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To overcome such inhomogeneous condition, we designed a stirring reactor by packing catalyst pellets inside four static columns, and then stirred to mix soybean oil and methanol in the reactor.
The washed SEWS was delignified by ethanol extraction in a mechanical stirring reactor (GSF, DLZK, Beijing, China).
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Even without stirring, the reactor internals cause already interaction between the gas and the liquid, resulting in a mass transfer coefficient amounting to 1.17 × 10−2 s−10−2
This glass reactor (AGR) is a spherical vessel (capacity 0.5 dm3) equipped with a temperature indicator cum controller, a long vertical condenser for condensing the vapor, and a magnetic stirrer with variable speed for stirring the reactor contents.
Comparing with the stirring batch reactor, the designed microreactor provides constant reaction temperature and the reaction time can be shortened significantly to 29 s with 1-butene conversion of 91.4%.
The effect of different operational conditions such as stirring speed, reactor length, foam porosity, foam thickness and the presence of baffles on the gas liquid mass transfer and the gas liquid flow distribution is discussed for the systems water/air and glycerol/air.
Pretreated material was enzymatically hydrolyzed in stirred reactors at different controlled stirring rates.
In addition, the influence of free fatty acid (FFA) was also studied in the stirring packed-bed reactor.
We performed the transesterification of soybean oil with methanol to synthesize biodiesel using Ca(C3H7O3 2/CaO solid-base catalyst in a stirring packed-bed reactor.
The Langmuir Hinshelwood model was used to establish a rate equation for the transesterification of soybean oil with methanol in the stirring packed-bed reactor.
Exothermically reacting fluid poses the danger of temperature run-away (thermal explosion) in some circumstances (e.g. interruption of stirring in a reactor and during storage).
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