Waste rubber cracking gas purifying process and equipment thereof
A technology for cracking flue gas and purification process, applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of ineffective removal of exhaust nitrogen oxides and particulate matter, affecting production progress, and low purification efficiency. The effect of long service life, saving floor space and reasonable arrangement
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Embodiment 1
[0027] A waste rubber pyrolysis flue gas purification process. The main steps include: the pyrolysis flue gas undergoes air-cooled heat exchange, is cooled to 60°C, and enters the pickling process, where the volume content of oxygen in the flue gas is 8%, and it passes through 15% sequentially. Nitric acid solution pickling, the nitrogen oxide content in the flue gas after pickling is 150mg / m 3 .
[0028] The flue gas after acid washing is alkali-washed with 5% sodium hydroxide solution; the sulfur oxide content in the flue gas after alkali-washing is 30mg / m 3 .
[0029] The pyrolysis flue gas after alkaline washing is discharged from the exhaust fan after two-stage physical adsorption, and the exhaust gas index nitrogen oxide content is 145mg / m 3 , Sulfur oxide content 30mg / m 3 , Smoke and dust content 9mg / m 3 , Reaching EU2000 / 76 / EC flue gas emission standards.
Embodiment 2
[0031] A waste rubber pyrolysis flue gas purification process. The main steps include: the pyrolysis waste flue gas undergoes water-cooled heat exchange, is cooled to 50°C, and enters the acid absorption process, where the volume content of oxygen in the flue gas is 10%, and it passes through 30% Nitric acid solution pickling, the content of nitrogen oxides in the flue gas after pickling is 130mg / m 3 .
[0032] The flue gas after acid washing is alkali-washed with 10% sodium hydroxide solution; the content of sulfur oxides in the flue gas after alkali-washing is 50 mg / m 3 .
[0033] The cracking waste flue gas after alkaline washing is discharged from the exhaust fan after one-stage physical adsorption. Exhaust flue gas index nitrogen oxide content 125mg / m 3 , Sulfur oxide content 48mg / m 3 , The smoke and dust content is 8.6mg / m 3 , Reaching EU2000 / 76 / EC flue gas emission standards.
[0034] At the same time, 100°C hot air is used to desorb another part of the filler that has been a...
Embodiment 3
[0036] A waste rubber pyrolysis flue gas purification process. The main steps include: the pyrolysis waste flue gas is cooled to 40°C through air-cooling and water-cooling heat exchange, and then enters the acid absorption process, wherein the volume content of oxygen in the flue gas is 12%, and then After pickling with 25% nitric acid solution, the nitrogen oxide content in the flue gas after pickling is 140mg / m 3 .
[0037] The flue gas after acid washing is alkali-washed with 7% sodium hydroxide solution; the sulfur oxide content in the flue gas after alkali-washing is 40mg / m 3 .
[0038] The cracking waste flue gas after alkali washing is discharged from the exhaust fan after two-stage physical adsorption. Exhaust flue gas index NOx content 135mg / m 3 , Sulfur oxide content 35mg / m 3 , Soot content 9.2mg / m 3 , Reaching EU2000 / 76 / EC flue gas emission standards.
[0039] At the same time, 120°C hot air is used to desorb another part of the filler that has been adsorbed in the physic...
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