Novel method for capturing and separating carbon dioxide
A carbon dioxide, separation rate technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., to achieve the effects of less equipment investment, environmental friendliness, and low energy consumption
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Embodiment 1
[0021] Raw material gas composition: nitrogen: 89.9%, carbon dioxide: 10.0% and the balance is inert gas.
[0022] The absorbent is [Proline Hydroxycholine Salt] ([Choline][Pro]). Adjust the temperature of the system to 20°C, adjust the pressure to 0.1Mpa, start the supergravity rotating bed reactor, adjust the rotor speed to 2825r / m, and then open the control valve of the liquid inlet of the reactor, and the absorbent is distributed by the liquid through the liquid phase inlet pipe 1 The device is sprayed to the inner edge of the supergravity rotating bed rotor 4, and the flow rate of the regulating liquid is 2.65L / h. 2 The mixed gas enters the high-gravity rotating bed reactor through the gas phase inlet pipe 2, and countercurrently contacts with the absorption liquid in the rotor of the high-gravity rotating bed, and performs CO under high-gravity conditions. 2 The trap is then discharged from the gas phase outlet 5 and enters the subsequent section. The gas flow rate is ...
Embodiment 2-19
[0024] Process flow and step are with embodiment 1, and the flow rate of temperature, pressure, gas-liquid, rotor speed and test result of each embodiment are shown in Table 1.
[0025] The absorbent is ionic liquid [proline hydroxycholine salt] ([Choline][Pro]), [1-(3-propylamino)-3-butylimidazole tetrafluoroborate] ([Apbim][ BF 4 ]), [1-(3-propylamino)-3-butylimidazolium hexafluorophosphate] ([Apbim][PF 6 ]) and other ionic liquids with amino groups as functional groups or mixtures thereof.
[0026] The volume flow ratio of the absorbent to the mixed gas is 50-500:1.
[0027]Table 1 Process conditions and experimental results of each embodiment
[0028]
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