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Using liquid feedstock in combination with steam reforming technology allows for operating the system at high pressures of 12 bars resulting in significantly reduced system size and hydrogen production costs. With the envisaged process concept a system efficiency (LHV(H2) / LHV(fuel) of higher than 70 % can be achieved. The expected production costs per kg H2 are expected to be lower than 4.00 per kg of hydrogen. NEMESIS 2 study shows feasibility of direct steam reforming of diesel.

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    Using liquid feedstock in combination with steam reforming technology allows for operating the system at high pressures of 12 bars resulting in significantly reduced system size and hydrogen production costs. With the envisaged process concept a system efficiency (LHV(H2) / LHV(fuel) of higher than 70 % can be achieved. The expected production costs per kg H2 are expected to be lower than 4.00 per kg of hydrogen. NEMESIS 2 study shows feasibility of direct steam reforming of diesel.
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    Using liquid feedstock in combination with steam reforming technology allows for operating the system at high pressures of 12 bars resulting in significantly reduced system size and hydrogen production costs. With the envisaged process concept a system efficiency LHVH2 LHVfuel of higher than 70 can be achieved. The expected production costs per kg H2 are expected to be lower than 4.00 per kg of hydrogen. NEMESIS 2 study shows feasibility of direct steam reforming of diesel.
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    Using liquid feedstock in combination with steam reforming technology allows for operating the system at high pressures of 12 bars resulting in significantly reduced system size and hydrogen production costs. With the envisaged process concept a system efficiency (LHV(H2) / LHV(fuel) of higher than 70 % can be achieved. The expected production costs per kg H2 are expected to be lower than 4.00 per kg of hydrogen. NEMESIS 2 study shows feasibility of direct steam reforming of diesel.

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