Silicon powder composition, method, reactor and device for producing hydrogen
A technology of reaction device and composition, applied in the field of silicon powder composition, to achieve the effect of improving practicability, stable reaction, stable and controllable reaction
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Embodiment 1
[0058] 1.05g silicon powder (about 3 / 80MOL), 2.1g CaO (about 3 / 80MOL), 0.5g NaAlO 2 After uniform mixing, a 10ml syringe is filled with a scale indicating that the volume of the composition is approximately 4.5cc.
[0059] The heater was used for the first 15 minutes, after which the heater was removed and an insulating cover was used instead.
[0060] The hydrogen production is recorded every 30 minutes, which are 130cc\160cc\210cc\220cc\210cc\210cc\180cc\130cc in sequence. At this time, the machine stops due to a significant drop in speed.
[0061] The cumulative hydrogen production is 1450cc, and the theoretically calculated reaction adequacy is 86.3%.
Embodiment 2
[0063] 1.05g silicon powder (about 3 / 80MOL), 2.1g CaO (about 3 / 80MOL), 0.5g Na 2 SiO 3 After uniform mixing, a 10ml syringe is filled with a scale indicating that the volume of the composition is approximately 4.0cc.
[0064] The heater was used for the first 15 minutes, after which the heater was removed and an insulating cover was used instead.
[0065] The hydrogen production volume is recorded every 30 minutes, which is 80cc\140cc\220cc\230cc\230cc\180cc\200cc\130cc in sequence. At this time, the machine stops due to a significant drop in speed.
[0066] The cumulative hydrogen production is 1410cc, and the theoretically calculated reaction adequacy is 83.9%.
Embodiment 3
[0068] 1.05g silicon powder (about 3 / 80MOL), 2.1g CaO (about 3 / 80MOL), 0.5g Na 2 CO 3 After uniform mixing, a 10ml syringe is filled with a scale indicating that the volume of the composition is approximately 4.0cc.
[0069] The heater was used for the first 15 minutes, after which the heater was removed and an insulating cover was used instead.
[0070] The hydrogen production volume is recorded every 30 minutes, which is 80cc\160cc\240cc\240cc\240cc\220cc\190cc\70cc in sequence. At this time, the machine stops due to a significant drop in speed.
[0071] The cumulative hydrogen production is 1440cc, and the theoretically calculated reaction adequacy is 85.7%.
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