Removal Method of Volatile Sulfur Compounds in Mixed Hydrocarbons
A technology of sulfide and mixed hydrocarbons, applied in the field of desulfurization, can solve the problems of difficult treatment, high cost, and large consumption of lye, and achieve the effect of avoiding high treatment cost
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Embodiment 1
[0045] A crude oil processing station produces 45 tons of mixed hydrocarbons per day, the mass fraction of hydrogen sulfide in the mixed hydrocarbons is 0.12%, and the mass fraction of methyl mercaptan is 0.019%, C 1 ~C 4 The mass fraction is 4.9%, C 5 ~C 8 The mass fraction is 92.1%, C 9 + The mass fraction is 2.85%, and the content of other sulfides is 0.011%; the saturated vapor pressure is 98.2kPa. The temperature of the mixed hydrocarbons entering the tower is 50°C, the bottom temperature is 130°C, the tower pressure is 900kPa, and the reflux ratio is 1:2. After the mixed hydrocarbons are treated, the stable light hydrocarbon hydrogen sulfide mass fraction at the bottom of the tower is 0%. The mass fraction is 0.0045%, and the saturated vapor pressure is 63.3kPa.
Embodiment 2
[0047] A crude oil processing station produces 45 tons of mixed hydrocarbons per day, the mass fraction of hydrogen sulfide in the mixed hydrocarbons is 0.12%, and the mass fraction of methyl mercaptan is 0.019%, C 1 ~C 4 The mass fraction is 4.9%, C 5 ~C 8 The mass fraction is 92.1%, C 9 + The mass fraction is 2.85%, and the content of other sulfides is 0.011%; the saturated vapor pressure is 98.2kPa. The temperature of the mixed hydrocarbons entering the tower is 60°C, the bottom temperature is 135°C, the tower pressure is 600kPa, and the reflux ratio is 1:2. After the mixed hydrocarbons are treated, the stable light hydrocarbon hydrogen sulfide mass fraction at the bottom of the tower is 0%. The mass fraction is 0.0041%, and the saturated vapor pressure is 62.8kPa.
Embodiment 3
[0049] A crude oil processing station produces 45 tons of mixed hydrocarbons per day, the mass fraction of hydrogen sulfide in the mixed hydrocarbons is 0.12%, and the mass fraction of methyl mercaptan is 0.019%, C 1 ~C 4 The mass fraction is 4.9%, C 5 ~C 8 The mass fraction is 92.1%, C 9 + mass fraction is 2.85%, other sulfide content is 0.011%; saturated vapor pressure is 98.2kPa. The temperature of the mixed hydrocarbons entering the tower is 45°C, the bottom temperature is 140°C, the tower pressure is 800kPa, and the reflux ratio is 1:2. After the mixed hydrocarbons are treated, the stable light hydrocarbon hydrogen sulfide mass fraction at the bottom of the tower is 0%. The mass fraction is 0.0037%, and the saturated vapor pressure is 62.7kPa.
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