Phase II Amount
$1,050,000
Dimethyl carbonate (DMC) is a promising green chemical due to its simplicity, versatility, low toxicity, high polarity, low corrosivity, and biodegradability. Further, direct synthesis of DMC using CO2 as a reactant offers a pathway forward to effective greenhouse gas reutilization. DMC is one of the most promising organic carbonates in terms of the range of applications.The US EPA has exempted DMC under its VOC classification rules making it a viable substitute for hydrocarbon solvents such as MEK, t-butyl acetate, etc. It has been proposed for use as a fuel additive (MTBE substitute), lithium ion battery electrolyte, and a platforming chemical for higher carbonates, polyurethanes, isocyanates, and polycarbonates. However, the commercial impact of DMC has been muted with worldwide production limited to <800MM lb/year or <5% of the potential 20,000MM lb/year demand from the fuel additives and polymer synthetics markets alone. Penetration of DMC into these markets is limited due to its currently high production cost, a result of the low reactor yields, and resultant high energy cost associated with product recovery and reactant recycle. To develop DMC as a commodity chemical, it is necessary to focus on solving the reactor yield and the downstream separation problems, simultaneously. In this project, MPT proposes to integrate its high-performance carbon molecular sieving inorganic membranes into the DMC synthesis process. These membranes are ideally suited to this process, given their demonstrated high selectivity and excellent stability in high temperature aggressive chemical environments. In the first step, a membrane reactor (MR) will be deployed to simultaneously remove product water and substantially enhance the reactor conversion. In the second step, a membrane separator (nanofilter, NF) will be deployed to efficiently break the methanol/DMC azeotrope. Significant processing cost savings are achieved due to overlapping synergies that develop between these technologies. During the Phase I program laboratory scale feasibility testing of MPT membranes in the MR and NF configurations was completed. In the MR testing, >600% enhancement in DMC yield over the equilibrium limit was demonstrated. In the NF testing, 96 to >98% DMC rejection from methanol was obtained. Membrane performance stability was demonstrated in both subsystems at the target operating temperature. With this data, an integrated MR/NR process model was developed and technoeconomic analysis was completed. The TEA demonstrated substantial savings, yielding DMC production costs below competing petroleum derived chemicals. During the Phase II program, the primary objective will be to demonstrate the integrated CME-DMC process at a pilot scale of 1 to 5 lb/hr at the target operating conditions developed in Phase I. This unit will be the basis for the Phase III commercialization scale-up. In parallel, system optimization and finished product development activities will be undertaken to further improve process economics. Utilization of CO2 captured from power plant emissions remains a significant challenge. DMC represents a significant opportunity to tap this no cost reactant, with a market potential of over $3 billion/year. Further, renewable chemicals will improve US security and stability by reducing dependence upon depleting fossil oil supplies from politically volatile regions.