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Publication numberUS20090114567 A1
Publication typeApplication
Application numberUS 12/267,536
Publication dateMay 7, 2009
Filing dateNov 7, 2008
Priority dateNov 7, 2007
Publication number12267536, 267536, US 2009/0114567 A1, US 2009/114567 A1, US 20090114567 A1, US 20090114567A1, US 2009114567 A1, US 2009114567A1, US-A1-20090114567, US-A1-2009114567, US2009/0114567A1, US2009/114567A1, US20090114567 A1, US20090114567A1, US2009114567 A1, US2009114567A1
InventorsJames F. Maxwell
Original AssigneeMaxwell James F
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Cracking hydrocarbonaceous materials with heating bodies
US 20090114567 A1
Abstract
A continuous process and apparatus for treating feedstocks containing carbonaceous materials involves heating bodies to heat the feedstock to vaporize and crack hydrocarbons and carbon formed on heating bodies is removed through direct contact to a flame heater.
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Claims(10)
1. A process for processing materials with a major proportion of hydrocarbon component:
contacting the materials directly with heated iron balls to heat the materials to a temperature to vaporize and crack the hydrocarbons in the material;
recovering vapors produced by the contacting.
2. A process for processing materials with a major hydrocarbon content comprising:
contacting in an oxygen-free atmosphere the materials directly with heating bodies that have been heated, the contacting sufficient to heat the materials to a temperature to vaporize and crack hydrocarbons in the material;
in an oxidizing atmosphere heating and moving the heating bodies to remove carbon formed on the heating bodies by combusting the carbon and by moving the heating bodies such that the moving removes carbon by abrading the carbon;
directing the heating bodies from the heating to the contacting the materials;
recovering vapors from the cracked and vaporized materials produced during the contacting;
the heating bodies heated during the heating sufficiently to heat the materials during the contacting of the materials.
3. A process as in claim 2 wherein after the heating, the heating bodies are directed to pass through vapors produced in the contacting to further heat and crack the vapors before the vapors are recovered.
4. A process as in claim 2 wherein in solid residues are separated from the heating bodies after the heating of the heating bodies.
5. A process as in claim 1 wherein noncondensed portions of the recovered vapors are directed to the heater, and function as fuel for the heater.
6. A process as in claim 1 wherein nonvaporized and noncombusted materials from the feedstock are separated from the heating bodies as they together leave the heating of the heating bodies.
7. An apparatus for processing materials with a hydrocarbon content comprising;
a continuous mixer configured to transport feedstock and heating bodies co-currently through the mixer in non-oxidizing conditions such that hydrocarbonaceous material the feedstock is heated by the heating bodies sufficiently to vaporize and crack the hydrocarbonaceous materials;
a continuous heater configured to heat and move the heating bodies under oxidizing conditions and moving conditions to remove carbon deposits from the balls through oxidation and abrasion of the carbon deposits;
the mixer and heater arranged to continuously cycle the heating bodies through the mixer, into and through the heater, and back into the mixer.
8. An apparatus as in claim 7 additionally comprising a vapor-excluding transport configured to allow the heated heating bodies from the heater to pass through vapors produced in the mixer to further crack the vapors.
9. An apparatus as in claim 7 additionally comprising a vapor-condenser-feedstock preheater and precondenser to vaporize and remove light hydrocarbons and water from the feedstock.
10. An apparatus as in claim 9 wherein the removed light hydrocarbons and water are directed to the heater, where the light hydrocarbons function as fuel for the heater.
Description
    CROSS REFERENCE TO RELATED APPLICATIONS
  • [0001]
    This application claims priority from U.S. Provisional Application 60/986,284, filed Nov. 7, 2007, which is hereby incorporated by reference.
  • BACKGROUND OF INVENTION
  • [0002]
    The present disclosure relates to processes for hydrocarbonaceous feedstocks containing a high percentage of hydrocarbons, such as heavy liquids and solids, which require vaporization and cracking to make diesel fuel and other fuels. These processes are frequently used to process liquids such as used motor oils, and solids such as tires. A problem with these kinds of processes is that the vaporization and cracking of the hydrocarbons results in the formation of carbon on the heat source, which then can interfere with and foul up process equipment. This requires frequent shut-downs and maintenance.
  • SUMMARY OF INVENTION
  • [0003]
    A process that avoids the problems due to carbon buildup can be practiced with the use of heating bodies, such as iron balls. Hot iron balls are mixed with hydrocarbonaceous feedstock under non-oxidizing conditions, to vaporize and crack hydrocarbon materials in the feedstock. A buildup of carbon or coke will form on the iron balls during the vaporization and cracking process. To remove the carbon, the heating bodies are then continuously circulated through a heating unit under oxidizing conditions where the balls are passed through a heating fire to burn off carbon. In the heating unit the balls are rolled and exposed directly to a heating fire. The rolling action rubs carbon deposits off the balls and the oxidizing conditions oxidize carbon. After balls are reheated and cleaned of coke, they are recirculated to the mixing chamber through a vapor-lock feeder. Vapors leave the mixer and pass through incoming heated iron balls to further crack vapors as needed to make fuels of a desired viscosity. Nonvaporized feedstock materials are removed from the mixer/vaporizer with iron balls and separated out before or after iron balls circulate through the heater.
