Method for absorbing and separating carbon dioxide
A carbon dioxide and separation method technology, applied in the direction of chemical instruments and methods, inorganic chemistry, carbon compounds, etc., can solve the problems of high regeneration energy consumption, high regeneration temperature, equipment corrosion, etc., to achieve extended service life, low reaction conditions, avoid The effect of corrosion
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Embodiment 1
[0023] First, monoethanolamine was used as a solute and triethylene glycol as a solvent, and 1 L of a solution was prepared by mixing to obtain an absorbent, wherein the concentration of monoethanolamine was 0.1 mol / L. Then, under the condition that the temperature is 50°C and the pressure is 200kPa, the absorbent is fully contacted with the mixed gas of carbon dioxide and nitrogen in the gas-liquid mass transfer equipment for 7 minutes, wherein the total amount of the mixed gas of carbon dioxide and nitrogen is 0.5mol, and the mixed gas of carbon dioxide is The volume fraction is 5%. Finally, the obtained liquid phase product is desorbed at 50° C. and a pressure of 0.2 kPa to realize the regeneration of carbon dioxide, and at the same time recover the absorbent for recycling.
[0024] It is detected that the absorption rate of carbon dioxide is greater than 90%.
Embodiment 2
[0026] First, diethanolamine was used as a solute and diethylene glycol as a solvent, and 1 L of a solution was prepared by mixing to obtain an absorbent, wherein the concentration of diethanolamine was 1.5 mol / L. Then, under the condition that the temperature is 25°C and the pressure is 4kPa, the absorbent is fully contacted with the mixed gas of carbon dioxide and nitrogen in the gas separation equipment for 3 minutes, wherein the total amount of the mixed gas of carbon dioxide and nitrogen is 0.01mol, and the gas volume fraction of carbon dioxide is 60%. Finally, the obtained liquid phase product is desorbed at 80° C. and a pressure of 2 kPa to realize the regeneration of carbon dioxide, and at the same time recover the absorbent for recycling.
[0027] It is detected that the absorption rate of carbon dioxide is greater than 90%.
Embodiment 3
[0029] First, diethanolamine was used as a solute and triethylene glycol as a solvent, and 1 L of a solution was prepared by mixing to obtain an absorbent, wherein the concentration of diethanolamine was 2 mol / L. Then, under the condition that the temperature is 35°C and the pressure is 500kPa, the absorbent and the mixed gas of carbon dioxide and nitrogen are fully contacted in the gas separation equipment for 5 minutes, wherein the total amount of the mixed gas of carbon dioxide and nitrogen is 1mol, and the gas volume fraction of carbon dioxide is 30%. Finally, the obtained liquid phase product is desorbed at 110° C. and a pressure of 200 kPa to realize the regeneration of carbon dioxide, and at the same time recover the absorbent for recycling.
[0030] It is detected that the absorption rate of carbon dioxide is greater than 90%.
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