NOVELTY - The process comprises generating a hot raw synthesis gas (4), optionally enriching hydrogen in the synthesis gas to obtain hydrogen enriched synthesis gas by conversion of carbon monoxide, separating hydrogen from the hydrogen enriched synthesis gas to obtain hydrogen and residual gas, and compressing the resulting hydrogen. The separation step is carried out using a palladium membrane in a membrane reactor, at a temperature (T83) of 320-440 degrees C and a pressure (P83) of less than or equal to 1 bar. The compression is carried out in a thermokinetic compressor.    USE - The process is useful for production of hydrogen from hydrocarbides such as natural gas or fossil fuels obtained by vapor reforming, auto-thermal reforming or partial oxidation.    ADVANTAGE - The process ensures automatic, economical, easy and rapid production of hydrogen from hydrocarbides in a systematic manner with increased pressure and temperature and less consumption of energy using a pressure swing adsorption unit.    DETAILED DESCRIPTION - The process comprises generating a hot raw synthesis gas (4), optionally enriching hydrogen in the synthesis gas to obtain hydrogen enriched synthesis gas by conversion of carbon monoxide, separating hydrogen from the hydrogen enriched synthesis gas to obtain hydrogen and residual gas, and compressing the resulting hydrogen. The separation step is carried out using a palladium membrane in a membrane reactor, at a temperature (T83) of 320-440 degrees C and a pressure (P83) of less than or equal to 1 bar. The compression is carried out in a thermokinetic compressor, which simultaneously cools and compresses the synthesis gas to produce a compressed and cold hydrogen using a cold liquid such as water. The membrane reactor produces a hydrogen flow at a pressure (P82) of less than or equal to 1 bar and a temperature (T82) of 500-550 degrees C. The compressed and cold hydrogen is subjected to additional compression. The hydrocarbides are initially desulfurized and optionally pre-reformed. An INDEPENDENT CLAIM is included for an installation for the production of hydrogen gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for production of hydrogen from hydrocarbides.    Hydrosulfurizing reactor (1)    Pre-reformer (2)    Vapor (3)    Synthesis gas (4)    Shift reactor. (5)