Method for performing pyrolysis and a pyrolysis apparatus

US10023803B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10023803-B2
Application numberUS-201314441812-A
CountryUS
Kind codeB2
Filing dateNov 7, 2013
Priority dateNov 9, 2012
Publication dateJul 17, 2018
Grant dateJul 17, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Solid fuel in the form of particles is supplied to a pyrolyzer, and pyrolysis conditions are maintained in the pyrolyzer for separating condensable gaseous substances from the fuel. Heat required by the pyrolysis conditions is supplied at least partly with solid fluidized bed material which passes through the pyrolyzer simultaneously as it is fluidized by fluidizing gas in the pyrolyzer. Condensable gaseous substances separated from the fuel are conveyed from the pyrolyzer to a condenser, in which they are separated as so-called pyrolysis oil in liquid form, and solid fluidized bed material taken from the pyrolyzer and containing combustible pyrolysis residue originating from the fuel is circulated through a gasifier, in which product gas, which is burnt in a boiler or a kiln, is formed from the pyrolysis residue.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for performing pyrolysis, comprising: supplying solid fuel in the form of particles to a pyrolyzer; maintaining pyrolysis conditions in the pyrolyzer in order to separate condensable gaseous substances from the solid fuel; supplying heat required by the pyrolysis conditions at least partly with solid fluidized bed material which passes through the pyrolyzer simultaneously as the solid fluidized bed material is fluidized in the pyrolyzer by fluidizing gas; under said pyrolysis conditions, separating condensable gaseous substances from the solid fuel; conveying said condensable gaseous substances from the pyrolyzer to a condenser; in the condenser, separating said condensable gaseous substances as pyrolysis oil in liquid state; taking the solid fluidized bed material containing combustible pyrolysis residue from the solid fuel from the pyrolyzer; circulating said solid fluidized bed material containing the combustible pyrolysis residue from the solid fuel through a gasifier gasification process; in the gasifier gasification process, performing a gasification process by introducing oxygen-containing gas to cause partial combustion of the combustible pyrolysis residue thereby forming product gas from the combustible pyrolysis residue and utilizing the energy content of the combustible pyrolysis residue in heating of the fluidized bed material by transferring heat produced by the gasification process to the fluidized bed material to form heated fluidized bed material, returning the heated fluidized bed material from the gasifier gasification process to the pyrolyzer; burning the product gas formed from the combustible pyrolysis residue in a kiln in which thermal energy from combustion is utilized for the processing of materials; and adjusting a pyrolysis temperature in the pyrolyzer by adjusting a temperature of the solid fluidized bed material by a heat exchanger, wherein the solid fluidized bed material is sand. 2. The method according to claim 1 , wherein condensable gaseous substances and non-condensable combustible gases are separated from the solid fuel and the condensable gaseous substances produced in the pyrolyzer are separated from the non-condensable combustible gases; the method and further comprising: burning at least part of the non-condensable combustible gases produced in the pyrolyzer with the product gas. 3. The method according to claim 1 , wherein the solid fuel is solid bio-based or semi-bio-based fuel. 4. The method according to claim 1 , wherein the pyrolysis conditions comprise a temperature of 400 to 800° C., and the gasification process comprises a temperature of 600 to 1200° C., the temperature of the gasification process being higher than the temperature of the pyrolysis conditions.

Assignees

Inventors

Classifications

  • Recycle loops, e.g. gas, solids, heating medium, water · CPC title

  • Inert particles, e.g. as heat exchange medium in a fluidized or moving bed, heat carriers, sand · CPC title

  • Combustion processes · CPC title

  • with separate withdrawal of the distillation products · CPC title

  • Gasification of granular or pulverulent flues in suspension · CPC title

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What does patent US10023803B2 cover?
Solid fuel in the form of particles is supplied to a pyrolyzer, and pyrolysis conditions are maintained in the pyrolyzer for separating condensable gaseous substances from the fuel. Heat required by the pyrolysis conditions is supplied at least partly with solid fluidized bed material which passes through the pyrolyzer simultaneously as it is fluidized by fluidizing gas in the pyrolyzer. Conden…
Who is the assignee on this patent?
Valmet Technologies Oy, Valmet Technologies Inc
What technology area does this patent fall under?
Primary CPC classification C10B49/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jul 17 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).