Device and method for preparing synthesis gas under the assistance of high-temperature electrochemical device
A synthesis gas and electrochemical technology, applied in chemical instruments and methods, hydrogen/syngas production, inorganic chemistry, etc., can solve problems such as carbon deposition in the negative electrode, and achieve the effect of reducing carbon emissions and perfectly coupled operation.
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Embodiment 1
[0026] like figure 1As shown, the device for assisting the preparation of synthesis gas according to the high-temperature electrochemical device of the present invention includes a dehydration treatment device and a solid oxide electrolysis cell (Solid Oxide Electrolysis Cell, SOEC for short) system 8, and industrial waste gas 1 is separated from water vapor by the dehydration treatment device 9 After obtaining the remaining gas 1a, the water vapor 9 enters the SOEC system 8 through the first flow valve for electrolysis, the power supply 7 applies current and voltage to the two ends of the electrolytic cell of the SOEC system 8, and the hydrogen and water vapor mixture of the negative electrode of the electrolytic cell passes through The metal Pd membrane separator 17 performs high-temperature separation to obtain hydrogen 10, and the positive electrode obtains oxygen 11. In this embodiment, the flow rate of water vapor 9 entering the SOEC system 8 is 0.1MpaG, and the power su...
Embodiment 2
[0033] The parts that are the same as those in Embodiment 1 will not be repeated, and only the differences will be given below. The flow rate of water vapor 9 entering the SOEC system 8 through the first flow valve is 5MpaG, and the current and voltage applied to both ends of the electrolytic cell of the SOEC system 8 by the power supply 7 are 20A / 1V. The thermal management system 16 provides thermal energy to the electrolytic cells of the SOEC system 8 such that the operating temperature of the electrolytic cells is 850°C. The flow molar ratio of the remaining gas 1a entering the first desulfurization treatment device 2 to the hydrogen 10a is 20:1. The flow molar ratio of natural gas 6 and hydrogen 10b entering the second desulfurization treatment device 5 is 20:1. The high-purity CO entering the first reaction chamber 3 through the second flow valve 2 The flow molar ratio of the gas and the hydrogen 10 entering the first reaction chamber 3 is 3:1, and the high-purity CH en...
Embodiment 3
[0035] The parts that are the same as those in Embodiment 1 will not be repeated, and only the differences will be given below. The flow rate of water vapor 9 entering the SOEC system 8 through the first flow valve is 2MpaG, and the current and voltage applied to both ends of the electrolytic cell of the SOEC system 8 by the power supply 7 are 15A / 0.9V. The thermal management system 16 provides thermal energy to the electrolytic cells of the SOEC system 8 such that the operating temperature of the electrolytic cells is 750°C. The flow molar ratio of the residual gas 1a entering the first desulfurization treatment device 2 to the hydrogen 10a is 17:1. The flow molar ratio of natural gas 6 and hydrogen 10b entering the second desulfurization treatment device 5 is 13:1. The high-purity CO entering the first reaction chamber 3 through the second flow valve 2 The flow molar ratio of the gas to the hydrogen 10 entering the first reaction chamber 3 is 2.3:1, and the high-purity CH ...
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