Plastics Conversion Supply System

Abstract

The plastic conversion feed system is adapted to transport feedstock through various processing units or stations to a vessel where chemical and / or physical reactions occur to produce a suitable and useful end product. The various processing units include a homogenizer for pulverizing the feedstock, a size reduction device for reducing and densifying the feedstock into particles, a heating and / or mixing device for heating the feedstock, and a feed conduit connecting the heating and mixing device to the vessel, and the feedstock conversion unit vessel produces a mixture of useful gases and condensable gases through various operations such as cracking, reforming, condensation, recombination, and re-cracking.

Description

[Technical field]

[0001]

[0001] The present invention relates to a plastics conversion and feeding system for transporting chopped and / or pelletized solid feedstock comprising plastics or hydrocarbon materials, or any combination thereof, to a vessel for producing usable compounds under controlled chemical and physical reactions, preferably in the absence of air and / or oxygen. The present invention also relates to an improved plastics conversion and feeding system for transporting the plastic or hydrocarbonaceous feedstock, or combinations thereof, preferably in homogenized, preferably in briquette and / or cube form, to an extruder which feeds the plastic or hydrocarbonaceous feedstock, or combinations thereof, to a reaction vessel as a solid or semi-solid feedstock. [Background technology]

[0002]

[0002] US Publication No. 2017 / 0283706 relates to a process and apparatus for pyrolysis of mixed plastic feedstocks to produce petroleum products. In one example, a process for producing petroleum products includes charging a mixed polymeric material feedstock into a reactor apparatus. Thermal energy is added to the feedstock while advancing the feedstock through the vessel apparatus in an anaerobic operation. Energy input to the reactor is controlled by controlling a temperature gradient in the reactor vessel to produce petroleum gas products. The process includes in situ chemical reactions, including cracking and recombination reactions, that convert the solid hydrocarbon portion of the feedstock into molten fluids and gases in the reactor vessel and are controlled to produce gaseous petroleum products that exit the reactor vessel. Solid residues separated from the pyrolysis process are also removed from the reactor vessel.

[0003]

[0003] WO 2016 / 042213 A1 relates to a pyrolysis apparatus and a pyrolysis method. The pyrolysis apparatus is a continuous apparatus in which the material to be pyrolyzed is conveyed through the apparatus. The pyrolysis apparatus has at least two control sections through which the material to be pyrolyzed is conveyed. In the at least two different control sections, the material is subjected to thermal effects of different magnitudes. Furthermore, gases evaporated from the material are recovered from the at least two control sections.

[0004]

[0004] US Publication 2016 / 017232 A1 relates to an apparatus and method for pyrolyzing hydrocarbon-based materials to produce useful vapor and solid products. The apparatus for producing vapor and solid products includes a generally cylindrical linear reactor having a screw means for transporting hydrocarbon-based materials through the reactor, means for feeding and heating the hydrocarbon-based materials whereby they are treated and pyrolyzed to produce vapor and solid products, means for removing vapor products from the treated hydrocarbon-based materials, means for removing solid products, means for maintaining the hydrocarbon-based materials within a zone for a defined residence time range, means for rotating the screw having a multiple flight configuration to compress, and melt the hydrocarbon-based materials to convert them from solid to liquid, mix, destabilize, and dehalogenate the hydrocarbon-based materials, pyrolyze the hydrocarbon-based materials, devolatilize the pyrolyzed hydrocarbon-based materials, and discharge solid products.

[0005]

[0005] EP 2457977 A2 publication relates to various embodiments of a process for pyrolysis of hydrocarbonaceous materials. In one embodiment, the process for pyrolysis of hydrocarbonaceous materials includes charging a reactor with a feedstock containing hydrocarbonaceous materials, heating the feedstock, and collecting a liquid product from the reactor, which is an anaerobic operation. At least 5% of the organic carbon atoms that are not present in the aromatic rings of the compounds of the feedstock are present in the aromatic rings of the compounds in the liquid portion of the product.

[0006]

[0006] European Patent Publication 1647589A2 relates to a continuous pyrolysis system for waste synthetic polymer compounds, which continuously pyrolyzes combustible waste by indirect heating in a pyrolysis chamber that maintains an anaerobic or low-oxygen environment, produces refined oils such as heavy oil and light oil according to the boiling point in a distillation tower, and uses the refined oils as a heat source for pyrolysis of waste. This continuous pyrolysis system includes a hopper, an automatic waste feed device that discharges a predetermined amount of waste from the hopper, a pyrolysis chamber that maintains a high-temperature low-oxygen environment and continuously pyrolyzes the waste by indirect heating, a gas combustion chamber that burns non-condensable gases among pyrolysis gases generated during pyrolysis of waste and provides heat of a predetermined temperature to the outer surface of the pyrolysis chamber to provide heat of a predetermined temperature to the outer surface of the pyrolysis chamber used as a heat source for pyrolysis of waste, a refined oil production means that produces refined oil from pyrolysis gas reformed through a catalytic reaction and supplies residual non-condensable gases to the gas combustion chamber, and an automatic discharge device that sequentially discharges ash that has been pyrolyzed and transported from the pyrolysis chamber.

[0007]

[0007] US Patent No. 5,057,189A discloses an apparatus for recovering char, oil and fuel gas from vehicle tires, either whole or physically shredded tires. The tires can be washed to remove dirt and road film. The tires are dried and preheated with superheated steam. The hot tires are pyrolyzed to partially devolatilize most of the hydrocarbons and produce a char that can be separated from the steel and glass fibers. The char can then be pyrolyzed with microwaves to increase the temperature of the tire and devolatilize the remaining hydrocarbons as gases from the char. The hot gases are cooled and partially condensed. The uncondensed gases are used as fuel. The char can then be pyrolyzed with microwaves to increase the temperature of the tire and devolatilize the remaining hydrocarbons as gases from the char. The hot gases are cooled and partially condensed. The uncondensed gases are used as fuel. The condensed oil is sent to storage. The solid residue from tire pyrolysis is essentially charcoal, glass fibre and steel. The charcoal is mechanically separated from the glass and steel. Alternatively, the charcoal, glass and steel are separated by pouring the hot mixture into a water quench tank. The mixture is cooled. The charcoal floats to the surface and is removed. The glass and steel sink to the bottom of the tank and are removed separately. The charcoal can be sold, burned or milled to break up the agglomerates and then pelletised and bagged. The steel and glass are disposed of as waste.

