Simulation of a pilot‐scale dual‐fluidized‐bed gasifier for biomass. Issue 3 (3rd February 2014)
- Record Type:
- Journal Article
- Title:
- Simulation of a pilot‐scale dual‐fluidized‐bed gasifier for biomass. Issue 3 (3rd February 2014)
- Main Title:
- Simulation of a pilot‐scale dual‐fluidized‐bed gasifier for biomass
- Authors:
- Liao, Chang‐hsien
Summers, Matthew
Seiser, Reinhard
Cattolica, Robert
Herz, Richard - Abstract:
- <abstract abstract-type="main"> <title> <x xml:space="preserve">Abstract</x> </title> <p>A dual‐fluidized‐bed gasifier was constructed and operated at the Woodland Biomass Research Center in Woodland, CA. The pilot‐scale gasifier had a capacity of 5 tons/day of feedstock and was based on the Pyrox process developed by Kunii et al. In this system, the fluidized‐bed combustion process with air is separated from the biomass gasification process with steam and recycle gas. This decreases the nitrogen content in the producer gas. The heat released in the combustion of the char is transported by a ceramic bed material circulating between the combustor and gasifier. Commercial wood pellets were used as feedstock for the present study. Gas composition, temperatures, and pressures were measured to characterize the operation of the gasifier. A positive feature of the system was the high circulation rate and efficient energy transfer between the combustor and gasifier. Analysis of the system was performed using Aspen Plus™ software to calculate mass and energy‐balances. A restricted equilibrium model for the producer‐gas composition agreed reasonably well with the measured non‐equilibrium gas composition for most gases. The restricted equilibrium model over‐predicted the H<sub>2</sub> concentrations. A more complex rate‐based kinetic model would be necessary to fully capture the details of the non‐equilibrium gas composition in this pilot‐scale gasifier. © 2014 American Institute of<abstract abstract-type="main"> <title> <x xml:space="preserve">Abstract</x> </title> <p>A dual‐fluidized‐bed gasifier was constructed and operated at the Woodland Biomass Research Center in Woodland, CA. The pilot‐scale gasifier had a capacity of 5 tons/day of feedstock and was based on the Pyrox process developed by Kunii et al. In this system, the fluidized‐bed combustion process with air is separated from the biomass gasification process with steam and recycle gas. This decreases the nitrogen content in the producer gas. The heat released in the combustion of the char is transported by a ceramic bed material circulating between the combustor and gasifier. Commercial wood pellets were used as feedstock for the present study. Gas composition, temperatures, and pressures were measured to characterize the operation of the gasifier. A positive feature of the system was the high circulation rate and efficient energy transfer between the combustor and gasifier. Analysis of the system was performed using Aspen Plus™ software to calculate mass and energy‐balances. A restricted equilibrium model for the producer‐gas composition agreed reasonably well with the measured non‐equilibrium gas composition for most gases. The restricted equilibrium model over‐predicted the H<sub>2</sub> concentrations. A more complex rate‐based kinetic model would be necessary to fully capture the details of the non‐equilibrium gas composition in this pilot‐scale gasifier. © 2014 American Institute of Chemical Engineers Environ Prog, 33: 732–736, 2014</p> </abstract> … (more)
- Is Part Of:
- Environmental progress & sustainable energy. Volume 33:Issue 3(2014:Oct.)
- Journal:
- Environmental progress & sustainable energy
- Issue:
- Volume 33:Issue 3(2014:Oct.)
- Issue Display:
- Volume 33, Issue 3 (2014)
- Year:
- 2014
- Volume:
- 33
- Issue:
- 3
- Issue Sort Value:
- 2014-0033-0003-0000
- Page Start:
- 732
- Page End:
- 736
- Publication Date:
- 2014-02-03
- Subjects:
- Environmental engineering -- Periodicals
Sustainable engineering -- Periodicals
Environmental chemistry -- Periodicals
333.7 - Journal URLs:
- http://onlinelibrary.wiley.com/journal/10.1002/(ISSN)1944-7450 ↗
http://www3.interscience.wiley.com/journal/121640218/grouphome/home.html ↗
http://onlinelibrary.wiley.com/ ↗ - DOI:
- 10.1002/ep.11945 ↗
- Languages:
- English
- ISSNs:
- 1944-7442
- Deposit Type:
- Legaldeposit
- View Content:
- Available online (eLD content is only available in our Reading Rooms) ↗
- Physical Locations:
- British Library DSC - 3791.547400
British Library DSC - BLDSS-3PM
British Library HMNTS - ELD Digital store - Ingest File:
- 4225.xml