US20030185730A1 - Plant for polyolefines waste conversion into liquid hydrocarbons - Google Patents

Plant for polyolefines waste conversion into liquid hydrocarbons Download PDF

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Publication number
US20030185730A1
US20030185730A1 US10/419,205 US41920503A US2003185730A1 US 20030185730 A1 US20030185730 A1 US 20030185730A1 US 41920503 A US41920503 A US 41920503A US 2003185730 A1 US2003185730 A1 US 2003185730A1
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Prior art keywords
tank
reactor
plant
chamber
raw material
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Abandoned
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US10/419,205
Inventor
Henryk Zmuda
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Smuda Technologies Inc
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Henryk Zmuda
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Publication date
Application filed by Henryk Zmuda filed Critical Henryk Zmuda
Priority to US10/419,205 priority Critical patent/US20030185730A1/en
Publication of US20030185730A1 publication Critical patent/US20030185730A1/en
Assigned to SMUDA TECHNOLOGIES, INC. reassignment SMUDA TECHNOLOGIES, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ZMUDA, HENRYK
Abandoned legal-status Critical Current

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    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • 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
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
    • 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
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/002—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument
    • 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
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/087—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
    • C10B1/00—Retorts
    • C10B1/02—Stationary retorts
    • C10B1/04—Vertical retorts
    • 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
    • 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
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • 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
    • B01J2208/00504—Controlling the temperature by means of a burner
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • 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 subject-matter of the invention is a plant for polyolefines waste conversion into liquid hydrocarbons.
  • the known plant with the object to make plastics for utilization comprises the reactor, the raw material dosage system, the condenser of product, the buffer tank and the distillation column.
  • the reactor in form of vertical tank is equipped with the hatch, the raw material receiving connection pipe, the control system and the heating system.
  • the heating system consists of heating tubes which are placed on the tank's surface or within the tank. Such a heating system causes sinter and coke formation.
  • a process of the transformation of polyolefine wastes to liquid hydrocarbons is carried out in a plant according to the invention, comprising at least one reactor in a shape of vertical tank, provided with an inlet charging hole, connected to a polyolefine raw material and catalyst dosing device, combustion gases outlet pipe, product receiving pipe, mixer and sieve membrane and a heating system in a form of a combustion chamber surrounding a tank from below and the said chamber is heated with at least one burner, supplied with reaction products, and in the combustion chamber, symetrically distributed on a tank circumference, preferably in some rows, heating pipes are located, which pass throughout inside of the tank above the level of an upper wedge of a mixer and which are led out through sieve membrane to the combustion gases outlet chamber.
  • the plant comprises also a condenser for a product condensation, a raw product buffer tank and a distillation column. Products of the reaction coming out from the reactor through an outlet pipe are cooled and condensed and then are directed to a buffer tank, heated up to 40° C.
  • FIG. 1 is a schematic view of the apparatus of the present invention.
  • FIG. 2 is a side, partially cutaway view of the apparatus of the present invention.
  • a plant according to the invention is presented on the enclosed drawing in a form of an exemplary embodiment of the invention.
  • a plant comprises one reactor 1 according to the invention, in a shape of vertical tank, provided with an inlet charging hole 2 , connected to a polyolefine raw material and catalyst dosing device 3 , combustion gases outlet pipe 4 , product receiving pipe 5 , mixer 6 and a sieve membrane 7 and a heating system in a form of a combustion chamber 8 surrounding a tank 1 from below and the said combustion chamber 8 is heated with at least one burner 9 supplied with reaction products, and in the combustion chamber 8 , symetrically distributed on a reactor tank circumference, preferably in some rows, heating pipes 10 are located, which pass throughout inside of the tank above the level of an upper wedge of a mixer 6 and which are led out through a sieve membrane 7 to the combustion gases outlet chamber.
  • the plant comprises also a condenser 11 for a product condensation, a raw product buffer tank 12 and a distillation column 13 .
  • the reaction products coming out from the reactor through a product receiving pipe, are directed to a condenser 11 wherein they are cooled and condensed and then directed to the buffer tank 12 , which is heated to 40° C.
  • a buffer tank 12 is provided with a level sensor, included into a raw material dosing device 3 automatic regulation system, ensuring keeping a level of a reactor 1 content at the same range, which is for achieving the preferable regulation of a process.

