Hydrogen Supply Chains 2018
DOI: 10.1016/b978-0-12-811197-0.00006-3
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Lowering Energy Spending Together With Compression, Storage, and Transportation Costs for Hydrogen Distribution in the Early Market

Abstract: This present paper is dedicated to the optimization of cost and energy consumption for compression, transportation and storage of hydrogen for vehicle refueling in the current hydrogen emerging market. So it considers only small refueling stations (20 to 200 kg/day) and currents costs. It considers 2 cases: the case of a refueling station on the site of the hydrogen production and the case of a production unit supplying hydrogen to several distant refueling stations. In the case of production and distribution … Show more

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Cited by 10 publications
(5 citation statements)
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References 13 publications
(49 reference statements)
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“…However, despite the many interesting and positive aspects that this technology offers, it is necessary to carry out an objective assessment of the environmental impacts associated with its use in different applications. In fact, both the compression and storage steps still represent one of the bottlenecks in moving towards a sustainable carbon-free economy based on hydrogen [131,132].…”
Section: Life Cycle Assessment (Lca) Of Hydrogen Systems Based On Hyd...mentioning
confidence: 99%
“…However, despite the many interesting and positive aspects that this technology offers, it is necessary to carry out an objective assessment of the environmental impacts associated with its use in different applications. In fact, both the compression and storage steps still represent one of the bottlenecks in moving towards a sustainable carbon-free economy based on hydrogen [131,132].…”
Section: Life Cycle Assessment (Lca) Of Hydrogen Systems Based On Hyd...mentioning
confidence: 99%
“…Considering the compression demand, selecting a reasonable gas feeding method could reduce the energy consumption of hydrogen compression. Assuming hydrogen is compressed with isentropic, the temperature of hydrogen outflowed from compressor could be calculated by equation (26). Then, the energy consumption of the compressor can be calculated with equation ( 27), according to the conservation of energy and the formula of hydrogen enthalpy, as for equation ( 10) and (11).…”
Section: Energy Consumptionmentioning
confidence: 99%
“…The total energy consumption in cascade refueling stations has been studied by Rothuizen et al [24] and the result shows that the energy consumption is effected by the number and volume of reservoirs and the pressure within reservoirs. The energy saved with a cascade storage has also been estimated as a function of the number of stages in [25,26] it can reach 16.5% with 3 stages and 20% with 4 stages refueled to 35 MPa. The prediction of temperature of hydrogen flowing from pre-cooler to inlet of vehicle tank could contribute to developing a control strategy of the pre-cooling system [27].…”
Section: Introductionmentioning
confidence: 99%
“…However, when the dry reforming of methane reaction is integrated into a multi-step process, the realization of this reaction at high pressure is sometimes necessary to optimize global energy balance. This is the case for the production of green hydrogen from landfill gas using steam reforming followed by the water-gas-shift reaction (WGSR) and pressure swing adsorption (PSA) steps (Grouset and Ridart 2018). Figure 2 shows the influence of the pressure on thermodynamic equilibrium of a mixture containing initially 1 mol of CH 4 and 1 mol of CO 2 at 800 and 900 °C.…”
Section: Thermodynamics Of Dry Reforming Of Methanementioning
confidence: 99%
“…The selection of operating pressure for the dry reforming of methane at a large scale must be carefully examined taking into account other factors of the global process. It is worth noting that the steam reforming of methane is usually performed at around 900 °C and 15-30 bar with a molar ratio of steam/methane close to 3/1 (Grouset and Ridart 2018).…”
Section: Thermodynamics Of Dry Reforming Of Methanementioning
confidence: 99%