Tar removal from biomass derived fuel gas by pulsed corona discharges: chemical kinetic study II

S.A. Nair; K. Yan; A.J.M. Pemen; E.J.M. Heesch, van; K.J. Ptasinski; A.A.H. Drinkenburg

doi:10.1021/ie049292t

Tar removal from biomass derived fuel gas by pulsed corona discharges: chemical kinetic study II

S.A. Nair, K. Yan, A.J.M. Pemen, E.J.M. Heesch, van, K.J. Ptasinski, A.A.H. Drinkenburg

Onderzoeksoutput: Bijdrage aan tijdschrift › Tijdschriftartikel › Academic › peer review

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Tar (heavy hydrocarbon or poly aromatic hydrocarbon (PAH)) removal from biomass derived fuel gas is one of the biggest obstacles in its utilization for power generation. We have investigated pulsed corona as a method for tar removal. Our previous experimental results indicate the energy consumption of 400 J/L for naphthalene removal (model tar compound) from synthetic fuel gas (CO, CO2, H2, CH4, N2) at a temperature of 200 °C. The present study extends our work on experimental and kinetic calculations for temperatures up to 500 °C. Radical yields are evaluated at various temperatures. According to the kinetic model and experimental results we concluded that the optimum temperature for tar removal is around 400 °C. The energy consumption for tar removal at 400 °C is about 200-250 J/L, whereas at 200 °C, this is about 400-600 J/L.

Originele taal-2	Engels
Pagina's (van-tot)	1734-1741
Aantal pagina's	8
Tijdschrift	Industrial and Engineering Chemistry Research
Volume	44
Nummer van het tijdschrift	6
DOI's	https://doi.org/10.1021/ie049292t
Status	Gepubliceerd - 2005

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title = "Tar removal from biomass derived fuel gas by pulsed corona discharges: chemical kinetic study II",

abstract = "Tar (heavy hydrocarbon or poly aromatic hydrocarbon (PAH)) removal from biomass derived fuel gas is one of the biggest obstacles in its utilization for power generation. We have investigated pulsed corona as a method for tar removal. Our previous experimental results indicate the energy consumption of 400 J/L for naphthalene removal (model tar compound) from synthetic fuel gas (CO, CO2, H2, CH4, N2) at a temperature of 200 °C. The present study extends our work on experimental and kinetic calculations for temperatures up to 500 °C. Radical yields are evaluated at various temperatures. According to the kinetic model and experimental results we concluded that the optimum temperature for tar removal is around 400 °C. The energy consumption for tar removal at 400 °C is about 200-250 J/L, whereas at 200 °C, this is about 400-600 J/L.",

author = "S.A. Nair and K. Yan and A.J.M. Pemen and {Heesch, van}, E.J.M. and K.J. Ptasinski and A.A.H. Drinkenburg",

year = "2005",

doi = "10.1021/ie049292t",

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T1 - Tar removal from biomass derived fuel gas by pulsed corona discharges: chemical kinetic study II

AU - Nair, S.A.

AU - Yan, K.

AU - Pemen, A.J.M.

AU - Heesch, van, E.J.M.

AU - Ptasinski, K.J.

AU - Drinkenburg, A.A.H.

PY - 2005

Y1 - 2005

N2 - Tar (heavy hydrocarbon or poly aromatic hydrocarbon (PAH)) removal from biomass derived fuel gas is one of the biggest obstacles in its utilization for power generation. We have investigated pulsed corona as a method for tar removal. Our previous experimental results indicate the energy consumption of 400 J/L for naphthalene removal (model tar compound) from synthetic fuel gas (CO, CO2, H2, CH4, N2) at a temperature of 200 °C. The present study extends our work on experimental and kinetic calculations for temperatures up to 500 °C. Radical yields are evaluated at various temperatures. According to the kinetic model and experimental results we concluded that the optimum temperature for tar removal is around 400 °C. The energy consumption for tar removal at 400 °C is about 200-250 J/L, whereas at 200 °C, this is about 400-600 J/L.

AB - Tar (heavy hydrocarbon or poly aromatic hydrocarbon (PAH)) removal from biomass derived fuel gas is one of the biggest obstacles in its utilization for power generation. We have investigated pulsed corona as a method for tar removal. Our previous experimental results indicate the energy consumption of 400 J/L for naphthalene removal (model tar compound) from synthetic fuel gas (CO, CO2, H2, CH4, N2) at a temperature of 200 °C. The present study extends our work on experimental and kinetic calculations for temperatures up to 500 °C. Radical yields are evaluated at various temperatures. According to the kinetic model and experimental results we concluded that the optimum temperature for tar removal is around 400 °C. The energy consumption for tar removal at 400 °C is about 200-250 J/L, whereas at 200 °C, this is about 400-600 J/L.

U2 - 10.1021/ie049292t

DO - 10.1021/ie049292t

M3 - Article

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VL - 44

SP - 1734

EP - 1741

JO - Industrial and Engineering Chemistry Research

JF - Industrial and Engineering Chemistry Research

IS - 6

ER -

Tar removal from biomass derived fuel gas by pulsed corona discharges: chemical kinetic study II

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