Method to treat flushing liquor systems in coke plants
US-2015053622-A1 · Feb 26, 2015 · US
US10047301B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10047301-B2 |
| Application number | US-201615291511-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 12, 2016 |
| Priority date | Oct 12, 2015 |
| Publication date | Aug 14, 2018 |
| Grant date | Aug 14, 2018 |
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Disclosed herein are methods for resolving emulsions formed from oils present in quench waters of ethylene manufacturing operations. The methods include adding a cationic oligomer to the base of a water quench tower having an emulsion formed therein, and collecting a water phase therefrom. The water phase can be applied to a water recycling loop within the manufacturing facility.
Opening claim text (preview).
What is claimed is: 1. A method of resolving pygas emulsions, the method comprising: adding about 0.1 ppm to 200 ppm of a cationic oligomer to a pygas emulsion present within a water recycling loop of an ethylene manufacturing plant; and collecting a water phase resolved therefrom, wherein the cationic oligomer has a molecular weight of about 400 g/mol to 2000 g/mol and comprises repeat units derived from (2,3-epoxypropyl)trialkylammonium chloride. 2. The method of claim 1 wherein the pygas emulsion is present in a water quench tower or in an oil/water separator. 3. The method of claim 1 wherein the pygas emulsion is present in the base of the water quench tower at about 60° C. to 100° C. 4. The method of claim 1 wherein the pygas emulsion comprises a pytar fraction. 5. The method of claim 1 comprising adding about 1 ppm to 10 ppm of the cationic oligomer to the pygas emulsion. 6. The method of claim 1 wherein the molecular weight of the cationic oligomer is about 500 g/mol to 1000 g/mol. 7. The method of claim 1 wherein the oligomer consists essentially of a homo-oligomer comprising repeat units derived from (2,3-epoxypropyl)trialkylammonium chloride. 8. The method of claim 1 wherein the cationic oligomer comprises a net charge of about +3 to +20. 9. The method of claim 1 wherein the addition and the collection are carried out continuously. 10. The method of claim 1 wherein the collected water phase is applied to a water recycling loop within the ethylene manufacturing plant. 11. A resolved pygas emulsion present within a water recycling loop of an ethylene manufacturing plant, the resolved pygas emulsion comprising a pygas phase and water phase, the resolved pygas emulsion comprising a cationic oligomer comprising repeat units derived from a (2,3-epoxypropyl)trialkylammonium chloride and having a molecular weight of about 400 g/mol to 2000 g/mol and a net charge of about +3 to +20. 12. The resolved pygas emulsion of claim 11 wherein the water phase comprises about 1% to 25% lower total organic carbon content than a water phase of a resolved emulsion wherein no cationic oligomer was added to the emulsion. 13. The resolved pygas emulsion of claim 11 characterized by the absence of precipitated pygas emulsion components. 14. The resolved pygas emulsion of claim 11 wherein the pygas phase comprises a pytar fraction. 15. The resolved pygas emulsion of claim 11 wherein the 2,3-epoxypropyl)trialkylammonium chloride is 2,3-epoxypropyl)trimethylammonium chloride.
containing halogen · CPC title
with chemical means · CPC title
with separation aids · CPC title
by addition of specified substances, e.g. trace elements, for ameliorating potable water (medicinal water A61K) · CPC title
containing nitrogen · CPC title
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