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The dimension of pipe condition and performance is the consequence scale considered as relevant for this paper.
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It is proved that only one of these components depends on time, and it is common in all EPs of the same diameter, the other three depending on the basic design parameters of the EPs, i.e. the number of pipes, the type and dimensions of pipes and the heat/flow characteristics in the pipes.
In terms of the geometrical dimensions of pipes, the critical compressive stress increases with thickness and decreases with diameter.
Dimensions of the pipe varied in each case depending on the type of material used.
To simulate the dimensions of the pipe and achieve similar conditions to that of the experimental setup, the final radius was chosen to be 80 mm.
The possibility to reduce the radial dimension of the beam-pipe, down to ≃1cm, allows to measure the first hit of the tracks very close to the interaction point, by adding a layer-0 to the present BABAR five-layer vertex detector configuration.
The scaling process consists of heat transfer scaling of the heat exchanger and the pressure resistance scaling of the riser and downcomer sections, the purpose of which is to keep the driven force and pressure resistance of the model same with those of the prototype by changing the dimensions of the pipes.
Analytical solutions were used to derive steady-state reference rupture stresses, from which the effects of pipe dimensions and the tri-axial stress state parameter can be assessed.
These findings are explained using an analogy with the effect of pipe dimensions on the fluid flow through a pipe and by considering the role of forced convection on the oxygen transport to the membrane/cathode interface.
In terms of pipe dimensions, both the pipe diameter and thickness can enhance the pipe stiffness.
Get a piece of pipe the same dimensions as what is left on the exhaust mounting flange.
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