超临界区域(3区)的后向方程v(p,T)在2005年的补充版本中发布(IAPWS-IF97-S05)[9,10];见图1。为了确定给定的状态点是位于单相区域之一中还是位于两相区域中,对于给定特性(p,h),(p,s)或(h,s)。为了避免这些迭代,开发了特殊的区域边界方程,并将其作为补充版本IAPWS-IF97-03rev和IAPWS-IF97-S04的一部分。总之,使用IAPWS-IF97方程,补充反向方程和区域边界方程,无需输入变量(p,T),(p,h),(p, s)和(h,s)在IAPWS-IF97的整个有效范围内,包括确定区域(高温区域5除外)。向后和区域边界方程的数值一致性足以满足大多数热循环,锅炉和蒸汽轮机的计算要求。对于不满意的用户

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