(514ae) Biogas Upgrading to Methane Using Amine-Impregnated Resins | AIChE

(514ae) Biogas Upgrading to Methane Using Amine-Impregnated Resins

Authors 

Joseph, B., University of South Florida
Kuhn, J., University of South Florida
Separation of CO2 from CH4 is important for increasing the heating value of biogas prior to use as a vehicle fuel or for natural gas grid injection. Solid porous adsorbents are considered as a promising technology for biogas upgrading because of low energy consumption and low capital investment in comparison to conventional separation methods such as ammonia or amine solvent absorption. The use of porous materials such as activated carbons (AC)1, zeolites2, metal-organic frameworks (MOFs)3, covalent organic frameworks (COFs)4, and mesoporous silica5 have been extensively researched in CO2 separation technologies. However, many of these materials exhibit poor selectivity, low adsorption capacity, poor water resistance, and low tolerance to impurities present in LFG, which limit their applications. Commercial adsorption resin, HP2MGL, is a crosslinked polymethacrylate with a porous structure and has been successfully modified with PEI and used in separating low-concentration CO2 from atmospheric air6. The objective of this work is to evaluate its potential for use with biogas upgrading.

In the present work, we synthesized the PEI-impregnated polymeric resin (HP2MGL) sorbent for the utilization in biogas upgrading to methane via CO2 adsorption for the first time. Samples were characterized using N2 physisorption, FTIR, CO2 chemisorption, and in-situ DRIFTS techniques. Through the characterization of the pore properties and chemical components of the sorbent, we explored the underlying causes of parameter influence and the potential degradation mechanism. The effects of loadings, adsorption, and regeneration were studied. The sorbent exhibited the highest adsorption capacity of 2.73 mmolCO2/gads at 30% amine mass loading, with negligible CH4 adsorbed in simulated biogas experiments, proving a high affinity towards CO2 over CH4. In the presence of water, the saturation capacity of the sorbent increased to 2.92 mmolCO2/gads. The sorbent was regenerated completely at 100 °C.Cyclic stability, tolerance of impurities such as H2S in the feed gas and column breakthrough experiments will be conducted in a fixed-bed system, in addition to the test of the economic viability of the PEI-impregnated resin via techno-economic analysis and results will be reported.

REFERENCES

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