[0008]

[0008] US Patent No. 8,282,787 relates to a system and process that can use pyrolysis to gasify a carbonaceous feedstock to produce a gas product that can include methane, ethane, and other desirable hydrocarbon gases, and a solid product that includes activated carbon or carbon, followed by filtration of the gas product using at least a portion of the activated carbon from the solid product as a filtration medium. In one embodiment, at least a portion of the harmful chemicals are sequestered or removed from the gas product in one or more filtration steps using activated carbon as a filtration medium. In a further embodiment, the filtration steps are performed in stages using activated carbon at different temperatures. A high-temperature pyrolysis system that produces activated carbon can be combined with another high-temperature pyrolysis system that does not produce activated carbon to filter harmful compounds using activated carbon from the first high-temperature pyrolysis system. The high-temperature pyrolysis system can be combined with one or more low-temperature feedstock conversion processes such that waste heat from the high-temperature pyrolysis system is used to operate the low-temperature process. This system and process can be used to produce non-wettable carbon with pores fused with silica. Summary of the Invention [Problem to be solved by the invention]

[0009] [Means for solving the problem]

[0010] The feedstock conversion and feeding system of the present invention serves to transport the feedstock through different processing units or stations to a reaction vessel where chemical and / or physical reactions take place to produce a suitable and useful end product. The various processing units of the present invention include size reduction equipment such as one or more shredders, or one or more pelletizers, or a combination of both. Desirably, the feedstock is often first shredded and then pelletized. The pelletizing unit operation generally reduces the feedstock and densifies the feedstock. Other processing units of the present invention include heating and blending equipment that may include one or more feeders and / or one or more extruders (extruders). A variety of different types of feeders may be utilized in the present invention, some of which include rams, or chain conveyors, helical screws, and the like. The one or more extruders may be any type of extruder known in the literature and in the art, such as a single screw extruder in general or a twin screw extruder which is generally preferred.

[0011]

[0010] In another embodiment, the conversion feed system transports the feedstock through various stages to the pyrolysis reactor, which also produces a stable and useful end product, as described below. The various processing units of the present invention generally include a homogenizer that generally does not shred, but rather breaks (comminutes), separates, or forcibly separates the typically compressed feedstock that is subsequently mixed or blended, so that the feedstock generally contains similar types of specific plastics, carbonaceous materials, or any combination thereof. Such feedstock is then fed to a shredder that further separates the feedstock, and then preferably to a pelletizer that forms small briquettes, cubes, etc. of the feedstock, which are then heated and fed to an extruder, from which the solid or semi-solid mass is fed to the pyrolysis reactor.

[0012]

[0011] A plastic conversion feed system for transporting feedstock to a reaction vessel includes a homogenizer capable of grinding and breaking down a feedstock containing a plastic material or a hydrocarbon-based material or a combination thereof, a pelletizer capable of reducing size and densifying the homogenized feedstock, and an extruder capable of forming a continuous mass of feedstock which is fed to the reaction vessel.

[0013]

[0012] A method for transporting a feedstock to a reaction vessel includes breaking down (grinding) the feedstock, which may include plastic, a hydrocarbon-based material, or a combination thereof, in a homogenizer, reducing the size of the feedstock in a pelletizer, and forming a continuous mass of the feedstock in an extruder, which is fed to the reaction vessel.

[0014]

[0013] A plastic conversion feed system for transporting a feedstock to a reaction vessel comprises a size reduction device capable of reducing the size and densifying the feedstock which may include a plastic material or a hydrocarbon-based material or a combination thereof, a heating device capable of heating the reduced size feedstock and transferring it to an extruder having an output shaft, and a conduit connecting the extruder to the vessel and capable of supplying the feedstock to the vessel, the conduit having an output shaft at a radial angle of up to about 5° relative to the output shaft of the extruder apparatus.

[0015]

[0014] A method of transporting a feedstock to a reaction vessel includes reducing the size of a feedstock comprising plastic, or a hydrocarbon-based material, or a combination thereof, in a size reduction device; heating and blending the reduced-size feedstock; transferring the reduced-size feedstock to a feed conduit connected to the vessel; and feeding the reduced-size feedstock to the reaction vessel.

[0016]

[0015] These and other features of the present invention will become apparent to those skilled in the art to which this disclosure pertains upon reading the following description in conjunction with the accompanying drawings. [Brief description of the drawings]

[0017] [Figure 1]

[0016] Figure 1 is a schematic diagram showing a plastic converting and feeding system for size reduction equipment such as shredders and / or pelletizers to reduce the size of hydrocarbon materials and / or plastic polymers, and for heated blending equipment such as feeders and / or extruders to prepare suitable feedstock for reaction vessels in which subsequent chemical and / or physical reactions take place. [Diagram 2] FIG. 2 is a schematic diagram of a vessel in which various reactions can take place. [Diagram 3]

[0018] FIG. 3 is a side view of a feed conduit that transports ingredients from a feeder and / or extruder to a reaction vessel. [Figure 4]

[0019] FIG. 4 is a schematic diagram of an alternative feed system of the present invention for transporting the feedstock from the homogenizer to the reaction vessel. [Figure 5A]

[0020] FIG. 5A is a perspective view of an adjustable plug fixedly attached to a supply conduit at a substantially perpendicular angle to the supply conduit. [Figure 5B]

