Method of preventing corrosion of oil pipelines, storage structures and piping
View Patent ↗Corrosion of ferrous material such as steel or stainless steel is a problem in oil pipelines, oil storage tanks, and the piping and process equipment at oil refineries, and this corrosion may be reduced by reducing the TAN value of the oil feedstock that is used/transported within the ferrous material. This TAN value may be reduced by reacting the oil feedstock with an alkali metal, thereby forming a de-acidified alkali metal. The de-acidified alkali metal has a TAN value of less than or equal to 1 mgKOH/g.
1. A method comprising:
electrochemically producing an alkali metal in its metallic state,
reacting an oil feedstock comprising naphthenic acids with the alkali metal in its metallic state to form a de-acidified oil feedstock, and
processing and/or transporting the de-acidified oil feedstock in a ferrous material,
wherein
the oil feedstock has a TAN value greater than or equal to 1 mg KOH/g, and
the de-acidified oil feedstock has a TAN value that is at or near 0 mg KOH/g.
2. The method of claim 1 , wherein the alkali metal in its metallic state comprises lithium, sodium, potassium and/or alloys thereof.
3. The method of claim 1 , wherein the de-acidified oil feedstock comprises a quantity of the alkali metal in its metallic state.
4. The method of claim 1 , wherein the oil feedstock comprises heteroatoms/heavy metals, and
the alkali metal further reacts with the heteroatoms/heavy metals such that a heteroatom to carbon ratio of the de-acidified oil feedstock is less than a heteroatom to carbon ratio of the oil feedstock.
5. The method of claim 4 , wherein the reaction of the alkali metal occurs in the presence of a non-oxidizing gas.
6. A method comprising:
reacting an alkali metal in its metallic state with an oil feedstock in the presence of a non-oxidizing gas comprising hydrogen and/or hydrocarbon gases, wherein the oil feedstock comprises naphthenic acids and the oil feedstock has a TAN value of greater than or equal to 1 mg KOH/g;
removing solids formed from the reaction to provide a liquid de-acidified oil feedstock, and
contacting the de-acidified oil feedstock liquid with a ferrous material,
wherein the liquid de-acidified oil feedstock has a TAN value that is at or near 0 mg KOH/g;
and wherein the alkali metal in its metallic state is formed by electrochemically reducing alkali metal ions.
7. The method of claim 6 wherein the non-oxidizing gas comprises hydrogen, methane, natural gas, shale gas, and/or mixtures thereof.
8. The method of claim 6 wherein the non-oxidizing gas comprises methane, ethane, propane, butane, pentane, isomers of the foregoing, ethene, propene, butene, pentene, dienes, and/or mixtures thereof.