Heating devices in proton exchange membrane fuel cell stacks
A fuel cell stack and proton exchange membrane technology, which is applied in the fields of fuel cell heat exchange, fuel cell, fuel cell additives, etc., can solve the problems of slow start of proton exchange membrane fuel cell, influence of fuel cell startup, and startup failure, etc. To achieve the effect of good heating effect, compact and ingenious structure, and short cold start time
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Embodiment 1
[0032] Environmental conditions: specific heat of graphite 710 J / (kg K); calorific value of hydrogen 1.4×10 8 J / kg; battery stack mass 200kg; ambient temperature -30°C; temperature after heating up 0°C; heat dissipation rate 5%.
[0033] Hydrogen consumption = (temperature after heating - ambient temperature) × specific heat of graphite × mass of battery stack ÷ calorific value of hydrogen × (1+ heat dissipation rate).
[0034] Hydrogen consumption=30×710×200÷(1.4×10 8 )×1.05=0.032kg.
Embodiment 2
[0036] Environmental conditions: ambient temperature -20°C; temperature after heating up 0°C; hydrogen consumption flow rate 0.048kg / min; graphite specific heat 710 J / (kg K); hydrogen calorific value 1.4×10 8 J / kg; battery stack mass 200kg; heat dissipation rate 5%.
[0037] Among them: the hydrogen consumption flow is determined according to the hydrogen supply capacity of the hydrogen supply system for the fuel cell system, and the working hydrogen consumption under the rated power of the fuel cell is determined, taking a 36kw fuel cell as an example.
[0038] Hydrogen consumption = (temperature after heating - ambient temperature) × specific heat of graphite × mass of battery stack ÷ calorific value of hydrogen × (1+ heat dissipation rate).
[0039] Hydrogen consumption=20×710×200÷(1.4×10 8 )×1.05=0.022kg.
[0040] Cold start time = hydrogen consumption ÷ hydrogen flow.
[0041] Cold start time=0.022÷0.048=0.46 min=28 s.
[0042] That is: from the ambient temperature -...
Embodiment 3
[0044] Environmental conditions: ambient temperature -10°C; temperature after heating up 0°C; hydrogen consumption flow rate 0.048kg / min; graphite specific heat 710 J / (kg K); hydrogen calorific value 1.4×10 8 J / kg; battery stack mass 200kg; heat dissipation rate 5%.
[0045] Among them: the hydrogen consumption flow is determined according to the hydrogen supply capacity of the hydrogen supply system for the fuel cell system, and the working hydrogen consumption under the rated power of the fuel cell is determined, taking a 36kw fuel cell as an example.
[0046] Hydrogen consumption = (temperature after heating - ambient temperature) × specific heat of graphite × mass of battery stack ÷ calorific value of hydrogen × (1+ heat dissipation rate).
[0047] Hydrogen consumption=10×710×200÷(1.4×10 8 )×1.05=0.011kg.
[0048] Cold start time = hydrogen consumption ÷ hydrogen flow.
[0049] Cold start time=0.011÷0.048=0.23 min=14 s.
[0050] That is: from the ambient temperature -...
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