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Table 5 Parameters and financial assumptions for the techno-economic study

From: Economic feasibility of gasoline production from lignocellulosic wastes in Hong Kong

Items

Estimation Assumption

Plant Location

Hong Kong

Design Capacity

100,00 kg of wood per batch

Feedstock

Ash Wood

Main Products

Bio-gasoline

Capital Cost

Capital cost = FCI + working capital

Direct Cost (DC)

 Purchase Cost (PC)

Listed Equipment Purchase Cost

 Unlisted Equipment Cost

0.50 x PC

 Piping

0.30 x PC

 Instrumentation

0.40 x PC

 Insulation

0.03 x PC

 Electrical Facilities

0.10 x PC

 Buildings

0.15 x PC

 Yard Improvement

0.12 x PC

 Auxiliary Facilities

0.25 x PC

Indirect Cost (IC)

 Engineering

0.25 x DC

 Construction

0.34 x DC

 Contractor’s Fee

0.05 x (DC + IC)

 Contingency

0.10 x (DC + IC)

 Fixed Capital Investment (FCI)

FCI = DC + IC

 Working Capital

0.08 x FCI

 Start-up cost

5% DFC

 Annual operating cost

Annual operating cost - total viable production costs + fixed charges + plant overhead

Total variable production costs

 Raw materials

From Mass Balance

 Labour-dependant

Hourly rate RMB ¥ 32.10

 Utilities cost

Steam: RMB ¥ 81/MT

 

Steam (high P): RMB ¥ 94/MT

 

CaCl2: RMB ¥ 530/MT

 

Glycol: RMB ¥ 235/MT

 

Freon: RMB ¥ 1.01/MT

 

Std Power: RMB ¥ 0.82/MT

 Chemical Waste Disposal

RMB ¥ 2984/MT

 Industrial Wastewater Treatment

RMB ¥ 502/MT (Sent offsite for treatment)

 Transportation

Facility Owned Truck

 Quantity Dependant Cost

RMB ¥ 24.3/ m3

 Quantity and Distance Dependent Cost

RMB ¥ 0.25/ m3km

 Gas flaring

RMB ¥ 60/MT

 Equipment Maintenance & Repair

6% of DFC

 Laboratory cost for QC and QA

15% of Total Labour Cost

Fixed charges

 Depreciation (10-year straight line)

5% DFC

 Insurance

0.1% DFC

 Local Taxes

0.2% DFC

 Factory Expenses

0.5% DFC

 Laboratory, Quality Control & Quality Assurance Cost

10% TLC