Method to treat flushing liquor systems in coke plants

US10308532B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10308532-B2
Application numberUS-201214394272-A
CountryUS
Kind codeB2
Filing dateApr 18, 2012
Priority dateApr 18, 2012
Publication dateJun 4, 2019
Grant dateJun 4, 2019

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Abstract

Official abstract text for this publication.

Methods are disclosed for reducing oil in water emulsions in coking processes. One exemplary method comprises: providing an aqueous stream with an oil in water emulsion; providing a treatment composition, wherein the treatment composition comprises at least one cationic polyacrylamide; and contacting the aqueous stream with the treatment composition.

First claim

Opening claim text (preview).

What is claimed is: 1. A method of demulsifying an oil in water emulsion present in an aqueous stream of a coking process comprising: passing said aqueous stream comprising an oil in water emulsion from an upstream to downstream direction to and through a decanter, wherein said oil in water emulsion comprises tars and other contaminants formed in a coking process; and contacting said aqueous stream with a treatment composition prior to introducing said aqueous stream into the decanter of said coking process, said treatment composition comprising a cationic polyacrylamide copolymer and downstream from said decanter, contacting said aqueous stream with an ethoxylated surfactant in addition to, or instead of any surfactant present in said treatment composition, wherein said ethoxylated surfactant comprises at least one ethoxylated compound having the formula: R—O—(CH 2 CH 2 O) n —H where n is equal to or greater than about 20; and R is at least one chain of a branched alkyl phenol, a branched or linear fatty alcohol, a fatty acid alkanolamide, or a fatty acid, and said cationic polyacrylamide copolymer comprising repeat units (x) and (y) of the formula wherein R 1 and R 2 are the same or different and are chosen from H and CH 3 ; Q is —C(O)O—, or —OC(O)—, or —C(O)NH—; R 3 is branched or linear C 1 -C 4 alkyl; R 4 , R 5 , and R 6 are independently chosen from H, C 1 -C 4 linear or branched alkyl, or a C 5 -C 8 aromatic or alkylaromatic group; A is an anion selected from Cl − , Br − , HSO 4 − , or MeOSO 3 − wherein the molar ratio of repeat units (x):repeat units (y) is about 10:90 to about 40:60. 2. The method of claim 1 , wherein said repeat unit (y) comprises at least one member selected from the group consisting of dimethylaminoethyl (meth)acrylate methyl chloride quaternary salt, dimethylaminoethyl (meth)acrylate methyl sulfate quaternary salt, dimethylaminoethyl (meth)acrylate benzyl chloride quaternary salt, acrylamidopropyl trimethylammonium chloride, dimethylaminopropyl (meth)acrylamide methyl sulfate quaternary salt, diallyldiethylammonium chloride, and diallyldimethyl ammonium chloride. 3. The method of claim 2 , wherein: said repeat unit (y) comprises dimethylaminoethyl (meth)acrylate methyl chloride quaternary salt; and said repeat unit (x) comprises acrylamide. 4. The method of claim 3 , wherein a molar ratio of repeat units (x):repeat units (y) is about 20:80. 5. The method of claim 1 , wherein said treatment composition comprises about 0.01 ppm to about 1000 ppm by volume of said aqueous stream. 6. The method of claim 5 , wherein said treatment composition comprises from about 0.5 ppm to about 500 ppm by volume of said aqueous stream. 7. The method of claim 6 , wherein said treatment composition comprises from about 1 ppm to about 10 ppm by volume of said aqueous stream. 8. The method of claim 7 , wherein a concentration ratio in ppm of said ethoxylated surfactant to said cationic polyacrylamide copolymer in said treatment composition ranges from about 4:1 to about 1:4. 9. The method of claim 1 , wherein a concentration ratio in ppm of said ethoxylated surfactant to said cationic polyacrylamide copolymer in said treatment composition is about 2:1.5. 10. The method of claim 1 , wherein a concentration ratio in ppm of said ethoxylated surfactant to said cationic polyacrylamide copolymer in said treatment composition is about 2:1. 11. The method as recited in claim 1 , wherein said contaminants comprise ammonia, hydrophobic compounds, coal powder, coke powder, solids, or a combination thereof. 12. A method of demulsifying an oil in water emulsion present in an aqueous stream of a coking process comprising: passing said aqueous stream comprising an oil in water emulsion from an upstream to downstream direction to and through a decanter, wherein said oil in water emulsion comprises tars and other contaminants formed in a coking process; and contacting said aqueous stream with a treatment composition prior to introducing said aqueous stream into the decanter of said coking process, said treatment composition comprising a cationic acrylamide copolymer and downstream from said decanter, contacting said aqueous stream with an ethoxylated surfactant in addition to, or instead of any surfactant present in said treatment composition, wherein said ethoxylated surfactant comprises at least one ethoxylated compound having the formula: R—O—(CH 2 CH 2 O) n —H where n is equal to or greater than about 20; and R is at least one chain of a branched alkyl phenol, a branched or linear fatty alcohol, a fatty acid alkanolamide, or a fatty acid, and said cationic acrylamide copolymer comprising repeat units of (x) (meth)acrylamide and (y) quaternary ammonium salt; wherein said repeat unit (y) of said cationic acrylamide copolymer comprises a member selected from the group consisting of: a) dimethylaminoethyl (meth)acrylate methyl chloride; b) dimethylaminoethyl (meth)acrylate methyl sulfate; c) dimethylaminoethyl (meth)acrylate benzyl chloride; d) acrylamidopropyl trimethylammonium chloride; e) dimethylaminopropyl (meth)acrylamide methyl sulfate; f) diallyldiethyl ammonium chloride; and g) diallyldimethylammonium chloride. 13. The method as recited in claim 12 , wherein said repeat unit (y) is dimethylaminoethyl (meth)acrylate quaternary ammonium salt and wherein the molar ratio of repeat units (x):repeat units (y) is from about 10:90 to about 40:60. 14. The method as recited in claim 13 , wherein said repeat unit (y) is dimethylaminoethyl (meth)acrylate methyl chloride. 15. The method as recited in claim 14 , wherein said molar ratio of repeat units (x):repeat units (y) is about 20:80. 16. The method as recited in claim 15 , further comprising contacting said aqueous stream with a sorbitan mono-oleate surfactant. 17. The method as recited in claim 12 , wherein said contaminants comprise ammonia, hydrophobic compounds, coal powder, coke powder, solids, or a combination thereof.

Assignees

Inventors

Classifications

  • Acrylamide; Methacrylamide · CPC title

  • Tensides · CPC title

  • C02F1/5272Primary

    using specific organic precipitants · CPC title

  • Use of specific compounds during water treatment · CPC title

  • Coking (in order to produce liquid products mainly) · CPC title

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What does patent US10308532B2 cover?
Methods are disclosed for reducing oil in water emulsions in coking processes. One exemplary method comprises: providing an aqueous stream with an oil in water emulsion; providing a treatment composition, wherein the treatment composition comprises at least one cationic polyacrylamide; and contacting the aqueous stream with the treatment composition.
Who is the assignee on this patent?
Zhang Guixi, Zhao Jason, Bl Technologies Inc
What technology area does this patent fall under?
Primary CPC classification C02F1/5272. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jun 04 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).