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The virtual model of shell and tube heat exchanger is used for numerical analysis as shown in Fig. 7.

A genetic algorithm procedure coupled with an analytical model of shell buckling has been developed to determine numerically optimized stacking sequences.

In this research paper, numerical model of shell and helical tube heat exchanger is investigated to assess heat transfer coefficient and exergy loss.

Finally, the above two properties are demonstrated vividly by a finite element model of beam elements, and the accuracy of the proposed method is proven by another finite element model of shell elements.

With the analysis of a parameter optimization model of Shell 60/70 asphalt, the better foaming properties are the maximum expansion ratio of 12.28 times and half-life time of 11.02 s at the foaming condition of asphalt temperature of about 168 °C, the water content of about 1.5 wt% and the air pressure of about 1 bar.

The lack of intermediate forms has reinforced the de novo model of shell evolution, and some have described the shell to have appeared within a short geological time frame through the differentiation of dermal bones (Gilbert et al. 2001).

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In this paper, a mathematical model of shell-and-tube latent heat thermal energy storage (LHTES) unit of two-dimension of three phase change materials (PCMs) named PCM1, PCM2 and PCM3 with different high melting temperatures (983 K, 823 K and 670 K, respectively) and heat transfer fluid (HTF: air) with flowing resistance and viscous dissipation based on the enthalpy method has been developed.

Consider the initial agent-based model of Shelling as shown in Fig. 1a.

A computational model for structural free-form shell generation is presented to simulate physical models of shell optimization.

Modelling of shell and tube heat exchanger, for design and performance evaluation, is now an established technique in industrial fields.

Two models of shell percentage were formulated from TEM images using Image J software to estimate the size of shell.

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