[0021] FIG. 5B is a perspective view of a portion of a supply channel with an adjustment plug at a right angle and extending partially into the supply channel. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0018]

[0022] Feed Conversion Unit (FCU)

[0023] The vessel 300 of the present invention is generally any vessel known in the art or literature in which physical and / or chemical reactions can occur, desirably substantially free of air and oxygen. That is, the total amount of oxygen based on the total internal volume of the vessel is less than about 3 volume percent, desirably less than about 2 volume percent, preferably less than about 1 volume percent, and more preferably completely free of air or oxygen. Thus, reaction vessels such as pyrolysis vessels can be utilized. The vessels can generally have multiple heating units, multiple reaction stages, multiple product gas exhaust vents, etc., or any combination thereof. Optionally but preferably, the vessel 300 includes an outer shroud 360 having multiple inner walls 365 that extend from the shroud to the vessel outer wall and form heating channels for hot gases that heat the vessel. A preferred vessel, as shown diagrammatically in FIG. 2, is described in U.S. Pat. No. 10,711,202 B2, issued July 14, 2020, which is incorporated herein by reference in its entirety with respect to all aspects thereof. As is well known in the art and literature, various pyrolysis vessels crack a variety of substances, compounds, and materials, such as alkane gases, various hydrocarbon gases such as naphtha, various diesel fuels such as heavy oils, diesel fuel, jet fuel, marine fuel, various waxes, lubricants, additives, various distillates, light organic compounds, etc., through various reactions such as cracking, reforming, recombination, recracking, etc., to produce various gases, including alkane gases.

[0019]

[0024] The feedstock conversion and feeding system 400 includes a variety of different processing units or stations. The feedstock is generally plastic, or hydrocarbon-based material 405, or any combination thereof, fed by a hopper system 410 to a particle size reduction device 420. The hopper system includes an upper large hopper 412 that receives a large volume of feedstock and upon receiving an electronic signal from a lower small hopper 414 that the feedstock is low, opens an orifice device, such as a lower valve 413, to transfer the feedstock (e.g., charge) to the lower hopper 414. The lower hopper 414 has an orifice therein, such as a lower valve 415, that can transfer, convey, or feed a constant rate or steady state amount of waste material to the size reduction device 420. The lower hopper feed valve can be programmed to increase or decrease the amount of waste material entering the size reduction device 420 in a manner well known in the art and literature to stabilize and generally equalize the flow of the subsequent reduced size solid feedstock or semi-molten or molten feedstock to the FCU vessel 300.

[0020]

[0025] A desirable embodiment of the vessel 300 is to produce oil and gas products in general. Preferred plastic waste feedstock items include waste polymers such as in the form of sheets, wrappers, packaging, furniture, plastic housings, containers, waste plastics, and the like, utilizing those containing essentially only hydrogen and carbon atoms such as high density polyethylene, low density polyethylene, linear low density polyethylene, polypropylene, polystyrene, and the like. Other suitable commercially available polymers include polyesters, polycarbonates, polymethylmethacrylates, nylons, polybutylenes, acrylonitrile-butadiene-styrene (ABS) copolymers, polyurethanes, polyethers, poly(oxides), poly(sulfides), polyarylates, polyetherketones, polyetherimides, polysulfones, polyvinyl alcohols, polymers formed by polymerization of dienes, vinyl esters, acrylates, acrylonitrile, methacrylates, methacrylonitrile, diacids, diols, or lactones, or any combination thereof. Still other polymers include the block copolymers described above, and alloys thereof. Polymeric materials include, for example, thermosetting polymers such as epoxy resins, phenolic resins, melamine resins, alkyd resins, vinyl ester resins, crosslinked polyester resins, crosslinked polyurethanes, and also crosslinked elastomers including, but not limited to, polyisoprene, polybutadiene, polystyrene-butadiene, polystyrene-isoprene, polyethylene-propylene, ethylene-propylene-diene, and the like, and blends thereof.

[0021]

[0026] The hydrocarbon materials generally include compounds having primarily only carbon and hydrogen atoms, such as various bitumens including bituminous tailings from mines, various heavy fractions of fractionators including various heavy oils, greases, semi-asphalt compounds, and the like, and various types of hydrocarbon-containing gases, most of which have been reduced to lighter components by the present invention.

[0022]

[0027] The various polymeric feedstocks described above often contain fillers, pigments, flame retardants, clays, and the like. Typically, the amount is about 2% to about 25% by weight, or desirably about 3% to about 20% by weight, or preferably about 3% to about 15% by weight, or most preferably less than about 7% by weight, all based on the total weight of the polymeric feedstock or feedstocks. Such compounds generally do not react chemically or physically, and are often released from the vessel 300 through the vessel discharge channel 330 as a solid, inert residue.

[0023]

[0028] In a preferred embodiment, the different types of raw material compositions often comprise about 40% to about 90%, desirably about 50% to about 85%, and preferably about 70% to about 80% by weight of polyethylene, polypropylene, and polystyrene polymers, and any remaining polymers can be, but are not limited to, polyurethane, nylon, PET, and polyvinyl chloride, as well as any of the remaining polymers listed above.

