Abstract
The performance of NH3-based CO2 absorption under static magnetic field conditions was examined. The removal efficiency of CO2, CO2 load, and absorption capacities were investigated using a bubble reactor system. The CO2 removal efficiencies, CO2 load, and absorption capacity under static magnetic field conditions were calculated at four kinds of different operating conditions, which included CO2 concentration in flue gas, gas flow rate, concentrations of aqueous NH3, and reaction temperature. The initial removal efficiency of CO2 reached 98.5% by 10 wt.% NH3 solution under static magnetic field conditions, and it was 7% higher than that under the no magnetic field conditions. The effect of magnetic field on CO2 load and absorption capacity was more obvious when the inlet CO2 concentration in the simulated flue gas is 10 vol.%, the CO2 load increased 11.7% from 1.45 mol/L to 1.62 mol/L, and the absorption capacity increased from 0.668 kg CO2/kg NH3 to 0.738 kg CO2/kg NH3. Compared with the absorption of CO2 under static magnetic field conditions and no magnetic field conditions, the absorption process of CO2 was enhanced by the magnetic field, and the removal efficiency of CO2, CO2 load, and absorption capacity demonstrated superior performance.
| Original language | English |
|---|---|
| Pages (from-to) | 1462-1467 |
| Number of pages | 6 |
| Journal | Canadian Journal of Chemical Engineering |
| Volume | 96 |
| Issue number | 7 |
| DOIs | |
| State | Published - Jul 2018 |
| Externally published | Yes |
Keywords
- CO load
- absorption capacity
- removal efficiency
- static magnetic field
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