SBIR-STTR Award

Inorganic Membrane-based Process for High Efficiency Catalytic Conversion and Product Separation in Direct Synthesis of Dimethyl Carbonate
Award last edited on: 9/4/2019

Sponsored Program
SBIR
Awarding Agency
DOE
Total Award Amount
$1,199,974
Award Phase
2
Solicitation Topic Code
22c
Principal Investigator
Richard Ciora

Company Information

Media and Process Technology Inc (AKA: MPtech~Media and Process Tech Inc)

1155 William Pitt Way
Pittsburgh, PA 15238
   (412) 826-3721
   N/A
   www.mediaandprocess.com
Location: Single
Congr. District: 17
County: Allegheny

Phase I

Contract Number: DE-SC0019556
Start Date: 2/19/2019    Completed: 11/18/2019
Phase I year
2019
Phase I Amount
$149,974
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, an alternative methylating and carbonlylating agent to highly toxic chemicals such as phosgene and a platforming chemical for higher carbonates, polyurethanes, isocyanates, and polycarbonates. However, the commercial impact of DMC has been miniscule with worldwide production limited to <200MM lb/year or <1% 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 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 will be deployed to simultaneously remove product water and substantially enhance the reactor conversion. In the second step, a membrane separator 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 we will be conducting bench scale testing of MPT membranes in the membrane reactor and membrane separator configurations. In the membrane reactor testing, the focus will be on determining DMC yield improvement under various reactor operating conditions. In the membrane separator testing, the focus will be on integration of the membrane reactor with the downstream distillation as a hybrid system to overcome the energy intensive azeotrope distillation. With this data, a membrane reactor and process model will be developed and technoeconomic analysis will be conducted/refined. This information will be used to establish the program technical approach in the Phase II pilot scale demonstration. 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.

Phase II

Contract Number: DE-SC0019556
Start Date: 4/6/2020    Completed: 4/5/2022
Phase II year
2020
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.