Plant Operation
Fixed Process Assumptions
Calibrated from DWSIM Gibbs reactor model
SMR reformer temperature
900 °C
SMR reformer pressure
3 bar
MeOH reactor temperature
251 / 231 °C
MeOH reactor pressure
55 bar
MeOH yield model
COx conversion limited
Operating Costs
CAPEX Factors
Fixed CAPEX Assumptions (Turton 2018)
CEPCI base year
2001 (index 397)
CEPCI target year
2025 (index 820)
Contingency factor
18% (×1.18)
Fixed O&M fraction
5% of CAPEX/yr
MeOH catalyst life
3 years
Syngas Stoich. Number
—
—
SN = (H₂−CO₂)/(CO+CO₂)
H₂/COx ratio: —
MeOH Production
—
ton / year
Total Cost (LCOM)
€—
per ton MeOH
Detailed Economic Analysis
Equipment Summary
SMR Reactor
Diameter—
Length—
Catalyst bed—
MeOH Reactor 1
Diameter—
Length—
MeOH Reactor 2
Diameter—
Length—
Total CAPEX (Denmark)
Installed cost—
Incl. 18% contingency
+ location factor 1.54×
⚠️
Accuracy note: This calculator uses DWSIM-calibrated yield and energy factors (5500 kg/h reference case, 60% CH₄, no H₂).
Accuracy is approximately ±10–15% vs full DWSIM simulation for the base case; larger deviations expected at compositions far from 60% CH₄ or with H₂ co-feed.
CAPEX correlations are Turton 2018 (±30% inherent uncertainty). Not suitable for investment decisions without full process simulation.