Room temperature ionic liquid, method and device for removing sulfur dioxide and carbon dioxide in tail gas
A room temperature ionic liquid, carbon dioxide technology, applied in the field of chemical engineering, can solve the problems of high cost, complex sulfur dioxide and carbon dioxide processes, etc., and achieve the effects of low cost, high use value and easy operation
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0053] The tail gas inlet of the tail gas purification tower in embodiment 1 passes into the carbon dioxide concentration in the tower to be 24wt%, and the sulfur dioxide concentration is 32g / m 3 The exhaust gas is introduced at a superficial flow rate of 0.1cm / s (exhaust gas temperature is 40°C and pressure is 0.1MPaG). The exhaust gas first enters the exhaust gas distributor, and the exhaust gas enters from the lower phase room temperature ionic liquid B (abbreviated as the lower phase) Phase room temperature ionic liquid A (referred to as the upper phase) overflows, and the loaded upper and lower phase ionic liquids are recycled after washing with alkali and water. Wherein, 95%wt quaternary ammonium salt ionic liquid, lower phase 5%wt[C 4 mim]Br / FeCl 3 . Finally, the purified exhaust gas from the power plant is discharged into the atmosphere. After testing, the concentration of carbon dioxide in the purified tail gas is 1.31wt%; the concentration of sulfur dioxide is 0.7...
Embodiment 2
[0055] In embodiment 2, the tail gas inlet of the tail gas purification tower leads to the carbon dioxide concentration in the tower is 15wt%, and the sulfur dioxide concentration is 40g / m 3 Exhaust gas, the gas superficial flow rate is 1cm / s (exhaust gas temperature 40 ℃, pressure 0.5MPaG), the exhaust gas first enters the exhaust gas distributor, the exhaust gas enters from the lower phase, overflows from the upper phase, and the loaded upper and lower phase ionic liquid passes through Recycled after alkali washing and water washing. Among them, 75%wt pyrrole salt ionic liquid, lower phase 25%wt[C 4 mim] BF 4 / FeCl 3 . Finally, the purified exhaust gas from the power plant is discharged into the atmosphere. After testing, the concentration of carbon dioxide in the purified tail gas is 0.79wt%; the concentration of sulfur dioxide is 0.81g / m 3 .
Embodiment 3
[0057] In embodiment 3, the tail gas inlet of the tail gas purification tower leads to the carbon dioxide concentration in the tower is 30wt%, and the sulfur dioxide concentration is 10g / m 3 The exhaust gas is introduced at a superficial velocity of 7cm / s (exhaust gas temperature 40°C, pressure 1MPaG), the exhaust gas first enters the exhaust gas distributor, the exhaust gas enters from the lower phase, overflows from the upper phase, and the loaded upper and lower phase ionic liquids pass through Recycled after alkali washing and water washing. Wherein, 85%wt quaternary ammonium salt ionic liquid, lower phase 15%wt[C 4 mim] BF 4 / FeCl 3 . Finally, the purified exhaust gas from the power plant is discharged into the atmosphere. After testing, the concentration of carbon dioxide in the purified tail gas is 1.81wt%; the concentration of sulfur dioxide is 1.11g / m 3 .
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