Abstract

A plant for transformation of polyolefine wastes into useful hydrocarbons is provided which comprises a reactor in a shape of a vertical tank provided with an inlet charging hole, connected to a polyolefine raw material and catalyst dosing device, product vapour receiving pipe, a mixer and a liquid level regulation system, and a distillation column. In addition, a reactor is provided with a heating system in a form of a combustion chamber (8) surrounding a tank from below, and the chamber (8) is heated with at least one burner (9), supplied with reaction products.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a divisional application of U.S. Ser. No. 09/958,875, filed Oct. 17, 2001.[0001]
    • FIELD OF THE INVENTION
  • The subject-matter of the invention is a plant for polyolefines waste conversion into liquid hydrocarbons. [0002]
    • BACKGROUND OF THE INVENTION
  • Nowadays the utilization of objects made of plastics is an ecologic problem. The known plant with the object to make plastics for utilization comprises the reactor, the raw material dosage system, the condenser of product, the buffer tank and the distillation column. The reactor in form of vertical tank is equipped with the hatch, the raw material receiving connection pipe, the control system and the heating system. The heating system consists of heating tubes which are placed on the tank's surface or within the tank. Such a heating system causes sinter and coke formation. [0003]
    • SUMMARY OF THE INVENTION
  • A process of the transformation of polyolefine wastes to liquid hydrocarbons is carried out in a plant according to the invention, comprising at least one reactor in a shape of vertical tank, provided with an inlet charging hole, connected to a polyolefine raw material and catalyst dosing device, combustion gases outlet pipe, product receiving pipe, mixer and sieve membrane and a heating system in a form of a combustion chamber surrounding a tank from below and the said chamber is heated with at least one burner, supplied with reaction products, and in the combustion chamber, symetrically distributed on a tank circumference, preferably in some rows, heating pipes are located, which pass throughout inside of the tank above the level of an upper wedge of a mixer and which are led out through sieve membrane to the combustion gases outlet chamber. The plant comprises also a condenser for a product condensation, a raw product buffer tank and a distillation column. Products of the reaction coming out from the reactor through an outlet pipe are cooled and condensed and then are directed to a buffer tank, heated up to 40° C. [0004]
  • The preferable regulation of a process is achieved, when a buffer tank is provided with a level sensor, included into a raw material dosing device automatic regulation system, ensuring keeping a level of a reactor content at the same range. [0005]
  • From a buffer tank a product is directed to a distillation column, where fractions of various boiling temperatures are separated. [0006]
  • The introduction of heating pipes above the upper wedge of a mixer enables more efficient mixing, especially of a bottom zone, an uniform distribution of a catalyst in a reaction mass and remarkably decreases formation of agglomerates and coke.[0007]
    • BRIEF DESCRIPTION OF THE DRAWING FIGURES
  • FIG. 1 is a schematic view of the apparatus of the present invention. [0008]
  • FIG. 2 is a side, partially cutaway view of the apparatus of the present invention.[0009]
    • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • A plant according to the invention is presented on the enclosed drawing in a form of an exemplary embodiment of the invention. [0010]
  • A plant comprises one [0011] reactor 1 according to the invention, in a shape of vertical tank, provided with an inlet charging hole 2, connected to a polyolefine raw material and catalyst dosing device 3, combustion gases outlet pipe 4, product receiving pipe 5, mixer 6 and a sieve membrane 7 and a heating system in a form of a combustion chamber 8 surrounding a tank 1 from below and the said combustion chamber 8 is heated with at least one burner 9 supplied with reaction products, and in the combustion chamber 8, symetrically distributed on a reactor tank circumference, preferably in some rows, heating pipes 10 are located, which pass throughout inside of the tank above the level of an upper wedge of a mixer 6 and which are led out through a sieve membrane 7 to the combustion gases outlet chamber. The plant comprises also a condenser 11 for a product condensation, a raw product buffer tank 12 and a distillation column 13. The reaction products, coming out from the reactor through a product receiving pipe, are directed to a condenser 11 wherein they are cooled and condensed and then directed to the buffer tank 12, which is heated to 40° C.
  • A [0012] buffer tank 12 is provided with a level sensor, included into a raw material dosing device 3 automatic regulation system, ensuring keeping a level of a reactor 1 content at the same range, which is for achieving the preferable regulation of a process.
  • From the [0013] buffer tank 12 raw product is directed to the distillation column 13, where fractions of different boiling temperatures are separated.

