Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
  • B01J8/0285—Heating or cooling the reactor
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B19/00—Heating of coke ovens by electrical means
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
  • C10B49/14—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot liquids, e.g. molten metals
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
  • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
  • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00008—Controlling the process
  • B01J2208/00017—Controlling the temperature
  • B01J2208/00433—Controlling the temperature using electromagnetic heating
  • B01J2208/00469—Radiofrequency
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00008—Controlling the process
  • B01J2208/00017—Controlling the temperature
  • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
  • B01J2208/00796—Details of the reactor or of the particulate material
  • B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P20/00—Technologies relating to chemical industry
  • Y02P20/141—Feedstock
  • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics

Definitions

• the invention relates to a reactor for gasifying and / or purifying plastic material, comprising (a) a reactor vessel for receiving the plastic material, (b) a heater for heating the plastic material in the reactor vessel, (c) wherein the reactor vessel is at least partially filled with a molten metal ,
• the invention relates to a process for at least partial decomposition, in particular depolymerization ren, and / or cleaning of plastic material.
• used plastic products are usually recycled material that they are processed into products in which the plastic quality plays a minor role, for example, benches or piles.
• these applications can not absorb the immense amounts of plastic waste, so that a large part of the plastic waste is used as fuel, which is undesirable from an environmental point of view.
• US Pat. No. 5,436,210 A discloses a device for treating waste, in which the waste is introduced from below into a bath of liquid metal. The waste decomposes and leaves the bath liquid or in gaseous form.
• a depolymerization reactor in which balls are also provided for heating by an inductive heating. This reactor also does not comprise a metal bath.
• Impurities are a particular challenge for the recycling of plastic. It must therefore be ensured that any impurities, such as sand, organic residues or the like, do not impair the recycling process.
• the invention has for its object to reduce disadvantages in the prior art.
• the invention solves the problem by a reactor comprising a braking device arranged in an interior of the reactor vessel for slowing down a flow of liquefied plastic material in the reactor vessel, wherein the braking device has a plurality of movably arranged in the interior bodies.
• An advantage of the invention is that the braking device can be designed so that it forces the plastic material on a meandering way.
• the plastic material then travels a long way due to the presence of the braking device in the reactor vessel, so that it reacts chemically to a large extent.
• Due to the large number of bodies movably arranged in the interior, the plastic material heated by the heater and thus liquefied must therefore travel a long way past the bodies in order to pass through the reactor. This leads to a high yield of degradation products.
• the bodies are freely movable and therefore can move relative to each other. Although contamination of the plastic material can be reflected on the bodies, but by constant collisions of the body with each other any deposits are quickly detached and can leave the reactor upwards. It is also advantageous that the bodies can form reactive surfaces, which can accelerate the chemical reaction in the reactor. Thus, the bodies may have a coating with a catalyst.
• the reactor is understood in particular to mean a thermocatalytic depolymerization reactor.
• This is a reactor designed to thermally and / or catalytically depolymerize supplied polymers and / or to decompose them into materials having a lower melting or boiling point.
• the reactor can also be designed for cleaning plastic material.
• the temperature in the reactor is then preferably chosen so that the contaminant decomposes, but the plastic material remains unaffected.
• heating is meant any device designed to supply thermal energy to the plastic material in the reactor vessel.
• it is an inductive heating, the at least in parts of the reactor vessel and / or arranged in the interior of the reactor vessel components inductive manner generates heat. This has the advantage that even radially inner parts of the reactor vessel can be heated well.
• the braking device is understood in particular to mean an entirety of parts elements, called bodies, which are at least also arranged in the reactor vessel, so that a stream of liquefied plastic material is slowed down from an entry point to an exit point.
• the plurality of movable bodies is understood in particular to mean that at least 1000, in particular at least 10,000, such bodies are present.
