[go: up one dir, main page]

WO2017208268A1 - Procédé et système associé pour éliminer des cendres de biomasses - Google Patents

Procédé et système associé pour éliminer des cendres de biomasses Download PDF

Info

Publication number
WO2017208268A1
WO2017208268A1 PCT/IT2016/000140 IT2016000140W WO2017208268A1 WO 2017208268 A1 WO2017208268 A1 WO 2017208268A1 IT 2016000140 W IT2016000140 W IT 2016000140W WO 2017208268 A1 WO2017208268 A1 WO 2017208268A1
Authority
WO
WIPO (PCT)
Prior art keywords
solvent
ashes
organic material
biomasses
biomass
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
PCT/IT2016/000140
Other languages
English (en)
Inventor
Gian Claudio FAUSSONE
Miha GRILC
Blaz LIKOZAR
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.)
INSER ENERGIA SpA
Kemijski Institut
Original Assignee
INSER ENERGIA SpA
Kemijski Institut
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 INSER ENERGIA SpA, Kemijski Institut filed Critical INSER ENERGIA SpA
Priority to PCT/IT2016/000140 priority Critical patent/WO2017208268A1/fr
Priority to EP16747850.2A priority patent/EP3464514A1/fr
Publication of WO2017208268A1 publication Critical patent/WO2017208268A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/08Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
    • C10G1/083Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts in the presence of a solvent
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G31/00Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/09Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by filtration
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1011Biomass
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

Definitions

  • the present invention refers to a process and a related system for removing ashes from biomasses.
  • the present invention refers to a reactor for the thermal-chemical conversion of biomass having a high content of ashes to obtain a fuel without ashes.
  • the present invention refers to a reactor for the thermal-chemical conversion of biomass, wherein there is a step of removing ashes at liquid state with a solvent by using mixing means, for example stirrers.
  • Biomass with a high content of ashes used as fuel can imply serious problems, due to the presence of inorganic substances with low melting point and with high particulate emissions.
  • the trend is placing a limit to the acceptable content of ashes present in the fuels.
  • the acceptable content of ashes from wooden pellets is 0.5%
  • the one from dry cortex, rice husks and depuration sludges is respectively equal to 5%, 20% and 35% of the inorganic content.
  • Methods are known which are based on the removal of ash-rich biomass, before starting a process for pre-treating the biomass.
  • Patent application US20120009660A1 however has the following limitations:
  • the maximum process temperature is 90°C;
  • a distilling apparatus which lacks an auxiliary thrust ;
  • object of the present invention is solving the above prior art problems, by providing a process for removing ashes from biomasses and a related system to allow separating and removing ashes from biomasses.
  • a further object is providing a process for converting ash-rich solid biomasses into a liquid or solid fuel, which is without ash, and into an inorganic solid residue, which is rich of ash.
  • FIG. 1 shows the diagram of a system and of an embodiment of the process for removing ashes from biomasses according to the present invention.
  • a process for removing ashes from biomasses is implemented through a system 1 comprising mixing means 10 and 20, filtering means 30 and distilling means 40, and at least one storage system 50 to allow separating and removing ashes from biomasses.
  • the process for removing ashes from biomasses comprises the following steps:
  • the step of depolymerizing the organic material present in the biomass occurs at a reaction temperature included between 150 °C and 250°C, by melting in at least one solvent, of the methanol, ethanol, isopropyl alcohol, diethylene glycole, ethylene glycole, glycerol and water type, in combination with a homogeneous catalyst to allow accelerating the melting of the organic material.
  • the step of filtering the organic material, depolymerized and dissolved in the solvent occurs downstream of an environment with high autogenous pressure to be able to increase the filtering efficiency induced by autogenous pressure.
  • the step of distilling and regenerating the solvent occurs through vaporizing the solvent in an overheated environment.
  • Such process is adapted to be performed through a system 1 for removing ashes from biomasses, wherein the mixing means 10 comprise at least one continuous reactor with stirred tank suitable to allow controlling the melting degree in a solvent of the organic material present in the biomass, in order to generate an autogenous pressure which is enough to allow keeping at liquid state the majority of the volatile solvent.
  • the mixing means 10 comprise at least one continuous reactor with stirred tank suitable to allow controlling the melting degree in a solvent of the organic material present in the biomass, in order to generate an autogenous pressure which is enough to allow keeping at liquid state the majority of the volatile solvent.
  • the mixing means 20 comprise at least one continuous reactor with stirred tank adapted to contain the biomass without ashes.
  • the mixing means 10 and 20 are connected by the filtering means 30, through an inlet valve 31 and an outlet valve 32.
  • the filtering means 30 comprise porous means 33 suitable to keep big-sized particles of ashes due to the passage of organic material present in the biomass and of solvent pushed by the autogenous pressure of the continuous reactor with stirred tank of the mixing means 10.
  • the porous means 33 allow removing the ashes for following processing and disposing actions.
  • the continuous reactor with stirred tank of the mixing means 20 contains the solvent without ashes, hot filtered, at high pressure.
  • Such reactor comprises at least one heat exchanger 21 to integrate the necessary heat to allow the differential distillation of the solvent through the distilling means 40 by reducing the pressure through a valve 22.
  • the distilling means 40 comprise at least one condenser 41, water cooled at ambient pressure, and collecting means 42 for re-using the solvent.
  • the process and the related system for removing ashes from biomasses according to the present invention allow reaching the stated obj ects .
  • a third step of the process of the invention provides for the regeneration of solvent from hot and pressurized filtered material without ashes for differential distillation, in such second continuous reactor with stirred tank.
  • Heat of the liquid reaction mixture, at high pressure, at a temperature much greater than the boiling point at ambient pressure, is exploited for vaporizing the solvent, reducing the pressure by opening a valve. Possible further heat necessary for recovering the solvent is provided by the heat exchanger 21.
  • the solvent vapors condense in a water-cooled condenser at ambient pressure and are collected to re-use them.
  • the depolymerized biomass without ashes is a product of the process and remains in the second continuous reactor with stirred tank to be collected from its bottom.
  • Such process product can be solid, pasty or liquid according to the nature of the biomass and to the content of possibly unrecovered solvent.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

