Methods and systems for predicting a need for introducing anti-fouling additives to a hydrocarbon stream to reduce fouling of crude hydrocarbon refinery components
US-9416325-B2 · Aug 16, 2016 · US
US9657116B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9657116-B2 |
| Application number | US-201414900989-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2014 |
| Priority date | Sep 23, 2013 |
| Publication date | May 23, 2017 |
| Grant date | May 23, 2017 |
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Disclosed is a method of functionalizing a vinyl terminated polyolefin, the method comprising combining a vinyl terminated polyolefin and a α,β-unsaturated carbonyl compound at a temperature of at least 150° C. and a pressure of at least 14 psi, forming a functionalized polyolefin. The functionalized polyolefin comprises a compound or mixture of compounds represented the formula: wherein each R 1 is, independently, selected from hydrogen and C 1 to C 4 or C 10 alkyls; n is an integer from 2 to 800; and each X is, independently, a functional group derived from the α,β-unsaturated carbonyl compound.
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The invention claimed is: 1. A method of functionalizing a vinyl terminated polyolefin, the method comprising combining a vinyl terminated polyolefin and a α,β-unsaturated carbonyl compound at a temperature of at least 150° C. and a pressure of at least 14 psi, forming the functionalized polyolefin, wherein the α,β-unsaturated carbonyl compound is compound or mixture of compounds represented by one or more of the following formulae: wherein the functionalized polyolefin is a compound or mixture of compounds represented the one or more of the following formulae: wherein each R 1 is, independently, selected from hydrogen or C 1 to C 10 alkyls; n is an integer from 2 to 800; and each X is, independently, a functional group derived from the α,β-unsaturated carbonyl compound. 2. The method of claim 1 , wherein the vinyl terminated polyolefin is compound or mixture of compounds represented the formula: wherein R is selected from hydrogen and C 1 to C 4 or C 10 alkyls; and n is an integer from 2 or to 800. 3. The method of claim 1 , wherein the vinyl terminated polyolefin has a number average molecular weight (Mn) within the range from 200 g/mole to 30,000 g/mole. 4. The method of claim 1 , wherein the functionalized polyolefin has at least 0.3 functional groups per polyolefin chain. 5. The method of claim 1 , wherein the combining takes place in a period within the range from a few minutes or 10 minutes to 24 hours. 6. The method of claim 1 , wherein the combining takes place in the presence of a Lewis Acid selected from the group consisting of titanium halides, titanium alkyls and alkoxys, tin halides, tin alkyls and alkoxys, aluminum halides, aluminum alkyls and alkoxys, boron halides, boron alkyls and alkoxys, zinc halides, and combinations thereof. 7. The method of claim 6 , wherein the temperature of combining is within the range of from 0° C. to 60° C. 8. The method of claim 1 , wherein the combining takes place in an inert atmosphere. 9. The method of claim 1 , wherein from 0.8 to 6.0 equivalents of the α,β-unsaturated carbonyl compound are added per equivalent of VTP.
Reaction with unsaturated dicarboxylic acids or anhydrides thereof, e.g. maleinisation · CPC title
leading to the formation or introduction of aliphatic or alicyclic unsaturated groups · CPC title
taking place solely at one end or both ends of the polymer backbone, i.e. not in the side or lateral chains · CPC title
Propene · CPC title
Isobutene · CPC title
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