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12th International Symposium on District Heating and Cooling

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The <str<strong>on</strong>g>12th</str<strong>on</strong>g> <str<strong>on</strong>g>Internati<strong>on</strong>al</str<strong>on</strong>g> <str<strong>on</strong>g>Symposium</str<strong>on</strong>g> <strong>on</strong> <strong>District</strong> <strong>Heating</strong> <strong>and</strong> <strong>Cooling</strong>,September 5 th to September 7 th , 2010, Tallinn, Est<strong>on</strong>iac<strong>on</strong>versi<strong>on</strong>lossesnetw orkheatlossesbuildingheatlossesprimaryenergyheatgeneratorheatflowpumpingelectricitydistrictheatingnetw orkheatflowheatingsurfaceT = 20°Cheatflowpow er plantc<strong>on</strong>versi<strong>on</strong> lossesprimary energyFigure 2. Evaluati<strong>on</strong> boundaries of an energy supply system. The blue (outer) dashed line marks the complete system; theblack (inner) dashed line marks the network subsystem1.2. Integrated system evaluati<strong>on</strong>When evaluating a system it is important to specify theevaluati<strong>on</strong> boundaries (cf. fig. 2). It has to be pointedout that an integrated system evaluati<strong>on</strong> is m<strong>and</strong>atorysince otherwise results are ambiguous <strong>and</strong> misleading.This can be dem<strong>on</strong>strated by assuming e.g. evaluati<strong>on</strong>of the building subsystem <strong>on</strong>ly. If two systems arecompared, <strong>on</strong>e c<strong>on</strong>sisting of a target room equippedwith space heating <strong>and</strong> the other <strong>on</strong>e with a targetroom equipped with c<strong>on</strong>venti<strong>on</strong>al heating, <strong>on</strong>e couldarrive at the c<strong>on</strong>clusi<strong>on</strong>, that the system utilizing spaceheating is more efficient. However, assuming bothsystems are also equipped with an identicalc<strong>on</strong>densing gas boiler providing the heat, an evaluati<strong>on</strong>comprising the total system (c<strong>on</strong>sisting of heatgenerati<strong>on</strong> <strong>and</strong> heat transfer to the target) would arriveat a totally different c<strong>on</strong>clusi<strong>on</strong>. In this case, bothsystems possess the same exergy efficiency, which isapproximately 5% for the outlined case. This isbecause a potentially more efficient heating system isnot put to use as the same input <strong>and</strong> supply flowsoccur in both cases.1.3 Efficiency enhancement potentialsThe complete energy supply system can be dividedinto three subsystems – generati<strong>on</strong>, distributi<strong>on</strong> <strong>and</strong>building (representing the c<strong>on</strong>sumpti<strong>on</strong>). Thesesubsystems possess different potentials to enhanceoverall system efficiency.Currently heating dem<strong>and</strong>s are met by burning highexergyfuels, great enhancement potentials areavailable within the generati<strong>on</strong> subsystem. Firstly, fuelsshould not be used to directly satisfy thermal dem<strong>and</strong>sat all since this embodies pure exergy destructi<strong>on</strong>.41Instead thermal input flows as industrial waste heat3 orgeothermal energy should be applied. On the otherh<strong>and</strong>, if combustible fuels are used to meet thermaldem<strong>and</strong>s, at least Combined Heat <strong>and</strong>Power generati<strong>on</strong> (CHP) with a maximum electricaldegree of efficiency should be utilized. This allowstransforming part of the high-exergy fuel into highexergyelectric current. Heat is produced as ‗wasteproduct‘ of this c<strong>on</strong>versi<strong>on</strong>.Optimizati<strong>on</strong> potentials within the distributi<strong>on</strong>subsystem are basically indirect. At first glance, thedistributi<strong>on</strong> system has no influence at all since thenetwork acts as c<strong>on</strong>necti<strong>on</strong> between heat generati<strong>on</strong><strong>and</strong> heat c<strong>on</strong>sumpti<strong>on</strong>. C<strong>on</strong>sequently, no thermal flowsexist that pass the overall system evaluati<strong>on</strong>boundaries. However, two aspects remain <strong>and</strong> need tobe accounted for. One is heat losses occurringthroughout the network that have to be compensatedby additi<strong>on</strong>al heat generati<strong>on</strong>. The other is pumping tomaintain the heat transfer medium circulati<strong>on</strong>, which ismet by an unalterable high-exergy input (electricity).The main problem is that c<strong>on</strong>cepts, which lead todecreasing heat losses cause increasing pumpingefforts <strong>and</strong> vice versa. Nevertheless, heat losses arethe exergetically dominant influence, therefore thefocus should be to c<strong>on</strong>fine these losses. Heat lossesdepend <strong>on</strong> the driving temperature difference betweenmedium <strong>and</strong> surrounding ground <strong>and</strong> <strong>on</strong> surface area.Minimizati<strong>on</strong> of the losses can most easily be achievedby reducing the network temperatures since pipedimensi<strong>on</strong>s are affixed due to dem<strong>and</strong>s so that surfaceareas are not a modifiable parameter. This approach iseven more rewarding since it allows employing low3 Industrial waste heat in this sense is heat that can no more beput to any use within the industrial producti<strong>on</strong> process.

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