• the bodies are arranged movably in the interior, it is understood, in particular, that the bodies can move freely in at least one degree of freedom. It is particularly favorable if the bodies can move freely in two, three or more degrees of freedom. However, this does not rule out that the bodies are unable to reach any point in the interior. In particular, restraint devices may be present which prevent the bodies from moving freely anywhere in the interior of the reactor vessel. It is also possible for the individual bodies to be fastened, for example by means of flexible fastening elements, but this is costly.
• the bodies are, in particular, flowable bodies, that is to say that the bodies do not interlock with one another but can slide off one another.
• the bodies are in particular convex, for example spherical.
• a radius of an imaginary envelope ball minimum diameter which completely surrounds the body, at most twice as large as the radius the largest imaginary sphere that can be inscribed in the body.
• the bodies consist at least predominantly of ferromagnetic material. If the heater is an induction heater, the bodies heat up, so that a particularly intensive chemical reaction can take place on the surface of the body.
• This molten metal preferably has a melting point of below 150 ° C. But it is also possible to choose a molten metal whose melting point is below 250 ° C or even below 300 ° C.
• the reactor has a feeding device for feeding plastic material.
• This feeding device is preferably arranged near the bottom. It may comprise an extruder by means of which plastic material can be plasticized. It is advantageous if the extruder is arranged so that it pumps the plastic material near the bottom of the reactor vessel in the reactor vessel.
• the reactor comprises a condenser, by means of which gases can be condensed, which leave the reactor vessel.
• gases are, for example, decomposition products of the plastic material.
• the reactor vessel comprises polyolefin, which is introduced, for example via the metering device from below into the reactor vessel. If polyolefin decomposes, a petroleum-like liquid is formed which can be burned for heating purposes or is available for synthesis purposes.
• the reactor comprises at least one holding device for preventing floating of the balls.
• molten metals having a melting point below 300 ° C have a density that is above 8 grams per cubic centimeter.
• the holding devices are provided.
• the restraint device preferably has a multiplicity of recesses designed in such a way that the bodies can be retained, but gas can flow freely through them.
• the at least one restraint device is connected to at least one movement device for moving the restraint device upwards and downwards. This makes it possible to move the restraint device and thus the body resting against the restraint device so that the bodies come into contact with one another and any deposits on the bodies are removed.
• the moving device may comprise one or more rods that run along a longitudinal axis of the reactor vessel.
• the retaining device is connected to a drive, so that the retaining device is oscillatably movable.
• An oscillatory movement dissolves contaminants from the bodies and leads to the detachment of gas bubbles, so that the release of resulting gases is accelerated.
• a particularly efficient movement of the bodies is obtained when a plurality of restraint devices are provided, which are movable independently of one another automatically, in particular along the longitudinal axis of the reactor vessel, in an oscillatable manner.
• the viscosity of the plastic material changes in such a way that the viscosity (toughness) decreases towards the top.
• a substantially constant braking effect is achieved by the body is, according to a preferred embodiment provided that an average radius of the body decreases with increasing altitude.
• the radius of the body is the radius of a perfect sphere of the same size. If the bodies do not all have the same radius, then the corresponding radius always means the median of the stiffening of the radii.
• the plastic material consists at least predominantly of solid at 23 ° C Polyoelfin.
• other non-halo-containing plastics it is possible to use, at a limited percentage, for example less than 10% by weight, plastics containing halogen.
• FIG. 1 shows a reactor according to the invention for carrying out a method according to the invention.
• FIG. 1 shows a reactor 10 according to the invention for gasifying plastic material 12, in particular polyolefin polymers.
• the reactor comprises an example, substantially cylindrical reactor vessel 14 for heating the plastic material 12, which is introduced via an extruder 16 in the reactor vessel 14.
• the reactor 10 comprises a heater 18 in the form of an inductive heater, which has a plurality of coils 20.1, 20.2, 20.5, by means of which an alternating magnetic field is generated in an interior 22 of the reactor vessel 14.
• the coils 20 (reference numerals without counting suffix denote the object as such) are connected to a not shown power supply unit which applies an alternating current to the coils.
