Conversion of biomass in syngas by means of indirect gasification offers the option to improve the economic situation of any fuel cell system due to lower costs for feedstock and higher power revenues in many European countries. The coupling of an indirect gasification of biomass and residues with highly efficient solid oxide fuel cell (SOFC) systems is therefore a promising technology for reaching economic feasibility of small decentralized combined heat and power production (CHP).The predicted efficiency of common high temperature fuel cell systems with integrated gasification of solid feedstock is usually significantly lower than the efficiency of fuel cells operated with hydrogen or methane. Additional system components like the gasifier as well as the gas cleaning reduce this efficiency. Hence common fuel cell systems with integrated gasification of biomass will hardly reach electrical efficiencies above 30%. An extraordinary efficient combination is achieved in case that the fuel cells waste heat is used in an indirect gasification system. A simple combination of a SOFC and an allothermal gasifier enables then electrical efficiencies above 50%. However, this system requires an innovative cooling concept for the fuel cell stack. Another significant question is the influence of impurities on the fuel cell degradation. The European Research Project “BioCellus” focuses on both questions—the influence of the biogenous syngas on the fuel cells and an innovative cooling concept based on liquid metal heat pipes. First experiments showed that, in particular, higher hydrocarbons—the so-called tars—do not have any significant influence on the performance of SOFC membranes. The innovative concept of the TopCycle comprises to heat an indirect gasifier with the exhaust heat of the fuel cell by means of liquid metal heat-pipes. Internal cooling of the stack and the recirculation of waste heat increases the system efficiency significantly. This concept promises electrical efficiencies of above 50% even for small-scale systems without any combined processes.

1.
Scholtholt
,
H.
, 2005, “
Überblick über den europäischen Kraftwerkspark
,” VGB PowerTech 7∕2005, pp.
28
34
.
2.
Foscolo
,
P. U.
, “
Production of Hydrogen Rich Gas by Biomass Gasification Application to Small Scale Fuel Cell Electricity Generation in Rural Areas
,” Final Report, Joule III Project, JOR3-CT95-0037.
3.
Karl
,
J.
, and
Karellas
,
S.
, 2004, “
Highly Efficient SOFC Systems With Indirect Gasification
,”
Proceedings of the Sixth European Solid Oxide Fuel Cell Forum
,
Lucerne
, June 28–July 2, Vol.
2
, pp.
534
545
.
4.
Kendall
,
K.
,
Finnerty
,
C. M.
, and
Saunders
,
G.
, 2002, “
Effects of Dilution on Methane Entering an SOFC Anode
,”
J. Power Sources
0378-7753,
106
(
1–2
), pp.
323
327
.
5.
Saunders
,
G. J.
, and
Kendall
,
K.
, 2002, “
Reactions of Hydrocarbons in Small Tubular SOFCs
,”
J. Power Sources
0378-7753,
106
(
1–2
), pp.
258
263
.
8.
Stassen
,
H.
, and
Koele
,
H.-J.
, 1997, “
The Use of LCV-Gas From Biomass Gasifiers in Internal Combustion engines
,”
Biomass Gasification and Pyrolysis
,
CPL
,
Newbury
.
9.
Ouweltjes
,
J. P.
,
Aravind
,
P. V.
,
Woudstra
,
N.
, and
Rietveld
,
G.
, 2005, “
Biosyngas Utilization in Solid Oxide Fuel Cells with Ni∕GDC Anodes
,”
Proceedings of the First European Fuel Cell Technology & Applications Conference
,
Rome, Italy
, Dec. 14–16, Paper No. EFC2005-86089.
10.
Dunn
,
P. D.
, and
Reay
,
D. A.
, 1995,
Heat pipes
, 4th ed.,
Pergamon
,
Oxford
.
11.
Metz
,
Th.
,
Kuhn
,
St.
,
Karellas
,
S.
,
Stocker
,
R.
,
Karl
,
J.
, and
Hein
,
D.
, 2004, “
Experimental Results of the Biomass Heatpipe Reformer
,”
Proceedings of the Second World Conference on Biomass for Energy
,
Rome, Italy
, May 10–14.
You do not currently have access to this content.