Table 2: Technical assumptions.

ParameterInput valueUnitsSource

Working capital15%%[6]
Project contingency$61,490,157 $Calculated from data in [14]
Working capital expenditure$55,341,142 $Calculated from data in [14]
Total capital investment $429,000,000 $[6]
Land$4,717,915 $Calculated from data in [14]
Nominal fixed capital Investment$394,799,061 $Calculated from data in [14]
Plant operation/online time 329.5days/yrCalculated from data in [6]
Startup production rate75%%[14]
Startup variable expense87.5%%[14]
Input capacity2,000MT/day[6]
Annual feedstock use659,000MT/yr[6]
Bio-oil yield63.00%Mg/Mg[6]
Gas conversion rate21.0%Mg/Mg bio-oil[14]
Diesel conversion rate21.0%Mg/Mg bio-oil[14]
Feedstock cost83$/MT[6]
Catalyst replacement costs1,767,000$/yr[14]
Electricity produced223,000,000kwh/yr[6]
Electricity use11,490kw/hour[14]
Electricity price$0.0540 $/kwh[14]
Hydrogen use2,041kg/hour[14]
Hydrogen price$1.33 $/kg[6]