Using gases and hydrocarbon recovery fluids containing nanoparticles to enhance hydrocarbon recovery
A process of stimulating hydrocarbon recovery is described and claimed. This process includes introducing a gas, a liquified gas or a vaporized liquified gas, into an underground formation containing hydrocarbons such as crude oil and gas, permitting said gas to be absorbed by said hydrocarbons, and withdrawing said hydrocarbons containing the gas therein, wherein a pill of Hydrocarbon Recovery Fluid comprising surface functionalized nanoparticles is inserted into the underground formation containing hydrocarbons before, during or after the introduction of the gas, liquified gas or a vaporized liquified gas.
1. A process of stimulating hydrocarbon recovery comprising
(a) introducing a gas, a liquefied gas or vaporized liquefied gas into an underground formation containing hydrocarbons;
(b) permitting said gas, liquefied gas or vaporized liquefied gas to be absorbed by said hydrocarbons;
(c) withdrawing said hydrocarbons containing said gas, liquefied gas or vaporized liquefied gas absorbed therein; and
(d) inserting a pill of hydrocarbon recovery fluid comprising an aqueous silica sol comprising surface functionalized nanoparticles into the underground formation, before the introduction of the gas, liquefied gas or vaporized liquefied gas, wherein said surface functionalized nanoparticles are brine resistant silica sol nanoparticles surface functionalized with a silane compound having at least one organic functional group selected from the group consisting of a vinyl group, an ether group, an epoxy group, a styryl group, a methacryl group, an acryl group, an amino group, an isocyanurate group, an alkoxysilane group, a silazane group and a siloxane group, and wherein the surface functionalized nanoparticles alter wettability of solid/liquefied surfaces and facilitate flow of the hydrocarbons.
2. The process of claim 1 wherein the gas, liquefied gas or vaporized liquefied gas and the pill include one or more injectants selected from the group consisting of fresh water, potassium chloride water and diverters.
3. The process of claim 1 wherein said gas is selected from the group consisting of carbon dioxide, nitrogen, natural gas, and mixtures thereof.
4. The process of claim 3 wherein said gas is a mixture of two or more gases selected from the group consisting of carbon dioxide, nitrogen and natural gas.
5. The process of claim 3 wherein said process is part of a huff and puff treatment process.
6. The process of claim 5 wherein said process is a waterless fracturing process.
7. The process of claim 1 wherein the gas is introduced and said gas is carbon dioxide.
8. The process of claim 1 wherein the gas is introduced and said gas is nitrogen.
9. The process of claim 1 wherein the gas is introduced and said gas is natural gas.
10. The process of claim 1 wherein the liquefied gas is introduced and said liquefied gas is liquefied natural gas, liquefied carbon dioxide, or mixtures thereof.
11. The process of claim 1 wherein said hydrocarbon recovery fluid comprises:
sodium hydroxide,
one anionic surfactant, and
one nonionic surfactant.
12. The process of claim 1 , wherein the underground formation is a conventional well with a porosity of greater than 8%.
13. The process of claim 1 , wherein the underground formation is an unconventional well with a porosity of greater than 4%.
14. The process of claim 1 , wherein the underground formation has an API oil gravity of less than 30.