EP2558550A2 - Verfahren zur thermischen spaltung hochmolekularer organischer abfälle - Google Patents

Verfahren zur thermischen spaltung hochmolekularer organischer abfälle

Info

Publication number
EP2558550A2
EP2558550A2 EP11719755A EP11719755A EP2558550A2 EP 2558550 A2 EP2558550 A2 EP 2558550A2 EP 11719755 A EP11719755 A EP 11719755A EP 11719755 A EP11719755 A EP 11719755A EP 2558550 A2 EP2558550 A2 EP 2558550A2
Authority
EP
European Patent Office
Prior art keywords
organic waste
waste material
reactor
biogenic
molecular weight
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
EP11719755A
Other languages
German (de)
English (en)
French (fr)
Inventor
Thomas Willner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nexxoil AG
Original Assignee
Nexxoil AG
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 Nexxoil AG filed Critical Nexxoil AG
Publication of EP2558550A2 publication Critical patent/EP2558550A2/de
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • 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
    • C10B53/06—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of oil shale and/or or bituminous rocks
    • 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
    • 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
    • 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
    • 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
    • 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1003—Waste materials
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1014—Biomass of vegetal origin
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1018—Biomass of animal origin
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4006—Temperature
    • 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
    • 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
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • 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
    • Y02P20/145—Feedstock the feedstock being materials of biological origin
    • 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
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock

Definitions

  • the invention relates to a process for the thermochemical conversion of
  • organic waste material here are solid hydrocarbon-containing substances or mixtures of long-chain or crosslinked molecules to understand. Such waste materials may, for. As plastic or rubber waste,
  • the fluidized catalyst migrates back and forth between the cracking reactor operating at about 500 ° C and the regenerator operating at about 700 ° C.
  • the reactant in the reactor must be completely vaporized before the cracking reactions can take place on the fluidized catalyst particles. This is not possible with high-molecular weight hard-to-evaporate solids such as plastic, tar sands or oil shale.
  • CONFIRMATION COPY DE 102 15 679 B4 describes the thermal conversion of high molecular weight substances into liquid fuels, in which the cracking reactions take place in a heavy oil liquid phase, a so-called sump phase, in a temperature range between 350 and 500 ° C.
  • the autocatalytic action of the heavy oil fraction is used by using a gas stream which has a hydrogenating or reducing effect.
  • the use of hydrogenating or reducing gas requires increased
  • reaction temperatures must be sufficiently low so that the containers, pipes and heating elements do not coke. With critical coking temperatures one must expect material-dependent above 400 to 450 ° C. In order to avoid coking, the reaction temperatures must be below the respective critical coking temperature, in particular on heated walls. For temperature-stable hydrocarbons such as plastic and rubber waste, distillation residues from mineral oil processing, tar sands or oil shale higher reaction temperatures are necessary according to the method of DE 102 15 679 B4, so that for these hydrocarbons coking strongly affect the technical implementation. Another disadvantage of DE 102 15 679 B4 is the need for very rapid heating of the raw material. As a result, there are excessive
  • Hydrocarbons are also particularly applicable to pyrolysis processes, ie purely thermal decomposition, so that even there unwanted coking reactions represent a significant procedural problem.
  • Hydrocarbons which runs under atmospheric pressure, does not require the addition of catalysts and can be carried out at reaction temperatures below critical coking temperatures, where it also covers the non-evaporable
  • Components can convert high molecular weight organic waste material into liquid fuels.
  • the method according to the invention comprises the following steps:
  • the high-molecular organic waste material and the biogenic substances are to be supplied in a crushed state.
  • the waste material if fusible, may be processed in a molten state. It has proven advantageous to stir during the transformation or otherwise to keep the material in motion.
  • Other measures include, for example, inert fluidizing gases when the materials are in the reactor as a solid mixture, or circulation pumps when the waste material in the reactor is in a molten flowable state.
  • biogenic substances are understood to mean substances whose origin in the
  • organic waste material substances containing long-chain and / or branched hydrocarbon molecules, such as, for example Plastic or rubber waste, distillate residues from mineral oil processing, heavy oils of all kinds, asphalts, bitumen, tar sands or oil shale.
  • the high molecular weight organic waste material is brought to temperatures of 250 ° C to 500 ° C, preferably from temperatures between 280 ° C and 420 ° C, more preferably between 300 ° C and 400 ° C. This can be done in a reactor or in one
  • heaters of many types such as electric heating - for example, via resistance, induction or high frequency -, burner exhaust systems or many others can be used.
  • the high molecular weight organic waste materials After addition of biogenic substances according to the invention, the high molecular weight organic waste materials begin to break down into shorter-chain liquid fuels in the light and medium oil range.
  • biogenic substances themselves undergo pyrolytic decomposition reactions.
  • the resulting biogenic pyrolysis products during the reaction are first of all a solid residue which is discharged directly from the reactor and does not enter the gas-vapor phase, secondly leaving gases which do not condense and, thirdly, biogenic condensation phases.
  • a particular advantage of the process according to the invention is the fact that it is also possible to process here non-completely volatilizable high molecular weight organic residues which are solid at room temperature.
  • reaction auxiliaries such as As water or gases necessary.
  • the process of the invention can be carried out in batch mode or continuously.
  • Vacuum distillation residue from mineral oil processing which is solid at room temperature, presented in a laboratory stirred reactor.
  • this feedstock is heated to 390 ° C. Subsequently, as a biogenic substance dried and crushed straw by means of a screw conveyor continuously with constant stirring the reactor
  • the non-condensing gas phase is removed via a fume hood.
  • this noncondensing gas consists of about half of oxygen-containing fission products such as carbon dioxide and carbon monoxide and the other half of hydrocarbon fission products such as methane, ethane, propane and butane. Also their olefins ethylene, propylene and butylene were found.
  • Fig. 2 is a GC-MS analysis of the condensate phase 1, the inventive
  • a device from Agilent type HP5972A is used, as separation column was a cyanopropylphenol and polysiloxane coated type ZB1701 from Zebron used.
  • the heating rate is (3 ° C / min).
  • Temperature program covers the range from 45 ° C to 280 ° C. Fluoranthene (retention time 70.05 min) was used as the internal standard.
  • a C14 isotope analysis was performed. This resulted in a biogenic C content in the product oil of less than 5%.
  • the aqueous phase (condensate phase 3) contains acetic acid as well as water
  • Phase 2 and Phase 4 consist predominantly of oxygen-containing ring compounds such.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)
EP11719755A 2010-04-13 2011-03-03 Verfahren zur thermischen spaltung hochmolekularer organischer abfälle Ceased EP2558550A2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102010014768.0A DE102010014768B4 (de) 2010-04-13 2010-04-13 Verfahren zur thermischen Spaltung hochmolekularer organischer Abfälle
PCT/DE2011/000220 WO2011127881A2 (de) 2010-04-13 2011-03-03 Verfahren zur thermischen spaltung hochmolekularer organischer abfälle

