A set of modified isothermal batch reactors was designed to investigate the modes and kinetics of carbon oxide emission from different classes of coals (lignite, sub-bituminous coal, and bituminous coal) oxidized at temperatures below 200 °C.
Therefore, a batch series reactor was designed for semi-continuous lycopene extraction.
A laboratory batch electrocoagulation/flotation (ECF) reactor was designed to investigate the effects of different parameters such as electrolysis time, electrolyte pH, initial nitrate concentration, and current rate on the nitrate removal efficiency.
For chemical scaling of DW biomass, a batch-scale duckweed reactor was designed using urban wastewater (WW) and changes in WW characteristics were recorded at the end.
Using research on a batch system as basis, a flow reactor was designed and applied in the combined supercritical and subcritical hydrolysis of cellulose for fermentable hexose production.
Semi-batch experiments in the stirred tank reactor were designed to investigate the effects of temperature, air pressure, initial phenol concentration, catalyst loading, and catalyst size on the conversion of total organic carbon.
Intensified continuous reactor is designed to replace conventional batch reactor for three-phase catalytic slurry hydrogenation.
As a consequence these batch and semi-batch reactors are usually equipped with emergency relief systems sized once forever when the reactor is designed.
A simple batch reactor was first designed and constructed to examine applicability of thermal chemical destruction of PCBs.
