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Mass streams are characterized by their composition and properties.
Successive mass streams are 7 t of air-dry straw (15 wt.% H2O, LHV 4 kWh/kg) → 6 t of dry straw → ca. 4.7 t of biosyncrude (slurry or paste LH ca. 5.4 kWh/kg) → 1.25 t of FT raw product (LHV ca. 12 kWh/kg) → 1 t of biosynfuel (LHV 12 kWh/kg).
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First, the suspended solids which reach up to 10% of the mass stream are precipitated, flocculated and separated by means of a decanting centrifuge and flotation.
The equations governing the momentum, energy and mass transports in the two streams are established and solved together with the conjugate heat and mass transfer boundary conditions.
The parameters characterizing the plant streams are the total mass flow rate and the concentrations of individual components.
Because the osmolality of both streams are equal, no mass transfer will occur and any damage is expected to only be due to mechanical stresses.
As an important result, total capacity of a process among other design array does not suffice for decision making unless the mass fraction of hazards in product streams are appreciably low.
In the present work, mass sources are connected with mass sinks through alternative "operators" (processes) whose exit streams are of different compositions.
The main objective of these heuristical algorithms is to get a mass transfer network [1], where contaminants of rich streams are transferred to other poor streams, in an optimized structure of linked mass transfer operations.
The waste streams are different.
"The streams are smaller.
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