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The kinetics of the inverse microemulsion polymerization of MADQUAT initiated with sodium metabisulfite in both batch and semi-continuous reactors was studied using reaction calorimetry.
A promising catalytic system for the low temperature oxidation of methane to a methanol derivative has been investigated under both batch and semi-continuous operation in two different reactor types.
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Lab-scale and pilot-scale HASL systems were operated in batch and semi-continuous modes.
The content of methane in the biogas produced was from 70%to74%4% for batch and semi-continuous operation of HASL systems.
It was 0.33 l l−1 day−1 and 0.49 l l−1 day−1 for the pilot-scale HASL system operated in batch and semi-continuous modes, respectively.
Methane production was 0.49 l l−1 day−1 and 0.71 l l−1 day−1 for the lab-scale HASL system operated in batch and semi-continuous modes, respectively.
Example 2 is a hybrid batch water system comprising various operations (fixed load and fixed flowrate) and operating models (completely batch and semi-continuous).
This approach uses a mixed-integer nonlinear programming (MINLP) model that enables water re-use and regeneration re-use in batch and semi-continuous processes.
A mixed-integer nonlinear programming (MINLP) model is used for water re-use and regeneration re-use within batch and semi-continuous processes.
The deactivation mechanism of Pd supported on silica and mesoporous silica (SBA-15) using CO2-expanded methanol as solvent was studied in the direct synthesis of H2O2 in batch and semi-continuous batch reactor tests as well as its hydrogenolysis.
The experimental and theoretical results obtained were compared when the same chromatographic columns were operating in the batch and semi-continuous modes.
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