Method for cogenerating activated carbon and hydrogen by coal char gasification and methane reforming coupling technology
A coal char gasification and activated carbon technology, which is applied in chemical instruments and methods, bulk chemical production, hydrogen/synthesis gas production, etc., can solve problems that have not been seen yet, achieve hydrogen yield, and strengthen gasification reactivity , a wide range of effects
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Embodiment 1
[0029] The semi-coke from Yulin in northern Shaanxi (the bulk semi-coke from Wuzhou Coal Chemical Co., Ltd., Shenmu County, the same below) was taken as the sample raw material of coal coke, which was crushed and sieved into particles of 70-150 μm. According to the mass ratio of 1:1, weigh the coal char particles and Na 2 CO 3 (analytical pure), and simultaneously added to the water-ethanol binary solution (the volume ratio of water and ethanol is 5:1), stirred and mixed for 10 h, and then vacuum-dried to form mixture A.
[0030] Then, the mixture A with a mass of 5g is used as a catalyst for the steam reforming reaction of methane, and reacted in two traditional parallel fixed-bed reactors, and the conditions for regulating the steam reforming reaction of methane are: the temperature range is 900°C , the pressure is 0.1MPa, the molar ratio of methane to water vapor is 1:5, and the methane flow rate is 25mL / min. Collect the gas generated by the steam reforming of methane to ...
Embodiment 2
[0032] The semi-coke from Yulin in northern Shaanxi was taken as the sample raw material of coal coke, which was crushed and sieved into particles of 180-300 μm. According to the mass ratio of 1:5, weigh the coal char particles and KOH (analytical grade, the same below), and add them into the water-ethanol binary solution (the volume ratio of water and ethanol is 5:1) at the same time, and stir and mix After 10 h, mixture A was formed by drying in vacuo. Then, the mixture A with a mass of 5 g is used as a catalyst for the steam reforming reaction of methane, and reacted in two traditional parallel fixed-bed reactors, and the conditions for regulating the steam reforming reaction of methane are: the temperature range is 850 ° C , the pressure is 2.0MPa, the molar ratio of methane to water vapor is 1:4, and the flow rate of methane is 25mL / min. Collect the gas generated by the steam reforming of methane to obtain hydrogen-rich gas; under this condition, within 4 hours of reacti...
Embodiment 3
[0034] The semi-coke from Yulin in northern Shaanxi was taken as the sample raw material of coal coke, which was crushed and sieved into particles of 70-150 μm. According to the mass ratio of 1:10, weigh coal char particles and CaO (analytical pure, the same below), carry out mechanical stirring and grinding, so that the two are fully mixed to form mixture A. Then, the mixture A with a mass of 5 g is used as a catalyst for the steam reforming reaction of methane, and reacted in three traditional parallel fixed-bed reactors, and the conditions for regulating the steam reforming reaction of methane are: the temperature range is 650°C , the pressure is 1.0MPa, the molar ratio of methane to water vapor is 1:4, and the methane flow rate is 25mL / min. Collect the gas generated by the steam reforming of methane to obtain hydrogen-rich gas; under this condition, within 4 hours of reaction, the methane conversion rate is 76.83% to 83.68%, and the hydrogen gas fraction in the reaction ga...
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