Batch and continuous operating modes are compared for heterogeneous catalytic systems in which the internal accumulation of reactants and products is not negligible.
In addition, the catalysts have been tested in a batch and continuous reactor to evaluate the influence of the reactor configuration on the catalytic performance.
Experimental runs in batch and continuous flow microscale reactors have been carried out to investigate the reaction network, the role of the catalytic agents and the influence of the operating conditions over a wide experimental range.
The catalytic process A→R along with surface poisoning P+⁎→P⁎ (⁎ is an active site) was modelled for batch and continuous reactors.
Several operating procedures are given for batch and continuous mixers.
Fig. 6 Comparison of batch and continuous hydrolysis.
Batch and continuous modes of treatment were studied.
Operational practices such as batch, fed batch, and continuous culture are described.
Reconfigurable batch processes have higher agility and flexibility than multi-purpose, multi-product, dedicated batch and continuous processes.
As we compared the GC productivity in batch and continuous operation, the GC productivity in batch was five times (6.9 higherigher than that of continuous operation (1.38 h−1.38
