Pyrolysis method and system for recycled waste
AssigneeExxonMobil Product Solutions Company
InventorsXianchun Wu, Daryl Bitting, Kenny Randolph Parker, Michael Gary Polasek, David Eugene Slivensky, Damon Ray Billodeaux
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Abstract
A pyrolysis method and system are provided that utilizes a multistage dehalogenation method to effectively remove halogen-containing compounds that are present in an initial recycled plastic feedstock. More particularly, the multistage dehalogenation system and process may involve physical sorting the plastic feedstock, melting and separating the feedstock, and subjecting the feedstock a two-stage pyrolysis with intermediate HCl removal.
Claims21
A method of making a pyrolysis oil, said method comprising:
- a) providing a plastic-containing feed comprising at least one halogen-containing waste plastic;
- b) dehalogenating at least a portion of said plastic-containing feed in a pretreatment unit to thereby form a halogen waste stream and a dehalogenated feed, wherein the dehalogenating comprises physically separating solid halogen-containing waste plastic from at least one other type of waste plastic upstream of a pyrolysis unit;
- and
- c) pyrolyzing at least a portion of said dehalogenated feed to thereby form a pyrolysis effluent comprising a pyrolysis oil, wherein said pyrolysis oil:
- i.) comprises an aromatic content of less than 25 weight percent,
- ii.) comprises an alkane content of at least 25 weight percent,
- iii.) comprises a 90% boiling point of at least 350° C.;
- and
- iv.) exhibits a density at 15° C. of less than 0.9 g/cm3,
- wherein said dehalogenating of step (b) comprises pretreating said plastic-containing feed by heating to a temperature in a range from at least 150° C. and not more than 325° C. for a time sufficient to remove at least 5 percent of the halogen originally present in the plastic-containing feed and thereby release a halogen-containing waste stream and form a dehalogenated feed having a halogen content of not more than 1000 ppm,
- wherein said pyrolyzing of step (c) occurs at a temperature of at least 450° C. and not more than 1100° C., and
- wherein the pyrolysis oil is not hydrotreated.
Dependencies are inferred from the claim text.