首页> 外文期刊>Journal of Chemical Engineering of Japan >A NEW SIMULATION PROCEDURE FOR MULTICOMPONENT DISTILLATION COLUMN PROCESSING NONIDEAL SOLUTIONS OR REACTIVE SOLUTIONS
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A NEW SIMULATION PROCEDURE FOR MULTICOMPONENT DISTILLATION COLUMN PROCESSING NONIDEAL SOLUTIONS OR REACTIVE SOLUTIONS

机译:多组分精馏塔处理非理想溶液或反应溶液的新模拟过程

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References(20) Cited-By(18) A powerful new simulation procedure is developed for multicomponent distillation columns processing nonideal solutions or reactive solutions. Although the tridiagonal matrix algorithm is incorporated, the main calculational loop is the Newton-Raphson method in which liquid mole fractions are chosen for the independent variables and the functions to be zeroed are originally defined. The procedure does not vitiate at all such great advantages of the conventional tridiagonal matrix method as the ready incorporation of heat balances, nonideality of the solutions and chemical reactions, and still the algorithm and computer programming are rather simple. Nevertheless, the procedure presents much greater stability in finding converged solutions. A total of eight numerical experiments are made under a variety of conditions, and in all cases rigorous solutions are obtained achieving convergence in three to nine iterations.
机译:参考文献(20)Cited-By(18)针对多组分蒸馏塔的非理想溶液或反应溶液的开发,开发了一种功能强大的新模拟程序。尽管并入了三对角矩阵算法,但主要的计算循环是牛顿-拉夫森法,其中选择了液体摩尔分数作为自变量,并且最初定义了要归零的函数。该方法完全没有消除传统三对角矩阵方法的巨大优势,例如易于实现热平衡,溶液的非理想性和化学反应,并且算法和计算机编程仍然相当简单。然而,该程序在寻找收敛解方面表现出更大的稳定性。在各种条件下总共进行了八次数值实验,并且在所有情况下均获得了经过三到九次迭代实现收敛的严格解。

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