Ternary double liquid phase absorbent for treating carbon dioxide in flue gas
A carbon dioxide and absorbent technology, applied in gas treatment, chemical instruments and methods, separation methods, etc., can solve the problems of no research on special effects, only binary systems, and unsatisfactory absorption load, etc., and achieve excellent phase separation characteristics and obvious The effect of heat reduction
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Embodiment 1
[0028] Add water to triethylenetetramine (TETA), diethylaminoethanol (DEEA) and 1,3-dimethyl-2-imidazolidinone (DMI) to form a 30ml ternary absorbent, the total amine concentration is 4mol / L, the TETA concentration is 1mol / L, the mass fraction of TETA is 15%, the DEEA concentration is 3mol / L, the mass fraction of DEEA is 35%, the mass fraction of inert solvent DMI is 25%, and the mass fraction of water is 25% . Under the water bath of 40 ℃, under normal pressure, the nitrogen gas of 85% and the carbon dioxide of 15% are passed into by volume fraction until the absorbent is saturated, and the upper (lean) liquid phase of the absorbent is 11.8ml, CO 2 The load is 0.15mol / L, the lower (rich) liquid phase is 15.1ml, CO 2 The load is 4.47mol / L, with nearly 96.7% CO 2 Loaded in the lower liquid phase, the total load is 0.64mol / mol, which is 1.23 times that of MEA. See Table 1 for energy consumption.
Embodiment 2
[0030]Add water to triethylenetetramine (TETA), diethylaminoethanol (DEEA) and N,N-dimethylformamide (DMF) to make 30ml ternary absorbent, the concentration of TETA is 1mol / L, the mass of TETA The fraction is 15%, the DEEA concentration is 3mol / L, the mass fraction of DEEA is 35%, the mass fraction of the inert solvent DMF is 25%, and the mass fraction of water is 25%. Under the water bath of 40 ℃, under normal pressure, the volume fraction of 85% nitrogen and 15% carbon dioxide is introduced until the absorption of the absorbent is saturated, the upper (lean) liquid phase of the absorbent is 9.8ml, CO 2 The load is 0.34mol / L, the lower (rich) liquid phase is 17.8ml, CO 2 With a load of 4.35mol / L, nearly 92.7% of CO 2 Loaded in the lower liquid phase, the total load is 0.73mol / mol, which is 1.40 times that of MEA. See Table 1 for energy consumption.
Embodiment 3
[0032] Add water to triethylenetetramine (TETA), diethylaminoethanol (DEEA) and sulfolane to make 30ml ternary absorbent, the concentration of TETA is 1mol / L, the mass fraction of TETA is 15%, and the concentration of DEEA is 3mol / L , the mass fraction of DEEA is 35%, the mass fraction of the inert solvent sulfolane is 25%, and the mass fraction of water is 25%. Under the water bath of 40 ℃, under normal pressure, the volume fraction of passing through is 85% nitrogen and 15% carbon dioxide until the absorption of the absorbent is saturated, the upper (lean) liquid phase of the absorbent is 8ml, CO 2 The load is 0.38mol / L, the lower (rich) liquid phase is 20ml, CO 2 Load 3.91mol / L, nearly 91.1% CO 2 Loaded in the lower liquid phase, the total load is 0.73mol / mol, which is 1.40 times that of MEA. See Table 1 for energy consumption.
[0033] Table 1 Comparison of regeneration energy consumption of ternary dual-liquid phase absorbent
[0034] absorbent Regeneration ...
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