The steady flow parallel reactor device has been created to offer the quick and flawless transformation from the invention phase and production phase of chemical production certainly in the low volume and high potential medicines synthesis. By using the one fixed bed catalytic meso reactor device, the reaction can be made on the little invention sale rather than short time level. The strengthen technique generates an adequate material for the complete study.
With the replication of one reactor in parallel the equivalent chemistry can be obtained on the bigger scale without the need to follow the flow constraints of reactor scale in bunch.
The cross coupling reaction is a necessary tool in the organic reaction to prepare the medicines from the functional raw material.In most of the cases in the laboratory the coupling reactions are made in the blend batch reactors like circular bottom flask by using the homogenous catalyst and mostly activation means like replaced phosphines or other catalyst containing ligands with costly and complex. Mostly the scale at which these reactions are made is larger as compare to the scale needed for initial description and feature identification. After the identification of a compound for subsequent analysis and marketing it is then manufactured on the industrial level that is in large magnitude.
Then the issue faced is to transform the little invention to the large commercial scale such that scaling of production is not easy as the quantity of reactants and solvents is quite large. The issues are also faced when the manufacturers follow the same process for the wide scale production. At this time they need to move following the cost effective process in the reactor to supply the source without causing the hazardous issues.
Subsequently, the small scale synthesis is a benefit while considering the protection especially in the failure cases. The scaling the reactor has propositions on the mass and heat supply to the system to optimize the process for the existing environments. It can take lot of time and mostly results in the dumping of bench scale in the side of the conditions that more suggested in the large production. Certainly in the presence of homogenous catalysts in the scaling methods is difficult. The homogenous catalyst generally get dissociated in the reactions thus the actual active catalyst is actually not present in the reaction. This enables in the mending of catalyst and recycling of process is viable.
The batch reactions made in the presence of Radley Carousel parallel producer fit with the help of hairy logic controller device that provides controlled temperature environment. The production consists of twelve vessels that are fitted with the help of screw on Teflon caps consisting of valves to add the inert or active gasses for the inclusion of reagents. The twelve reaction vessels placed in the double staked aluminum platters and the lower placed on the hotplate blended and it can be uphold at the constant temperature.Normally the nickel mesh catalyst is used to make the reaction successful.