NOVELTY - A methanol steam hydrogen generation system comprises solid hydrogen storage container, rapid starting device, liquid storage container (10), raw material transporting device (50), hydrogen preparing device (20), film separating device and hydrogen generating device (200). The hydrogen preparing device comprises heat exchanger, gasification chamber, reforming chamber and membrane separation device set with separating chamber. The separating chamber is set on upper part of reforming chamber.    USE - Methanol steam hydrogen generation system.    ADVANTAGE - The system has fast power generation speed, increases hydrogen manufacture efficiency and power generation efficiency, and does not need electric energy conversion.    DETAILED DESCRIPTION - A methanol steam hydrogen generation system comprises solid hydrogen storage container, rapid starting device, liquid storage container (10), raw material transporting device (50), hydrogen preparing device (20), film separating device and hydrogen generating device (200). The hydrogen preparing device comprises heat exchanger, gasification chamber, reforming chamber and membrane separation device set with separating chamber. The separating chamber is set on upper part of reforming chamber. The solid hydrogen storage container and liquid storage container are connected with hydrogen preparing device. The liquid storage container is stored with liquid methanol and water. The solid hydrogen storage container stores solid hydrogen that converts to gaseous state hydrogen through gasification module. The gaseous state hydrogen generates electricity for hydrogen generation device as starting power supply. The rapid starting device comprises first starting device and second starting device. The first starting device comprises first heating mechanism with first gasification pipeline having inner diameter of 1-2 mm. The methanol is fed into first gasification pipeline through raw material transport device. The other end of first gasification pipeline comprises gasified methanol. The second starting device comprises second gasification pipeline main body provided with reforming chamber. The reforming chamber inner wall is set with heating pipeline placed in catalyst. The methanol and water in the liquid storage container is transported to heat exchanger through raw material transporting device and gasified into gasification chamber. The raw material transporting device provides raw material pressure at 1.1-5 MPa. The methanol steam and water vapor are entered into reforming chamber set with reforming catalyst at reforming chamber lower part and middle part temperature of 350-409 degrees C and reforming chamber upper part temperature of 400-570 degrees C. The reforming chamber and separating chamber are connected through pipeline. The separating chamber has set temperature of 400-570 degrees C. The catalyst comprises 0.6-1.8 wt.% platinum oxide, 1.1-4 wt.% palladium oxide, 6-12 wt.% copper oxide, 3-8 wt.% iron oxide, 8-12 wt.% zinc oxide, 6-40 wt.% rare earth metal oxide and balance transition metal oxide, or copper-bases catalyst comprising 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 generating device is connected with hydrogen preparing device. The hydrogen preparing device is prepared by the direct current power drive electromagnetic heating device (30) for heated reforming chamber and separating chamber. The electromagnetic heating device comprises forming reforming chamber of reforming cylinder body and forming separating chamber separating cylinder body. The first heating coil is set with reforming cylinder body. The second heating coil is set with separating cylinder body, cylinder body, separating temperature sensor, pressure sensor cylinder body and electromagnetic controller. The electromagnetic controller accords to temperature sensor. The pressure sensor controls data from first heating coil and second heating coil electric current. The separating chamber is equipped with membrane separator obtained with hydrogen from the end. The membrane separator separates hydrogen at pressure of more than 1.1 MPa. The membrane separator is porous ceramic surface vacuum plating palladium silver alloy membrane separator, and film layer of palladium-silver alloy. The palladium-silver alloy has 75-78 wt.% palladium and 22-25 wt.% silver. The hydrogen preparing device further comprises electric energy estimation module, hydrogen detection module and electric energy storage module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of methanol steam hydrogen generation system (Drawing includes non-English language text).    Liquid storage container (10)    Hydrogen preparing device (20)    Electromagnetic heating device (30)    Raw material transporting device (50)    Hydrogen generating device (200)