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US 12,753,352 B2Granted
Systems and methods for removal of halogenated contaminants from pyrolysis oil by inert gas purging
AssigneeSabic Global Technologies B.V.
InventorsFabrice Cuoq, Martijn Marcel Margaret Frissen, Carlo Jozef Maria Geijselaers, Kae Wong
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Abstract
Provided here are methods and systems for converting pyrolysis oil with halogenated contaminants to a substantially halogen-free pyrolysis oil by treatment with an inert gas.
Claims20
A method of treating a pyrolysis oil to remove halogenated contaminants, the method comprising:
- supplying an inert gas stream to a storage vessel containing a pyrolysis oil with halogenated contaminants while the storage vessel is maintained at ambient temperatures to produce a halogen-enriched inert gas stream and a first dehalogenated pyrolysis oil containing at least twenty weight percent less of the halogenated contaminants as compared to the pyrolysis oil, wherein the halogenated contaminants include organic chloride contaminants;
- conveying the first dehalogenated pyrolysis oil and water to a reactor equipped with a mixing element;
- mixing the first dehalogenated pyrolysis oil and water in the reactor to produce a halogen-enriched water stream and a second dehalogenated pyrolysis oil containing at least twenty weight percent less of the halogenated contaminants as compared to the first dehalogenated pyrolysis oil;
- and
- separating the halogen-enriched water stream from the second dehalogenated pyrolysis oil to produce a substantially halogen-free pyrolysis oil.
2 more elements
A system for treating a pyrolysis oil to remove halogenated contaminants, the system comprising:
- a storage vessel containing a pyrolysis oil with halogenated contaminants maintained at ambient temperatures and equipped with a first inlet for receiving an inert gas stream, a first outlet for discharging a halogen-enriched inert gas stream, and a second outlet connected to and in fluid communication with a second inlet of a reactor, the halogen-enriched inert gas stream being produced along with a first dehalogenated pyrolysis oil from interactions between the inert gas stream and the pyrolysis oil, and the first dehalogenated pyrolysis oil containing at least twenty weight percent less of the halogenated contaminants as compared to the pyrolysis oil, wherein the halogenated contaminants include organic chloride contaminants;
- the reactor equipped with the second inlet to receive the first dehalogenated pyrolysis oil, a third inlet to receive water, a mixing element to mix the first dehalogenated pyrolysis oil and the water, and a third outlet connected to and in fluid communication with a fourth inlet of a separator;
- and
- the separator equipped with the fourth inlet to receive a mixture of the first dehalogenated pyrolysis oil and the water from the third outlet, the separator being operated to separate the mixture of the first dehalogenated pyrolysis oil and the water to produce a halogen-enriched water stream and a second dehalogenated pyrolysis oil containing at least twenty weight percent less of the halogenated contaminants as compared to the first dehalogenated pyrolysis oil.
1 more element
Dependencies are inferred from the claim text.