L'invention concerne un procédé permettant d'éliminer des cendres de biomasses, par l'intermédiaire d'un système (1) comprenant des moyens de mélange (10) et (20), des moyens de filtration (30) et des moyens de distillation (40) et au moins un système de stockage (50) pour permettre la séparation et l'élimination de cendres de biomasses, comprenant les étapes suivantes : la dépolymérisation d'une matière organique présente dans la biomasse et la séparation de la matière organique, dépolymérisée et dissoute dans le solvant, relative à un résidu riche en cendres solides ; le filtrage de la matière organique, dépolymérisée et dissoute dans le solvant ; la distillation et la régénération du solvant présent dans un environnement à haute température ; et l'extraction et le stockage de la biomasse exempte de cendres. L'invention concerne également un système (1) destiné à éliminer les cendres des biomasses.
PCT/IT2016/000140 2016-05-30 2016-05-30 Procédé et système associé pour éliminer des cendres de biomasses Ceased WO2017208268A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PCT/IT2016/000140 WO2017208268A1 (fr) 2016-05-30 2016-05-30 Procédé et système associé pour éliminer des cendres de biomasses
EP16747850.2A EP3464514A1 (fr) 2016-05-30 2016-05-30 Procédé et système associé pour éliminer des cendres de biomasses

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/IT2016/000140 WO2017208268A1 (fr) 2016-05-30 2016-05-30 Procédé et système associé pour éliminer des cendres de biomasses

Publications (1)

Publication Number Publication Date
WO2017208268A1 true WO2017208268A1 (fr) 2017-12-07

Family

ID=56571347

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IT2016/000140 Ceased WO2017208268A1 (fr) 2016-05-30 2016-05-30 Procédé et système associé pour éliminer des cendres de biomasses

Country Status (2)

Country Link
EP (1) EP3464514A1 (fr)
WO (1) WO2017208268A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021025226A1 (fr) * 2019-08-08 2021-02-11 한국에너지기술연구원 Appareil et procédé mécano-catalytiques qui peuvent être appliqués chacun à température ambiante et qui éliminent des ingrédients produisant des cendres dans une biomasse

