(558g) Design and Intensification of Integrated Carbon Capture and Conversion to Chemicals
We propose one such intensified process exploiting an integrated adsorption-purge-reaction system2, which operates cyclically involving CO2 adsorption from flue gas in the first step, followed by purging due to methane rich feed in the second step. The desorption of CO2 from the column is achieved by a concentration driving force difference brought about by introduction of a second feed with a composition very different from that of flue gas. The N2 separated from the column is vented out, while the CH4/CO2 purge mixture becomes the feed for dry reforming of CO2 in the subsequent reactor section. A variety of methane rich feeds such as natural gas, fuel gas, unused methane, biogas etc. can be used by the process. The novel aspect of the process is the elimination of pressure and temperature swings employed in every cycle in conventional standalone CO2 capture and integrating it with reactor feed pre-mixing which results in reduction in the overall cost of CO2 capture and utilization. The process is integrated with existing CO2 capture and utilization technologies.
The entire process is simulated using high-fidelity non-linear algebraic partial differential equation (NAPDE) model to identify the key decision variables, process metrics and the interactions between the adsorption and reaction sections. While it is important to operate the process such that it meets constraints pertaining to greenhouse gas emissions and product quality, it is only possible to obtain the values of these constraints after performing computationally intensive simulations. This poses a challenge in identifying the feasible and optimal operating conditions of the process. A data-driven constrained grey-box optimization framework is employed to obtain feasible operating conditions and to proceed towards the optimal objective desired. Applying the optimization framework, we are able to achieve a maximum of 99.67% net overall CO2 utilization while accounting for auxiliary CO2 emissions at costs ranging from $110-$130 per ton of syngas. About 14.6% of the total CO2 input to the process is captured with low cost âdirectlyâ from flue gas while still maintaining 91% overall CO2 utilization. The rest of the CO2 input is sourced from existing capture plants integrated with the developed process.
Using the above design, intensification and optimization framework, we also develop a novel cyclic process for the direct utilization of CO2 to methanol. This process again uses a two-step process and exploits synergies between CO2 capture, CH4/CO2 mixing, syngas production and syngas conversion to methanol. In this presentation, we will further elucidate the techno-economic feasibility of the methanol process.
(1) Quadrelli, E. A.; Centi, G.; Duplan, J.-L.; Perathoner, S. Carbon Dioxide Recycling: Emerging Large-Scale Technologies with Industrial Potential. ChemSusChem 2011, 4 (9), 1194â1215.
(2) Iyer, S. S.; Bajaj, I.; Balasubramanian, P.; Hasan, M. M. F. Modular Process Intensification of Carbon Capture and Conversion to Syngas. Submitted.