Drag reduction of asphaltenic crude oils
Abstract
The process begins by obtaining a first batch of monomers selected from a group of acrylates with a molecular weight equal to or less than butyl acrylate and/or methacrylate with a molecular weight equal to or less than butyl methacrylate. A second batch of monomers is then selected from a group of acrylates with a molecular weight greater than butyl acrylate and/or methacrylate with a molecular weight greater than butyl methacrylate. A mixture is then prepared by mixing the first batch of monomers and the second batch of monomers, wherein the second batch of monomers are greater than 50% by weight of the mixture. Finally, the mixture is polymerized to produce a drag reducing polymer. The drag reducing polymer is capable of imparting drag reducing properties in liquid hydrocarbons.
Claims
exact text as granted — not AI-modified1 - 14 . (canceled)
15 . A method comprising:
introducing a drag reducing polymer into a liquid hydrocarbon in a pipeline to thereby produce a treated liquid hydrocarbon wherein the viscosity of the treated liquid hydrocarbon is not less than the viscosity of the liquid hydrocarbon prior to treatment with the drag reducing polymer; and the drag reducing polymer is added to the liquid hydrocarbon in the range from about 0.1 to about 500 ppmw.
16 . The method of claim 15 , wherein the solubility parameter of the drag reducing polymer is at least about 17 MPa1/2.
17 . The method of claim 15 , wherein the drag reducing polymer comprises at least about 25,000 repeating units.
18 . The method of claim 15 , wherein the drag reducing polymer has a weight average molecular weight of at least 1×106 g/mol.
19 . The method of claim 15 , wherein a plurality of the repeating units comprise a heteroatom.
20 . The method of claim 15 , wherein the heteroatom is selected from the group consisting of an oxygen atom, a nitrogen atom, a sulfur atom and/or a phosphorus atom.Join the waitlist — get patent alerts
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