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To give it increased resistance to weather, the wall surface is often treated with plaster, bitumen, or linseed oil.
The side wall surface is considered as a perfect thermal insulated surface.
The pore wall is hydrophobic because the wall surface is hydrogen-terminated.
To calculate the rate of heat transfer the temperature at the wall surface is accepted as steady, but in [5] a transient consideration was also implemented.
Conventional structured catalytic structures are constituted by a ceramic or metallic monolith whose wall surface is covered by a porous coating on which the active metal is deposited.
The strong temperature drop between the process gas and the wall surface is due to the large heat flux that can be in excess of 100 MW/m2 (Popp and Schmidt 1996; Quentmeyer 1977).
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Wall surface was reduced to the minimum to allow an almost continuous window expanse.
The heat flux and wall superheat were determined simultaneously as the wall surface was gradually heated.
A total of 450 micrographs of the canal wall surface were taken.
The ratio of acid insoluble lignin to acid soluble lignin was increased, while the formation of spherical lignin droplets on the cell wall surface was decreased.
The k ε realizable model is used as the turbulence model, where k is turbulent kinetic energy and ε is dissipation rate of k; and the flow fields near the wall surface are solved through scalable function.
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