2 research outputs found
Three-Component Coupling Based on Flash Chemistry. Carbolithiation of Benzyne with Functionalized Aryllithiums Followed by Reactions with Electrophiles
A flow
microreactor method for three-component coupling of benzyne
was developed based on flash chemistry. <i>o</i>-Bromophenyllithium
generated from 1-bromo-2-iodobenzene and a functionalized aryllithium
generated from the corresponding aryl halide were mixed at −70
°C. In the subsequent reactor <i>o</i>-bromophenyllithium
is decomposed to generate benzyne without affecting the functionalized
aryllithium at −30 °C, and carbolithiation of benzyne
with the aryllithium took place spontaneously. The resulting functionalized
biaryllithium was reacted with an electrophile in the subsequent reactor
to give the corresponding three-component coupling product. The precise
optimization of reaction conditions using the temperature–residence
time mapping is responsible for the success of the present transformation.
The present method has been successfully applied to the synthesis
of boscalid
Feasibility Study on Continuous Flow Controlled/Living Anionic Polymerization Processes
A practical microchemical
reaction system for keeping process flow
at defined conditions, which is one of the key issues of industrial
production, was developed. Controlled/living anionic polymerization
was chosen as a test reaction because the molecular weight and molecular
weight distribution of polymer products are quite sensitive to the
relative flow rate of an initiator solution and that of a monomer
solution. The polymerization of styrene in THF/hexane was carried
out using a flow microreactor system consisting of two T-shaped micromixers
and two microtube reactors using Smoothflow pumps at 0 °C. PolyÂ(styrene)
with higher molecular weight such as Mn > 10000 could be synthesized
using <i>s</i>-BuLi (Mn = 14 000, <i>M</i><sub>w</sub>/<i>M</i><sub>n</sub> = 1.11). <i>n</i>-BuLi could also be used as an initiator. The continuous operation
was performed for 3 h without any problems to obtain ca. 1 kg of the
polymer, indicating the feasibility of continuous flow processes for
controlled/living anionic polymerization on a relatively large scale