Hydrogen fueling systems and methods
According to aspects, hydrogen fueling systems and methods are provided, including vehicle-to-vehicle communication techniques, hydrogen cooling techniques and/or hydrogen dispenser control techniques that facilitate improving aspects of a hydrogen fueling station. According to one aspect, an annular heat exchanger adapted to operate in a high-pressure and high-UA hydrogen fueling environment is provided.
1 . An annular heat exchanger comprising:
a shell having a coolant inlet and a coolant outlet;
at least one coil comprising tubing concentrically arranged within the shell, the tubing having a wall thickness between 0.03 and 0.08 inches and a length between 30 and 50 feet, the at least one coil further comprising a hydrogen inlet and a hydrogen outlet and having between 20 and 35 turns;
a plurality of fins attached to the at least one coil; and
at least one baffle arranged concentrically within the at least one coil to increase velocity and turbulence of coolant circulated through the shell, the at least one baffle comprising a plurality of pilot holes,
wherein the annular heat exchanger is configured to chill hydrogen gas that is caused to flow through the at least one coil via the hydrogen inlet and the hydrogen outlet via heat exchange with coolant that is caused to circulate through the shell via the coolant inlet and the coolant outlet.
2 . The annular heat exchanger of claim 1 , wherein the tubing has a wall thickness of greater than or equal to 0.04 inches and less than or equal to 0.05 inches.
3 . The annular heat exchanger of claim 1 , wherein the at least one coil comprises nickel alloy tubing, and wherein the plurality of fins comprise a plurality of copper fins attached to the at least one nickel alloy coil using silver or a silver alloy.
4 . The annular heat exchanger of claim 1 , wherein the annular heat exchanger is configured such that coolant circulates through the shell counter to the flow of hydrogen gas through the at least one coil.
5 . The annular heat exchanger of claim 1 , wherein the annular heat exchanger has a heat transfer capacity of between 50 kilowatts and 75 kilowatts.
6 . The annular heat exchanger of claim 5 , wherein the at least one coil comprises a plurality of coils including an outer coil and an inner coil arranged concentrically to the outer coil.
7 . The annular heat exchanger of claim 1 , wherein the annular heat exchanger further comprises an internal portion configured to hold phase-change material in thermal contact with the at least one coil, and wherein the annular heat exchanger is configured to chill hydrogen gas that is caused to flow through the at least one coil via the hydrogen inlet and the hydrogen outlet via heat exchange with the phase-change material when held by the internal portion.
8 . The annular heat exchanger of claim 1 , wherein:
the coolant inlet is coupled to receive chilled coolant from a coolant reservoir and the coolant outlet is coupled to return heated coolant to the coolant reservoir, and
wherein:
the hydrogen inlet is coupled to receive hydrogen gas from a hydrogen gas source located at a fueling station, and the hydrogen outlet is fluidly coupled to at least one dispenser to provide chilled hydrogen for dispensing via at one least one dispenser nozzle.
9 . The annular heat exchanger of claim 1 , wherein:
the coolant inlet is coupled to receive chilled coolant from a coolant reservoir and the coolant outlet is coupled to return heated coolant to the coolant reservoir, and
wherein:
the hydrogen inlet is coupled to receive chilled hydrogen gas from another heat exchanger, and the hydrogen outlet is coupled to at least one dispenser to provide chilled hydrogen for dispensing via at one least one dispenser nozzle.
10 . The annular heat exchanger of claim 1 , wherein the tubing has a wall thickness between 0.03 and 0.06.
11 . An annular heat exchanger comprising:
a shell having a coolant inlet and a coolant outlet;
at least one coil comprising nickel alloy tubing concentrically arranged within the shell, the at least one coil having a hydrogen inlet and a hydrogen outlet; and
a plurality of copper fins brazed to the at least one nickel alloy coil using silver or a silver alloy, wherein the annular heat exchanger is configured to chill hydrogen gas that is caused to flow through the at least one coil via the hydrogen inlet and the hydrogen outlet by heat exchange with coolant that is caused to circulate through the shell via the coolant inlet and the coolant outlet; and
at least one baffle arranged concentrically within the at least one coil to increase velocity and turbulence of coolant circulated through the shell, the at least one baffle comprising a plurality of pilot holes.
12 . The annular heat exchange of claim 11 , wherein the tubing has a length between 30 and 50 feet.
13 . The annular heat exchanger of claim 12 , wherein the at least one coil has between 20 and 35 turns.
14 . The annular heat of claim 11 , wherein the annular heat exchanger has a heat transfer capacity of between 50 kilowatts and 75 kilowatts.
15 . The annular heat of claim 11 , wherein the annular heat exchanger has a heat transfer capacity of 75 kilowatts.
16 . The annular heat exchanger of claim 15 , wherein the at least one coil comprises a plurality of coils including an outer coil and an inner coil arranged concentrically to the outer coil.
17 . The annular heat exchanger of claim 11 , wherein:
the coolant inlet is coupled to receive chilled coolant from a coolant reservoir and the coolant outlet is coupled to return heated coolant to the coolant reservoir, and
wherein:
the hydrogen inlet is coupled to receive hydrogen gas from a hydrogen gas source located at a fueling station, and the hydrogen outlet is fluidly coupled to at least one dispenser to provide chilled hydrogen for dispensing via at one least one dispenser nozzle.
18 . The annular heat exchanger of claim 11 , wherein:
the coolant inlet is coupled to receive chilled coolant from a coolant reservoir and the coolant outlet is coupled to return heated coolant to the coolant reservoir, and
wherein:
the hydrogen inlet is coupled to receive chilled hydrogen gas from another heat exchanger, and the hydrogen outlet is coupled to at least one dispenser to provide chilled hydrogen for dispensing via at one least one dispenser nozzle.
19 . The annular heat exchanger of claim 11 , wherein the tubing has a wall thickness between 0.03 and 0.06.