Abstract
BackgroundThe dramatic increase in emissions of greenhouse gases (GHGs) has led to an irreversible effect on the ecosystem, which in turn caused significant harm to human beings and other species. Exploring innovative and effective approaches to neutralizing GHGs is urgently needed. Considering the advancement of synthetic biology and the bioconversion process, C1-utilizing cell factories (CUCFs) have been modified to be able to effectively convert C1-gases includes biogas, natural gas, and carbon dioxide (CO2) into chemicals or fuels via biological routes, which greatly facilitates the inedible carbon sources used in biomanufacturing, increases the potential value of GHGs and meanwhile reduces the GHG emissions. Process design and resultsEven though the current experimental results are satisfactory in lab-scale research, the evaluation of economic feasibility as well as applications of CUCFs in industrial-scale still need to be analyzed. This study designed three scenarios of CUCFs-based conversion of biogas, natural gas, and CO2 into isobutanol, the detailed techno-economic analyses of these scenarios were conducted with the comparisons of capital cost, operating cost, and minimum isobutanol selling price (MISP). Results revealed that direct bio-conversion of CO2 by CUCFs into isobutanol exhibited the best economic performance with a MISP of $1.38/kg isobutanol. The single sensitivity analysis showed that the gas utilization rate, flow rate, and CO2 cost are the three most significant economic-driving forces on MISP of CO2-derived biological isobutanol. Multiple-point sensitivity analysis presented that the MISP for the long-term case can be as low as 0.99 $/kg with using ideal targets. ConclusionsOur findings provide a comprehensive assessment of bio-conversion of C1-gases via CUCFs to isobutanol in terms of the bioprocess design, mass/energy calculation, capital investment, operating expense, sensitivity analysis, and environmental impact. It is expected that this study may lead to the paradigm shift in isobutanol synthesis with C1-gases as substrates.