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Title: Gradient Amine Sorbents for Low Vacuum Swing CO2 Capture at Ambient Temperature

Technical Report ·
DOI:https://doi.org/10.2172/1992922· OSTI ID:1992922

The growing concerns over CO2 emissions have led to the development of various methods for CO2 capture. CO2 capture by amine-based sorbents has been achieved by temperature (thermal) swing adsorption (TSA) process, pressure swing adsorption (PSA) process, and temperature pressure or vacuuming swing adsorption (TPSA or TVSA) process for CO2 capture. Amine sorbents for energy-efficient TSA, PSA, VSA, TPSA or TVSA CO2 capture should possess a capability which allow adsorbed CO2 to desorb and amine sorbent to be regenerated at low temperatures or low vacuums. Development of such amine sorbents would significantly decrease energy consumption and sorbent degradation during the regeneration step. The objective of this project is to develop a low vacuum swing adsorption (VSA) process for the capture of CO2 from air. The focus is on the development of amine sorbent which allows CO2 to adsorb in the form of weakly adsorbed CO2. The weakly adsorbed CO2 species can be collected from the sorbent by applying a low vacuum at ambient temperature. Specifically, no heating (i.e., thermal energy) is needed for regeneration of amine sorbents. This novel sorbent allows VSA to be operated at ambient temperature without a significant energy demand. This process eliminates the energy-intensive heating and cooling process in temperature swing adsorption (TSA) process. Ambient temperature operation could prolong the lifetime of sorbent and minimize the maintenance cost. Extensive sorbent studies with in-situ infrared spectroscopy have revealed the modifications of conventional amine sorbents with additives can increase the fraction of weakly adsorbed CO2. The amine sorbents with loaded CO2 can be regenerated in part by the following approaches: (i) mild heating to temperatures below 70 °C, (ii) flowing purging gas over modified amine sorbents at temperatures below 40 °C, (iii) vacuuming at pressure below 0.2 atm and temperatures below 40 °C. The performance of these modified amine sorbents has been tested in a 60 grams VSA unit at ambient temperatures. The results show that weakly adsorbed CO2 which can be desorbed from modified amine sorbents with purging gas at 100 cc/min can also be evacuated at a vacuum of 1 psia at room temperature. A preliminary techno- economic analysis indicates the major cost of the VSA process with modified amine sorbents stems from the operation of vacuum pumps. Thus, developing an excellent sealing with minimum leakage for the VSA unit is the most critical task for further the development of this VSA technology.

Research Organization:
Univ. of Akron, OH (United States); Aspen Aerogels, Inc., Northborough, MA (United States)
Sponsoring Organization:
USDOE
DOE Contract Number:
FE0031958
OSTI ID:
1992922
Report Number(s):
DOE-Akron-DE-FE0031958
Country of Publication:
United States
Language:
English