混合三次函数方程的模糊稳定性

讨论并解决了模糊Banach空间上混合三次函数方程f(x1+x2,y1+y2)+f(x1+x2,y1-y2)=2f(x1,y1)+2f(x1,y2)+2f(x2,y1)+2f(x2,y2)的Hyers-Ulam-Rassias模糊稳定性.

二次-三次函数方程在Non-Archimedean赋范空间的Ulam稳定性

讨论了混合二次-三次函数方程6f(x+y)-6f(x-y)+4f(3y)=3f(x+2y)-3f(x-2y)+9f(2y)

二元三次函数方程的解及在模糊Banach空间上的稳定性

设X和Y是实向量空间,映射f:X2→Y称为二元三次函数,x1,x2,y1,y2∈X,都满足下面的二元三次函数方程:f(2x1+x2,2y1+y2)+f(2x1+x2,2y1-y2)+f(2x1-x2,2y1+y2)+f(2x1-x2,2y1-y2)=4f(x1+x2,y1+y2)+4f(x1-x2,y1+y2)+24f(x1,y1+y2)+4f(x1+x2,y1-y2)+4f(x1-x2,y1-y2)+24f(x1,y1-y2)+24f(x1+x2,y1)+24f(x1-x2,y1)+144f(x1,y1)。研究二元三次函数方程解的一般形式,证明了在模糊Banach空间上该方程的Hyers-Ulam稳定性。

Cauchy-三次函数方程及其Hyers—Ulam稳定性

给出Cauchy-三次函数方程f(x_1+x_2,2y_1+y_2)+f(x_1+x_2,2y_1-y_2)=2f(x_1,y_1+y_2)+2f(x_1,y_1-y_2)+12f(x_1,y_1)+2f(x_2,y_1+y_2)+2f(x_2,y_1-y_2)+12f(x_2,y_1)的一般解,并用直接方法和不动点方法研究它在Banach空间上的HyersUlam稳定性及模糊稳定性.

三次函数方程在模糊赋范空间上的稳定性

2007年,Najati给出了三次函数方程的通解及其在Banach空间上的Hyers-UlamRassias稳定性.本文运用不动点的择一性方法,证明了三次函数方程在模糊赋范空间上的Hyers-Ulam-Rassias稳定性.

二次-三次混合函数方程在Felbin型模糊Banach空间上的HUR稳定性

用直接法证明二次-三次混合函数方程在Felbin型的模糊赋范线性空间上的HUR稳定性。

Jensen-二次函数方程及其Hyers-Ulam稳定性

给出Jensen-二次函数方程f((x_1+x_2)/2,y_1+y_2)+f((x_1+x_2)/2,y_1-y_2)=f(x_1,y_1)+f(x_1,y_2)+f(x_2,y_1)+的一般解,并研究了它的Hyers-Ulam稳定性.

矩阵拟范空间上函数方程的Ulam稳定性

本文给出了矩阵拟范空间的定义,并在其上讨论了混合二次一三次函数方程6f(x+y)-6f(x-y)+4f(3y)=3f(x+2y)-3f(x-2y)+9f(2y)的Ulam稳定性.

A New Alpha-function for the Peng-Robinson Equation of State： Application to Natural Gas

Cubic equations of state(EOSs) are simple and easy at calculation. One way of improving the accuracy of a cubic EOS is through the modification of temperature-dependent energy parameter by using alpha-function.The industrial applications of natural gas are very wide and as a result, prediction of thermodynamic properties and phase behavior of natural gas is an important part of design for such processes. In this work we develop a newα-function for the Peng-Robinson(PR) EOS with the parameters optimized especially for natural gas components.The parameters are generalized as a linear function of acentric factor. The results are compared to the predictions from original PR EOS and other α-functions in literature. It is shown that the new α-function presents a good accuracy with the average deviation of 1.42% for natural gas components.