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The alcohol can be recovered by vacuum andjor steam distillation, and the solution used on site as a raw material or as a col1ector. From the description of the process, there are three critical steps involved: 1) the preparation of the alcoholate, 2) the xanthate reaetion, and 3) the drying step.
Apr 01, 2018 · The highest excess 224Ra value (2.90 dpm 100L-1) is located at the offshore of Linbian River and it is much higher than the value in the Linbian River (0.54 dpm 100L-1, salinity 0.2) which .
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Finally, this analysis suggests bubble-column reactor systems can reduce overall costs for oxygen delivery by 10-20% relative to stirred tanks at low to moderate oxygen transfer rates up to 150 mmol/L .
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German plant used 400% excess alcohol and equimolar quantities of carbon disulphide and 50% aqueous potassium hydroxide. The reaction temperature was maintained at 40C by cooling. This step took a half hour. The product was dried in a vacuum drier, and water was removed from the recovered alcohol by distillation.
In addition, plant inoculated with A. faecalis SF-60 showed the highest BAC and BCF values, and the lowest TF value compared to plant inoculated with B. diminuta SF-S1-5 and the control plant. This .
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Finally, this analysis suggests bubble-column reactor systems can reduce overall costs for oxygen delivery by 10-20% relative to stirred tanks at low to moderate oxygen transfer rates up to 150 mmol/L-h.« less. Aeration costs in stirred-tank and bubble column bioreactors. SciTech Connect. Humbird, D.; Davis, R.; McMillan, J. D.
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Finally, this analysis suggests bubble-column reactor systems can reduce overall costs for oxygen delivery by 10-20% relative to stirred tanks at low to moderate oxygen transfer rates up to 150 mmol/L-h.« less. Modeling and simulation of large scale stirred tank. NASA Astrophysics Data System (ADS) Neuville, John R.
Jun 12, 2018 · Beryllium Manufacturing Processes. SciTech Connect. Goldberg, A. 2006-06-30. This report is one of a number of reports that will be combined into a handbook on beryllium. Each rep
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Evaluation of a 75,000 gpd seawater desulphat-ing pilot plant. OSW R&D Progress Report 746 (1972). 63 /14/ Brookheaven National Laboratory. Scale control in high temperature distillation utilizing fluidized heat exchang-ers. OSW R&D Progress Report 571 (1970). /15/ Baldwin, Lima, Hamilton. Operation of the 16 stage high temperature flash pilot .
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Reactor engineering support of operations at the Davis-Besse nuclear power station. SciTech Connect. Kelley, D.B. 1995-12-31. Reactor engineering functions differ greatly from unit to unit; however, direct support of the reactor operators during reactor startups and operational transients is common to all units. This paper summarizes the support the reactor engineers provide the reactor .