Environmentally friendly dispersion system used in the preparation of inverse emulsion polymers
US-9193898-B2 · Nov 24, 2015 · US
US9840654B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9840654-B2 |
| Application number | US-201213679457-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2012 |
| Priority date | Nov 16, 2012 |
| Publication date | Dec 12, 2017 |
| Grant date | Dec 12, 2017 |
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A kinetic gas hydrate inhibitor is provided as a polyester polymer with a plurality of amino or ammonium groups pendent directly from the backbone. A composition containing concentrated kinetic inhibitor is injected into gas wells, or into other systems involving transporting liquid gas mixtures through a conduit. Use of the kinetic inhibitor prevents formation of gas hydrates under conditions of temperature and pressure where they would otherwise occur.
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What is claimed is: 1. A method for inhibiting gas hydrate formation in an aqueous phase that is in contact with a gaseous or liquid organic phase, the method comprising: preparing a composition comprising 10-50% by weight of a kinetic inhibitor, and injecting the composition into the aqueous phase to provide the aqueous phase with 0.01-3% by weight of the kinetic inhibitor, wherein the kinetic inhibitor is a polyester polymer comprising a polyester backbone chain and a plurality of pendent amino groups that are directly attached to the polyester backbone chain, and wherein the polyester polymer is produced by polymerizing a plurality of acid monomers with a plurality of polyols, each of the acid monomers comprising the pendent amino group. 2. The method according to claim 1 , wherein the aqueous phase comprises 0.01-2 weight % of the kinetic inhibitor. 3. The method according to claim 1 , wherein the inhibitor is made by polymerizing an amino functional diacid, diester, or mixed acid ester with an alkylene or oxyalkylene diol or triol. 4. The method according to claim 1 , wherein the inhibitor is made by polymerizing a diacid, diester, or mixed acid ester with an amine functional diol or triol. 5. The method according to claim 1 , wherein the acid monomers have the following structure and the polyols have the following structure B(OH) n wherein X is amino, A is alkylene of 1 to 40 carbon atoms, R 1 and R 2 are independently —H or alkyl, B is selected from branched or unbranched alkylene and branched or unbranched oxa-substituted alkylene, and n is 2, 3, or 4. 6. The method according to claim 5 wherein A is C 2 -C 6 alkylene, B is C 2 -C 12 alkylene or polyoxyalkylene, and n is 2 or 3. 7. The method according to claim 5 , wherein A is C 3 alkylene or C 4 alkylene and the polyol component is ethylene glycol, diethylene glycol, or triethylene glycol. 8. The method according to claim 5 , wherein the acid monomers are selected from the group consisting of aspartic acid, glutamic acid, protected aspartic acid, and protected glutamic acid. 9. The method according to claim 8 , wherein the polyols are selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, and tetraethylene glycol. 10. The method according to claim 1 , further comprising providing the aqueous phase with a synergist made of C 3 to C 10 ethers of C 2 to C 4 glycols. 11. The method according to claim 10 , wherein the synergist is C 3 to C 6 ethers of C 2 to C 3 glycols. 12. The method according to claim 10 , wherein the synergist is selected from the group consisting of 2-butoxyethanol, 2-isopropoxyethanol, 1-propoxy-2-propanol, 2-(2-butoxyethoxy)ethanol, 1-butoxy-2-propanol, and 2-propoxyethanol. 13. The method according to claim 1 , wherein a solution of the kinetic inhibitor is greater than 20% biodegradable, exhibits no inherent cloud point behavior upon heating, and gives an induction time greater than 24hours at 6° C. subcooling using synthetic natural gas.
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