The experiments on hydrogenation of ethyl ether of p-nitrobenzoic acid to anesthesyne on suspended 5% Pd/C catalyst in a batch reactor were carried out for verification of the main results from the proposed model (PH2=40 bar, T=20 120 °C).
Experiments on batch and semi-batch reactors are carried out to emphasize the performances of the aforementioned controller with respect to those of an auto-calibrated PID controller.
A mass balance over the reactor is carried out defining the design as a stirred tank reactor batch process, leading to the reaction rate shown in Eq. 1.
Batch reactor experiments were carried out by using powder sulfated zirconia catalyst.
Batch reactor studies were carried out in a 5-L Biostat B fermentor (B. Braun, Germany) containing 2 L of non-sterilized SCB hydrolysate.
The photodegradation of the seven molecules in the batch reactor was successfully carried out and the behaviour was in accordance with pseudo-first order kinetics.
For activated sludge under steady state, batch experiments were carried out to examine activities of nitrification and denitrification for activated sludge acclimated in the AO reactor and the multiple AO reactor.
Three batch experiments were carried out.
Batch studies were carried out on a small laboratory scale electrochemical cell and flow-through treatment studies were carried out in a pilot scale circulating fluidised bed reactor.
The polymerizations were performed under batch condition and were carried out in a 250-ml thermostated reactor, round-bottomed four-necked flask, equipped with a glass anchor-shaped stirrer, condenser, thermocouple and nitrogen inlet.
