2.2多组分物系的泡点和露点计算.ppt
文本预览下载声明
2.2 多组分物系的泡点和露点计算 2.2.1 泡点温度和压力的计算 2.2.2 露点温度和压力的计算 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 2.2.1 泡点温度和压力的计算 规定液相组成 x 和压力p(或温度T),计算汽相组成 y 和温度T(或压力p)。 已知: x 、p 计算: y 、T 泡点温度计算 已知: x 、T 计算: y 、p 泡点压力计算 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 计算出发点: 单级汽液平衡系统,汽液相具有相同的温度T和压力p,组分的液相组成与汽相组成成平衡关系。 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 计算方程: (1)相平衡方程: C个 (2)摩尔分率加和方程: 2个 (3)汽液平衡常数关联式: C个 2C+2 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 方程总数: 2C+2个 变量数: 3C+2个 P) T K x (y i i i , , , , 已知变量数: C个 未知变量数: 2C+2个 唯一解 计算复杂程度取决于Ki。 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 一、泡点温度的计算 1.Ki与组成无关: 假定T 已知P 得到Ki ?Kixi f(T)=|?Kixi-1|? yes T,yi no 调整T 泡点方程: Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. (1)温度T初值的选定 取纯物质的沸点作为温度的迭代初值。 (2)Ki值的获得 1)p-T-K图(烃类物系) 2)简化表达式: P P K s i i / = 3)经验关系式 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. (3)温度T的调整 T设高了,降低T。 T设低了,提高T。 T的调整幅度可采用牛顿-拉普森法: 参见例[2-3],例[2-4] Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 2. Ki与组成有关: 由状态方程法或活度系数法求取Ki: Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 活度系数法计算泡点温度的框图 Evaluation only. Created with Aspose.Slides for .NET 3.5 Client Profile 5.2.0.0. Copyright 2004-2011 Aspose Pty Ltd. 几点说明: (1)内、外循环的安排: 当压力不大时(2MPa以下), Ki对yi不敏感,而对温度较为敏感,因此将yi放在内层循环。 (2)圆整yi: (3)判断收敛的准则或者是温度的调节方案直 接关系到收敛速度和稳定性。 参见例[2-5] Evaluation only. Created with Aspose.Slides for .NET 3.5 Client
显示全部