Hybrid Adsorption + Liquefaction Process for Post-combustion CO2 Capture

• Author / Creator

  Pawar, Sunny Jitendra

• Greenhouse gas (GHG) emissions reduction through carbon capture and storage (CCS) will be pivotal in achieving the world’s net zero emissions target by 2050. However, we have a long way to go before CCS is implemented at scale worldwide.
  Emerging technologies such as adsorption-based CO2 capture have shown promise in treating flue gas streams with relatively high CO2 partial pressures, such as the cement or steel industry. Despite their competitive advantages in energy efficiency in gas separation applications, they struggle to meet the scalability requirements compared to mature technologies like physical solvent absorption. In low CO2 partial pressures, even with the best possible adsorbents, the capture costs for pressure-vacuum swing adsorption (PVSA) processes are significantly higher than the Mono-ethanolamine (MEA) absorption-based processes. Hence, it is imperative to explore and evaluate scalable and economically viable alternative options, which is critical in determining the success of CCS in cutting emissions.
  This study aims to assess the effectiveness of a hybrid process that combines pressure-vacuum swing adsorption (PVSA) with liquefaction to determine if it is cost-effective and energy-efficient in capturing CO2. Modelling and optimization studies
  are conducted for both processes independently to test the performance limits. The dynamic adsorption process is simulated using detailed first principles models consisting of a system of coupled partial differential equations of mass, heat and momentum transfer solved numerically in space and time. The liquefaction process is simulated using Aspen Plus® from AspenTechnology, a commercial process simulation software using the Peng-Robinson (PR) thermodynamics property package.
  The hybrid process is optimized by minimizing the capture cost by constraining the recovery to at least 90 mol % of the CO2 at a purity of 95 mol % from the overall process. The flue gas streams with CO2 composition ranging from 3.5 - 30 mol %, representative of emissions from Natural-gas combined cycle (NGCC) power plants, coal-fired power plants, and cement and steel kilns, are studied. The variant of the PVSA process studied is a 4-step Light product pressurization (LPP) cycle. The performance of these processes for commercially available adsorbent materials like Zeolite 13X is studied. The liquefaction uses compression and refrigeration to purify CO2 up to 95 mol %.
  The hybrid process reduces the overall specific energy consumption and, thus, capital and operational costs by more than 50 % compared to a standalone PVSA process in the low CO2 partial pressure ranges. It leverages the ability of the pressure-vacuum swing adsorption process to recover CO2 at a high rate in the low CO2 partial pressure ranges. In contrast, the liquefaction process takes the load of purifying it from an intermediate purity of 40-75 mol % to the desired purity of 95 mol % to deliver it at conditions suitable for transport and storage. The hybrid process reduces the number of parallel PVSA trains required to process the same amount of flue gas, thus improving the scalability of the process.

• Subjects / Keywords

  • Hybrid
  • process
  • capture
  • costs
  • adsorption
  • liquefaction
  • post-combustion

• Graduation date

  Spring 2024

• Type of Item

  Thesis

• Degree

  Master of Science

• DOI

  https://doi.org/10.7939/r3-gkth-td41

• License

  This thesis is made available by the University of Alberta Libraries with permission of the copyright owner solely for non-commercial purposes. This thesis, or any portion thereof, may not otherwise be copied or reproduced without the written consent of the copyright owner, except to the extent permitted by Canadian copyright law.