  • BRIEF DESCRIPTION OF DRAWINGS
  • [0004]
    FIG. 1 is a schematic diagram of an apparatus viewed from the top.
  • [0005]
    FIG. 2A is a schematic diagram of a portion of an apparatus as in FIG. 1 viewed from the side.
  • [0006]
    FIG. 2B is a schematic diagram of an alternate construction to FIG. 2A.
  • [0007]
    FIG. 3 is a cross-section of a burner.
  • DETAILED DESCRIPTION EXAMPLE
  • [0008]
    Reference is made to FIG. 1, which is a schematic view from the top of a system, and FIGS. 2A and 2B, which are each schematics from the side of a portion of exemplary systems for processing used motor oil. With appropriate modification, the system can be used for processing shredded tires, tar sand crudes, oil shale crudes, recycled plastics, or any other feed stock where a major portion is hydrocarbonaceous in nature. The feedstock can also be mixtures of any of these.
  • [0009]
    Used motor oil is introduced into a mixer 11, through an inlet conduit 13. The motor oil can be introduced into a first end 15, as illustrated in FIG. 2A, or the conduit can extend up through the mixer and be introduced at the mixer second end 17 so that the oil flows counter current to the heated heating bodies 19. Heated heating bodies 19, such as iron balls, are introduced into the first end. The mixer is in the form of a drum with an auger flight 21 (or other transport structure) on the inside will, so that as the drum rotates, the iron balls 19 are moved toward the second end 17 and mixed with the oil.
  • [0010]
    In FIG. 2A, the heating bodies and the oil move together up through the mixer. In FIG. 2B, at least some of the oil flows counter-current to the heating bodies, with the oil flowing through holes 23 in the auger flight 21.
  • [0011]
    In both cases, the iron balls mix with the oil and heat the oil to a temperature that will vaporize the hydrocarbon, crack hydrocarbons in the feedstock, and crack volatilized hydrocarbon vapors. Accordingly, the mixer also functions as a vaporizer and cracker. The mixer may also be inclined to carry the balls upward to the heater 25, and thus functions as an elevator. The drum of the mixer is disposed in a containment 27 and has appropriate vapor lock transporters 29 for solid material transfer in and out of the mixer to maintain a non-oxidizing environment.
  • [0012]
    At the second end of the mixer, the balls and any other nongaseous materials carried up by the flight are withdrawn from the mixer and passed to a heater 25 using a vapor lock system 29 to exclude air from the mixer. In the mixer, some carbon formed upon the balls is removed by the rubbing or abrasive action of the balls in the mixer. The non-gaseous materials withdrawn with the balls includes this carbon, as well as any other solid and non-gaseous materials, such as solid unreacted or partially reacted hydrocarbons in the feedstock and inert materials, which include mineral and metal contaminants. If the feedstock includes shredded tires, such solid materials may include tire cord materials, such as steel and unvolatized polymers.
  • [0013]
    Referring to FIG. 1 and FIG. 3, which is a cross-sectional schematic, the heater 25 is generally in the form a rotating drum with a system, such as paddles, auger flights, and elevator bars 31 to transport and roll balls 19 along with solid materials through the heater. In the heater carbon on the balls is fractured from the balls by the rolling and moving of the balls due to rotation of the heater. In addition, carbon and other solid materials are combusted as balls are exposed to fire in the heater.
  • [0014]
    The balls can be exposed and heated by the fire by any suitable system, that may, for example, include elevating and and dropping the balls through the fire. In FIG. 3, the heater 25 includes a burner 33 that extends the length of the heater 25 that directs blue flame directly upon balls being rolled in the heater. A feed pipe 35 for air is also provided that directs oxidizing atmosphere directly on the balls through air conduits 36 to promote oxidation of carbon. In this way carbon that has accumulated in the system is continuously removed. The oxidizing carbon also functions as a fuel in the heater.
  • [0015]
    The heater also functions to heat the iron balls to a high temperature. When these heated iron balls are introduced into the mixer, they must be hot enough to sufficiently heat the feedstock to vaporization and cracking temperatures in the mixer.
  • [0016]
    After leaving the heater any remaining solid materials are separated from the balls, and the balls are recycled back through a vapor-lock transport to the mixer. The separation may be by any suitable technique, such as screening. Effluent combustion gasses from the heater are directed to a stack 45 or other suitable structure.
