2013
DOI: 10.1016/j.ijhydene.2012.09.118
|View full text |Cite
|
Sign up to set email alerts
|

System design and process layout for a SOFC micro-CHP unit with reduced operating temperatures

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1

Citation Types

0
13
0

Year Published

2015
2015
2021
2021

Publication Types

Select...
4
3

Relationship

0
7

Authors

Journals

citations
Cited by 26 publications
(13 citation statements)
references
References 25 publications
0
13
0
Order By: Relevance
“…The data were obtained from a proprietary 0‐D stack model, which was calibrated with actual measurement data from CFY stack tests, series Mk351. The stack model and fitting procedure is described in more detail in . In Figure , the area of suitable conditions for steady‐state stack operation is shown over the fuel input and electrical current for a given stack temperature of 830 °C and gas‐inlet temperatures of 700 °C (air) and 800 °C (fuel), respectively.…”
Section: Hotbox Concept and Operating Windowmentioning
confidence: 99%
See 1 more Smart Citation
“…The data were obtained from a proprietary 0‐D stack model, which was calibrated with actual measurement data from CFY stack tests, series Mk351. The stack model and fitting procedure is described in more detail in . In Figure , the area of suitable conditions for steady‐state stack operation is shown over the fuel input and electrical current for a given stack temperature of 830 °C and gas‐inlet temperatures of 700 °C (air) and 800 °C (fuel), respectively.…”
Section: Hotbox Concept and Operating Windowmentioning
confidence: 99%
“…The fluid enthalpy flows, heat flows and thermal losses were calculated and balanced with a 0‐D process model, which includes chemical equilibrium calculations and a calibrated SOFC stack model, and provides the missing gas compositions for the complete substance and energy balance, approximatively. Further details on the SOFC stack and process model are given in . At the process set point depicted in Figure , the POX‐reformer was operated with a stoichiometric air ratio of 0.27, and the air flow entering the reactor was pre‐heated to 526 °C.…”
Section: Proof‐of‐concept Prototype Development and Testingmentioning
confidence: 99%
“…Most SOFCs are designed to function at elevated temperatures, thereby generating higher cell efficiencies in comparison to other kinds of fuel cells when operating on hydrocarbon fuels [16]. However, many research groups are working to reduce the operating temperature of SOFCs to under 650 • C in order to reduce material degradation, prolong stack-lifetime and decrease stack material costs by enabling the use of common metallic materials [17][18][19]. Therefore, it is of paramount importance to manage the stack temperature of the SOFC in a uniform manner, particularly for planar SOFCs [20].…”
Section: Introductionmentioning
confidence: 99%
“…The market opportunity for micro cogeneration of heat and power (μCHP) application on the scale of a household or group of houses, brought several SOFC producers and system developers to start demonstrating this technology mainly in Europe [24][25][26] and in Japan [27,28]. Recent research focuses on the optimization of system design [29][30][31][32][33][34][35] and the study of μCHP integration strategies [36][37][38][39][40]. System design studies have been performed applying external reforming [29,31,33], innovative designs with low temperature SOFC's [32], with and without gas recirculation [30] and substitution of steam reforming by dry reforming [34,35].…”
mentioning
confidence: 99%
“…Recent research focuses on the optimization of system design [29][30][31][32][33][34][35] and the study of μCHP integration strategies [36][37][38][39][40]. System design studies have been performed applying external reforming [29,31,33], innovative designs with low temperature SOFC's [32], with and without gas recirculation [30] and substitution of steam reforming by dry reforming [34,35]. The integration strategy studies focus mainly on the economical valorization of heat and power depending on the specific geographical application conditions [36], on the type of building [37,38] and on the network integration strategy [39].…”
mentioning
confidence: 99%