Composite membranes for reverse osmosis were fabricated by low temperature plasma polymerization process. Microporous polysulfone and polypropylene membranes were used as the support for the composite membranes. Various hydrophilic monomers were employed in the plasma polymerization process to form the hydrophilic active layers on the support. Each combination of monomer and support membrane showed its own characteristics. Polysulfone and polypropylene membranes treated with allylamine showed the comparable performances to those of the commercial ones. As plasma polymerization time increased, more plasma polymer was deposited on the support to result in the flux decline and rejection increase. Input power had influence on the plasma polymer deposition rate at low power range especially for monomer-deficient system. Sample got damaged at excess power to reduce the performances in every case. Proper combination of polymerization time and power can secure the economic aspects of the process. At too low monomer flow rate, plasma polymer was not formed enough to cover the surface of the microporous membrane to result in high flux with poor rejection. In the optimum monomer flow rate range highly cross-linked coating layer was formed. When the monomer flow rate exceeded the optimum range, energy transferred to monomer molecule was decreased to result in less cross-linked and unstable layer formation despite the increase of deposition.