The postcombustion CO 2 capture technology (PCC) is the topic of surplus study because it offers ease of implementation in the existing systems. To the best of the authors' knowledge, this technique has never been used for the automobile sector which has a major contribution toward anthropogenic CO 2 . In this article, experimental investigation has been carried out on the chemical solvents to determine the efficacy of capturing CO 2 from multi-pollutant diesel engine exhaust. The captured CO 2 is measured in terms of percentage by volume of the total exhaust gas from three primary amines solvents, that is, monoethanolamine (MEA), N,N-dimethylethanolamine (DMEA), and ammonia at seven brake power values, and their capture efficiencies are compared. A proposed design for the implementation of carbon capture unit in the existing heavy-duty diesel engine has also been presented with theoretical calculation on the weight of the storage tank. Energy balance analyses have been performed to determine the energy needed to regenerate the solvents. It is found that the regeneration energy required for solvents MEA, DMEA, and ammonia is 2.2, 0.7, and 1.1 kWh, respectively which is quite lower than the total energy available with exhaust gas. Experimental results show that capture efficiency at ambient conditions with absorbents MEA, DMEA, and chilled ammonia is 90.95, 57.66, and 80.08, respectively. It reveals that the PCC method can be implemented in an existing diesel engine with MEA as an efficient and safe solvent.
Chemical looping combustion (CLC) is the most reliable carbon capture technology for curtailing CO2 insertion into the atmosphere. This paper presents the cold flow simulation results necessary to understand the hydrodynamic viability of the fast-fluidized bed air reactor. Hematite is selected as an oxygen carrier due to its easy availability and active nature during the reactions. The dense discrete phase model (DDPM) approach using the commercial software Ansys Fluent is applied in the simulation. An accurate and stable solution is achieved using the second-order upwind numerical scheme. A pressure difference of 150 kPa is obtained between the outlet and inlet of the selected air reactor, which is necessary for the movement of the particle. The stable circulating rate of hematite is achieved after 28 s of particle injection inside the air reactor. The results have been validated from the experimental results taken from the literature.
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