DoW/NAVY · DoW STTR 2027 BAA
DON27TZ02-NV008 — Membranes for Separation, Purification, Compression, and Storage of Carbon Resources from Alkaline Water
Pre-Release | released 2026-11-04 | opens 2026-12-02 | closes 2027-01-06 | CMMC Level 2 (Self), STTR
SBIR.gov page | DSIP topics app (search DON27TZ02-NV008)
TPOC: Heather Willauer <[email protected]>; Cameron Holder <[email protected]>
Keywords: Synthesis, carbon, membrane, separation, purification, seawater, alkaline water
Technology areas: None
Objective
Develop a low-cost, robust, energy-efficient, and scalable membrane process to continuously separate, purify, compress, and store carbon dioxide from electrochemically processed alkaline water sources to support the local synthesis of fuels, nutrients, materials, and pharmaceuticals in austere, forward-deployed environments.
Description
This STTR topic seeks to develop a low-cost, low-energy, low-temperature (not to exceed 50°C), high-throughput nonmetallic membrane process to purify and store carbon dioxide (CO 2 ) (from acidic seawater solutions). Carbon resources harvested from seawater represent a critical renewable feedstock for the localized synthesis of tactical fuels, materials, nutrients, and pharmaceuticals. Developing the capability to generate these resources in-theater or at the tactical edge enhances multi-domain operational sustainment. Current technologies used to recover the dissolved CO 2 produced from electrochemically processed seawater often result in dilution of the CO 2 with air and water vapor that can lead to detrimental sintering and oxidation of catalysts used in thermochemical and biological synthetic approaches. In addition, there are volumetric and compression penalties associated with the dilution of the targeted gas. The proposed membrane process will reduce the complexity, size, and costs associated with supplying pure carbon dioxide resources from alkaline water sources.
The integrated membrane, purification, and compression process will provide equipment, process, design criteria, energy and material balance; and establish operational performance parameters.
Phase I
Define a concept for a specific membrane process for the separation and purification of CO 2 from acidified seawater solutions. Define, develop, and perform initial laboratory assessment of the proposed membrane process to validate the technical feasibility of the approach for the capture, purification, and storage of CO 2 from seawater over a pH range of 2 to 5. Perform analysis of the CO 2 to determine yield and purity. Perform analysis on the membrane to determine the membranes’ ability to maintain performance, structural and chemical integrity.
Phase II
Develop a prototype process based on the work achieved in Phase I. Design the prototype as a continuous process to capture, purify, and store 90 to 100% of CO 2 from a 25,000 gal/day acidified seawater source; and to purify the captured CO 2 to 98% with the resulting purified CO 2 stream free of oxygen (O 2 ) and water (H 2 O), compressed to at least 300psi, and stored for utilization in various synthetic processes. Establish performance parameters and proof of concept for development of full-scale process. Prepare a Phase III commercialization/transition plan.
Phase III / dual use
Using data on the resulting integrated membrane, purification, and compression process, provide the design criteria for transitioning the technology to larger capacities. Develop and test a 250,000 gal/day process. Provide a cost-benefit analysis to show process outperforms current cryogenic distillation and pressure swing adoption processes.
Dual use applications include: (1) breweries and distilleries to recover and reuse CO 2 , (2) desalination plants for post treatment of CO 2 capture and mineral scaling prevention, (3) offshore oil, gas, and maritime industries for commercial fuel synthesis, (4) commercial aquaculture, (5) fire suppression, and (6) dry ice for preservation.
References
- Marquez, R. A., Nielander, A. C., Resasco, J., Jaramillo, T. F. and Mullins, C. B. “Electrochemical Ocean-Based Carbon Capture: Roadblocks to Scale-Up.” ACS Energy Letters, American Chemical Society, February 13, 2026, pp 1241-1259. https://carbondioxide-removal.eu/2026/02/07/marquez-et-al-2026-electrochemical-ocean-based-carbon-capture-roadblocks-to-scale-up/
- Digdaya, I. A.; Sullivan, I., Lin, M., Han, L., Cheng, W. H., Atwater, H. A. and Xiang, C. “A Direct Coupled Electrochemical System for Capture and Conversion of CO2 from Oceanwater.” Nat Commun 2020, 11 (1). https://www.nature.com/articles/s41467-020-18232-y Captura “Innovation & cost reductions in Direct Ocean Capture, 08/13/2024.” Captura CORP, 2024. https://capturacorp.com/wp-content/uploads/2024/08/DOC-innovations-and-cost-reductions.pdf
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