Mixed absorbing agent for catching or separating carbon dioxide
A carbon dioxide, absorbent technology, applied in the direction of absorption, carbon compounds, separation methods, etc., can solve the problems of high use cost and more degradation, and achieve the effects of low reaction heat, high solubility and good stability
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Embodiment 1
[0026] Get three parts of 3-dimethylamino-1-propanol (DMAP) content is 10wt%, primary amine monoethanolamine (MEA) content is 5.1wt% aqueous solution (i.e. 84.9% water), temperature is 40 ℃, will gas phase CO 2 Partial pressure of 9.8kPa, 46kPa, 90kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the absorbent 2 The molar ratio of the amine to the amine and the CO in the absorbent 2 See Table 1 for the solubility.
[0027] Table 1 Experimental results of aqueous solution of 10wt% 3-dimethylamino-1-propanol+5.1wt% monoethanolamine at 40°C
[0028]
Embodiment 2
[0030] Get three parts of 3-dimethylamino-1-propanol content is 10wt%, monoethanolamine content is 5.1wt% aqueous solution (i.e. 84.9% water), temperature is 120 ℃, gas phase CO 2 Partial pressure of 25kPa, 55kPa, 100kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 The molar ratio of the amine to the amine and the CO in the absorbing solvent 2 See Table 2 for the solubility.
[0031] Table 2 Experimental results of 120°C, 10wt% 3-dimethylamino-1-propanol + 5.1wt% monoethanolamine aqueous solution
[0032]
Embodiment 3
[0034] Get three parts of 3-dimethylamino-1-propanol content is 50wt%, monoethanolamine content is 9.9wt% aqueous solution (i.e. 40.1% water), temperature is 40 ℃, gaseous phase CO 2 Partial pressure of 15kPa, 30kPa, 80kPa containing CO 2 and N 2 The mixed gas of the mixed gas is input into three parts of the solvent respectively, and after the gas-liquid two-phase reaches equilibrium, the CO in the solvent is absorbed 2 The molar ratio of the amine to the amine and the CO in the absorbing solvent 2 See Table 3 for the solubility.
[0035] Table 3 Experimental results of aqueous solution of 50wt% 3-dimethylamino-1-propanol + 9.9wt% monoethanolamine at 40°C
[0036]
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