[0024]

[0029] The processing size reduction device 420 includes one or more shredders 422 and / or one or more pelletizers 424. They can be in any order, but preferably as shown in FIG. 1, the feedstock is first shredded and then pelletized. The shredders and pelletizers can be spaced apart from each other, adjacent or consecutive to each other, or even integral, i.e., in one combined unit. They are preferably separated by a short distance so that there is a direct feed from the shredder 422 to the pelletizer 424. The shredder 422 can include any conventional shredder known in the art and literature, which typically reduces the size of the feedstock to small particles in one or more stages. Similarly, the pelletizer 424 can be any conventional pelletizer known in the literature and art, which reduces the size of the feedstock 405 in one or more stages and preferably densifies it into small particles 428. Generally, the reduction size of the individual plastic pelletized feedstock 428 formed and densified into spheres, blocks, cylinders, or other random shapes can vary widely, such as from about 0.25 to about 6 inches, desirably from about 0.5 to about 5 inches, preferably from about 1 to about 4 inches, and more preferably from about 1 to 2 inches. The feedstock 405 can be optionally heated in the shredder and / or pelletizer 420 or in the feed stream 430, for example in an oven (not shown), by any conventional means known in the art and literature, such as hot air, hot oil, steam, or infrared, electric heat, or mechanical processing. The heating temperature of the feedstock can vary widely, such as from about ambient temperature, i.e., from about 40° F. to about 100° F., or even to about 160° F., or below the melting temperature of the lowest plastic melting temperature. One advantage of densifying the waste, plastic, and / or carbonaceous waste is to produce a pelletized feed stream 430 having a desired density, typically greater than about 15 pounds / cubic foot, or desirably greater than about 20 pounds / cubic foot, and the feed stream 430 emerging from the shredder 422 and / or pelletizer 424 has a reduced amount of air contained therein.

[0025]

[0030] The reduced waste feed in the form of a feed stream 430, as on a conveyor 435, is fed to another processing unit, a heating and mixing unit 440. The unit 440 includes one or more feeding units and / or one or more extruders. The feeders and / or extruders can be arranged in a sequence as shown in FIG. 1, preferably with the feeder first, followed by a single downstream extruder. The two separate units can be spaced apart from each other, adjacent to each other, or in conjunction with each other, or as an integrated unit. As shown in FIG. 1, a feeding unit arranged adjacent to the extruder is preferred, with the shredded and / or pelletized feed material fed directly from the feeder 442 to the extruder 444. The feeder 442 can be any conventional feeder known in the art and literature, which is generally optional, but desirably heats the material. The feeder 442 can typically include a piston ring, or a conveyor, or a helical screw (not shown) that directly heats and transfers the feedstock directly to the extruder 444 or to the feed conduit 500. Similarly, the extruder 444 can be any conventional extruder known in the literature and the art that heats and transfers various feedstocks, e.g., chopped and / or pelletized, to the vessel 300. Alternatively and desirably, the extruder heats and densifies the feedstock particles, generally converting it to a semi-molten or molten flowable mass, or preferably a non-molten mass, which is fed to the conduit 500. Suitable temperatures of the feedstock 460 exiting the feeder 442 and / or extruder 444 can range from about 200°F to about 300°F, or up to about 400°F, or even up to about 500°F, or the desired ranges are from about 250°F to about 400°F, and from about 300°F to about 350°F. The twin screw extruder 444 in this embodiment preferably includes a jacketed barrel and internally ported screws to allow for the use of a thermal heat transfer medium such as hot oil. Additionally, independent heating sections in the barrel allow for careful control of the feed stream mass temperature.

[0026]

[0031] Another preferred aspect of utilizing an extruder is that the densification of the feed stream (outlet) therefrom can be easily increased to a fully dense state, typically greater than about 25 pounds per cubic foot, desirably about 30 to about 38 pounds per cubic foot. Such increased density further eliminates air ingress through the feedstock into any FCU vessel 300, generally minimizing air ingress.

[0027]

[0032] Another important aspect of the present invention is the use of a processing unit, which is a feed conduit 500 that extends from the extruder 444 into said vessel 300 and transfers said material from the extruder into the vessel. Such a processing unit can be made of conventional types of metals, such as stainless steel, cast iron, carbon steel, etc. This device is generally a flexible conduit or pipe with a smooth interior that connects the output of the feeder 442 and / or extruder 444 to the FCU vessel 300, ensuring a steady rate and smooth flow of the feed material or semi-molten material and / or molten material waste to the vessel, regardless of the input position of the vessel relative to the feeder and / or extruder outlet, e.g., height, distance, lateral position, etc. The feed conduit output or shaft 452 can be precisely aligned with the extruder output shaft 448 or can generally be moved in a moderate radial direction. That is, it can be moved vertically, i.e., up and down, left or right, or any combination thereof, within a radial angle of up to about 5°, desirably within an angle of about 3° or less, relative to the extruder output shaft 448. The axis 452 of the conduit 500 may be perpendicular to the inlet face of the feed conduit. If desired, the entire conduit may be placed in a flexible tube to allow angular movement of the feed into the vessel. Such movement allows the shredded or pelletized or semi-molten or molten waste feed stream from the extruder 444 to be easily transferred in a smooth, consistent, steady flow at a uniform flow rate to the inlet 310 of the vessel 300. This is an important aspect as the vessel may be operated in a stable reaction state such as pyrolysis, cracking, reforming, etc., thereby allowing efficient output of the various components of the shredded or pelletized fluid waste as described above, typically converted to gas such as petroleum gas. The length of the conduit 500 may vary from about 24 inches to about 240 inches, and more preferably from about 36 inches to about 120 inches. The length of the conduit is adjusted to account for the layout of the plant, but also to ensure sufficient length for the development of a steam seal through which the feedstock is fed to the reactor.

[0028]

[0033] A detailed view of a preferred conduit 500 is shown in FIG. 3. The feeder, or preferably extruder, is a conduit 500 connected to the extruder 444 in any conventional manner, such as by nuts and bolts, welding, etc., so that it can rotate at a radial angle of up to about 5° with respect to the output shaft 448 of the extruder 444, with respect to a flange (not shown) at the extruder outlet, and supplies such conduit 500 with solid, semi-molten, or molten feedstock. The feed conduit 500 is typically heated in any conventional manner, such as by hot oil, infrared heating, heating tape, etc., to maintain the waste as a flowable mass as it exits the extruder 444. The input hopper 505 has a jacket around it that can contain hot gases, such as air, hot oil, etc. The hopper 505 is connected to a slide valve 510, which can be a gate valve, ball valve, or any other type of valve that can easily shut off the flow of raw material to the vessel 300. The captured material then needs to be reheated, such as during a restart of the raw material conversion feeding system. As shown in FIG. 3, the supply conduit 500 has an extension tube 515 that connects a valve 510 to a flexible tube 530 that is connected to the vessel 300. To maintain the waste in a flowable state within the supply conduit 500, hot oil can be added to the heating pipe system 520 via an inlet 521, which can include a valve connected to an extension tube 515 having a heating jacket around it. The heating fluid is countercurrent exiting the extension tube 515 and circulated by the valve 510 and applied, also countercurrent, to the input hopper 505 from which it exits through a hot oil outlet 523. The flexible tube 530 desirably includes flexible insulation 540 to maintain the waste in a semi-molten state. Thus, raw waste is supplied to the vessel 300 through the outlet feed delivery tube 550 or the supply conduit 500.

