Membranes for Separation, Purification, Compression, and Storage of Carbon Resources from Alkaline Water

Navy Phase I STTR Topic: DON27TZ02-NV008
Pre-release Nov 4, 2026   Opens to accept proposals Dec 2, 2026   Closes Jan 6, 2027 12:00pm ET    [ View TPOC Information ]

DON27TZ02-NV008 TITLE: Membranes for Separation, Purification, Compression, and Storage of Carbon Resources from Alkaline Water

OUSW (R&E) CRITICAL TECHNOLOGY AREA(S): Contested Logistics Technologies (LOG)

COMPONENT TECHNOLOGY PRIORITY AREA(S): Biotechnology;Renewable Energy Generation and Storage;Sustainment

PROJECTED CMMC LEVEL REQUIREMENT: Level 2 (Self)

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 (CO2) (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 CO2 produced from electrochemically processed seawater often result in dilution of the CO2 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 CO2 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 CO2 from seawater over a pH range of 2 to 5. Perform analysis of the CO2 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 CO2 from a 25,000 gal/day acidified seawater source; and to purify the captured CO2 to 98% with the resulting purified CO2 stream free of oxygen (O2) and water (H2O), 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 APPLICATIONS: 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 CO2, (2) desalination plants for post treatment of CO2 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:

  1. 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/
  2. 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
  3. 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

KEYWORDS: Synthesis, carbon, membrane, separation, purification, seawater, alkaline water

TPOC 1: Heather Willauer
heather.d.willauer.civ@us.navy.mil

TPOC 2: Cameron Holder
Cameron.f.holder.civ@us.navy.mil

** TOPIC NOTICE **

The Navy Topic above is an "unofficial" copy from the Navy Topics in the DoW FY-27 Release 2 STTR BAA. Please see the official DoW Topic website at www.dodsbirsttr.mil/submissions/solicitation-documents/active-solicitations for any updates.

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