Treating method for waste gas containing sulfur and hydrocarbons
A treatment method, sulfur-containing hydrocarbon technology, applied in separation methods, chemical instruments and methods, refined hydrocarbon oil, etc., can solve problems such as long process flow, economic impact, and undisclosed prior art, and achieve simplified absorption process flow , The effect of simple device structure
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Embodiment 1
[0039] The gas discharged from the top of a sour water tank farm has a temperature of about 45°C and a total hydrocarbon concentration of 10í10 4 ~100í10 4 mg / m 3 , the sulfide concentration is 1000~3000 mg / m 3 . The absorbent is crude kerosene from the fractionation tower of the refining unit at a temperature of 60°C, and the solvent used in the lye absorption unit is NaOH solution with a mass fraction of 40%.
[0040] Gas oil enters as figure 1 For the rotary bed shown in the structure, the bed rotation speed is 600 rpm. The liquid phase discharged from the rotating bed is cooled to 15°C and enters the bubbling bed with waste gas for hydrocarbon absorption. The gas space velocity in the bubbling bed is 60h -1 , the volume ratio of the absorbent at the inlet of the bubbling bed to the waste gas is 0.1, the rich absorbent discharged from the bubbling bed and the gas phase discharged from the rotating bed are re-absorbed and mixed by an injector, and then used as the feed...
Embodiment 2
[0044] Exhaust gas is discharged from a waste oil tank farm, the temperature is about 40°C, and the total hydrocarbon concentration is 10×10 4 ~40×10 4 mg / m 3 . Sulfide concentration 200~500mg / m 3 , the absorbent is gas oil from the fractionation tower of the catalytic cracking unit of the refinery, the temperature is 60°C, and the solvent used by the lye absorption unit is NaOH solution with a mass fraction of 40%.
[0045] Gas oil enters as figure 1 For the rotary bed shown in the structure, the bed rotation speed is 960 rpm. The liquid phase and exhaust gas discharged from the rotating bed enter the bubbling bed for hydrocarbon absorption, and the gas space velocity in the bubbling bed is 150h -1 , the volume ratio of the absorbent at the inlet of the bubbling bed to the exhaust gas is 0.2, and the rich absorbent discharged from the bubbling bed and the gas phase discharged from the rotating bed are reabsorbed and mixed by an injector, and then used as the feed to the...
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