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- W2387780047 abstract "The helical ribbon stirred tank was put forward for the simultaneous saccharification and fermentation at high solids loadings based on the reaction characteristics in the context of production of ethanol from lignocellulosic biomass.Attention was paid on the investigation of mixing performance of the helical ribbon stirred tank by cold-flow model experiments in the range of 0.2~0.8 m diameter,1~2 aspect ratio and 20~120 r/min rotation speed,providing the basis for the reactor scale up.The experimental results showed that power consumption decreased significantly with the fluid pseudoplastic,while the dimensionless mixing(Ntm) did not change obviously;for geometry similar impellers,Ntm was nearly the same as the tank diameter increased if kept the specific power equal,which offering a rule of thumb for the reactor scale up;the power consumption and Ntm increased with the aspect ratio;Finally,the dispersive mixing efficiency was studied in the tank employing numerical methods.It was found that the helical ribbon stirred tank can be divided into different sections based on the magnitude of the dispersive mixing efficiency.The volumetric average dispersive mixing efficiency in the helical ribbon stirred tank was 0.5(simple shear flow).As to the scale up of the reactor,bench scale experiments give key parameter(volumetric productivity) and cold-flow model provides the basis of mixing performance and geometry design.Combine the experimental results with computational fluid dynamics,concerning the size effect of flow field and consider the specific power and the maximum shear strain rate." @default.
- W2387780047 created "2016-06-24" @default.
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- W2387780047 date "2012-01-01" @default.
- W2387780047 modified "2023-09-28" @default.
- W2387780047 title "Development and scale up of the enzymatic cellulose hydrolysis reactor" @default.
- W2387780047 hasPublicationYear "2012" @default.
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