NOVELTY - Methanol water vapor hydrogen generation system comprises a solid hydrogen storage container, a rapid starting device, a liquid storage container, a raw material transporting device, a hydrogen preparing device, a film separating device and a hydrogen generation device. The hydrogen preparing device comprises a heat exchanger, a gasification chamber and a membrane separation device. The membrane separation device is set with indoor and the separating chamber is set on upper part of reforming chamber.    USE - Used as methanol water vapor hydrogen generation system.    ADVANTAGE - The system does not require power conversion and has fast power generation speed.    DETAILED DESCRIPTION - Methanol water vapor hydrogen generation system comprises a solid hydrogen storage container, a rapid starting device, a liquid storage container, a raw material transporting device, a hydrogen preparing device, a film separating device and a hydrogen generation device. The hydrogen preparing device comprises a heat exchanger, a gasification chamber and a membrane separation device. The membrane separation device is set with indoor and the separating chamber is set on upper part of reforming chamber. The solid hydrogen storage container and liquid storage container are respectively connected with the hydrogen preparing device. The liquid storage container is meant for storing methyl alcohol and water. The solid state hydrogen storage container is for storing solid hydrogen. The fast starting device is providing starting energy of the solid hydrogen storage container to the hydrogen preparing device. The gasification module is meant for solid state hydrogen conversion to gaseous state hydrogen. The gaseous state hydrogen is for generating electricity from hydrogen generation device. The starting power supply and the fast starting device of hydrogen device comprise first starting device and second starting device. The first starting device comprises the first heating mechanism and the first gasification pipeline. The inner diameter of the first gasification pipeline is 1-2 mm. The first gasification pipeline is tightly wound on the first heating mechanism. The one end of the first gasification pipeline is connected with liquid storage container. The raw material transport device is meant for feeding methanol in the first gasification pipeline. The other end of the first gasification pipeline is connected with the methyl alcohol gasification output and ignition mechanism. The other end of the first gasification pipeline is connected with the methanol gasification output. The methanol output reaches to temperature from combustion point and directly after ignition methanol from the first gasification pipeline output. The second starting device comprises a second gasification pipeline. The main body of the second gasification pipeline is provided with the reforming indoor. The first gasification pipeline and/or the second gasification pipeline input is set with the methanol reforming chamber for heating. The second gasification pipeline utilizes the methanol gasification wall within the reforming chamber. The second gasification pipeline is set with heating pipeline. The heating pipeline is placed with a catalyst. The fast starting device is heated by the heating pipeline for reforming chamber. The methyl alcohol and water in the liquid storage container through are transported to heat exchanger via raw material transporting device, and after heat exchange enter into gasification chamber gasification of the raw material transporting device supply power. The liquid storage container is connected with raw material to transport the hydrogen preparation device. The raw material is transported to raw material transporting device under pressure of 1.1-5 MPa. The hydrogen preparing device makes the prepared hydrogen has the enough pressure, and after gasification of methyl alcohol vapor and water vapor enter into the reforming chamber. The inner chamber is set with a reforming catalyst. The reforming chamber lower part and middle part temperature is 350-409 degrees C. The reforming chamber upper part temperature is 400-570 degrees C. The reforming chamber and separating chamber are connected through pipeline. The temperature set in the separating chamber is 400-570 degrees C. The catalyst comprises platinum oxide, palladium oxide, copper oxide, iron oxide, zinc oxide, rare earth metal oxide or transition metal oxide. The amount of platinum is 0.6-1.8% of the total mass of catalyst. The amount of palladium is 1.1-4% of the total mass of catalyst. The amount of copper is 6-12% of the total mass of catalyst. The amount of iron is 3-8% of the total mass of catalyst. The amount of zinc is 8-20% of the total mass of catalyst. The amount of rare earth metal oxide is 6-40% of the total mass of catalyst and remaining amount of transition metal oxide. The catalyst is a copper-based catalyst, including 3-17 pts. wt. copper oxide, 3-18 pts. wt. zinc oxide, 0.5-3 pts. wt. zirconium oxide, 55-80 pts. wt. aluminum oxide, 1-3 pts. wt. cerium oxide and 1-3 pts. wt. lanthanum oxide. The hydrogen generation device is connected with the hydrogen preparing device. The direct current part of transporting power is to direct current power hydrogen preparing device. The hydrogen preparing device by itself prepare and drives electromagnetic heating device for reforming chamber, and separating chamber for heating. The electromagnetic heating device comprises a reforming cylinder body of reforming chamber and separating cylinder body. The first heating coil is set with the reforming cylinder. The second heating coil is set with the separating cylinder body. The cylinder body, the temperature sensor and pressure sensor are set in the cylinder body. The electromagnetic controller is set with a temperature sensor a pressure sensor and interaction to the data controlling of the first heating coil and the second heating coil. An INDEPENDENT CLAIM is also included for fuel cell system, comprising a gas supply device and the stack, the gas supply deice utilizes compressed gas as the driving force and the required stack gas to electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methanol water vapor hydrogen generation system (Drawing includes non-English language text).