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A Central Composite Rotatable Design was employed to search for the optimal conversion of -menthol and enantiomeric excess.
The maximum bio-oil yield was 75.45 % with optimal conversion of 86.01 % at 320 °C and 30 min under 10 MPa hydrogen initial pressure.
The reaction time and CTO to methanol molar ratio were the two most contributing factors for the optimal conversion of CTO to biodiesel.
Kinetic modeling of the catalytic FCC reactor will give a further understanding of the process and explain the complicated mechanism involved for an efficient and optimal conversion of the feed stock.
The optimal conversion of CTO to crude biodiesel was obtained at 16 h reaction time, 40 °C reaction temperature, 1 1.5 CTO to methanol molar ratio, and 1.0 wt% enzyme dose.
From the end-users' perspective, optimal conversion of huge files of spatio-temporal data for further dissemination, accuracy of conversion, organization of content and security have a key role for effective geo-collaboration.
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The final optimal conversion efficiency of 19.18% for the PERC device with the improved stacked passivation film is obtained.
The optimal conversion efficiency of the In2S3/ZnO-50 In2S3/ZnO-505% at 0.9 V versus RHE, which is 6.5 times larger thaNSAsat of the pristine In2S3 NSAs (0.085% at 0.9 V versusE).
The optimal conversion efficiency of 3.89 % was achieved under AM 1.5 G light illumination on ITO/glass substrate and 3.4 % on ITO/PEN flexible substrate, which is the highest among flexible, room temperature-fabricated ZnO DSSCs.
However, optimal conversion in the sense of maximum likelihood presented in these prior works requires prohibitively high computation, which prevents their direct deployment to an embedded platform.
The optimal results included the choice of optimal conversion pathway, biomass type, biomass locations, facility locations, and network topology structure in the biofuel supply chain.
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CEO of Professional Science Editing for Scientists @ prosciediting.com