CA2816195C - Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel - Google Patents

Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel Download PDF

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Publication number
CA2816195C
CA2816195C CA2816195A CA2816195A CA2816195C CA 2816195 C CA2816195 C CA 2816195C CA 2816195 A CA2816195 A CA 2816195A CA 2816195 A CA2816195 A CA 2816195A CA 2816195 C CA2816195 C CA 2816195C
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CA
Canada
Prior art keywords
char
organic matter
reactor
slurry
solid
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Active
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CA2816195A
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English (en)
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CA2816195A1 (fr
Inventor
Paolo De Filippis
Marco Scarsella
Sergio Carnevale
Christina Garritano
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BFCC TECH Ltd
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BFCC TECH Ltd
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.)
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Publication date
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Priority to CA2816195A priority Critical patent/CA2816195C/fr
Priority to PCT/EP2014/060562 priority patent/WO2014187910A2/fr
Priority to CN201480013553.9A priority patent/CN105121604B/zh
Publication of CA2816195A1 publication Critical patent/CA2816195A1/fr
Application granted granted Critical
Publication of CA2816195C publication Critical patent/CA2816195C/fr
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Classifications

    • 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
    • C10G1/083—Production 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
    • 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
    • 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
    • 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

Landscapes

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

Abstract

La conversion de matière organique en produits dhydrocarbures valorisés comprend létape de décomposition de la matière organique en du liquide, du produit de carbonisation et du gaz à laide dune méthode hydrothermique catalytique rapide ayant une efficacité améliorée grâce à un transfert élevé dénergie locale par un effet de cavitation. La matière organique et des catalyseurs sont alimentés dans un réacteur de décomposition hydrothermique pour décomposer la matière organique en gaz, en vapeurs et en produit de carbonisation, le réacteur utilisant le transfert élevé dénergie locale par effet de cavitation. Le réacteur fonctionne à des températures denviron 200 °C à 380 °C et présente un temps de séjour denviron 1 à 60 minutes. Le produit est séparé en une boue lourde de produit de carbonisation et dhuile, en vapeurs et en gaz, les vapeurs étant ensuite condensées et séparées en partie aqueuse et une partie dhydrocarbures. Une partie de la boue de produit de carbonisation est recyclée en chambre de cavitation et le produit de carbonisation excédentaire est sorti de la chambre de décomposition.
CA2816195A 2013-05-22 2013-05-22 Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel Active CA2816195C (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CA2816195A CA2816195C (fr) 2013-05-22 2013-05-22 Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel
PCT/EP2014/060562 WO2014187910A2 (fr) 2013-05-22 2014-05-22 Procédé et appareil de décomposition hydrothermique permettant de fabriquer un liquide de pyrolyse de type carburant diesel
CN201480013553.9A CN105121604B (zh) 2013-05-22 2014-05-22 用于制造柴油燃料范围内的热解液体的水热分解方法和设备

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA2816195A CA2816195C (fr) 2013-05-22 2013-05-22 Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel

Publications (2)

Publication Number Publication Date
CA2816195A1 CA2816195A1 (fr) 2014-11-22
CA2816195C true CA2816195C (fr) 2021-11-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CA2816195A Active CA2816195C (fr) 2013-05-22 2013-05-22 Procede de pyrolyse aqueuse et appareil permettant d'obtenir un liquide de pyrolyse dans la plage du carburant diesel

Country Status (3)

Country Link
CN (1) CN105121604B (fr)
CA (1) CA2816195C (fr)
WO (1) WO2014187910A2 (fr)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106315578B (zh) * 2016-08-19 2018-08-03 华中科技大学 一种联产超级活性炭和液体产品的系统及方法
CN108218160A (zh) * 2018-02-02 2018-06-29 中国科学院生态环境研究中心 一种高压水热及循环流化床热解辅助的污泥快速无害化处理工艺
CN109569476B (zh) * 2018-10-24 2023-07-04 浙江海洋大学 淡水鱼废弃物制备生物质油的方法
EE05860B1 (et) * 2021-01-17 2023-11-15 Jüri LIIV Biomassi hüdrotermilise veeldamise ja gaasistamise meetod ning süsteem
NL2027380B1 (nl) 2021-01-25 2022-08-12 Bintell B V Werkwijze voor het onder hoge druk en temperatuur in een waterige omgeving behandelen van een organisch uitgangsmateriaal.
CN114149167B (zh) * 2021-12-20 2024-02-06 黑龙江省科学院高技术研究院 一种空化技术处理剩余污泥释放内碳源处理装置及方法
WO2023181038A1 (fr) * 2022-03-22 2023-09-28 Latent Energy Ltd. Procédé intégré de conversion de déchets plastiques

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5914027A (en) * 1994-09-12 1999-06-22 Thermtech A/S Thermo-mechanical cracking and hydrogenation
DE102006052995B4 (de) * 2006-11-10 2008-12-18 Tschirner, Erhard, Dr. Verfahren zur Herstellung von Gasöl aus kohlenwasserstoffhaltigen organischen Reststoffen und nachwachsenden Rohstoffen durch Reaktionsführung und Energieeintrag mittels prozeßintegrierter Kavitation/Friktion
FR2929287A1 (fr) * 2008-03-28 2009-10-02 Europ Ltd Procede d'obtention d'hydrocarbures liquides.
RU2011119612A (ru) * 2008-10-14 2012-11-27 Каи Байоэнерджи Корпорэйшн Гидродинамическое извлечение масел из фотосинтезирующих культур
CN102459520B (zh) * 2009-05-15 2014-09-17 澳斯生物柴油控股有限公司 制备燃料的方法和装置
JP2013535539A (ja) * 2010-07-26 2013-09-12 アー．ヨット． ヴィーザー−リンハート エミール バイオマス／プラスチック混合物から燃料を作成するためのプラント及び方法

Also Published As

Publication number Publication date
CN105121604B (zh) 2018-05-18
CA2816195A1 (fr) 2014-11-22
CN105121604A (zh) 2015-12-02
WO2014187910A2 (fr) 2014-11-27
WO2014187910A3 (fr) 2015-07-23

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