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Rodrigo Gonzalez

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Economic Feasibility of Solar Powered Methanol Production

Methanol Production Powered by Solar Power

The purpose of this project is to design and analyze the economic feasibility of constructing a methanol production facility that is powered by solar-thermal energy.  The solar process used has an advantage over other technologies in that it does not produce tar byproducts, which are costly to remove in non-solar-thermal processes, additionally this process is much more environmentally friendly, compared to the current practice of using fossil fuels for energy uses. 

This project uses a variety of computational methods for calculating the design, instrumentation and process controls of the chemical processes and reactions; costing & sizing of the equipment; solar reactor energy requirements and reactor design; using multivariate data analysis & chemical process optimization software. Economic and financial models for the creation of projections, expected trends and forecasts. The use of industry comparisons, ratio analysis,  scenario/sensitivity and IRR returns analysis, were used to determine overall profitability over a 16-year period.

The project’s objective is an annual production of 56 million gallons of fuel grade methanol.  Seventy acres of 4000 concentrated sun heliostats with a secondary radiation recovery mirror will provide an estimated 553GW-hr annually to the solar reactor.  

The economic feasibility was analyzed over a 16-year period, which includes one year for plant construction.  Total permanent investment (TPI) of capital into the project is approximately $294 MM with a working capital requirement of $31.58 MM.  In order to achieve a 12.5% investor’s rate of return (IRR) the selling price of methanol is calculated to be $1.56/gal.  Returns on investment (ROI) and corresponding payback period are 15.4% and 6.5 years respectively.  The net present value (NPV) at the end of the first year is $203.02 MM.  Given a market price of $1.13/gallon, the process is not economically viable given the current economic conditions.

Access Full Report

 

 

ACKNOWLEDGEMENTS: DR. ALAN WEIMER of the University of Colorado assisted with the solar reactor and chemical process modeling

 

 

Economic Feasibility of Solar Powered Methanol Production

Methanol Production Powered by Solar Power

The purpose of this project is to design and analyze the economic feasibility of constructing a methanol production facility that is powered by solar-thermal energy.  The solar process used has an advantage over other technologies in that it does not produce tar byproducts, which are costly to remove in non-solar-thermal processes, additionally this process is much more environmentally friendly, compared to the current practice of using fossil fuels for energy uses. 

This project uses a variety of computational methods for calculating the design, instrumentation and process controls of the chemical processes and reactions; costing & sizing of the equipment; solar reactor energy requirements and reactor design; using multivariate data analysis & chemical process optimization software. Economic and financial models for the creation of projections, expected trends and forecasts. The use of industry comparisons, ratio analysis,  scenario/sensitivity and IRR returns analysis, were used to determine overall profitability over a 16-year period.

The project’s objective is an annual production of 56 million gallons of fuel grade methanol.  Seventy acres of 4000 concentrated sun heliostats with a secondary radiation recovery mirror will provide an estimated 553GW-hr annually to the solar reactor.  

The economic feasibility was analyzed over a 16-year period, which includes one year for plant construction.  Total permanent investment (TPI) of capital into the project is approximately $294 MM with a working capital requirement of $31.58 MM.  In order to achieve a 12.5% investor’s rate of return (IRR) the selling price of methanol is calculated to be $1.56/gal.  Returns on investment (ROI) and corresponding payback period are 15.4% and 6.5 years respectively.  The net present value (NPV) at the end of the first year is $203.02 MM.  Given a market price of $1.13/gallon, the process is not economically viable given the current economic conditions.

Access Full Report

 

 

ACKNOWLEDGEMENTS: DR. ALAN WEIMER of the University of Colorado assisted with the solar reactor and chemical process modeling

 

 
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