[0029]

[0034] Another advantage of the conduit 500 is that it is flexible, which means that the feed conduit axis 452 of the conduit 500 can be substantially aligned with the horizontal axis 448 of the extruder 444 at one end, and aligned approximately parallel to the input axis 305 of entry of the vessel 300 at the other end when in a slightly different position, e.g. vertical, horizontal, etc.

[0030]

[0035] The conduit 500 can be supported by any conventional scaffolding or other support device, or can be suspended from an overhead truss system or the like. The supply transfer pipe or conduit 500 can deliver 2500-7500 lbs / hr of material to the vessel.

[0031]

[0036] In summary, the advantages of the above plastic conversion feedstock 405 in FIG. 1 include a continuous or steady state flow of the waste feedstock stream with a minimal amount of entrained air or air intrusion into the vessel 300. This is achieved primarily by applying pressure to the feedstock as the extruder 444 pushes it into the vessel 300, which squeezes air and oxygen out of the feedstock. Also, the temperature and density of the feedstock are controlled. The feed conduit 500 is also subjected to minimal stress. This is achieved by an optional flexible bellows with a smaller inner pipe (not shown), allowing angular bending of the feed conduit system which increases the life of the system. Additionally, the flexible feed conduit allows the shape, length, and angle of the PCU vessel 300 to be changed.

[0032]

[0037] It is desirable to have a vessel 300 whose axis 305 can be set at a slight upward incline or angle, i.e., from about 0° to about 10°, desirably from about 1° to about 5°, and preferably from about 1.5° to about 4° upward incline or angle, from the reference point of the level ground (not a slope, hill, or upturned or downturned ground) on which the vessel is optionally situated. In this way, if desired, complete pyrolysis of the feedstock mass 460 can be achieved before the mass of unreacted feedstock waste reaches the top end or outlet 320 of the vessel, as shown in FIG. 2. In other words, efficient utilization of the vessel is an important feature of the present invention to prevent discharge of unreacted feedstock from the outlet end of the vessel. As shown in FIG. 2, the feedstock 460 is first filled at a certain amount at the bottom of the vessel, heated, and gradually moved through the vessel by the helical screw blade 340, where it is pyrolyzed and vaporized into components that undergo various cracking, condensation, reforming, and recombination (chemical and physical) reactions to produce a desired mixture of various hydrocarbon products.

[0033]

[0038] The beach head point 350 is located at the bottom of the vessel upstream from the vessel inlet or opening 310 at a distance where the elevation of the vessel bottom is approximately equal to the initial vertical height of the mass of feedstock being poured into the vessel. The point 350 should be at least about 2%, desirably at least about 5%, and preferably at least about 10% of the distance from the top outlet or discharge channel 330 of the vessel, based on the overall length of the vessel.

[0034]

[0039] The yield of gaseous products produced by the present invention is very high, at least about 70%, desirably at least about 80%, and preferably at least about 85% or 90% by weight of the feedstock admitted to the vessel. The remaining material, generally classified as a dry, solid, inert residue, often including fillers and other inert materials, is discharged from the top or outlet end 320 of the vessel 300 through discharge channel 330.

[0035]

[0040] A desired reaction vessel similar to that described in U.S. Patent No. 10,711,202, issued July 14, 2020, is shown in FIG. 2 and is incorporated herein by reference in its entirety. However, it should be understood that many other types of vessels may exist. The vessel 300 does not rotate and does not contain a catalyst; that is, the vessel is free and unconstrained. The vessel 300 includes a shroud 360 that extends substantially around it, preferably extending across the entire exterior area of ​​the vessel 300. A number of interior walls 365 connect the shroud 360 to the vessel 300, forming heating and / or reaction zones within the vessel 300. Heat is provided to the vessel through standard or conventional heating units 370 that are typically present within each section of the vessel separated by the interior walls 365. Thus, heat travels around the circumference (ring) of the generally cylindrical vessel 300 and exits the vessel through a heat rejection channel 375 at the top of the vessel. The heat in the different sections of the vessel 300 generally volatilizes the feedstock 460, and the gases produced therefrom exit the vessel through product exhaust flowpath 380, which are fed to a condensation unit (not shown) and can take the form of many different types of products. Various preferred petroleum products include naphtha, distillates such as diesel, jet fuel, gas oils such as heavy oil, greases, semi-asphaltic compounds, waxes, steam cracking feedstocks, and the like.

[0036]

[0041] Pyrolysis occurs as the feedstock mass 460 flows along the vessel, or is transported from the inlet 310 to the vessel top 320, as shown in Figure 2, via cracking, recombining, reforming, recracking, etc. In general, suitable pyrolysis temperatures along the axis 305 within the vessel 300, i.e., from left to right in Figure 2, range from about 700°F to about 1,200°F.

[0037]

[0042] Alternative embodiments

[0043] In accordance with another embodiment of the present invention, an improved feed system 600, shown generally in Figure 4, may be utilized to achieve a steady flow of generally homogenized pyrolysis feedstock to the pyrolysis reactor 300, as shown in Figure 2. In this embodiment, the feedstock is preferably melted, rather than semi-molten or molten, but preferably heated, and importantly contains flowable solid particles or masses.

