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Title: Sorption Enhanced Mixed Matrix Membranes for Hydrogen (H2) Purification and Carbon Dioxide (CO2) Capture

Technical Report ·
DOI:https://doi.org/10.2172/1603097· OSTI ID:1603097
 [1];  [1];  [2];  [3]
  1. Univ. at Buffalo, NY (United States)
  2. Membrane Technology and Research, Inc., Newark, CA (United States)
  3. Univ. of Kentucky, Lexington, KY (United States)

The technical objective of this project was to develop sorption enhanced mixed matrix membranes with H2 permeance of 500 gas permeance units (GPU) and H2/CO2 selectivity of 30 at 150-200 °C. These membranes will be the central component in the design of membrane based systems for 90% capture of CO2 from coal-derived syngas, with 95% CO2 purity at a cost of electricity 30% less than baseline capture approaches. The unique approach in this proposal is to design crosslinked polymers containing Pd-based nanoparticles achieving strong H2 sorption and size sieving ability and thus H2/CO2 selectivity. The specific objectives for each budget period (BP) are described below. BP 1: Identify polymer matrix with strong size sieving ability and palladium (Pd)-containing nanomaterials to prepare freestanding mixed matrix films with H2 permeability of 50 Barrer and H2/CO2 selectivity of 30 at 150-200°C with simulated syngas. BP 2: Prepare and optimize thin film mixed matrix composite membranes materials with H2 permeance of 500 GPU and H2/CO2 selectivity of 30 at 150-200 °C, and complete the modification of the membrane test unit for the field test in the BP 3. BP 3: Conduct a 20-day field test of the membranes with real syngas at Center for Advanced Energy Research (CAER) of the University of Kentucky (UKy). During the BP2, we have successfully prepared thin-film composite (TFC) membranes based on mixed matrix materials (MMMs) containing Pd nanoparticles in polymers, and demonstrated their superior and robust performance for H2/CO2 separation at 150 – 225 °C. (1) Production of the Pd based nanoparticles with a diameter of 4 nm has been scaled up to 200 mg/day. (2) We have prepared TFC membranes with H2 permeance above 500 GPU and H2/CO2 selectivity above 30 at temperatures up to 225 °C, which meet the targets for the BP2. (3) We have conducted parametric studies of TFC membranes with a mixed gas containing H2S and H2O and demonstrated the stability of the membranes. (4) We have established a new testing plan at the Center for Advanced Energy Studies (CAER) at the University of Kentucky because NCCC decided to shut down their gasifier. During this project, four Ph.D. students received the inter-disciplinary training and graduated, including Shailesh Konda, Maryam Omidvar, Deqiang Yin, and Lingxiang Zhu. One postdoctoral researcher (Dr. Liang Huang) and two Ph.D. students (Abhishek Kumar and Hien Nguyen) are involved in this project. The project leads to one provisional patent application, eight peer-reviewed articles, and one manuscript in preparation. The details are shown below.

Research Organization:
Univ. at Buffalo, NY (United States)
Sponsoring Organization:
USDOE Office of Fossil Energy and Carbon Management (FECM)
DOE Contract Number:
FE0026463
OSTI ID:
1603097
Report Number(s):
DOE-UB-26463-1
Country of Publication:
United States
Language:
English