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Multistage thermolysis method for safe and efficient conversion of carpet/rug, polymeric materials and other waste sources

CHZ TECHNOLOGIES, LLC
2023
Online Patent

Titel:
Multistage thermolysis method for safe and efficient conversion of carpet/rug, polymeric materials and other waste sources
Autor/in / Beteiligte Person: CHZ TECHNOLOGIES, LLC
Link:
Veröffentlichung: 2023
Medientyp: Patent
Sonstiges:
  • Nachgewiesen in: USPTO Patent Grants
  • Sprachen: English
  • Patent Number: 11613,704
  • Publication Date: March 28, 2023
  • Appl. No: 16/701407
  • Application Filed: December 03, 2019
  • Assignees: CHZ TECHNOLOGIES, LLC (Austintown, OH, US)
  • Claim: 1. A Clean Fuel Gas source and a Char source, wherein a method for producing the Clean Fuel Gas source and the Char source comprises: inputting a carpet, rug, plastic, tire, manure, auto shredder residue, glass and carbon fiber composite material, municipal solid waste, medical waste, and/or waste wood waste source into a thermolysis system, wherein the thermolysis system comprises at least two reactors, at least two gas scrubbers, an oil/water separator, and an oil/tar cracker, wherein the reactors have a process temperature of about 300° C.-800° C. and generate tars and oils, and wherein all of the oils and tars are separated in the oil/water separator and the at least two gas scrubbers, thereafter cracked in the oil/tar cracker, and sent back to the secondary reactor; optionally increasing the moisture content of the waste source by injecting steam into the system or drying the waste source to decrease the moisture content; destroying and/or removing toxic compounds present in the waste source; and generating the Clean Fuel Gas source and the Char source, wherein the Clean Fuel Gas source and the Char source contain less than about 10 ppb of halogenated organic compounds.
  • Claim: 2. The Clean Fuel Gas source and the Char source of claim 1 , wherein the Clean Fuel Gas source and the Char source generated are free of the halogenated organic compounds.
  • Claim: 3. The Clean Fuel Gas source and the Char source of claim 1 , wherein the Clean Fuel Gas source and the Char source generated are free of tars and/or oils.
  • Claim: 4. The Clean Fuel Gas source and the Char source of claim 1 , wherein the toxic compounds and the halogenated organic compounds comprise aromatics and polycyclic aromatic hydrocarbons, halogenated dibenzodioxins, halogenated dibenzofurans, biphenyls, pyrenes, cadmium, lead, antimony, arsenic, beryllium, chlorofluorocarbons, mercury, and nickel present in the waste source.
  • Claim: 5. The Clean Fuel Gas source and the Char source of claim 1 , wherein the Char source comprises carbon and fillers, and wherein the Char source is suitable for further recycling or an additional step of removing fillers from the carbon for further reuse of the carbon and/or fillers.
  • Claim: 6. The Clean Fuel Gas source and the Char source of claim 1 , wherein the method further comprises the separation of oil-soluble substances from a gas/vapor mixture following the thermolytic conversion of hydrocarbons in the waste source.
  • Claim: 7. The Clean Fuel Gas source and the Char source of claim 1 , wherein the Clean Fuel Gas source is an energy source with from about 3,000 to 20,000 BTUs per pound of the waste source.
