Concentrated orange juice was spray dried at inlet air temperatures of 110, 120, 130, and 140 °C and (concentrated orange juice solids)/(maltodextrin solids) ratios of 4, 2, 1, and 0.25.
The location of the pump with respect to the surface of the ocean would depend on the fluid-solids ratio of the material in the pipe as well as the fluid velocity.
Raw cassava stems were pretreated at 170 °C for 20 min in a 1%% (w/w) aqueous solution of H2SO4 that was added to the biomass at a liquid-to-solids ratio of 9 1.
Figure 6 29 Si MAS NMR of batch reactions at a solution:solid ratio of 10 1.
Extractions were carried out with 10%% (w/v) aqueous glycerol, at a liquid-to-solid ratio of 50 mL g−1.
The maximum zerumbone recovery (5.08 mg/g DM) was observed at a liquid-to-solid ratio of 30 mL/g.
Extractions were carried out under stirring at 400 rpm, 70 °C and a liquid-to-solid ratio of 50 mL g−1.
We show in Figure 629Si MAS NMR spectra from the batch reaction at a solution:solid ratio of 10 1.
The zerumbone yield was maximized using a liquid-to-solid ratio of 30 over a range of the other operational factors (microwave power and irradiation time).
The 27Al MAS NMR data for batch reactions with a solution:solid ratio of 5 1 are virtually identical except that reaction rates are considerably faster (Figure 9).
For the batch reactions with a solution:solid ratio of 5 1, we observe similar trends in the diffraction data except that reaction rates are significantly faster (Figure 11).
