Ziyi Li , Cong Wang , Jin Xiao , Xu Jiang , Ningqi Sun , Xiong Yang , Yingshu Liu
{"title":"Washcoated zeolite structured adsorbents for CO2 capture and recovery by rotary adsorption","authors":"Ziyi Li , Cong Wang , Jin Xiao , Xu Jiang , Ningqi Sun , Xiong Yang , Yingshu Liu","doi":"10.1016/j.ccst.2025.100378","DOIUrl":null,"url":null,"abstract":"<div><div>Adsorption has long been recognized as a vital and extensively utilized technology for CO2 capture, for which developing a cost-effective process is a long-sought goal. The structured adsorbent with faster heat and mass transfer, present new opportunities for advancing rotary adsorption process, however, lacks comprehensive evaluation and discussion on CO<sub>2</sub> sorption. In this study, structured adsorbents were prepared by washcoating commercial NaY and 13X zeolites onto a fiberglass honeycomb support. A series of characterizations and breakthrough test demonstrated the advantages of structured adsorbents over conventional pellets. NaY zeolite emerged as the thermodynamically and kinetically preferred CO<sub>2</sub> adsorbent, exhibiting an equilibrium adsorption capacity of 5.972 mmol·g<sup>-1</sup> and an internal mass transfer coefficient of 5.12 × 10<sup>–3</sup> s<sup>-1</sup> (15 % CO<sub>2</sub>, 298 K, 1 bar). These values are 18.3 % and 164 % higher than those of its pellet counterpart and 12.3 % and 36.9 % higher than those of the 13X honeycomb. NaY's great adaptability across various applications was indicated by its breakthrough capacities at different temperatures and CO<sub>2</sub> feed concentrations, as well as the minimal influence of feed gas flow rate on CO<sub>2</sub> adsorption equilibrium and kinetics. By employing a recirculating thermal desorption strategy, CO<sub>2</sub> can be enriched from 5 % to 61 %, 15 % to 79 %, and 55 % to 92 %, achieving a 90 % recovery under mild desorption conditions. A two-stage rotary adsorption process for low-concentration CO<sub>2</sub> capture was proposed, enabling CO<sub>2</sub> enriched from 5 % to 55 % in the first stage, and further to 90 % in the second stage. This work introduces a promising approaches for low-cost industrial carbon capture and even direct air carbon capture.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"14 ","pages":"Article 100378"},"PeriodicalIF":0.0000,"publicationDate":"2025-01-25","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Carbon Capture Science & Technology","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2772656825000181","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
Adsorption has long been recognized as a vital and extensively utilized technology for CO2 capture, for which developing a cost-effective process is a long-sought goal. The structured adsorbent with faster heat and mass transfer, present new opportunities for advancing rotary adsorption process, however, lacks comprehensive evaluation and discussion on CO2 sorption. In this study, structured adsorbents were prepared by washcoating commercial NaY and 13X zeolites onto a fiberglass honeycomb support. A series of characterizations and breakthrough test demonstrated the advantages of structured adsorbents over conventional pellets. NaY zeolite emerged as the thermodynamically and kinetically preferred CO2 adsorbent, exhibiting an equilibrium adsorption capacity of 5.972 mmol·g-1 and an internal mass transfer coefficient of 5.12 × 10–3 s-1 (15 % CO2, 298 K, 1 bar). These values are 18.3 % and 164 % higher than those of its pellet counterpart and 12.3 % and 36.9 % higher than those of the 13X honeycomb. NaY's great adaptability across various applications was indicated by its breakthrough capacities at different temperatures and CO2 feed concentrations, as well as the minimal influence of feed gas flow rate on CO2 adsorption equilibrium and kinetics. By employing a recirculating thermal desorption strategy, CO2 can be enriched from 5 % to 61 %, 15 % to 79 %, and 55 % to 92 %, achieving a 90 % recovery under mild desorption conditions. A two-stage rotary adsorption process for low-concentration CO2 capture was proposed, enabling CO2 enriched from 5 % to 55 % in the first stage, and further to 90 % in the second stage. This work introduces a promising approaches for low-cost industrial carbon capture and even direct air carbon capture.