A method for the production of a synthetic gasoline with a high isoparaffin content in the range of 50-65 mass% and a low aromatics content in the range of 20-35 mass%, comprising the following steps: I. catalytic conversion of feed alcohol in a feed gas into a product mixture containing water and a hydrocarbon mixture of olefins, n-paraffins, isoparaffins, aromatics, and naphthenes within an isothermal tubular reactor containing a catalyst, wherein the reaction temperature within the tubular reactor is between 300 and 370 °C, wherein the feed alcohol has a water content of less than 20 mass%, II. separation of the product mixture obtained in step I) into: - a liquid hydrocarbon phase, - an aqueous phase containing the unconverted alcohol, and - a gas phase containing C 1 - to C 5 - hydrocarbons, III. recycling of the gas phase obtained in step II) to step I), IV. separation of the liquid hydrocarbon phase obtained in step II) into - an olefin-containing C 3 - to C 4 - hydrocarbon fraction and - a gasoline hydrocarbon fraction (= C 5+ fraction) containing a durene-containing heavy aromatics fraction, V. separation of the gasoline hydrocarbon fraction obtained in step IV) into a durene-containing heavy aromatics fraction and a stable gasoline fraction, wherein in step I) the alcohol load of the catalyst is 2 to 5 m 3 alcohol /hm 3 c at, wherein for producing an isoparaffin-rich gasoline, the catalyst is partially diluted in the inlet region of the alcohol with inert material with a mass fraction of 5 to 30 %, based on the total mass of catalyst and inert material, and wherein the olefin-containing C 3 - to C 4 - hydrocarbon fraction separated off in step IV) is recycled to step I) as feed material, wherein in step I) the mole fraction of alcohol, which is to be converted, in the total amount of feed gas at the reactor inlet comprises 25 to 50 mol%, wherein the feed gas comprises the feed alcohol and the recycled components. I. catalytic conversion of feed alcohol in a feed gas into a product mixture containing water and a hydrocarbon mixture of olefins, n-paraffins, isoparaffins, aromatics, and naphthenes within an isothermal tubular reactor containing a catalyst, wherein the reaction temperature within the tubular reactor is between 300 and 370 °C, wherein the feed alcohol has a water content of less than 20 mass%, wherein the reaction temperature within the tubular reactor is between 300 and 370 °C, wherein the feed alcohol has a water content of less than 20 mass%, II. separation of the product mixture obtained in step I) into: - a liquid hydrocarbon phase, - an aqueous phase containing the unconverted alcohol, and - a gas phase containing C 1 - to C 5 - hydrocarbons, - a liquid hydrocarbon phase, - an aqueous phase containing the unconverted alcohol, and - a gas phase containing C 1 - to C 5 - hydrocarbons, III. recycling of the gas phase obtained in step II) to step I), IV. separation of the liquid hydrocarbon phase obtained in step II) into - an olefin-containing C 3 - to C 4 - hydrocarbon fraction and - a gasoline hydrocarbon fraction (= C 5+ fraction) containing a durene-containing heavy aromatics fraction, - an olefin-containing C 3 - to C 4 - hydrocarbon fraction and - a gasoline hydrocarbon fraction (= C 5+ fraction) containing a durene-containing heavy aromatics fraction, V. separation of the gasoline hydrocarbon fraction obtained in step IV) into a durene-containing heavy aromatics fraction and a stable gasoline fraction, wherein in step I) the alcohol load of the catalyst is 2 to 5 m 3 alcohol /hm 3 c at, wherein for producing an isoparaffin-rich gasoline, the catalyst is partially diluted in the inlet region of the alcohol with inert material with a mass fraction of 5 to 30 %, based on the total mass of catalyst and inert material, and wherein the olefin-containing C 3 - to C 4 - hydrocarbon fraction separated off in step IV) is recycled to step I) as feed material, wherein in step I) the mole fraction of alcohol, which is to be converted, in the total amount of feed gas at the reactor inlet comprises 25 to 50 mol%, wherein the feed gas comprises the feed alcohol and the recycled components.