Publications (1)

Publication Number Publication Date
EP2558550A2 true EP2558550A2 (de) 2013-02-20

Family

ID=44626387

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11719755A Ceased EP2558550A2 (de) 2010-04-13 2011-03-03 Verfahren zur thermischen spaltung hochmolekularer organischer abfälle

Country Status (9)

Country Link
US (1) US8858656B2 (zh)
EP (1) EP2558550A2 (zh)
CN (1) CN103038317B (zh)
AU (1) AU2011240449B2 (zh)
BR (1) BR112012026395B1 (zh)
CA (1) CA2814880C (zh)
DE (1) DE102010014768B4 (zh)
IL (1) IL222416A (zh)
WO (1) WO2011127881A2 (zh)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10364400B2 (en) 2011-09-01 2019-07-30 Akbev Group, Llc Spent grain fuel product and process
US10982162B2 (en) 2011-09-01 2021-04-20 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
US10781388B2 (en) 2011-09-01 2020-09-22 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
US11866669B2 (en) 2011-09-01 2024-01-09 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
US11441090B2 (en) 2011-09-01 2022-09-13 Akbev Group, Llc High protein organic materials as fuel and processes for making the same
CN105419839A (zh) * 2015-11-03 2016-03-23 交通运输部公路科学研究所 一种改性生物沥青及其制备方法
CN105295982B (zh) * 2015-11-18 2017-06-16 上海交通大学 一种油页岩伴生物质的多联产综合利用系统及其工艺
CN105295983B (zh) * 2015-11-18 2017-06-16 上海交通大学 一种油页岩伴有机固体废弃物的多联产利用系统及其工艺
CN105802655B (zh) * 2016-03-11 2017-12-01 中山大学 废弃硒鼓碳粉热解生产燃料油和气的装置
FI3532569T3 (fi) * 2016-10-28 2023-01-13 Menetelmä runsasproteiinisten orgaanisten polttoaineiden valmistamiseksi
WO2019085528A1 (zh) * 2017-11-03 2019-05-09 董平年 一种生活有机垃圾的裂解还原转化处理方法

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004038220A1 (de) * 2004-08-05 2006-03-16 Proton Technology Gmbh I.Gr. Thermische Biomassenverölung

