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A mechanical refining step is applied after the pretreatment reactor in the whole slurry case, and is applied after the washing step in the washed solids option due to the complexity introduced by trying to filter fine particles generated in mechanical refining.
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In addition, higher levels of xylose oligomers were found in the hydrolysis slurry in the case of the F-1663 enzymes.
The slurry in this case was split into a solid fraction and a liquid fraction, where the solid fraction was used to produce ethanol and the liquid fraction to produce biogas.
It was verified experimentally that the Simha's model was able to predict the slurry viscosity for the case of the suspensions with particle size distribution.
The scope of the study incorporated the application of cathodic protection to prohibit the effects of corrosion in the case of slurry erosion testing.
The movement of the reaction boundary is well-understood quantitatively only in the absence of particles and this paper attempts to provide a theoretical model and its experimental validation, for the case of slurries.
In all cases the slurry was adjusted to a pH of 5.0 prior to the start of the hydrolysis experiments by the addition of 12 M NaOH.
At the beginning of the recycle experiment, initial glucose concentrations were ~5 g/L from the pretreated slurry, and in some cases reached 20 g/L in the beginning of the 4th recycle round for conditions with 100% recycle (data not shown).
"Slurry impregnation" is a special case of equilibrium adsorption impregnation.
Results showed that both biomass and NO2− concentrations had a significant effect on the SDA in the presence of acetate, in the case of swine slurry, pH also affected the SDA.
In the case of pyrite slurries, probes that have been applied to determine.
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