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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2018, Vol. 12 Issue (4): 598-618   https://doi.org/10.1007/s11705-018-1752-5
  本期目录
Techno-economic evaluation of a biogas-based oxidative coupling of methane process for ethylene production
Alberto T. Penteado(), Mijin Kim, Hamid R. Godini, Erik Esche, Jens-Uwe Repke
Process Dynamics and Operations Group, Technische Universität Berlin, D-10623 Berlin, Germany
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Abstract

This contribution is a preliminary techno-economic assessment of a biogas-based oxidative coupling of methane (OCM) process. Biogas is frequently utilized as a renewable energy source within small scale combined heat and power plants or as a natural gas substitute. The activation of methane also enables its utilization as a feedstock to produce chemicals. In this sense, the OCM process allows for the direct conversion of methane into ethylene, which is a major building block for the chemical and polymer industries. Biogas resulting from the anaerobic digestion of vinasse, a liquid effluent from bioethanol industry, is treated for contaminant removal and its methane content is converted into ethylene, which is then purified as the main product. The biogas cleaning process is assessed based on literature data, while an experimentally validated simulation model is used to assess the OCM process. A techno-economic evaluation is then performed through a Monte Carlo simulation, wherein uncertain parameters take random values between reasonable bounds. The net present value results positive in 74% of the cases, indicating that the project is profitable under a wide range of scenarios. Some performance improvement opportunities have been identified and highlighted to guide future studies in the topic.

Key wordsbiogas conversion    ethylene production    oxidative coupling of methane    feasibility study
收稿日期: 2018-02-28      出版日期: 2019-01-03
Corresponding Author(s): Alberto T. Penteado   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2018, 12(4): 598-618.
Alberto T. Penteado, Mijin Kim, Hamid R. Godini, Erik Esche, Jens-Uwe Repke. Techno-economic evaluation of a biogas-based oxidative coupling of methane process for ethylene production. Front. Chem. Sci. Eng., 2018, 12(4): 598-618.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-018-1752-5
https://academic.hep.com.cn/fcse/CN/Y2018/V12/I4/598
Flow /(Nm3?h–1) 2200
Pressure /bar 1.6
Temperature /°C 30
CH4 mole fraction 0.70
CO2 mole fraction 0.30
Tab.1  
Desulfurization method Iron chloride dosing Biological scrubbing Adsorption
Achievable H2S outlet concentration /ppmv 100 50 0.1
Specific removal cost /EUR per kg H2S 0.85 0.20 3.85
Tab.2  
Kij H2 N2 O2 CH4 C2H4 C2H6 CO CO2 H2O
H2 X X X X X X
N2 X X X X X X
O2 X
CH4 X X X X
C2H4 X X X
C2H6 X X
CO
CO2 X
H2O
Tab.3  
Fig.1  
Fig.2  
Fig.3  
Fig.4  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
Fig.10  
Fig.11  
Item Membrane area per module /m2 Number of modules CO2 removal C2H4 recovery CO2 mole fraction
Inlet Outlet
1st stage 7.5 50 67.6% 89.5% 0.227 0.093
2nd stage 8.0 11 96.9% 72.5% 0.732 0.929
Overall 61 66.9% 96.8% 0.234 0.093
Tab.4  
Fig.12  
Fig.13  
Fig.14  
Fig.15  
Fig.16  
Fig.17  
Fig.18  
Item Description Lower bound Reference value Upper bound Units
Treated biogas ≤0.1 ppm H2S 0 0.002 0.028 USD/Nm3
Liquid oxygen ≥95 mol-% 0.05 0.06 0.074 USD/Nm3
Ethylene Polymer grade 700 1000 1400 USD/t
Ethane Refinery grade 46.74 68.61 96.06 USD/t
Carbon dioxide ≥92 mol-% 3.00 4.00 5.00 USD/t
Electricity 0.05 0.0775 0.09 USD/kWh
Medium pressure steam 8.87 bar 1.76×10–6 2.20×10–6 2.54×10–6 USD/kJ
Low pressure steam 2.31 bar 1.52×10–6 1.90×10–6 2.28×10–6 USD/kJ
Refrigeration 168 K 6.0×10–6 8.5×10–6 11.0×10–6 USD/kJ
Cooling water 293–298 K 1.70×10–7 2.12×10–7 2.54×10–7 USD/kJ
Operation & maintenance 38675 55250 71825 USD/a
Tab.5  
Fig.19  
Item Fraction of Lower bound Upper bound
Direct costs
**Installation Plant equipment cost 0.01 0.06
**Pipelines Plant equipment cost 0.05 0.15
**Sensors & automation Plant equipment cost 0.05 0.15
Electric Plant equipment cost 0.05 0.15
Service facilities Plant equipment cost 0.70 1.00
Land and terrain Plant equipment cost 0 0.10
Civil engineering Plant equipment cost 0.15 0.90
Indirect costs
Engineering Plant equipment cost 0.25 0.75
Construction site Direct cost 0.10 0.15
Contingency Direct cost 0.08 0.25
Other costs
Start-up Fixed capital investment 0.05 0.12
Working capital Fixed capital investment 0.10 0.20
Tab.6  
Item Lower bound Upper bound
Inflation rate (ri) 0.02 0.09
Real escalation rate (rR) 0.03 0.06
Nominal escalation rate (rN) (1+ri) ? (1+rR) – 1
Effective interest rate (ieff) ri 0.15
Total income tax 0.10 0.30
Operation factor 0.85 0.98
Yearly operating hours 7446 h 8585 h
Plant operating life 30 years
Tab.7  
Fig.20  
Fig.21  
Fig.22  
Fig.23  
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