Abstract: The disclosed invention relates to a process for converting ethylbenzene to styrene, comprising: flowing a feed composition comprising ethylbenzene in at least one process microchannel in contact with at least one catalyst to dehydrogenate the ethylbenzene and form a product comprising styrene; exchanging heat between the process microchannel and at least one heat exchange channel in thermal contact with the process microchannel; and removing product from the process microchannel. Also disclosed is an apparatus comprising a process microchannel, a heat exchange channel, and a heat transfer wall positioned between the process microchannel and heat exchange channel wherein the heat transfer wall comprises a thermal resistance layer.

Abstract: The disclosed invention relates to a process for conducting a multiphase reaction in a microchannel. The process comprises: forming a multiphase reaction mixture comprising a first reactant and a second reactant; the first reactant comprising at least one liquid; the second reactant comprising at least one gas, at least one liquid, or a combination of at least one gas and at least one liquid; the first reactant forming a continuous phase in the multiphase reaction mixture; the second reactant forming gas bubbles and/or liquid droplets dispersed in the continuous phase; and reacting the first reactant with the second reactant in a process microchannel in the presence of at least one catalyst to form at least one product.

Abstract: The disclosed invention relates to a process for conducting an equilibrium limited chemical reaction in a microchannel reactor. The process involves the use of active heat exchange and is suitable for conducting exothermic and endothermic reactions. The process is particularly suitable for synthesizing methanol and dimethyl ether.