12.07.2015 Views

Energy Systems and Technologies for the Coming Century ...

Energy Systems and Technologies for the Coming Century ...

Energy Systems and Technologies for the Coming Century ...

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

exhaust gas temperature, which can be utilized <strong>for</strong> additional power generation in heatengines or used <strong>for</strong> o<strong>the</strong>r heating purposes, whe<strong>the</strong>r internal in or external to <strong>the</strong> system.The Danish SOFC developer Topsoe Fuel Cell A/S states that <strong>the</strong> electrical efficiency ofdistributed power generation can be increased from average 40% in traditional powerplants to 55% when using SOFC technology [2]. SOFCs can electrochemically convertH 2 <strong>and</strong> CO to electricity <strong>and</strong> heat as well as internally re<strong>for</strong>m CH 4 into more H 2 <strong>and</strong> COdue to <strong>the</strong>ir high operating temperature <strong>and</strong> <strong>the</strong> presence of a nickel catalyst. Comparedto o<strong>the</strong>r fuel cell types, <strong>the</strong>se conversion pathways make SOFCs very fuel flexible <strong>and</strong>ideal <strong>for</strong> conversion of product gas from <strong>the</strong>rmal gasification.Generally, a major issue of combining gasification <strong>and</strong> SOFC technology has proved tobe gas conditioning, as SOFCs have strict requirements <strong>for</strong> fuel cleanliness [3]. In typicalgasifiers, relatively high levels of contaminants are entrained in <strong>the</strong> product gas flow,thus advanced gas cleaning is needed. In this study, a novel two-stage gasificationconcept producing a very clean product gas at high cold gas efficiency is used, thus onlysimple gas conditioning is necessary. General documentation of <strong>the</strong> demonstrated twostagegasification concept has previously been published [4]-[5]. The concept is scalableup to <strong>the</strong> range of 3-10 MW th [6], <strong>and</strong> it has been demonstrated up to 0.6 MW th (based onlower heating value, LHV) at present [7]. Hoffman et al. [8] operated an SOFC oncleaned product gas from a demonstrated two-stage gasifier <strong>for</strong> 150 hours without anyprove of cell degradation.Previous studies by <strong>the</strong> authors have shown that combining SOFC <strong>and</strong> gas turbinetechnology significantly enhances <strong>the</strong> power yield from <strong>the</strong>rmally gasified biomasscompared to using only one of <strong>the</strong> two technologies [9]-[11]. A small-scale gasifier-SOFC-MGT hybrid plant can reach an electrical efficiency around 50% (LHV).Fur<strong>the</strong>rmore, an exergy analysis study has revealed that optimization of <strong>the</strong> heatmanagement can increase <strong>the</strong> electrical efficiency even more [12]-[13].This work presents <strong>the</strong>rmodynamic assessments of alternative plant layouts of apreviously studied novel hybrid CHP plant combining two-stage biomass gasification,simple gas conditioning, an SOFC stack <strong>and</strong> a MGT. These alternative plant layoutsinclude optimization ef<strong>for</strong>ts by introducing a methanation reactor to increase <strong>the</strong> CH 4content in <strong>the</strong> anode feed, thus ensuring more SOFC cooling by <strong>the</strong> endo<strong>the</strong>rmic internalre<strong>for</strong>ming reactions. Hereby, <strong>the</strong> parasitic loss of <strong>the</strong> plant can be reduced due tolowering of <strong>the</strong> excess air flow to <strong>the</strong> SOFCs. The <strong>the</strong>rmodynamic assessments areconducted by use of ma<strong>the</strong>matical models describing <strong>the</strong> <strong>the</strong>rmodynamic processes. Themodels rely on connecting zero-dimensional component models to generate <strong>the</strong> completeplant-level models. The simulation tool used in this modelling study is DNA (DynamicNetwork Analysis), which is made <strong>for</strong> simulations of ma<strong>the</strong>matical models representing<strong>the</strong>rmodynamic processes [14]-[16].2 Reference Plant DesignsThe plant is divided into a gasification plant part <strong>and</strong> a CHP producing plant part. Woodchips are converted to product gas in <strong>the</strong> gasification part, <strong>and</strong> in <strong>the</strong> CHP producingpart, <strong>the</strong> product gas is converted to electric power <strong>and</strong> heat by use of an SOFC stack <strong>and</strong>a MGT.The gasification plant part is based on <strong>the</strong> two-stage gasification concept, whichcomprises a technique where drying <strong>and</strong> pyrolysis take place prior to an auto<strong>the</strong>rmaldowndraft gasification reactor, <strong>and</strong> where partial oxidation creates a high-temperaturetar-cracking zone in between <strong>the</strong> pyrolysis <strong>and</strong> char gasification steps. By thisgasification concept, a very clean product gas can be produced, thus avoiding advancedgas conditioning <strong>and</strong> easier utilization in an SOFC. The simple gas conditioningper<strong>for</strong>med in this plant includes gas cooling, a bag filter <strong>and</strong> a condensing gas cooler.The CHP producing plant part comprises an SOFC stack <strong>and</strong> a MGT. The SOFC ensuresefficient power production from <strong>the</strong> product gas, while <strong>the</strong> MGT ensures additionalRisø International <strong>Energy</strong> Conference 2011 Proceedings Page 299

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!