Dergiler / International Journal of Thermodynamics / 2012 / Cilt: 15 - Sayı: 1

Experimental investigation of the absorption enhanced reforming of biomass in a 20 $kW _{th}$ dual fluidized bed system

Sayfa
53–59
Yayın Tarihi
2022-10-18
DOI
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It shows also that beyond a certain value of this parameter, the tar and gas composition is stabilized.

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Amaç & Hipotez:A gasification product gas with a hydrogen content over 75 vol-%db and a heating value of 15 MJ/$m^3 _{STP,db}$ has been obtained through the absorption enhanced reforming of biomass.
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Temel Bulgular & Veri:In the DFB system, the Ca - looping ratio is an important parameter defined as the ratio of the molar flow rate of regenerated sorbent ($F _{Ca}$) and carbon (Fc) which enters the gasifier as fuel.
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Sonuç & Katkı:It shows also that beyond a certain value of this parameter, the tar and gas composition is stabilized.
🔬Tür:Araştırma Makalesi
📍Kapsam:Genişletilmiş Akademik Örneklem
⚙️Değişkenler:Alan Parametreleri

Abstract

A gasification product gas with a hydrogen content over 75 vol-%db and a heating value of 15 MJ/$m^3 _{STP,db}$ has been obtained through the absorption enhanced reforming of biomass. The Absorption Enhanced Reforming (AER) process involves a Dual Fluidized Bed (DFB) system consisting of a gasifier and a regenerator (calciner). In the DFB system, the Ca - looping ratio is an important parameter defined as the ratio of the molar flow rate of regenerated sorbent ($F _{Ca}$) and carbon (Fc) which enters the gasifier as fuel. A special feature of the 20 $kW _{th}$ DFB test facility at IFK is the Ca - looping rate control through a cone valve. Therefore, the Ca - looping ratio ($F _{Ca}$/FC) was varied between a value of 2 and 12 molCaO/molC to investigate its influence on the cold gas efficiency, product gas yield, yield of gas components and gravimetric tar concentration during the AER of biomass. The experiments were carried out with wood pellets and a Greek limestone as $CO _2$ sorbent. The experimental work shows a clear influence of the Ca - looping ratio on the AER process. It shows also that beyond a certain value of this parameter, the tar and gas composition is stabilized.

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Bu Makaleye Atıf Yap

ZIEBA, M., SCHEFFKNECHT, G., POBOSS, N., SWIECKI, K., CHARITOS, A., HAWTHORNE, C. (2022). Experimental investigation of the absorption enhanced reforming of biomass in a 20 $kW _{th}$ dual fluidized bed system. International Journal of Thermodynamics, Cilt: 15 - Sayı: 1, 53–59. https://ajindex.com/articles/541869

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Kaynakça (6)

  1. Florin, N. H., Harris, A. T., 2008, Enhanced hydrogen production from biomass with in situ carbon dioxide capture using calcium oxide sorbents, Chemical Engineering Science 63, pp. 287 - 316 Higman, C., van der Burgt, M., 2003, Gasification. Gulf Professional Publishing. United States of America Corella, J., et. al., 2008, Biomass gasification with pure steam in fluidised bed: 12 variables that affect the effectiveness of the biomass gasifier, Int. J. Oil, Gas and Coal Technology, Volume 1, Number 1-2, pp. 194 – 207 Soukup, G., et. al., 2009, In situ $CO _2$ capture in a dual fluidized bed biomass steam gasifier: bed material and fuel variation, Chem. Eng. Technol. 32, No.3, pp. 348-354
  2. Corella, J., et. al., 2007, A Review on Dual Fluidized-Bed Biomass Gasifiers, Industrial & Engineering Chemistry Research, American Chemical Society, 46, pp. 6831-6839
  3. Hofbauer, H. et al., 2002, Six Years Experience with the FICFB-Gasification process, 12th European Biomass Conference, Italy, pp. 982-985 Neues Biomassekraftwerk Oberwart, 2009, Optimierte Konzeption der Biomassevergasung aufbauend auf dem DFB-Konzept aus Güssing, Der Reaktor, Vereinszeitung des Vereins der StudentInnen und AbsolventInnen der Verfahrenstechnik an der TU Wien, Jahrgang 19, Ausgabe 88, Nr.4 Pfeifer, C., et. al., 2007, In-Situ $CO _2$-Absorption in a Dual Fluidized Bed Biomass Steam Gasifier to Produce a Hydrogen Rich Syngas International Journal of Chemical Reactor Engineering, Vol. 5, Article A9 Grasa, G.S., Abanades, J.C., 2006. $CO _2$ capture capacity in long series of carbonation/ calcination cycles. Ind. Eng. Chem. Res. 45, pp. 8846-8851
  4. Abanades, J.C., et al., 2004, Capture of $CO _2$ from combustion flue gases in a fluidized bed of CaO, AIChE J. 50 (7), pp. 1614-1622
  5. Charitos, A., et al., 2010, Parametric study of the Calcium Looping process for $CO _2$ capture in a 10 kWth Dual Fluidized Bed, Int. J. of Greenhouse Gas Control, submitted for publication Corella, J., et. al., 2006, Steam Gasification of Coal at Low-Medium (600°C~800°C) Temperature with Simultaneous $CO _2$ Capture in Fluidized Bed at Atmospheric Pressure: The Effect of Inorganic Species. 1. Literature Review and Comments, Industrial & Engineering Chemistry Research, American Chemical Society, 45, pp. 6137-6146
  6. Charitos, A., et al., 2009, Hydrodynamic analysis and design of a 10 kWth Calcium Looping Dual Fluidized Bed for post-combustion $CO _2$ capture. Powder Technol., accepted for publication. Hawthorne, C., et al., 20