Claims (2)

What is claimed is:
1. A plant for transformation of polyolefine wastes into hydrocarbons, comprising a reactor in a shape of a vertical tank provided with an inlet charging hole, connected to a polyolefine raw material and catalyst dosing device, product vapour receiving pipe, a mixer and a liquid level regulation system and a distillation column, characterized in, that a reactor is provided with a heating system in a form of a combustion chamber (8) surrounding a tank from below and the said chamber (8) is heated with at least one burner (9), supplied with reaction products, and in the combustion chamber, symetrically distributed on a tank circumference, preferably in some rows, heating pipes (10) are located, which pass throughout inside of the tank above the level of an upper wedge of a mixer (6) and which are led out through sieve membrane (7) to the combustion gases outlet chamber.
2. A plant according to claim 1, characterized in, that a buffer tank (12) is provided with a level sensor, included into a raw material dosing device (3) automatic regulation system.
US10/419,205 1999-04-26 2003-04-21 Plant for polyolefines waste conversion into liquid hydrocarbons Abandoned US20030185730A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US10/419,205 US20030185730A1 (en) 1999-04-26 2003-04-21 Plant for polyolefines waste conversion into liquid hydrocarbons

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
PLP332762 1999-04-26
PL99332762A PL188936B1 (en) 1999-04-26 1999-04-26 Method of converting polyolefinic waste materials into hydrocarbons and plant therefor
US09/958,875 US6777581B1 (en) 1999-04-26 2000-04-10 Method for transformation of polyolefine wastes into hydrocarbons and a plant for performing the method
US10/419,205 US20030185730A1 (en) 1999-04-26 2003-04-21 Plant for polyolefines waste conversion into liquid hydrocarbons

Related Parent Applications (2)

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US09/958,875 Division US6777581B1 (en) 1999-04-26 2000-04-10 Method for transformation of polyolefine wastes into hydrocarbons and a plant for performing the method
PCT/PL2000/000027 Division WO2000064998A1 (en) 1999-04-26 2000-04-10 A method for transformation of polyolefine wastes into hydrocarbons and a plant for performing the method

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US20030185730A1 true US20030185730A1 (en) 2003-10-02

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US10/419,205 Abandoned US20030185730A1 (en) 1999-04-26 2003-04-21 Plant for polyolefines waste conversion into liquid hydrocarbons

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EP (1) EP1212387B1 (en)
JP (1) JP3875494B2 (en)
KR (1) KR100474396B1 (en)
AT (1) ATE317886T1 (en)
AU (1) AU776901B2 (en)
BR (1) BR0011161A (en)
CA (1) CA2367937C (en)
CZ (1) CZ20013791A3 (en)
DE (1) DE60026014T2 (en)
DK (1) DK1212387T3 (en)
ES (1) ES2258449T3 (en)
HU (1) HUP0200078A3 (en)
ID (1) ID30451A (en)
IL (1) IL145928A0 (en)
IS (1) IS2510B (en)
MX (1) MXPA01010840A (en)
MY (1) MY133387A (en)
NO (1) NO20015229L (en)
NZ (1) NZ514978A (en)
PE (1) PE20010089A1 (en)
PL (1) PL188936B1 (en)
PT (1) PT1212387E (en)
SK (1) SK285956B6 (en)
TR (1) TR200103087T2 (en)
WO (1) WO2000064998A1 (en)
ZA (1) ZA200108350B (en)

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CA2367937A1 (en) 2000-11-02
IS2510B (en) 2009-05-15
MY133387A (en) 2007-11-30
DE60026014T2 (en) 2007-02-15
PE20010089A1 (en) 2001-04-05
ATE317886T1 (en) 2006-03-15
SK285956B6 (en) 2007-12-06
SK15272001A3 (en) 2002-03-05
IL145928A0 (en) 2002-07-25
KR100474396B1 (en) 2005-03-08
JP3875494B2 (en) 2007-01-31
TR200103087T2 (en) 2002-04-22
ES2258449T3 (en) 2006-09-01
AU776901B2 (en) 2004-09-23
EP1212387B1 (en) 2006-02-15
HUP0200078A2 (en) 2002-05-29
CZ20013791A3 (en) 2002-04-17
BR0011161A (en) 2006-07-18
IS6113A (en) 2001-10-19
DK1212387T3 (en) 2006-06-19
US6777581B1 (en) 2004-08-17
WO2000064998A1 (en) 2000-11-02
AU3577900A (en) 2000-11-10
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KR20010106138A (en) 2001-11-29
ID30451A (en) 2001-12-06

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