Process of injecting a micellar dispersion into a subterranean reservoir

Claim 2

In a process of injecting a micellar dispersion into a subterranean reservoir wherein the micellar dispersion is comprised of a petroleum sulfonate surfactant, hydrocarbon and water in an amount of from about 20 to about 95 percent by weight and the dispersion contains sufficient amounts of wax having an average molecular weight of about 240 to about 600 to adversely influence the injectivity of the micellar dispersion into the reservoir, the improvement comprising incorporating about 0.1 to about 10 weight percent of a paraffinic hydrocarbon having an average molecular weight of about 50 to about 200 within the micellar dispersion and then injecting the dispersion into the reservoir.

Claim 3

The process of claim 1 wherein the average molecular weight of the paraffinic hydrocarbon is about 75 to about 150.

Claim 4

The process of claim 1 wherein the micellar dispersion contains about 0.005 to about 0.5 percent of wax.

Claim 5

The process of claim 1 wherein the petroleum sulfonate is obtained by sulfonating crude oil.

Claim 6

The process of claim 1 wherein about 0.5 to about 5 percent of the paraffinic hydrocarbon is incorporated into the micellar dispersion.

Claim 7

The process of claim 1 wherein the micellar dispersion contains about 1 to about 75 percent by weight of hydrocarbon and at least about 2.5 percent by weight of Petroleum sulfonate.

Claim 8

In a process of injecting a micellar dispersion into a subterranean reservoir wherein the dispersion is comprised of a petroleum sulfonate obtained by sulfonating whole crude oil, about 1 to about 75 percent by weight of hydrocarbon and water in an amount of from about 20 to about 95 percent by weight and the dispersion contains a sufficient amount of a wax (defined as the precipitate which forms after 1 part of the hydrocarbon within the micellar dispersion is dissolved in 2 parts of methylethyl ketone at about 80°C. and the mixture chilled to -25°C.) to adversely influence the injectivity of the micellar dispersion and wherein the micellar dispersion, before injection, is subjected to a reduction in temperature which results in the formation of wax particles causing the adverse injectivity, the improvement comprising incorporating into the micellar dispersion about 0.5 to about 5 weight percent of a paraffinic hydrocarbon having an average molecular weight of about 50 to about 200 and thereafter injecting the dispersion into the reservoir.

Claim 9

In a process of injecting a micellar dispersion into a subterranean reservoir wherein the dispersion is comprised of a petroleum sulfonate obtained by sulfonating whole crude oil, about 1 to about 75 percent by weight of hydrocarbon and water in an amount of from about 20 to about 95 percent by weight and the dispersion contains a sufficient amount of a wax (defined as the precipitate which forms after 1 part of the hydrocarbon within the micellar dispersion is dissolved in 2 parts of methylethyl ketone at about 80°C. and the mixture chilled to -25°C.) to adversely influence the injectivity of the micellar dispersion and wherein the micellar dispersion, before injection, is subjected to a reduction in temperature which results in the formation of wax particles causing the adverse injectivity, the improvement comprising incorporating into the micellar dispersion about 0.5 to about 5 weight percent of a paraffinic hydrocarbon having an average molecular weight of about 50 to about 200 and thereafter injecting the dispersion into the reservoir.

Claim 10

The process of claim 7 wherein the average molecular weight of the paraffinic hydrocarbon is about 75 to about 150.

Claim 11

The process of claim 7 wherein the wax concentration of the micellar dispersion is about 0.05 to about 0.25.

Claim 12

The process of claim 7 wherein the micellar dispersion contains about 5 to about 15 percent by weight of hydrocarbon, about 4 to about 25 percent by weight of petroleum sulfonate and about 65 to about 80 percent by weight of water.