ES2165192T3 - Procedimiento para el tratamiento termico de material que contiene componentes combustibles volatiles. - Google Patents

Procedimiento para el tratamiento termico de material que contiene componentes combustibles volatiles.

Info

Publication number
ES2165192T3
ES2165192T3 ES98945153T ES98945153T ES2165192T3 ES 2165192 T3 ES2165192 T3 ES 2165192T3 ES 98945153 T ES98945153 T ES 98945153T ES 98945153 T ES98945153 T ES 98945153T ES 2165192 T3 ES2165192 T3 ES 2165192T3
Authority
ES
Spain
Prior art keywords
reactor
zone
sliding
solid materials
bed
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.)
Expired - Lifetime
Application number
ES98945153T
Other languages
English (en)
Inventor
Hans-Jurgen Weiss
Udo Zentner
Jorg Schmalfeld
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.)
MG Technologies AG
Original Assignee
MG Technologies 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 MG Technologies AG filed Critical MG Technologies AG
Application granted granted Critical
Publication of ES2165192T3 publication Critical patent/ES2165192T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/16—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form
    • C10B49/20—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form
    • C10B49/22—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form according to the "fluidised bed" technique
    • 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
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/16—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided 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
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Dispersion Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

Procedimiento para el tratamiento térmico de material de carga de partida que contiene componentes combustibles volátiles, con un contenido de agua de hasta el 20 % en peso, en el que se mezcla el material de carga de partida en un reactor de pirólisis (1) con materiales sólidos en grano a alta temperatura, que llegan desde un silo colector (22) a temperaturas de entre 700 y 1.100 C, se extraen (9) desde la parte superior del reactor gases y vapores y se realiza en el reactor una mezcla de los materiales sólidos, que es evacuada (6) desde el reactor, calentándose por lo menos una parte de ellos (20, 21) fuera del reactor y reconduciéndolos otra vez (3) a través del silo colector hasta el reactor de pirólisis, teniendo el reactor en la parte superior una zona de corrimiento (1a) del material y un lecho deslizante o lecho fluidizado (4)debajo dela zona de corrimiento del material con temperaturas de entre 650 y 1.000 C, conduciéndose luego los materiales sólidos en grano a alta temperatura yel material de carga de partida, por lo menos en parte, conjuntamente hacia abajo a través de la zona de corrimiento del material hasta el lecho deslizante o lecho fluidizado e introduciendo los materiales sólidos en grano a alta temperatura en la parte superior de la zona de corrimiento del material, caracterizado porque el material de carga de partida se introduce (2a, 1b) en la parte central o en la parte inferior de la zona de corrimiento del material y porque los gases y vapores procedentes del lecho deslizante o lecho fluidizado son conducidos hacia arriba a contracorriente respecto a los materiales sólidos a alta temperatura a través de la zona de corrimiento del material, hasta llegar a la parte superior de la zona de corrimiento del material, antes de ser extraídos (9) del reactor.
ES98945153T 1997-09-01 1998-08-06 Procedimiento para el tratamiento termico de material que contiene componentes combustibles volatiles. Expired - Lifetime ES2165192T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19738106A DE19738106C2 (de) 1997-09-01 1997-09-01 Verfahren zum thermischen Behandeln von flüchtige, brennbare Bestandteile enthaltendem Material

Publications (1)

Publication Number Publication Date
ES2165192T3 true ES2165192T3 (es) 2002-03-01

Family

ID=7840821

Family Applications (1)

Application Number Title Priority Date Filing Date
ES98945153T Expired - Lifetime ES2165192T3 (es) 1997-09-01 1998-08-06 Procedimiento para el tratamiento termico de material que contiene componentes combustibles volatiles.

Country Status (5)

Country Link
EP (1) EP1015527B1 (es)
AU (1) AU9257398A (es)
DE (2) DE19738106C2 (es)
ES (1) ES2165192T3 (es)
WO (1) WO1999011736A1 (es)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19961437C2 (de) * 1999-12-20 2002-04-18 Kopf Ag Verfahren und Anlage zur Gewinnung von brennbarem Gas aus Klärschlamm
DE10157163A1 (de) * 2001-11-22 2003-06-18 Gfe Gmbh & Co Kg Ges Fuer Ents Verfahren und Vorrichtung zur Entsorgung von hochenergetische Stoffe enthaltenden Materialien, insbesondere von Granaten
DE10204815B4 (de) * 2002-02-06 2005-09-15 Eisenmann Maschinenbau Gmbh & Co. Kg Vorrichtung zur Entsorgung gefährlicher oder hochenergetischer Materialien
DE10253678A1 (de) * 2002-11-18 2004-05-27 Otto Dipl.-Ing. Heinemann Verfahren und Vorrichtung zur Gewinnung von Kohlenwasserstoffen
DE102007032683B4 (de) 2007-07-13 2014-09-11 Outotec Oyj Verfahren und Anlage zur Raffination ölhaltiger Feststoffe
NL2000772C2 (nl) * 2007-07-22 2009-01-23 Btg Bioliquids B V Pyrolyse-reactor.
DE102008008943B4 (de) 2008-02-13 2016-10-27 Outotec Oyj Verfahren und Anlage zur Raffination organische Anteile enthaltender Rohstoffe
DE102008008942B4 (de) 2008-02-13 2015-02-12 Outotec Oyj Verfahren und Anlage zur Raffination organische Anteile enthaltender Rohstoffe
WO2012004709A1 (en) 2010-07-06 2012-01-12 Koninklijke Philips Electronics N.V. Generation of high dynamic range images from low dynamic range images
CN104230135B (zh) * 2014-09-26 2016-11-16 中国石油天然气股份有限公司 含油污泥热解装置
CN108619890B (zh) * 2018-04-24 2019-03-08 东莞市泰昌纸业有限公司 废纸造纸废气的处理方法
CN112899000B (zh) * 2019-11-19 2022-06-03 上海工程技术大学 一种生物质废弃物挥发分催化油页岩干馏耦合系统及方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1909263C3 (de) * 1969-02-25 1974-04-25 Metallgesellschaft Ag, 6000 Frankfurt Verfahren und Vorrichtung zum Schwelen von feinkörnigen bituminösen Stoffen, die einen staubförmigen Schwelrückstand bilden
DE2537732C3 (de) * 1975-08-25 1981-12-10 Gosudarstvennyj naučno-issledovatel'skij energetičeskij institut imeni G.M. Kržižanovskogo, Moskva Verfahren zur thermischen Verarbeitung von festen bituminösen Stoffen
US4199432A (en) * 1978-03-22 1980-04-22 Chevron Research Company Staged turbulent bed retorting process
DE2946102A1 (de) * 1979-11-15 1981-05-27 Metallgesellschaft Ag, 6000 Frankfurt Verfahren und vorrichtung zum schwelen von feinkoernigem schwelgut mit heissem, feinkoernigem waermetraegermaterial
DE3835941A1 (de) * 1988-06-09 1990-04-26 Artur Richard Greul Verfahren der kunststoffpyrolyse im sandkoker

Also Published As

Publication number Publication date
WO1999011736A1 (de) 1999-03-11
EP1015527B1 (de) 2001-10-24
EP1015527A1 (de) 2000-07-05
DE19738106A1 (de) 1999-03-04
AU9257398A (en) 1999-03-22
DE59801891D1 (de) 2001-11-29
DE19738106C2 (de) 2001-01-04

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