NOVELTY - Conversion of carbon oxide(s) and hydrogen containing feed to alcohols involves converting feed in presence of particulate catalyst in homologation reactor into stream A with alcohol(s), ester(s), hydrogen, carbon monoxide/dioxide; separating stream A into inorganic stream B and organic stream C that is recovered with increased weight content of total ethanol and propanol(s); and separating stream C into stream J with methanol that is recycled into homologation reactor, stream K with ethanol and propanol(s) alcohols, and stream X with ester(s) that are recycled into methanol reactor.    USE - For the conversion, of carbon oxide(s) and hydrogen containing feedstocks, into alcohols in the presence of a particulate catalyst (claimed).    ADVANTAGE - The process shows high alcohols (especially ethanol) selectivity, while simultaneously increasing catalyst activity and improving operating life. The process converts carbon oxide(s) and hydrogen containing feedstocks, into alcohols with less waste; less by-products and thus higher carbon efficiency, less capital, fewer separations and reduced storage tanks; and there is no corrosion and metallurgy constraints due to the potential hydrolysis of the esters during subsequent purification and storage stages. The process is highly economically advantageous compared to existing technologies in the field for producing n-propanol, which incur large operating expenses.    DETAILED DESCRIPTION - Conversion, of carbon oxide(s) and hydrogen containing feedstocks, into alcohols in the presence of a particulate catalyst involves: a) converting a carbon oxide(s) (CO or (CO2) and hydrogen (H2) feed having a (H2-CO2):(CO+CO2) molar ratio of 0.5 - 2, in the presence of a particulate catalyst in a homologation reactor under 150 - 400degreesC and a pressure of 50 - 250 bars, into a stream A, comprising essentially alcohol(s), ester(s), H2, CO and CO2; b) separating the alcohol stream A, into a stream B comprising H2, CO and CO2 and a stream C comprising the alcohol(s) and ester(s); c) optionally separating the stream B into a H2 and CO2 depleted stream D' having a (H2-CO2):(CO+CO2) molar ratio of lower than 0.5 and a H2 and CO2 enriched stream D having a (H2-CO2):(CO+CO2) molar ratio higher than 3; d) converting a CO/CO2/H2 feed (optionally comprising stream D) having a (H2-CO2):(CO+CO2) molar ratio higher than 3 in a methanol reactor into a stream E comprising essentially methanol, water, H2, CO and CO2; e) separating stream E into stream F comprising H2, CO and CO2 and stream G comprising methanol and water; f) separating stream G into stream H consisting essentially of water and stream I comprising essentially methanol; g) reintroducing stream I into the homologation reactor of step a; h) recovering a stream C comprising an increased weight content of total ethanol and propanol(s); and i) where the recovered stream C from step h) is separated into a stream J comprising essentially methanol which is then preferably recycled into the homologation reactor of step a), a stream K comprising essentially the ethanol and propanol(s) alcohols, and a stream X comprising essentially the ester(s) which are then preferably recycled into the methanol reactor of step d).