Carbon Capture and Storage: CO2 Management Technologies by Amitava Bandyopadhyay

By Amitava Bandyopadhyay

Carbon seize and garage (CCS) refers to a suite of applied sciences and techniques for the mitigation, remediation, and garage of business CO2 emissions, the main approaching and virile of the greenhouse gases (GHG). The booklet addresses the tools and applied sciences at present being utilized, constructed, and so much short of additional research.The booklet: Discusses tools of carbon seize in commercial settings Presents Read more...

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The operating temperature was ranging between 25 and 55°C. The overall CO2 removal efficiency was experimentally shown to be 95%. It was proved that NH4HCO3 was the main product of the CO2–NH3 reaction. A life cycle analysis was finally carried out from the experimental findings that are discussed latter. Kim et al. 8 m; random packing materials: Raschig ring with specific surface area of 712 m2/m3 and Pro-Pak with specific surface area of 1,890 m2/m3). The simulated flue gas consisted of 25% CO2 and balance N2.

Subsequent treatment of the SO2-rich stream to obtain a first regenerated absorbent stream which is used back for SO2 scrubbing; 2. CO2 scrubbing loop: Treating the SO2-lean stream in a CO2 scrubbing loop with a second absorbent stream to obtain a CO2-rich stream. Subsequent treatment of the CO2-rich stream to obtain a Amine vs. Ammonia Absorption of CO2 17 second regenerated absorbent stream which is used back for CO2 scrubbing; and 3. treating at least a portion of one or both of the first and second regenerated absorbent streams to remove heat stable salts.

The consumption of process energy was analyzed based on sensible heat, reaction energy, and energy for steam stripping. The sensible heat was the energy required to raise the temperature of the scrubbing liquid to the stripper temperature that would be lost. Reaction energy was the heat of reaction for absorption of CO2. Finally, the energy for steam stripping was the energy associated with the steam needed during the stripping operation. The estimated total energy requirement for the NH3-based process was 1,147 kJ/kg-CO2 that was only about 27% of the energy requirement of MEA-based process of 4,215 kJ/ kg-CO2.

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