PL434735A1 - Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles - Google Patents

Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles

Info

Publication number
PL434735A1
PL434735A1 PL434735A PL43473520A PL434735A1 PL 434735 A1 PL434735 A1 PL 434735A1 PL 434735 A PL434735 A PL 434735A PL 43473520 A PL43473520 A PL 43473520A PL 434735 A1 PL434735 A1 PL 434735A1
Authority
PL
Poland
Prior art keywords
char
pyrolysis
thermal insulation
pyrolysis gas
reactor
Prior art date
Application number
PL434735A
Other languages
Polish (pl)
Other versions
PL241665B1 (en
Inventor
Bogusław Kusz
Bartosz Trawiński
Original Assignee
Politechnika Gdańska
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Politechnika Gdańska filed Critical Politechnika Gdańska
Priority to PL434735A priority Critical patent/PL241665B1/en
Priority to PCT/PL2021/000043 priority patent/WO2022019787A1/en
Priority to EP21846667.0A priority patent/EP4185658A4/en
Publication of PL434735A1 publication Critical patent/PL434735A1/en
Publication of PL241665B1 publication Critical patent/PL241665B1/en

Links

Classifications

    • 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
    • C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • 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
    • 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
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
    • 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
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
    • C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
    • 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
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/16—Features of high-temperature carbonising processes
    • 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
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/18—Modifying the properties of the distillation gases in the oven
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Reaktor do przeprowadzania pirolizy materiałów wybranych z grupy składającej się ze zrębków, drewna podkładowego, odpadów drzewnych, odpadów leśnych, osadów ściekowych, koksu naftowego, komunalnych odpadów stałych (MSW), paliw pochodzących z odpadów (RDF) lub dowolnej kombinacji paliw z biomasy charakteryzuje się tym, że szczelna próżniowo komora reaktora (1) o pionowej budowie podzielona jest funkcjonalnie na cztery kompartymenty w tym: najwyższy kompartyment (C1) gdzie pod pokrywą (4) komory reaktora (1) znajduje się wykonana z mało nasiąkliwych materiałów izolacja termiczna (12), zaś drugi kompartyment (C2) pirolizy wsadu z wykonaną z mało nasiąkliwych materiałów izolacją termiczną (45), gdzie łopatki (26) mieszadła (25) mieszają wsad (13) i gdzie ten wsad jest rozgrzewany do temperatury powyżej 200°C, zaś trzeci kompartyment (C3) zawierający kolumnę grzewczą (29) z grzałką elektryczną (31) lub opcjonalnie z palnikiem gazu pirolitycznego, warstwę izolacji termicznej (45) oraz warstwę o grubości minimum 10 cm rozgrzanego do temperatury 900 - 1000°C karbonizatu (14), w którym zachodzi redukcja i oczyszczanie gazu pirolitycznego, zaś czwarty kompartyment (C4) zawiera pod warstwą karbonizatu (14) kolumnę karbonizatu (20) oraz wykonaną z mało nasiąkliwych materiałów izolację termiczną (23), a także znajdujący się  pod pokrywą dolną (3) zbiornik (21) na karbonizat i wodę chłodzącą (38) wprowadzaną rurką (36) i wyprowadzaną rurką (37) oraz system wyprowadzania karbonizatu (22) i wylot oczyszczonego gazu pirolitycznego (40).A reactor for pyrolysis of materials selected from the group consisting of wood chips, undercoat, wood waste, forest waste, sewage sludge, petroleum coke, municipal solid waste (MSW), waste derived fuels (RDF) or any combination of biomass fuels is characterized by that the vacuum-tight reactor chamber (1) with a vertical structure is functionally divided into four compartments, including: the highest compartment (C1) where under the cover (4) of the reactor chamber (1) there is a thermal insulation made of low-absorbent materials (12) , while the second compartment (C2) of the charge pyrolysis with thermal insulation (45) made of low-absorbent materials, where the blades (26) of the stirrer (25) mix the charge (13) and where this charge is heated to a temperature above 200 ° C, and the third a set (C3) containing a heating column (29) with an electric heater (31) or optionally with a pyrolysis gas burner, a thermal insulation layer (45) and layers ę with a minimum thickness of 10 cm of a char (14) heated to a temperature of 900 - 1000 ° C, in which the reduction and purification of pyrolysis gas takes place, while the fourth compartment (C4) contains a char column (20) under the char layer (14) and made of little absorptive materials, thermal insulation (23), as well as a container (21) for char and cooling water (38) located under the bottom cover (3) for charcoal and cooling water (38) introduced with a tube (36) and an exiting tube (37), as well as the char discharging system (22) and the outlet purified pyrolysis gas (40).

