Analytical Solution of Transient Response of Gas-to-Gas Parallel and Counterflow Heat Exchangers

1987 ◽  
Vol 109 (4) ◽  
pp. 848-855 ◽  
Author(s):  
D. D. Gvozdenac

This paper shows how the transient response of gas-to-gas parallel and counterflow heat exchangers may be calculated by an analytical method. Making the usual idealizations for analysis of dynamic responses of heat exchangers, the problem of finding the temperature distributions of both fluids and the separating wall as well as the outlet temperatures of fluids is reduced to the solution of an integral equation. This equation contains an unknown function depending on two independent variables, space and time. The solution is found by using the method of successive approximations, the Laplace transform method, and special functions defined in this paper.

1978 ◽  
Vol 45 (1) ◽  
pp. 153-158 ◽  
Author(s):  
K. Nagaya

This paper deals with vibration and dynamic response problems of an arbitrary-shaped membrane subjected to general dynamic loads. The exact solution for an equation of motion in terms of general dynamic loads is used, and the boundary conditions of the membrane are satisfied by means of the Fourier expansion method. The results of free vibration and dynamic response problems are shown in generalized forms for arbitrary-shaped membranes. As examples of these problems, free vibrations of elliptical and crescent-shaped membranes and dynamic responses of elliptical membranes to annular impact loads are discussed by applying the Laplace transform method. For some typical cases, the results obtained are compared with those of the exact method.


2021 ◽  
Vol 2021 (1) ◽  
Author(s):  
Azhar Ali Zafar ◽  
Jan Awrejcewicz ◽  
Olga Mazur ◽  
Muhammad Bilal Riaz

AbstractOur aim in this article is to solve the composite fractional relaxation differential equation by using different definitions of the non-integer order derivative operator $D_{t}^{\alpha }$ D t α , more specifically we employ the definitions of Caputo, Caputo–Fabrizio and Atangana–Baleanu of non-integer order derivative operators. We apply the Laplace transform method to solve the problem and express our solutions in terms of Lorenzo and Hartley’s generalised G function. Furthermore, the effects of the parameters involved in the model are graphically highlighted.


1983 ◽  
Vol 105 (3) ◽  
pp. 563-570 ◽  
Author(s):  
F. E. Romie

The transient mixed mean temperatures of the two gases leaving a crossflow heat exchanger are found for a unit step increase in the entrance temperature of either gas. The temperature responses are given in graphical form for the range of parameters: Ntu from 1 to 8, capacity rate ratio from 0.6 to 1.67, and conductance, ratio from 0.5 to 2.0. The solutions are found using the Laplace transform method and apply to single-pass crossflow exchangers with neither gas mixed.


1985 ◽  
Vol 52 (2) ◽  
pp. 439-445 ◽  
Author(s):  
T. J. Ross

The problem of a viscoelastic Timoshenko beam subjected to a transversely applied step-loading is solved using the Laplace transform method. It is established that the support shear force is amplified more than the support bending moment for a fixed-end beam when strain rate influences are accounted for implicitly in the viscoelastic constitutive formulation.


Author(s):  
Bakhtiyar Ismailov ◽  
Zhanat Umarova ◽  
Khairulla Ismailov ◽  
Aibarsha Dosmakanbetova ◽  
Saule Meldebekova

<p>At present, when constructing a mathematical description of the pyrolysis reactor, partial differential equations for the components of the gas phase and the catalyst phase are used. In the well-known works on modeling pyrolysis, the obtained models are applicable only for a narrow range of changes in the process parameters, the geometric dimensions are considered constant. The article poses the task of creating a complex mathematical model with additional terms, taking into account nonlinear effects, where the geometric dimensions of the apparatus and operating characteristics vary over a wide range. An analytical method has been developed for the implementation of a mathematical model of catalytic pyrolysis of methane for the production of nanomaterials in a continuous mode. The differential equation for gaseous components with initial and boundary conditions of the third type is reduced to a dimensionless form with a small value of the peclet criterion with a form factor. It is shown that the laplace transform method is mainly suitable for this case, which is applicable both for differential equations for solid-phase components and calculation in a periodic mode. The adequacy of the model results with the known experimental data is checked.</p>


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