• the frequency of the AC current is, for example, in the range of 25 to 50 kHz. Higher frequencies are possible, but lead to an increase in the so-called skin effect, which is undesirable.
• a braking device 24 is arranged, by means of which the flow of liquefied plastic material 12 can be slowed down in the reactor vessel 14.
• the brake device 24 includes a
• the bodies 25 are heated by the inductive heating 18 and thus heat a molten metal 26 present in the reactor vessel 14.
• the molten metal consists of Wood's metal, the Lipowitz alloy, the Newton alloy, the Lichtenberg alloy and / or an alloy comprising gallium and indium.
• the molten metal 26 usually has a density of more than 9 grams per cubic centimeter, so that the plastic material 12 undergoes a strong buoyancy. This buoyancy accelerates the plastic material 12.
• the bodies 25 counteract this acceleration.
• the plastic material 12 decomposes successively, forming gas bubbles 28, which rise upwards.
• the molten metal 26 may have a catalytic effect on the decomposition process, so that the reactor 10 may be a thermo-catalytic depolymerization reactor.
• the supplied through the extruder 16 plastic material passes through an inlet opening 30, which is preferably arranged at the bottom of the reactor vessel 14, in the interior 22.
• the plastic material is polyolefin.
• the braking device 24 comprises retaining devices 32.1, 32.2, which in the present case in frames 34.1, 34.2 comprise tensioned meshes whose meshes are so small that the bodies 25 can not pass upwards.
• the retaining device 32.2 is connected to a movement device 36 which has along a longitudinal axis L of the reactor vessel 14 extending rods 38 which are attached to not shown eccentric motors, which may be located on an upper side of the reactor vessel 14.
• the rods 38 are connected via bellows to the reactor vessel 14.
• Exentermotoren the rods 36 can be moved up and down, so that the retaining device 32 is oscillating up and down movable.
• the distribution of the bodies 25, in the present case of the balls, is drawn purely schematically in FIG.
• the bodies 25 are also drawn in Figure 1 in a constant radius R. It is particularly favorable, however, if the radius R decreases towards the top.
• the reactor vessel 14 is constructed on its side facing the interior 22 of a ferromagnetic material, for example of iron or magnetic steel.
• the induction heater 18 is designed so that a temperature gradient results, with the temperature increasing with increasing height.
• the reactor 10 has a pollutant discharge 40, which is arranged at the upper end of the reactor vessel 14. Because typical contaminants of plastic material, such as sand, are lighter than the metal bath, they float up and can be pulled off at the top.
• the reactor 10 also comprises a gas outlet 42, which opens into a condenser 44 and draws off emerging gas. Liquid material leaving the condenser 44 enters a collector 46.

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• 2010
  • 2010-11-02 DE DE102010050152.2A patent/DE102010050152B4/de not_active Expired - Fee Related
• 2011
  • 2011-11-01 CA CA2816477A patent/CA2816477A1/en not_active Abandoned
  • 2011-11-01 US US13/883,022 patent/US20130303810A1/en not_active Abandoned
  • 2011-11-01 CN CN201180053046.4A patent/CN103282462B/zh not_active Expired - Fee Related
  • 2011-11-01 AU AU2011325551A patent/AU2011325551A1/en not_active Abandoned
  • 2011-11-01 BR BR112013010906A patent/BR112013010906A2/pt not_active IP Right Cessation
  • 2011-11-01 MX MX2013004884A patent/MX2013004884A/es not_active Application Discontinuation
  • 2011-11-01 WO PCT/DE2011/001975 patent/WO2012059091A1/de active Application Filing
  • 2011-11-01 EP EP11810786.1A patent/EP2635656A1/de not_active Withdrawn
  • 2011-11-01 JP JP2013537001A patent/JP2014500343A/ja not_active Ceased
  • 2011-11-01 RU RU2013125465/05A patent/RU2587184C2/ru not_active IP Right Cessation

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