  • Claim: 8. A Clean Fuel Gas source and a Char source, wherein a method for producing the Clean Fuel Gas source and the Char source comprises: shredding or grinding a carpet, rug, plastic, tire, manure, auto shredder residue, glass and carbon fiber composite material, municipal solid waste, medical waste, and/or waste wood waste source to provide a substantially uniform waste source into a thermolysis system providing indirect heat in a system that is free of oxygen, wherein the thermolysis system comprises at least two reactors, at least two gas scrubbers, an oil/water separator, and an oil/tar cracker, wherein all of the oils and tars are separated in the oil/water separator and the at least two gas scrubbers, thereafter cracked in the oil/tar cracker, and sent back to the secondary reactor, wherein at least one reactor has a process temperature of from about 300° C.−800° C. and a pressure range from about 10 to about 100 millibar; optionally increasing the moisture content of the waste source to about 5-20% by injecting steam into the system or by drying a waste source to have a moisture content of about 5-20%; destroying and/or removing toxic compounds present in the waste source; generating a Char source, wherein the Char source comprises carbon and fillers and is suitable for further recycling; and generating a Clean Fuel Gas source from the pyrolytic conversion of hydrocarbons in the waste source, wherein the Clean Fuel Gas source is free of toxic compounds and halogenated organic compounds, and wherein from about 3,000 to 20,000 BTUs per pound of the waste source is generated as the Clean Fuel Gas source.
  • Claim: 9. The Clean Fuel Gas source and the Char source of claim 8 , wherein the toxic compounds and the halogenated organic compounds comprise aromatics and polycyclic aromatic hydrocarbons, halogenated dibenzodioxins, halogenated dibenzofurans, biphenyls, pyrenes, cadmium, lead, antimony, arsenic, beryllium, chlorofluorocarbons, mercury, and nickel present in the waste source.
  • Patent References Cited: 3825464 July 1974 Crowley ; 4159241 June 1979 Simo ; 4317800 March 1982 Sloterdijk et al. ; 5045177 September 1991 Cooper et al. ; 5427650 June 1995 Holloway ; 5771822 June 1998 Rizzon ; 6084139 July 2000 Van Der Giessen et al. ; 6178899 January 2001 Kaneko et al. ; 8419902 April 2013 Feerer et al. ; 8864057 October 2014 Bork et al. ; 8915199 December 2014 Bohlig et al. ; 11306255 April 2022 Brandhorst, Jr ; 20020117388 August 2002 Denison ; 20070045455 March 2007 Tuzson et al. ; 20080028889 February 2008 Irizarry-Rivera et al. ; 20090020052 January 2009 Becchetti et al. ; 20090062581 March 2009 Appel et al. ; 20100293853 November 2010 Feerer et al. ; 20130256113 October 2013 Tumiatti et al. ; 20140069798 March 2014 Hayward et al. ; 8112580 May 1996 ; 201077260 April 2010 ; 2011219708 November 2011 ; 20120055756 June 2012 ; 2015090477 June 2015
  • Other References: Zhou et al., “Polycyclic Aromatic Hydrocarbon Formation from the Pyrolysis/Gasification of Lignin at Different . . . ”, Energy and Fuels, pp. 6371-6379. Oct. 2014. cited by applicant ; Guidelines for Post Consumer Recycled Content in Plastic Packaging; GreenBlue, Aug. 24, 2014, http://web.archive.org/web/*/http://www.sustainablepackaging.org/uploads/resources/spc_pcr_plastic_packaging.pdf; p. 2, col. 2; p. 8, col. 2, accessed Feb. 21, 2017. cited by applicant ; Mitchell, Carey, “Are There Real Differences Between Type 6 and 6,6 Nylons?”, The Digest, 4 pages, downloaded May 13, 2016. cited by applicant ; SWICOFil, “Polytrimethylene terephthalate PTT yarns—Corterra”, 5 pages, last accessed on Jan. 18, 2016. cited by applicant ; Pakpahan, Edward Nixon, International Conference on Emerging Technologies in Environmental Science and Engineering, “Effect of Temperature on the Formation and Degradation of Polycyclic Aromatic Hydrocarbons”, pp. 569-575. Oct. 28, 2009. cited by applicant ; Diaz et al. “Comprehensiver Process for the Recovery of Value and Critical Materials from Electronic Waste” Manuscript, 38 pages Mar. 22, 2016. cited by applicant
  • Primary Examiner: Miller, Jonathan
  • Attorney, Agent or Firm: McKee, Voorhees & Sease, PLC

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