  • [0017]
    The vapor-lock transport inlet 29 to mixer can also function as a cracker, as particularly shown in FIG. 2A and FIG. 2B. In FIG. 2A, the hot iron balls fall through vapors leaving the mixer, which further heats and cracks the vapors. A spreader 37 can be used to mix the heating bodies and increase the gas permeability for vapor flow. In FIG. 2B, screens or ramps 39 with holes 41 (to allow passage of vapors) cause the balls to roll through the vapors.
  • [0018]
    The heating bodies are transported from the vapor lock transport 29 back into the mixer, to again be transported through the mixer.
  • [0019]
    The vapors from the vapor lock transport are passed to a condenser 41, where condensible liquid hydrocarbons are produced for fuels and as hydrocarbon feedstocks. The non-condensible vapors from the condenser are recycled back to the heater, where they are used as fuel for the heater.
  • [0020]
    Optionally heat from condensing the vapors can be used to pretreat the feedstock to remove both condensible vapors and water in the feedstock before it is heated and cracked in the mixer. These vapors can be passed to the burner of the heater. A counter-flow heat exchanger using hot vapors to heat the feed stock can be used in this function, where it acts as a vapor condenser-feedstock heater.
  • [0021]
    The heating bodies may be any suitable material that can be heated and transfer heat in the process, and is tough enough to withstand the tumbling in mixer and heater. In addition, denser materials are preferred to help with the removing of the carbon effect in the heater. Balls of iron, or an iron alloy, have been found suitable. Reference to “iron balls” or “balls” in this disclosure refers generally to heating bodies of any suitable material.
  • [0022]
    While this invention has been described with reference to certain specific embodiments and examples, it will be recognized by those skilled in the art that many variations are possible without departing from the scope and spirit of this invention, and that the invention, as described by the claims, is intended to cover all changes and modifications of the invention which do not depart from the spirit of the invention.
Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2027862 *Nov 26, 1928Jan 14, 1936Ind Process CompanyProcess of converting hydrocarbons
US3008894 *May 20, 1958Nov 14, 1961Oil Shale CorpMethod and apparatus for producing oil from solids
US3018243 *Mar 9, 1959Jan 23, 1962Oil Shale CorpPlant and process for production of low temperature pumpable oil from oil shale and te like
US3020209 *Oct 20, 1958Feb 6, 1962Oil Shale CorpPlant and process for the production of oil
US3265608 *Feb 2, 1962Aug 9, 1966Technikoil IncMethod for pyrolyzing solid carbonaceous materials
US3630501 *Aug 21, 1970Dec 28, 1971Air Prod & ChemThermal treatment of powder
US3655518 *Nov 19, 1969Apr 11, 1972Metallgesellschaft AgRetort system for oil shales and the like
US4438161 *Sep 30, 1982Mar 20, 1984Phillips Petroleum CompanyIron-containing refractory balls for retorting oil shale
US4450895 *Nov 2, 1981May 29, 1984Tunzini-Nessi Enterprises D'equipementsProcess and apparatus for heating or cooling light solid particles
US4828681 *Jan 15, 1987May 9, 1989Exxon Research & Engineering CompanyProcess of thermally cracking hydrocarbons using particulate solids as heat carrier
US5914027 *Mar 11, 1997Jun 22, 1999Thermtech A/SThermo-mechanical cracking and hydrogenation
US6203765 *Oct 23, 1997Mar 20, 2001Alberta Oil Sands Technology & Research AuthorityThermal apparatus and process for removing contaminants from oil
US6589417 *May 22, 2001Jul 8, 2003Alberta Oil Sands Tech And Research AuthorityThermal apparatus and process for removing contaminants from oil
US20020029996 *May 22, 2001Mar 14, 2002Alberta Oil Sands Tech And Research AuthorityThermal apparatus and process for removing contaminants from oil
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US8042282 *Feb 26, 2007Oct 25, 2011Lg Electronics Inc.Drum for clothes dryer
US8647415Jul 20, 2012Feb 11, 2014Lummus Technology Inc.Coke catcher
CN104583370A *Jul 11, 2013Apr 29, 2015鲁姆斯科技公司Coke catcher
EP2571613A4 *Apr 18, 2011Aug 23, 2017Envirollea IncThermal processing reactor for mixtures, fabrication of the reactor, processes using the reactors and uses of the products obtained
WO2014014731A1 *Jul 11, 2013Jan 23, 2014Lummus Technology Inc.Coke catcher
Classifications
U.S. Classification208/126, 422/234
International ClassificationC10G9/30
Cooperative ClassificationC10G1/002, C10G9/30, C10G1/02
European ClassificationC10G1/02, C10G9/30, C10G1/00B