Organic isocyanates have achieved great commercial importance as chemical intermediates in the manufacture of thermoplastic foams, elastomers, adhesives, and agrochemicals. Aromatic isocyanates are currently synthesized via the two-step process: a catalytic reduction of the corresponding nitro compound to aromatic amine followed by a phosgenation of the amine to isocyanate. The phosgenation route has a number of serious problems; e.g., use of extremely toxic phosgene gas, and formation of a large amount of corrosive hydrochloric acid as a side product. It has been thus desired to develop alternative phosgene-free route for the isocyanate synthesis. Reductive carbonylation with carbon monoxide (CO) is an attractive alternative, because it enables a direct conversion of nitro aromatic to isocyanate. The direct carbonylation, however, needs very high CO pressure (> 10 MPa) to solubilize CO gas into liquid solvents. In the present study, microreaction technology is applied to the direct isocyanate synthesis in order to improve the mass-transfer across the gas-liquid interface. Here we present a direct carbonylation of nitrobenzene to phenylisocyanate in microflow reactor at CO pressure lower than 1 MPa. The isocyanate yield in microflow reactor is compared with that in batch reactor, and the effect of the microtube diameter on the isocyanate yield is discussed.