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20090016392A (ko) * 2007-08-10 2009-02-13 가부시키가이샤 미죠타 유용 물질의 추출 방법과 그 장치
US20120009660A1 (en) 2010-06-09 2012-01-12 Pa, Llc Method of ash removal from a biomass
EP2891748A1 (fr) * 2014-01-07 2015-07-08 Studiengesellschaft Kohle mbH Procédé de production de bio-huile à partir de matières ligno-cellulosiques non-pyrolytiques
WO2016058031A1 (fr) * 2014-10-15 2016-04-21 Licella Pty Ltd Lessives de réduction en pâte et utilisations de ceux-ci
WO2016150965A1 (fr) * 2015-03-24 2016-09-29 Studiengesellschaft Kohle Mbh Procédé de préparation de produit à base d'huile à partir de tourbe, de fibre de coco ou de substances de type tourbe

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20090016392A (ko) * 2007-08-10 2009-02-13 가부시키가이샤 미죠타 유용 물질의 추출 방법과 그 장치
US20120009660A1 (en) 2010-06-09 2012-01-12 Pa, Llc Method of ash removal from a biomass
EP2891748A1 (fr) * 2014-01-07 2015-07-08 Studiengesellschaft Kohle mbH Procédé de production de bio-huile à partir de matières ligno-cellulosiques non-pyrolytiques
WO2016058031A1 (fr) * 2014-10-15 2016-04-21 Licella Pty Ltd Lessives de réduction en pâte et utilisations de ceux-ci
WO2016150965A1 (fr) * 2015-03-24 2016-09-29 Studiengesellschaft Kohle Mbh Procédé de préparation de produit à base d'huile à partir de tourbe, de fibre de coco ou de substances de type tourbe

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021025226A1 (fr) * 2019-08-08 2021-02-11 한국에너지기술연구원 Appareil et procédé mécano-catalytiques qui peuvent être appliqués chacun à température ambiante et qui éliminent des ingrédients produisant des cendres dans une biomasse

Also Published As

Publication number Publication date
EP3464514A1 (fr) 2019-04-10

Similar Documents

Publication Publication Date Title
CA2647093C (fr) Carburants diesel multicomposants miscibles et procedes de transformation d'huile bio
EP2074192B1 (fr) Procede de pyrolyse de biomasse
JP3954544B2 (ja) 植物由来バイオマスの乾燥方法およびバイオマス燃料の製造方法
TW200916568A (en) Conversion of lignocellulosic biomass to chemicals and fuels
CN108291150A (zh) 由塑料生产碳氢燃料
CN102399565B (zh) 从煤直接液化残渣中萃取重质液化油的方法及提取的重质液化油及其应用
US9518226B2 (en) Solids removal from bio-oil using biomass filter aid
CN101988026A (zh) 由生质废材萃取精油所述的方法及装置
US10005962B2 (en) Method for preparing shut down of process and equipment for producing liquid hydrocarbons
CA2816195C (fr) Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel
CN102165049A (zh) 无灰炭的制造方法
WO2022002091A1 (fr) Procédé et système pour le traitement de déchets de matière plastique
CN103059896B (zh) 一种快速热解制备低含水率及低酸性生物油的方法及其装置
CN108559543A (zh) 超临界水热处理废塑料和秸秆混合物生产烃油的工艺
JP5255303B2 (ja) 無灰炭の製造方法
WO2017208268A1 (fr) Procédé et système associé pour éliminer des cendres de biomasses
CN107109240A (zh) 加工纤维素生物质的方法和系统
CN213172211U (zh) 费托渣蜡的处理系统
JP3508812B2 (ja) 超臨界水を用いた石炭の連続転換装置
CN106221851A (zh) 一种超声辅助褐煤热溶物的分级制备方法
CN116355643B (zh) 水热处理聚烯烃塑料的方法
CN107109241A (zh) 加工纤维素生物质的方法和系统
CN110387279B (zh) 用于脱除煤中硫分的亲水型离子液体的回收方法
CN116023962B (zh) 一种废塑料管式炉热解的方法和系统
EP3858950A1 (fr) Système de pyrolyse, procédé de production de gaz de pyrolyse purifié et de liquides de pyrolyse et utilisation d'un système de pyrolyse

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16747850

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2016747850

Country of ref document: EP

Effective date: 20190102