Hydrocarbon mobility and recovery through in-situ combustion with the addition of ammonia
View Patent ↗Air and ammonia gas are introduced into a subterranean formation during the in-situ combustion to increase the mobility of hydrocarbons in a subterranean formation and facilitate recovery of the hydrocarbons from the subterranean formation. The air supports in-situ combustion of a portion of the hydrocarbon within the subterranean formation to form water and establish a combustion front. The ammonia gas contacts the hydrocarbons ahead of the combustion front and reacts in-situ with naphthenic acid in the hydrocarbon to form a surfactant. The hydrocarbons, water and surfactant then form an oil-in-water emulsion that drains more freely through the formation. A production well, in fluid communication with the hydrocarbons ahead of the combustion front, may be used to remove the oil-in-water emulsion from the subterranean formation.
1. A method for recovering hydrocarbons from a subterranean formation, comprising:
introducing steam into the subterranean formation; and then
introducing air and ammonia gas into the subterranean formation, wherein the air supports in-situ combustion of a portion of the hydrocarbon within a subterranean formation to form water and establish a combustion front, wherein the ammonia gas contacts the hydrocarbons ahead of the combustion front and reacts in-situ with naphthenic acid in the hydrocarbon to form a surfactant, and wherein the hydrocarbons, water and surfactant form an oil-in-water emulsion thereby suspending the hydrocarbons in the water;
using a production well in fluid communication with the hydrocarbons ahead of the combustion front to remove the oil-in-water emulsion from the subterranean formation; and
breaking the oil-in-water emulsion to separate the hydrocarbons from the water.
2. The method of claim 1 , wherein the ammonia gas is substantially free from amines.
3. The method of claim 1 , wherein the air and the ammonia gas are substantially free from combustible compositions.
4. The method of claim 1 , wherein the steam includes ammonia gas.
5. The method of claim 4 , wherein the steam is substantially free from liquid water.
6. The method of claim 1 , wherein the air and the ammonia gas are introduced into the subterranean formation through an injection well.
7. The method of claim 1 , wherein the air and the ammonia gas are introduced into the subterranean formation through an injection well, and wherein the production well is a horizontal well disposed below the injection well.
8. The method of claim 1 , wherein the ammonia concentration in the air is from about 50 to about 50,000 ppm by weight.
9. The method of claim 1 , wherein the ammonia concentration in the air is from about 1,000 to about 10,000 ppm by weight.