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19742266A1 (de) 1997-09-25 1999-05-06 Ludger Dr Steinmann Aufwertung von Chemie- und Energierohstoffen durch Reaktion mit geringwertigen Rohstoffen
DE10215679B4 (de) 2002-04-10 2007-07-12 Ibh Ingenieurgesellschaft Mbh Direkte thermochemische Umwandlung von hochmolekularen organischen Substanzen in niedrigviskose flüssige Brennstoffe
AR057141A1 (es) * 2005-09-28 2007-11-21 Cwt Llc Ab Procesamiento de depolimerizacion para convertir productos de desecho organicos y no-organicos en productos utiles
US7834226B2 (en) * 2007-12-12 2010-11-16 Chevron U.S.A. Inc. System and method for producing transportation fuels from waste plastic and biomass
CA2753985C (en) * 2008-03-04 2017-12-19 University Of Massachusetts Catalytic pyrolysis of solid biomass and related biofuels, aromatic, and olefin compounds
CN101265412A (zh) * 2008-04-09 2008-09-17 江华鹏 生物质与废塑料共热解制取燃料油的方法
CN201265412Y (zh) * 2008-10-16 2009-07-01 刘小白 井下管径、管位温度测试仪
CN101508619B (zh) 2009-03-12 2013-03-27 浙江大学 生物质与聚合物催化共裂解制取碳氢化合物的方法

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004038220A1 (de) * 2004-08-05 2006-03-16 Proton Technology Gmbh I.Gr. Thermische Biomassenverölung

Also Published As

Publication number Publication date
CA2814880A1 (en) 2012-10-20
DE102010014768B4 (de) 2021-10-28
CN103038317A (zh) 2013-04-10
BR112012026395B1 (pt) 2019-09-03
IL222416A0 (en) 2012-12-31
CN103038317B (zh) 2015-05-13
WO2011127881A2 (de) 2011-10-20
IL222416A (en) 2017-08-31
WO2011127881A3 (de) 2011-12-29
US8858656B2 (en) 2014-10-14
AU2011240449B2 (en) 2014-12-18
US20130091761A1 (en) 2013-04-18
AU2011240449A1 (en) 2012-11-29
DE102010014768A1 (de) 2011-10-13
CA2814880C (en) 2018-04-03

Similar Documents

Publication Publication Date Title
DE102010014768B4 (de) Verfahren zur thermischen Spaltung hochmolekularer organischer Abfälle
Alvarez et al. Improving bio-oil properties through the fast co-pyrolysis of lignocellulosic biomass and waste tyres
Yang et al. Fast co-pyrolysis of low density polyethylene and biomass residue for oil production
Ly et al. Catalytic pyrolysis of bamboo in a bubbling fluidized-bed reactor with two different catalysts: HZSM-5 and red mud for upgrading bio-oil
EP3421572B1 (en) Method for increasing gasoline and middle distillate selectivity in catalytic cracking
FI126813B (en) The process of converting biomass into liquid fuels
Oudenhoven et al. Demineralization of wood using wood-derived acid: Towards a selective pyrolysis process for fuel and chemicals production
US8920609B2 (en) Method of increasing anhydrosugars, pyroligneous fractions and esterified bio-oil
Wan et al. Direct catalytic upgrading of biomass pyrolysis vapors by a dual function Ru/TiO2 catalyst
EP2324099B1 (de) Verfahren zur gewinnung von brenn- bzw. treibstoffen
EP2598605A2 (de) Anlage und verfahren zur erzeugung von treibstoffen aus biomasse / kunststoff - gemischen
Ansari et al. Investigating production of hydrocarbon rich bio-oil from grassy biomass using vacuum pyrolysis coupled with online deoxygenation of volatile products over metallic iron
Abnisa et al. Recovery of liquid fuel from the aqueous phase of pyrolysis oil using catalytic conversion
US10377953B2 (en) Fluidized upgrading/hydrostabilizing of pyrolysis vapors
US8287723B2 (en) Biomass pyrolysis in refinery feedstock
WO2012015575A1 (en) Metal impurity and high molecular weight components removal of biomass derived biocrude
Lin et al. Interactions between biomass-derived components and polypropylene during wood–plastic composite pyrolysis
WO2014001633A1 (en) Process for producing hydrocarbons
EP3094704A1 (de) Verfahren zur herstellung von pyrolysegas oder pyrolyseöl aus biogenen ausgangsmaterialien und damit herstellbares pyrolyseöl, pyrolysegas und desoxygenierungskatalysator
Divyabharathi et al. Hydrothermal liquefaction of paddy straw for biocrude production
WO2014182364A1 (en) Methods of and apparatuses for upgrading a hydrocarbon stream including a deoxygenated pyrolysis product
EP3215588A1 (de) Verfahren zur umsetzung von biomasse zu flüssigen und/oder gasförmigen energieträgern
EP3636729B1 (de) Verfahren zur herstellung von coker-kohle
EP2774971A1 (en) Process for the upgrading of gaseous products obtained from thermal processing of biomass
WO2023180796A1 (en) Catalytic hydrothermal liquefaction of waste plastic, biomass, in lignin containing solvent from 2g-ethanol plant

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20121024

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20140827

REG Reference to a national code

Ref country code: DE

Ref legal event code: R003

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN REFUSED

18R Application refused

Effective date: 20180423