Monomer selection to prepare ultra high molecular weight drag reducer polymer
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 an ultra high molecular weight polymer.
1. A process, comprising:
preparing a mixture comprising a first batch of monomers and a second batch of monomers distinct from the first batch of monomers, wherein the first batch of monomers comprises acrylates with side alkyl chains having four or less carbons, methacrylates with side alkyl chains having four or less carbons, or combinations thereof, the second batch of monomers comprises acrylates with side alkyl chains having greater than four carbons, methacrylates with side alkyl chains having greater than four carbons, or combinations thereof, and the second batch is greater than 50% by weight of the mixture; and
polymerizing the mixture to produce an ultra high molecular weight polymer including at least 25,000 repeating units and a weight average molecular weight greater than five million.
2. The process of claim 1 , further comprising adding the ultra high molecular weight polymer to a liquid hydrocarbon to produce a treated liquid hydrocarbon.
3. The process of claim 2 , wherein a viscosity of the treated liquid hydrocarbon is not less than a viscosity of the liquid hydrocarbon prior to adding the ultra high molecular weight polymer.
4. The process of claim 2 , wherein the ultra high molecular weight polymer reduces friction loss associated with a turbulent flow of the liquid hydrocarbon through a pipeline.
5. The process of claim 2 , wherein the ultra high molecular weight polymer is added to the liquid hydrocarbon in a range from about 0.1 ppmw to about 500 ppmw.
6. The process of claim 1 , wherein the second batch of monomers comprises pentyl acrylate, pentyl methacrylate, isopentyl acrylate, isopentyl methacrylate, hexyl acrylate, hexyl methacrylate, cyclohexyl acrylate, cyclohexyl methacrylate, heptyl acrylate, heptyl methacrylate, octyl acrylate, octyl methacrylate, isooctyl acrylate, isooctyl methacrylate, isodecyl acrylate, isodecyl methacrylate, lauryl acrylate, lauryl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, benzyl acrylate, benzyl methacrylate, 2-phenylethyl acrylate, 2-phenylethyl methacrylate, tridecyl acrylate, tridecyl methacrylate, isobornyl acrylate, isobornyl methacrylate, 3,5,5-trimethylehexyl acrylate, 3,5,5-trimethylhexyl methcrylate, 3,3,5-trimethylcyclohexyl acrylate, 3,3,5-trimethylcyclohexyl methacrylate, or combinations thereof.
7. A process, comprising:
preparing a mixture comprising a first batch of monomers and a second batch of monomers, wherein the first batch of monomers comprises acrylates with side alkyl chains having four or less carbons, methacrylates with side alkyl chains having four or less carbons, or combinations thereof, the second batch of monomers comprises acrylates with side alkyl chains having greater than four carbons, methacrylates with side alkyl chains having greater than four carbons, or combinations thereof; and
polymerizing the mixture to produce an ultra high molecular weight polymer including at least 25,000 repeating units and a weight average molecular weight greater than five million.
8. The process of claim 7 , further comprising adding the ultra high molecular weight polymer to a liquid hydrocarbon to produce a treated liquid hydrocarbon.
9. The process of claim 8 , wherein a viscosity of the treated liquid hydrocarbon is not less than a viscosity of the liquid hydrocarbon prior to adding the ultra high molecular weight polymer.
10. The process of claim 8 , wherein the ultra high molecular weight polymer reduces friction loss associated with a turbulent flow of the liquid hydrocarbon through a pipeline.
11. The process of claim 8 , wherein the ultra high molecular weight polymer is added to the liquid hydrocarbon in a range from about 0.1 ppmw to about 500 ppmw.
12. The process of claim 7 , wherein the second batch of monomers comprises pentyl acrylate, pentyl methacrylate, isopentyl acrylate, isopentyl methacrylate, hexyl acrylate, hexyl methacrylate, cyclohexyl acrylate, cyclohexyl methacrylate, heptyl acrylate, heptyl methacrylate, octyl acrylate, octyl methacrylate, isooctyl acrylate, isooctyl methacrylate, isodecyl acrylate, isodecyl methacrylate, lauryl acrylate, lauryl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, benzyl acrylate, benzyl methacrylate, 2-phenylethyl acrylate, 2-phenylethyl methacrylate, tridecyl acrylate, tridecyl methacrylate, isobornyl acrylate, isobornyl methacrylate, 3,5,5-trimethylehexyl acrylate, 3,5,5-trimethylhexyl methcrylate, 3,3,5-trimethylcyclohexyl acrylate, 3,3,5-trimethylcyclohexyl methacrylate, or combinations thereof.
13. A process, comprising:
preparing a mixture comprising a first batch of monomers and a second batch of monomers distinct from the first batch of monomers, wherein the first batch of monomers comprises acrylates with side alkyl chains having four or less carbons, methacrylates with side alkyl chains having four or less carbons, or combinations thereof, the second batch of monomers comprises pentyl acrylate, pentyl methacrylate, isopentyl acrylate, isopentyl methacrylate, hexyl acrylate, hexyl methacrylate, cyclohexyl acrylate, cyclohexyl methacrylate, heptyl acrylate, heptyl methacrylate, octyl acrylate, octyl methacrylate, isooctyl acrylate, isooctyl methacrylate, isodecyl acrylate, isodecyl methacrylate, lauryl acrylate, lauryl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, benzyl acrylate, benzyl methacrylate, 2-phenylethyl acrylate, 2-phenylethyl methacrylate, tridecyl acrylate, tridecyl methacrylate, isobornyl acrylate, isobornyl methacrylate, 3,5,5-trimethylehexyl acrylate, 3,5,5-trimethylhexyl methcrylate, 3,3,5-trimethylcyclohexyl acrylate, 3,3,5-trimethylcyclohexyl methacrylate, or combinations thereof; and
polymerizing the mixture to produce an ultra high molecular weight polymer including at least 25,000 repeating units and a weight average molecular weight greater than five million.
14. The process of claim 13 , further comprising adding the ultra high molecular weight polymer to a liquid hydrocarbon to produce a treated liquid hydrocarbon.
15. The process of claim 14 , wherein a viscosity of the treated liquid hydrocarbon is not less than a viscosity of the liquid hydrocarbon prior to adding the ultra high molecular weight polymer.
16. The process of claim 14 , wherein the ultra high molecular weight polymer reduces friction loss associated with a turbulent flow of the liquid hydrocarbon through a pipeline.
17. The process of claim 14 , wherein the ultra high molecular weight polymer is added to the liquid hydrocarbon in a range from about 0.1 ppmw to about 500 ppmw.
18. The process of claim 13 , wherein the polymerizing the mixture comprises emulsion polymerizing the mixture.
19. The process of claim 18 , wherein the mixture further comprises a continuous phase, at least one surfactant, and an initiation system.
20. The process of claim 19 , wherein the continuous phase comprises water, polar organic liquids, or mixtures thereof.