TECHNOLOGY FOCUS - INSTRUMENTATION AND TESTING - Preferred Components: 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. The raw material transporting device supply pressure of 0.15-5 MPa so that the hydrogen obtained by the hydrogen production device has sufficient pressure. The hydrogen production device produces part of the hydrogen and/or residual gas by burning hydrogen to maintain the operation of the hydrogen production device after the hydrogen production device start preparing hydrogen. The hydrogen prepared by the hydrogen production device is transported to the membrane separation device for separation. The pressure difference between the inside and outside of the membrane separation device for separating the hydrogen gas is not less than 0.7 MPa. The membrane separation device is set with porous ceramic surface of vacuum palladium silver alloy plating. The plating film layer is palladium silver alloy, comprising 75-78 wt.% palladium and 22-25 wt.% silver. The hydrogen sub-system is obtained by hydrogen transfer line real time transmission to the hydrogen generation system. The transmission line has a pressure regulator subsystem for adjusting transmission pipeline pressure. The hydrogen generation system utilizes hydrogen to obtain hydrogen generation sub-system. The pressure regulator system comprises a microprocessor, a gas pressure sensor, a controller valve, an air outlet valve and an air outlet pipeline. The pressure sensor is set with gas transmission pipeline so as to send the inductive transmission pipeline pressure data and pressure sensor data to the microprocessor. The microprocessor receives the air pressure data from the gas pressure sensor to set the threshold value area for comparison. The microprocessor control valve controller opens the valve set time if the received pressure data is greater than or equal to the maximum pressure range of the set threshold value so that the opens the valve set time so that the transmission line is set in the range of atmospheric pressure while one end of the air outlet pipeline is connected to the gas outlet valve and the other end is connected with the hydrogen production sub-system. The heating equipment to be heated by burning the hydrogen sub-system. The microprocessor controls the hydrogen sub-system to accelerate the rate of conveying raw materials if the received pressure data is less than or equal to the minimum set threshold value. The collection sub-system is connected with the exhaust outlet channel of the hydrogen generation system. The hydrogen, oxygen and water are separately collected from the exhaust gas. The collected hydrogen and oxygen is used for hydrogen production subsystem and/or hydrogen generation system and collected water as a raw material to produce hydrogen subsystem for recycling use. The collecting sub-system comprises a hydroxide separator, a hydrogen water separator, hydrogen check valve, oxygen water separator and oxygen check valve. The hydrogen is separated from the oxygen, hydrogen is separated from water and the oxygen is separated from the water. The hydrogen generation system comprises fuel cell comprising number of sub fuel cell module and each of sub fuel cell modules comprises at least one super-capacitor. The conveying tool further comprises at least one second electric motor connected to an energy storage unit and a kinetic energy conversion unit. The energy conversion unit converts the braking energy into an electrical energy which is stored in the energy storage unit providing electrical energy to the second electric motor which is further connected with the hydrogen generation system. The hydrogen generation system supplies energy to the second electric motor. The conveying tool further comprises road environment sensor module, allocating database and hydrogen distribution module. The hydrogen distribution module is respectively connected with the road environment sensor module for sensing data and allocating database for distribution of electric motor corresponding to the hydrogen gas. The road environment sensor module for sensing road congestion information and floor flatness information. The road congestion information is determined based on conveying tool real time speed acceleration, deceleration frequency, and parking time. The floor flatness information is determined based on angle sensor set on the conveying tool chassis. The number of data stored in the database allocation table, the data recorded in the table for each road congestion information, the floor flatness information of the corresponding electric motor and the second electric motor hydrogen distribution data. The electric motor and the second electric motor for driving the front wheel and other for driving the back wheels. The tool further comprises methanol steam reforming hydrogen production system for preparing hydrogen from methanol. The hydrogen is plated by palladium silver alloy membrane separation device, to obtain high-purity hydrogen. The hydrogen produced by hydrogen generation system generates electricity supplied to the electric motor. The catalyst is copper based catalyst, comprising 2-20 pts. wt. copper oxide, 2-20 pts. wt. zinc oxide, 0.1-5 pts. wt. zirconium oxide, 45-95 pts. wt. aluminum oxide, 0-5 pts. wt. cerium oxide and 0-5 pts. wt. lanthanum oxide.