Decontamination of sulfur contaminants from hydrocarbons
A method for removing hydrogen sulfide from a hydrocarbon. The method comprises introducing methylmorpholine-N-oxide to a vessel, wherein the vessel comprises the hydrocarbon, and wherein the hydrocarbon comprises hydrogen sulfide; and treating the hydrocarbon by allowing the methylmorpholine-N-oxide to react with the hydrogen sulfide.
1. A method for removing hydrogen sulfide from a hydrocarbon, comprising:
(A) introducing a methylmorpholine-N-oxide to a vessel, wherein the vessel comprises the hydrocarbon, and wherein the hydrocarbon comprises a hydrocarbon liquid layer and a hydrocarbon gas layer, and further wherein the methylmorpholine-N-oxide is introduced into the hydrocarbon liquid layer, and wherein the hydrocarbon comprises hydrogen sulfide;
(B) introducing steam to the hydrocarbon gas layer to allow at least a portion of hydrogen sulfide in the hydrocarbon gas layer to condense into the hydrocarbon liquid layer; and
(C) treating the hydrocarbon liquid layer by allowing the methylmorpholine-N-oxide to react with hydrogen sulfide, wherein treating the hydrocarbon comprises converting hydrogen sulfide to elemental sulfur.
2. The method of claim 1 , further comprising (D) removing at least a portion of elemental sulfur from the vessel.
3. The method of claim 1 , wherein at least a portion of the elemental sulfur is removed from the vessel.
4. The method of claim 1 , wherein a concentration of the methylmorpholine-N-oxide in the hydrocarbon liquid layer is between about 0.01 weight volume % and about 60 weight volume% of the hydrocarbon.
5. The method of claim 1 , wherein the methylmorpholine-N-oxide solution is introduced to the hydrocarbon liquid layer in an amount to provide a mole ratio of methylmorpholine-N-oxide to hydrogen sulfide in the vessel from about 1.0 mole methylmorpholine-N-oxide:1.0 mole hydrogen sulfide to about about 3.0 moles methylmorpholine-N-oxide: 1.0 mole hydrogen sulfide.
6. The method of claim 1 , wherein the steam comprises 150 psig steam or less.
7. The method of claim 1 , further comprising introducing the steam to the vessel to increase the temperature of the hydrocarbon to a temperature of from about 70° F. to about 150° F.
8. The method of claim 1 , further comprising recirculating between about one volume of the hydrocarbon in the vessel to about ten volumes of the hydrocarbon in the vessel.
9. The method of claim 8 , wherein the recirculating further comprises heating the hydrocarbon.