Amine absorbent for removing sulfur dioxide in mixed gas
A technology of sulfur dioxide and absorbent, applied in the field of amine absorbent, can solve the problems of high energy consumption, easy oxidation, easy corrosion of solution, etc., and achieve the effects of low energy consumption, low corrosion, and high absorption capacity
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Embodiment 1
[0019] Simulation of a factory flue gas outlet containing SO 2 2%, N 2 98% (both volume ratio), the absorbent composition is: main absorbent piperazine 2%, ethylenediamine 3%, first add 2% concentrated sulfuric acid, then add citric acid to adjust the pH value of the solution to about 6, add slow The etchant is 0.1% of mercaptobenzothiazole, and the rest is deionized water (the composition of the absorbent is all in mass ratio).
[0020] The whole absorption-regeneration process flow of the present embodiment is: preparing SO in the gas distribution tank 2 The content is 2%, N 2 98% of the simulated flue gas enters the bottom of the absorption tower and goes up the tower. At 40 ° C, the solution used in the present invention sprayed down from the top of the tower is in countercurrent contact with the filler. The purified gas after the acid gas is absorbed is released from the tower. Top vent. The rich liquid that has absorbed the acid gas is pumped into the regeneration to...
Embodiment 2
[0023] Simulation of a factory flue gas outlet containing SO 2 0.2%, N 2 99.8% (both volume ratio), the absorbent composition is: the main absorbent hydroxyethylpiperazine 2%, hydroxyethylethylenediamine 2%, first add 2% concentrated sulfuric acid, then add citric acid to adjust the pH of the solution 0.08% of benzotriazole as corrosion inhibitor, and deionized water as the rest (absorbent components are all in mass ratio).
[0024] SO in the purified gas after being treated by the absorption solvent of the present invention 2 Content3 , more than 80% of the sulfur dioxide in the rich solution can be regenerated, and the solution corrosion rate is only 0.018g / (m 2 h), the corrosion inhibition effect is over 99%, and the desorbed SO 2 By-product concentration greater than 99%. Experimental results show that using this desulfurization solvent, the corrosion inhibition efficiency is significantly improved compared with other methods.
Embodiment 3
[0026] Simulation of a factory flue gas outlet containing SO 2 0.2%, air 99.8% (both volume ratio), the absorbent composition is: the main absorbent hydroxyethylpiperazine 2%, ethylenediamine 2%, first add 2% concentrated sulfuric acid, then add citric acid to adjust the pH of the solution Adjust to about 6, add 0.1% compound antioxidant, that is, antioxidant 618, the chemical name is bis(octadecyl) pentaerythritol diphosphite and antioxidant 168, the chemical name is three (2,4 - Di-tert-butylphenyl) phosphite, adding 0.1% of mercaptobenzothiazole as a corrosion inhibitor, and the rest as deionized water (absorbent compositions are all in mass ratio).
[0027] SO in the purified gas after being treated by the absorption solvent of the present invention 2 Content3 , more than 80% of the sulfur dioxide in the rich solution can be regenerated, and the corrosion rate of the solution is only 0.022g / (m 2 h), the corrosion inhibition effect is over 98%, the anti-oxidative degradat...
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