[0038]

[0044] Recyclable materials received for pyrolysis from many sources, such as grocery stores, drug stores, hardware stores, mixed waste, municipal collection plants, as well as industrial sources, typically contain a wide variety of materials, some of which may be undesirable for use in some pyrolysis reactors. For this reason, manual sorting of such materials is performed to remove them from the waste feedstock 405, as shown in FIG. 4. Using human labor, undesirable pyrolysis feedstock items are manually separated, including, but not limited to, various metals, such as beverage and beer cans, wood, such as game boards and toys, and undesirable types of plastics, such as polyvinyl chloride, as well as glass, such as various beverage bottles, and various types of cardboard and paper.

[0039]

[0045] Since no fixed amount of a particular type of material enters one or more manual sorting areas, the amount of feedstock from each manual sorting area will vary and should desirably be adjusted with respect to the amount and type of feedstock to achieve approximately similar inputs of different types of plastic and hydrocarbon-based materials. For example, if polyolefins such as polyethylene and polypropylene are included in the initial manual sorting stock, polystyrene, polyurethane, polyester, nylon, etc. from other feedstocks can be added to it to generally maintain a similar overall input of various different polymers and hydrocarbon-based materials into the homogenizer 610. This procedure is generally accomplished manually by taking a stock from an assortment area that is rich in one type of material and adding it to a stock that is poor in said type of material.

[0040]

[0046] The above feedstock is fed into hopper system 410, described above and fully incorporated herein by reference. The hopper system is preferably the same size in this embodiment and can include upper and lower hoppers as described above for conveying or feeding the pyrolysis feedstock at a near constant or steady flow rate to stabilize the flow of the pyrolysis feedstock and equalize the feed to homogenizer 610. The upper hopper is also important because it allows for a large, metered feed rate, improving control of the process (pellets can be stored and replenished more or less independently of pyrolyzer demand).

[0041]

[0047] The purpose of the homogenizer 610 is to break down the feedstock and ensure that generally similar amounts of a particular feedstock are delivered to the pyrolysis reactor 300 so that various product outputs from the pyrolysis unit, such as naphtha, various distillates such as gasoline, various oil and gas products including heavy gases and waxes, various gas oil compounds such as diesel fuel, are produced at a nearly constant rate by the pyrolysis reactor. The homogenized material flows into the pyrolysis reactor, which ensures smooth production of various end products of interest, maximizes the efficiency of the pyrolysis reactor, and reduces various feed operations to ensure smooth operation of the pyrolysis reactor, such as desired temperatures at each of the heating sections of the pyrolysis reactor, generally desired flow rates of various end products from the product outlet streams 380 of the pyrolysis reactor, and approximately constant heat inputs through the various heaters 370 of the reactor.

[0042]

[0048] Homogenizers usually contain a rotating "breaker" shaft and are designed to accept and mix feedstock from various assortment areas, thus achieving an overall similar distribution of various polymers, etc., without clogging the equipment or stopping the process as described above. A common challenge with rotating equipment when exposed to films present in the feedstock is that the film wraps around the rotating shaft. Film wrapping increases energy requirements or stops or damages the equipment. The shape of the breaker shaft is designed to prevent the film from wrapping easily. Additionally, the bearings are free, i.e., they are protected from film ingress. If necessary, a blade can be used to continuously cut the film from the shaft and / or the shaft can be reversed to "take out" the wrapped film. In other systems, a moving rake maintains the depth level of the feed stream. Such types of rotating equipment are known in the art and literature.

[0043]

[0049] The homogenized feed stream 615 is then fed by any conventional transport device, such as a conveyor belt 625, to the next unit operation, preferably a shredder 442. As mentioned above, the shredder 442 is primarily utilized to reduce the size of the feedstock 405 and to break up chunks of feedstock. Such shredders, if equipped with a rotating shaft, rotate at a slow speed but with a high torque to prevent feedstock films from clogging the system. Various shredders are known in the literature and in the art, including machines manufactured by VECO and others. Such shredders require only a small amount of energy and promote a constant flow of feedstock, making it easier to pelletize the feedstock in the next unit operation step.

[0044]

[0050] Downstream of the shredder 422 is the pelletizer 424. As mentioned above, the primary purpose of the pelletizer is to reduce the size of the feedstock 405 into smaller particles. The pelletizer 424 densifies the feedstock in the form of briquettes and / or cubes, generally having a size of about 0.5 inches to about 3 or 4 inches, preferably about 1 to 2 inches. Standard compactors or densifiers can be used to produce the briquettes and / or cubes, such as those produced by the MUNCH machines.

[0045]

[0051] The next unit operation is to transfer the pellets to a heating and feeding device 640, where the aforementioned briquettes and / or cubes, etc. are generally heated to a temperature of about 50°F or about 100°F to about 400°F or about 500°F, desirably about 150°F to about 300°F, and preferably about 200°F to about 250°F. These low temperature heatings are desirable so that the feedstock 460 can be easily transported and then processed in the extruder without causing distortion to the extruder equipment. However, heating at or above about 500°F, especially above 500°F, should be avoided, since too much heat applied to the pelletized feedstock can cause significant distortion to the extruder equipment. The heating and feeding device can be a standard rotary kiln dryer or the like, well known in the art and literature.

[0046]

[0052] The next unit operation in the feeding system is then the utilization of an extruder 444, the general purpose of which is to heat and densify said feedstock in the form of briquettes or cubes to form a continuous mass or stream of feedstock emerging from the extruder 444 into the pyrolysis reactor 300, which can be converted by cracking, recombining, etc., into the various types of oil gases mentioned above. The advantage of the process according to FIG. 4 is that the extrusion temperatures mentioned above result in pellets in semi-molten or molten form, and subsequently, a physical plug 655 of material can be formed around the conduit 500 at the inlet to the pyrolysis to prevent the backflow of gases produced in the reactor 300, i.e., into the extruder 650. In general, any type of extruder can be used, the preferred type being a single screw extruder, as it has the ability to form a plug around the feed conduit 500 while transporting the densified material at the required or desired feed rate. An important aspect of this modified embodiment is that the feedstock fed from the extruder to the pyrolysis reactor is generally in the form of flowable material (lump), but not molten, i.e., not melted, i.e., in the form of flowable plastic and hydrocarbon particles.