PL434735A 2020-07-21 2020-07-21 Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles PL241665B1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
PL434735A PL241665B1 (en) 2020-07-21 2020-07-21 Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles
PCT/PL2021/000043 WO2022019787A1 (en) 2020-07-21 2021-06-29 Reactor and method for the pyrolysis of industrial or municipal waste and for the reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles
EP21846667.0A EP4185658A4 (en) 2020-07-21 2021-06-29 REACTOR AND PROCESS FOR PYROLYSIS OF INDUSTRIAL OR MUNICIPAL WASTE AND FOR REDUCING AND PURIFYING PYROLYSIS GAS FROM HEAVY HYDROCARBONS AND CARBON PARTICLES

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL434735A PL241665B1 (en) 2020-07-21 2020-07-21 Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles

Publications (2)

Publication Number Publication Date
PL434735A1 true PL434735A1 (en) 2022-01-24
PL241665B1 PL241665B1 (en) 2022-11-14

Family

ID=79729044

Family Applications (1)

Application Number Title Priority Date Filing Date
PL434735A PL241665B1 (en) 2020-07-21 2020-07-21 Reactor and method for industrial and municipal waste pyrolysis and for reduction and purification of pyrolysis gas from heavy hydrocarbons and carbon particles

Country Status (3)

Country Link
EP (1) EP4185658A4 (en)
PL (1) PL241665B1 (en)
WO (1) WO2022019787A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL443380A1 (en) * 2022-12-31 2024-07-01 Politechnika Gdańska Water steam feeder for a pyrolysis reactor and method for introducing water steam into a pyrolysis reactor
CN117735646B (en) * 2024-02-19 2024-04-19 深圳市纯水一号水处理科技有限公司 A high-concentration salt-containing wastewater deep treatment device

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL126989B1 (en) 1980-01-10 1983-09-30 Os Bad Rozwojowy Kauczukow Method of producing watery dispersions of styrene,butylmaleate and/met/acrylic acid copolymers used for protectively and decoratively coating structural components of a building using thermal methods
NL1009745C2 (en) 1998-07-27 2000-01-28 Stichting Energie Method and device for forming synthesis gas from biomass and residues.
WO2002046331A1 (en) 2000-12-04 2002-06-13 Emery Energy Company L.L.C. Multi-faceted gasifier and related methods
WO2003018720A2 (en) 2001-08-28 2003-03-06 Sasol-Lurgi Technology Company (Pty) Limited Apparatus and prcess for discharging ash from a high pressure gasifier
DE10216338A1 (en) 2002-04-13 2003-10-23 Rudolf Jeschar Modular five-stage cascade reactor process converts a mixture of organic and inorganic residues into gas for use as fuel in fuel cell or gas engine
CZ14193U1 (en) 2003-08-27 2004-03-29 Sýkoraáfrantišekáing Three-zone gasifier having a bypass and intended for gasification of biomass of vegetable origin
DE102005026764B3 (en) 2005-06-10 2007-04-05 Ws Reformer Gmbh Fixed bed gasifier and process for the gasification of solid fuel
WO2008058347A1 (en) 2006-11-17 2008-05-22 Millennium Synfuels, Llc Manufacture of fuels
US9587186B2 (en) 2008-09-04 2017-03-07 Epic Clean Technologies Corporation Pressurized gasification apparatus to convert coal or other carbonaceous material to gas while producing a minimum amount of tar
CZ26592U1 (en) 2013-12-18 2014-03-10 Tarpo Spol.S R.O. Apparatus for multistage gasification of carbonaceous fuels com
SE538794C2 (en) 2014-05-20 2016-11-29 Ses Ip Ab C/O Scandinavian Enviro Systems Ab Plant and process for the recovery of carbon and hydrocarbon compounds from organic feedstock by pyrolysis.
CZ28354U1 (en) 2015-03-31 2015-06-23 Pavel Záhořík Gas generator for biogas gasification, especially woodchips
WO2018044252A1 (en) * 2016-09-05 2018-03-08 Stryzhak Sergii Method of conversion of municipal solid and other carbon-containing waste into synthesis gas and the equipment based on this method
PL235081B1 (en) * 2016-09-20 2020-05-18 Akademia Gorniczo Hutnicza Im Stanislawa Staszica W Krakowie Method for homogeneous carbonisation and activation of organic materials and the device for homogeneous carbonisation and activation of organic materials
US20180086994A1 (en) 2016-09-29 2018-03-29 Expander Energy Inc. Process For Converting Carbonaceous Material Into Low Tar Synthetic Gas
CN206721116U (en) * 2017-04-28 2017-12-08 神雾科技集团股份有限公司 A kind of coal dust and biomass pyrolytic prepare also Primordial Qi and the system of activated carbon
PL429984A1 (en) * 2019-05-21 2020-11-30 Politechnika Gdańska Reactor for industrial or municipal waste pyrolysis and method of pyrolysis with purification of pyrolysis gas from heavy hydrocarbons and carbon particles

Also Published As

Publication number Publication date
EP4185658A4 (en) 2024-08-07
PL241665B1 (en) 2022-11-14
WO2022019787A1 (en) 2022-01-27
EP4185658A1 (en) 2023-05-31

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