NOVELTY - Alcoholic hydrogen complex power conveying tool comprises sequentially connected methanol and hydrogen production systems, hydrogen generation system and electric motor. The methanol and hydrogen production systems further comprises sequentially connected hydrogen production subsystem including a solid hydrogen storage container, a liquid storage container, a raw material transporting device, a fast starting device, hydrogen preparing device and film separating device, an air pressure regulating sub-system, hydrogen generation system, collection subsystem and utilization subsystem.    USE - Used as alcoholic hydrogen complex power conveying tool.    ADVANTAGE - The alcoholic hydrogen complex power conveying tool: utilizes methanol as a means of transportation energy; solves energy crisis; reduces vehicle emission; hydrogen production device has small volume, uses the unique palladium membrane purifying catalyst; can quickly prepare hydrogen; is stable; produces high purity product; and provides stable input energy for transporting.    DETAILED DESCRIPTION - Alcoholic hydrogen complex power converying tool comprises sequentially connected methanol and hydrogen production systems, hydrogen generation system and electric motor. The methanol and hydrogen production systems further comprises sequentially connected a hydrogen production subsystem, an air pressure regulating sub-system, hydrogen generation system, collection subsystem and utilization subsystem. The hydrogen production subsystem uses aqueous methanol for preparing hydrogen. The hydrogen production subsystem comprises a solid hydrogen storage container, a liquid storage container, a raw material transporting device, a fast starting device, hydrogen preparing device and film separating device. The hydrogen preparing device comprises a heat exchanger, a gasification chamber, a reforming chamber, a membrane separation device provided in a separating chamber, the separating chamber is set within the reforming chamber. The solid hydrogen storage container and the liquid storage container are respectively connected with the hydrogen preparing device. The liquid storage container is stored with liquid methanol and water. The fast starting device is for providing starting energy to the hydrogen preparing device. The fast starting device comprises the first starting device and the second starting device. The first starting device comprises the first heating mechanism and the first gasification pipeline having an inner diameter of 1-2 mm is tightly wound on the first heating mechanism. The one end of the first gasification pipeline is connected with the liquid storage container. The methanol is subjected through the raw material transporting device into the first gasification pipeline. The methanol is vaporized by the output of the other end of the first gasification pipeline, ignition and combustion through the ignition mechanism and/or the vaporization of the methanol by the other end of the output of the first gasification pipeline and making the output methanol temperature reach to the combustion point, spontaneous ignition of the methanol from the first gasification pipeline output. The second starting device comprises the second gasification pipeline having gasification body within the reforming chamber. The methanol of the first gasification pipeline and/or the second gasification pipeline is vaporized by heating the reforming chamber while heating the second gasification pipeline. The second gasification pipeline is for methanol vaporization. The interior wall of the reforming chamber in the second gasification pipeline is set with heating pipeline placed within the catalyst. The fast starting device is for heating by the heating pipeline of the reforming chamber. The hydrogen production system starts up and supplies the necessary energy needed to operate the hydrogen preparing device, to obtain the hydrogen. The initial start energy of the fast starting device is from a number of solar energy starting modules. Solar energy startup module comprises sequentially connected solar panels, solar power conversion circuits and solar cells. Solar energy start-up module is to provide power to the first heating mechanism and/or the initial start energy of fast start device for manual electric generator. The energy of the electric generator is stored in the battery power. The catalyst comprises 1.1-4 wt.% palladium oxide, 0.6-1.8 wt.% platinum oxide, 6-12 wt.% copper oxide, 3-8 wt.% iron oxide, 8-20 wt.% zinc oxide, 6-40 wt.% rare earth metal oxide and the remaining is transition metal oxide and/or the catalyst is a copper based 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, 1-3 pts. wt. lanthanum oxide. The stored solid hydrogen of a solid hydrogen storage container is converted to gaseous hydrogen through gasification by combustion heat providing start-up heat as activating energy for the hydrogen preparing device, when the hydrogen production system is started-up. The methanol and water in the liquid storage container through raw material transporting device is transported to the heat exchanger, gasification by gasification chamber, transferring methanol vapor and water vapor into the reforming chamber. The temperature of the inner chamber set with reforming catalyst, the lower part and middle part of the reforming chamber is 300-420 degrees C and the upper part of the reforming chamber is 400-570 degrees C. The reforming chamber is connected through connecting pipeline to the separating chamber. The connecting pipeline is all and/or partially set up on the upper part of the reforming chamber. The high temperature heated gas of the reforming chamber upper part is used for continuously heating reforming chamber from the output gas. The connection pipeline is used as buffer between the reforming chamber and the separation chamber so that the temperature of the separation chamber and the output gas from the reforming chamber is at and/or nearest to same. The temperature of the separation chamber is 350-570 degrees C. The inner separation chamber is set with membrane separator, to obtain the hydrogen gas from the end of the membrane separator. The raw material transporting device supplies power to the liquid storage container and the transport raw materials to the hydrogen production device.