[0047]

[0053] The amount of solid or softened feedstock fed to the feed conduit 500 through the extruder 650 can range from about 25 to about 50 pounds per cubic foot, desirably from about 30 to about 45 pounds per cubic foot.

[0048]

[0054] The feed conduit 500 is utilized to feed the solid or semi-solid feedstock from the extruder to the pyrolysis reactor 300. For this reason, the above description is fully incorporated herein by reference in all its aspects unless otherwise stated, with the caveat that the radial angle of the feeder output shaft, i.e., the extruder output shaft 652, can vary up to about 10°, typically ranging from about 1° to 7°, and most preferably ranging from about 1° to about 3°.

[0049]

[0055] To achieve a consistent steam seal, the compression of the flowing material can be adjusted by changing the cross-sectional shape of the supply pipe or by lengthening / shortening the supply pipe. One means of achieving this is by adding ports to the side of the supply tube. The depth to which the rod is inserted into the material flow can be adjusted. This increases the resistance to the material flow and increases the compression of the material in a tighter sealed supply tube. The rod is required to be sturdy enough not to deform in the flow, and a seal is required between the inside of the supply tube and the surrounding environment. This seal can be any of those commonly used in designs such as packing glands or mechanical seals. Common thread patterns are generally insufficient to achieve a steam seal while still allowing adjustment, but multiple fasteners such as nuts with or without gaskets can seal.

[0050]

[0056] More specifically, the present invention relates to the use of a regulating plug 660, as shown in Figures 5A and 5B. The purpose of the regulating plug 660, which is positioned at a substantially perpendicular angle on the feed conduit 500, is to further compress the feedstock or feed stream 615 before it enters the pyrolysis vessel 300. As shown in Figures 5A and 5B, the regulating plug 660 extends into the side of the conduit 500 and can be attached to the conduit 500 in a conventional manner, such as by welding, nuts and bolts, etc. The angle of attachment is generally from about 70° to about 110°, desirably from about 80° to about 90°, and preferably at an angle of approximately 90°. A piston 670, which is longitudinally slidable within a housing 675, can be forced into the feed conduit 500 upon rotation of a threaded rod 680, which further compresses the feed material. Conversely, when the threaded rod 680 rotates in the opposite direction, the pressure in the feed conduit 500 decreases.

[0051]

[0057] Another feature of the present invention is that as the feed stream 615 exits conduit 500 it encounters very high temperatures within the initial portion of the pyrolysis reactor 300 which causes liquefaction and results in the natural formation of a plug 655 which typically forms at the outlet of the feed conduit 500 as shown in FIG. 3 and which prevents product vapors formed within the vessel 300 from entering the feed conduit 500.

[0052]

[0058] In accordance with the patent statues, the best mode and preferred embodiments are set forth, but the scope of the invention is not limited thereto, but rather by the appended claims. The invention as originally claimed in the present application is set forth below. [1] A plastics conversion feed system for transporting a feedstock to a reactor vessel, comprising: a homogenizer capable of breaking down said feedstock comprising a plastic material or a hydrocarbon material, or any combination thereof; a pelletizer capable of reducing size and densifying the homogenized feedstock; an extruder capable of forming a continuous mass of said feedstock which is fed to said reactor vessel; A plastic converting and supplying system comprising: [2] The plastic converting and feeding system of [1], including a shredder capable of reducing the size of the feedstock. [3] The plastic converting and feeding system described in [2], further comprising a heating and feeding device that heats and feeds the pelletized feed material, and the heating and feeding device is capable of transporting the feed material toward the extruder. [4] The plastic converting and feeding system of [3], having a conduit extending from the extruder to the reaction vessel. [5] The plastic converting and feeding system of [4], comprising a plug of said feedstock disposed about said conduit at an inlet to said reactor vessel. [6] The plastic converting and feeding system of [3], wherein the feedstock exiting the extruder is a flowable, non-molten material. [7] A plastics conversion feed method for transferring a feedstock to a reaction vessel, comprising: breaking down said feedstock comprising plastics, hydrocarbon-based materials, or combinations thereof in a homogenizer; reducing the size of said feedstock in a pelletizer; extruding said feedstock into said reactor vessel by an extruder operably connected to said reactor vessel by a feed conduit; A method for converting and supplying plastics. [8] The method for plastic converting and feeding described in [7], wherein the pelletized feedstock is heated to a temperature of about 200°F to about 500°F in a heater. [9] The plastic conversion and feeding method of [7], further comprising forming a plug of the feed material disposed around the feed conduit at the inlet of the reactor vessel.

[10] A plastics conversion feed system for transporting a feedstock to a reactor vessel, comprising: a size reduction device capable of reducing the size and densifying said feedstock comprising plastic or hydrocarbon-based materials, or a combination thereof; a heating device capable of heating the reduced size feedstock and transferring it to an extruder having an output shaft; a conduit connecting said extruder to said reactor vessel and capable of supplying said feedstock to said reactor vessel, said conduit having an output shaft at a radial angle of about 5° or less relative to said output shaft of said extruder apparatus; A plastic converting and supplying system comprising:

[11] The plastic converting and feeding system of

[10] , wherein the size reduction device includes a shredder or a pelletizer or both, and the heating device includes a feeder.

[12] The plastic conversion and supply system of

[11] , wherein the reaction vessel is a pyrolysis reactor.

