Research-stage literature benchmark

Restelli ammonia carrier benchmark

A source-backed comparison of ammonia synthesis mass balance, makeup compression and carrier chronology at the operating point reported by Restelli et al.

PASS

Independent acceptance checks

NH₃ produced per kg H₂ must be within 3%; makeup-compression energy must be within 10%. Both pass.

Source

Restelli, F.; Spatolisano, E.; Pellegrini, L. A.; de Angelis, A. R.; Cattaneo, S.; Roccaro, E. (2024), “Detailed techno-economic assessment of ammonia as green H₂ carrier,” International Journal of Hydrogen Energy.

DOI · Author manuscript

Values taken from the paper

InputValueSource location
H₂ feed892.91 kmol/h, 20 bar, 25 °CTable 10 / Section 2
N₂ feed297.64 kmol/h at 8.04 barTable 10
NH₃ product595.27 kmol/hTable 10
Plant availability8,000 h/yTable 2
Sea distance≈2,500 kmSection 2
Ship speed30 km/h (≈16 kn)Section 3.2
Ship gross capacity3,900 m³Section 5
Boil-off at sea0.1%/daySection 3.2
Marine fuel use13 t/daySection 3.2

Generated comparison

MetricPublishedOffshoreLH2DeviationCriterion / basisStatus
Ammonia per kg H₂ feed5.632 kg/kg5.519 kg/kg−2.0%≤3%PASS
Makeup compression0.3119 kWh/kg NH₃0.3186+2.2%≤10%PASS
Ship calls33.33/y33.33/y0.0%Input/chronology checkBY CONSTRUCTION
Fuel per call90.28 t91 t+0.8%Input-derivedBY CONSTRUCTION
Cargo per call2,433 t2,385 t−2.0%DescriptiveREPORTED
Cracker H₂ yield0.1394 kg/kg NH₃0.13940.0%Input-derivedBY CONSTRUCTION

Scope. This is a model-to-model literature benchmark, not measured validation of an operating offshore ammonia supply chain. Published cost boundaries and heat-recovery conventions differ, so cost differences are reported descriptively rather than used to force a pass.

Reproducibility

Source register: python/offshore_lh2/data/carrier_benchmark_references.json. Runner: scripts/run_carrier_benchmarks.py.