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The Proportion of Different Heat in Reboiler Energy with the Optimal Process Parameters

https://doi.org/10.3390/pr9122184

“From the results above, the optimal process parameters and the lowest reboiler energy for different solvents can be obtained, which are listed in Table 2. The concentration of each solvent is selected in Section 3.1, the CO2 partial pressure of flue gas is selected as 10 kPa and the pressure of the desorption tower is 2.2 bar. The highest configurable concentration of PZ considered in this work, 10 wt.%, was selected as the concentration of the PZ solvent, and the reason for this has been provided in Section 3.1. Due to the low concentration of PZ, L/G is 6.167, which is too large, and the reboiler energy consumption is very high, so PZ is not suitable for use as an absorbent alone. The L/G of other solvents is between 1.3 and 2.7, which is a reasonable range.

Figure 9 shows the lowest reboiler energy consumption of different solvents and the contribution of the three types of heat for different solvents at the optimal concentration. The highest reboiler energy consumption is PZ, because L/G is relatively high, so the energy consumption for condensing and heating the liquid is also relatively high. The reboiler energy consumption of the MEA solvent is the second highest. Qcon and QT contribute less. The desorption heat, Qabs, contributes the most, and its value is higher than other solvent desorption heats. HEPZ has the lowest reboiler energy consumption, 3.018 GJ/tCO2, which is about 35.2% lower than Qreb of PZ and 11.6% lower than Qreb of MEA, and Qabs is almost the lowest among all solvents, only slightly higher than Qabs of DMEA. The reboiler energy consumption of 1-MPZ, DMEA and AMP is close. The three heat values and their proportions of 1-MPZ and AMP are close.
Figure 9. The proportion of different heat in the reboiler energy of different solvents.

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