Gasification gas cleaning with nickel monolith catalyst

Pekka Simell; Pekka Ståhlberg; Yrjö Solantausta; Jouko Hepola; Esa Kurkela

doi:10.1007/978-94-009-1559-6_89

Gasification gas cleaning with nickel monolith catalyst

Pekka Simell, Pekka Ståhlberg, Yrjö Solantausta, Jouko Hepola, Esa Kurkela

VTT (former employee or external)

Research output: Chapter in Book/Report/Conference proceeding › Conference article in proceedings › Scientific › peer-review

Abstract

Particulate-containing gas derived from fluidized-bed biomass gasification can be efficiently purified from tars and ammonia by using a nickel monolith catalyst. Catalyst deactivation by H₂S and carbon deposition can be avoided at 20 bar pressure by using temperatures over 900°C. Catalyst deactivation was not observed in a long-term test that lasted 500 h. According to a techno-economical evaluation catalytic hot gas cleaning is economically equal to ammonia removal by SCR in an 60 MWe IGCC plant.

Original language	English
Title of host publication	Developments in Thermochemical Biomass Conversion
Editors	A.V. Bridgewater, D.G.B. Boocock
Place of Publication	London
Pages	1103-1116
Volume	2
ISBN (Electronic)	978-94-009-1559-6
DOIs	https://doi.org/10.1007/978-94-009-1559-6_89
Publication status	Published - 1997
MoE publication type	A4 Article in a conference publication
Event	Developments in Thermochemical Biomass Conversion Conference - Banff, Canada Duration: 20 May 1996 → 24 May 1996

Conference

Conference	Developments in Thermochemical Biomass Conversion Conference
Country/Territory	Canada
City	Banff
Period	20/05/96 → 24/05/96

Keywords

gasification

Access to Document

10.1007/978-94-009-1559-6_89

Cite this

@inproceedings{75205ebf46df4992ac54a07684659737,

title = "Gasification gas cleaning with nickel monolith catalyst",

abstract = "Particulate-containing gas derived from fluidized-bed biomass gasification can be efficiently purified from tars and ammonia by using a nickel monolith catalyst. Catalyst deactivation by H2S and carbon deposition can be avoided at 20 bar pressure by using temperatures over 900°C. Catalyst deactivation was not observed in a long-term test that lasted 500 h. According to a techno-economical evaluation catalytic hot gas cleaning is economically equal to ammonia removal by SCR in an 60 MWe IGCC plant.",

keywords = "gasification",

author = "Pekka Simell and Pekka St{\aa}hlberg and Yrj{\"o} Solantausta and Jouko Hepola and Esa Kurkela",

year = "1997",

doi = "10.1007/978-94-009-1559-6\_89",

language = "English",

isbn = "978-0-7514-0350-3",

volume = "2",

pages = "1103--1116",

editor = "A.V. Bridgewater and D.G.B. Boocock",

booktitle = "Developments in Thermochemical Biomass Conversion",

note = "Developments in Thermochemical Biomass Conversion Conference ; Conference date: 20-05-1996 Through 24-05-1996",

}

Simell, P, Ståhlberg, P, Solantausta, Y, Hepola, J & Kurkela, E 1997, Gasification gas cleaning with nickel monolith catalyst. in AV Bridgewater & DGB Boocock (eds), Developments in Thermochemical Biomass Conversion. vol. 2, London, pp. 1103-1116, Developments in Thermochemical Biomass Conversion Conference, Banff, Alberta, Canada, 20/05/96. https://doi.org/10.1007/978-94-009-1559-6_89

Gasification gas cleaning with nickel monolith catalyst. / Simell, Pekka; Ståhlberg, Pekka; Solantausta, Yrjö et al.
Developments in Thermochemical Biomass Conversion. ed. / A.V. Bridgewater; D.G.B. Boocock. Vol. 2 London, 1997. p. 1103-1116.

Research output: Chapter in Book/Report/Conference proceeding › Conference article in proceedings › Scientific › peer-review

TY - GEN

T1 - Gasification gas cleaning with nickel monolith catalyst

AU - Simell, Pekka

AU - Ståhlberg, Pekka

AU - Solantausta, Yrjö

AU - Hepola, Jouko

AU - Kurkela, Esa

PY - 1997

Y1 - 1997

N2 - Particulate-containing gas derived from fluidized-bed biomass gasification can be efficiently purified from tars and ammonia by using a nickel monolith catalyst. Catalyst deactivation by H2S and carbon deposition can be avoided at 20 bar pressure by using temperatures over 900°C. Catalyst deactivation was not observed in a long-term test that lasted 500 h. According to a techno-economical evaluation catalytic hot gas cleaning is economically equal to ammonia removal by SCR in an 60 MWe IGCC plant.

AB - Particulate-containing gas derived from fluidized-bed biomass gasification can be efficiently purified from tars and ammonia by using a nickel monolith catalyst. Catalyst deactivation by H2S and carbon deposition can be avoided at 20 bar pressure by using temperatures over 900°C. Catalyst deactivation was not observed in a long-term test that lasted 500 h. According to a techno-economical evaluation catalytic hot gas cleaning is economically equal to ammonia removal by SCR in an 60 MWe IGCC plant.

KW - gasification

U2 - 10.1007/978-94-009-1559-6_89

DO - 10.1007/978-94-009-1559-6_89

M3 - Conference article in proceedings

SN - 978-0-7514-0350-3

SN - 978-94-010-7196-3

VL - 2

SP - 1103

EP - 1116

BT - Developments in Thermochemical Biomass Conversion

A2 - Bridgewater, A.V.

A2 - Boocock, D.G.B.

CY - London

T2 - Developments in Thermochemical Biomass Conversion Conference

Y2 - 20 May 1996 through 24 May 1996

ER -

Gasification gas cleaning with nickel monolith catalyst

Abstract

Conference

Keywords

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