[13] The plastic converting and feeding system of

[11] , wherein the size reduction device is the pelletizer, the pelletizer capable of densifying the feedstock to greater than about 15 pounds per cubic foot.

[14] The plastic converting and feeding system of

[10] , wherein the heating device is the extruder.

[15] A plastics conversion feed method for transferring a feedstock to a reaction vessel, comprising: reducing the size of said feedstock comprising plastic or hydrocarbon-based material or a combination thereof in a size reduction device; heating, blending and transferring the reduced size feedstock from the size reduction step into a feed conduit connected to the reactor vessel; feeding the feed conduit containing the reduced size of the feedstock into the reactor vessel; A method for converting and supplying plastics comprising the steps of:

[16] The method of

[15] , wherein the size reduction device comprises a pelletizer.

[17] The plastic converting and feeding method of

[16] , wherein the reduced size of the feedstock has a density greater than about 25 pounds per cubic foot.

[18] The plastic converting and feeding method of

[16] , wherein the feed conduit has an output radius axis that can vary by up to about 5° relative to the axis of the extruder.

[19] The plastic converting and feeding method of

[15] , having a hopper system including an upper hopper and a lower hopper, feeding the feedstock to the upper hopper and subsequently feeding the feedstock in the upper hopper to the lower hopper.

[20] The method of plastic converting and feeding as described in

[15] , wherein the feeding conduit is flexible and heated.

Claims

1. 1. A plastics conversion feed system for transporting a feedstock to a reactor vessel, comprising: a homogenizer capable of pulverizing said feedstock comprising a plastic material or a hydrocarbon material, or any combination thereof; a pelletizer disposed downstream of the homogenizer and operated at a temperature from ambient to about 160° F. (71.1° C.) to reduce the size of the ground homogenized feedstock and / or densify the ground homogenized feedstock to produce a pelletized feedstock; an extruder having an output shaft and positioned downstream of said pelletizer and capable of receiving said pelletized feedstock, heating said feedstock so that it emerges at a temperature range of from about 200° F. (93.3° C.) to about 400° F. (204.4° C.), and forming a continuous mass of feedstock which can be fed to said reaction vessel; a conduit extending from said extruder to said reaction vessel, said conduit having an axis at a radial angle of 5° or less relative to said output axis of said extruder; A plastic converting and supplying system comprising:

2. 10. The plastic converting and feeding system of claim 1 including a shredder positioned downstream of said homogenizer and upstream of said pelletizer, capable of reducing the size of said feedstock.

3. 3. The plastic converting and feeding system of claim 2, further comprising a heating and feeding device for heating and feeding the pelletized feedstock, the heating and feeding device being capable of transporting the feedstock toward the extruder.

4. A plastic converting and feeding system as described in claim 1, wherein the conduit has an axis at a radial angle of less than 3° relative to the output axis of the extruder.

5. 5. The plastics converting and feeding system of claim 4 including a plug of said feedstock disposed around said conduit at the inlet to said reactor vessel.

6. 4. The plastic converting and feeding system of claim 3, wherein said feedstock exiting said extruder is a flowable, non-molten material.

7. 1. A plastics conversion feed method for transferring a feedstock to a reactor vessel, comprising: comminuting the feedstock, which comprises plastic, hydrocarbon-based material, or a combination thereof, in a homogenizer; reducing the size of the feedstock with a pelletizer disposed downstream of the homogenizer and operating at a temperature range from ambient to about 160° F. (71.1° C.), thereby producing a pelletized feedstock; 1. A method for plastics conversion and feeding, comprising: providing an extruder having an output shaft and positioned downstream of said pelletizer to receive the pelletized feedstock; and a feed conduit extending from said extruder to said reactor vessel, said feed conduit having an axis at a radial angle of 5° or less relative to said output shaft of said extruder, operatively connecting said extruder to said reactor vessel and capable of feeding said feedstock to said reactor vessel; heating said feedstock in said extruder such that said feedstock exiting said extruder has a temperature in the range of about 200° F. (93.3° C.) to about 400° F. (204.4° C.); and extruding said feedstock into said reactor vessel by said extruder.

8. 8. The plastics converting and feeding method of claim 7, further comprising forming a plug of said feedstock disposed around said feed conduit at the inlet of said reactor vessel.

9. A plastic converting and feeding system as described in claim 1, further comprising a heating device positioned upstream of the extruder and capable of heating the reduced size feed material and transporting it to the extruder.

10. 10. The plastic converting and feeding system of claim 9, further comprising a size reduction device capable of reducing the size and densifying the feedstock comprising plastics or hydrocarbon-based materials, or a combination thereof, the size reduction device comprising a shredder disposed downstream of the homogenizer, and the heating device comprising a feeder.

11. 11. The plastics converting and feeding system of claim 10, wherein the reaction vessel is a pyrolysis reactor.

12. 11. The plastic converting and feeding system of claim 10, wherein said pelletizer is capable of densifying said feedstock to greater than about 15 pounds per cubic foot.

13. 10. The plastic converting and feeding system of claim 9, wherein the heating device is part of the extruder.

14. heating, blending and transferring the reduced size feedstock from the size reduction step into the feed conduit connected to the reactor vessel; 8. The method of claim 7 further comprising the step of: feeding said feed conduit containing said reduced size feedstock into said reactor vessel.

15. 15. The plastic converting and feeding method of claim 14, wherein the reduced size feedstock has a density greater than about 25 pounds per cubic foot.

16. 15. The plastic converting and feeding method of claim 14, wherein said feed conduit has its axis at a radial angle of 3 degrees or less relative to the output axis of said extruder.

17. 15. The plastic converting and feeding method of claim 14, further comprising a hopper system including an upper hopper and a lower hopper, feeding the feedstock to the upper hopper and subsequently feeding the feedstock in the upper hopper to the lower hopper, the hopper system being located upstream of the extruder.

18. 15. The plastic converting and feeding method of claim 14, wherein the feeding conduit is flexible and heated.

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