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.
temperature thermal input flows <strong>and</strong> thereforerepresents the prerequisite for an efficient generati<strong>on</strong>subsystem.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>iaThe last subsystem possessing enhancement potentialis the c<strong>on</strong>sumer. Since the target temperaturedetermines the exergetic quality of the thermaldem<strong>and</strong>, therein lays no significant optimizati<strong>on</strong>potential. However, as decreasing the amount ofenergy that has to be supplied is also part of the low-exc<strong>on</strong>cept insulati<strong>on</strong> can help to improve the system. Onthe other h<strong>and</strong>, benefits similar to those alreadydiscussed for the distributi<strong>on</strong> subsystem can beidentified for the c<strong>on</strong>sumer system as well. By choosingappropriate heating <strong>and</strong> cooling technologies, as e.g.investigated in [3], the exergy destructi<strong>on</strong> during heattransfer to the room air can be minimized. This isachieved by applying low-temperature heating <strong>and</strong>high-temperature cooling devices. Inlet <strong>and</strong> outlettemperatures of the heating/cooling devicesimultaneously define c<strong>on</strong>straints for the distributi<strong>on</strong>network subsystem, which in turn set c<strong>on</strong>straints for thegenerati<strong>on</strong>. In the end supply temperatures close to thetarget temperature form the basis for a ‗low-ex ready‘c<strong>on</strong>sumer. Without this step an exergetically optimalenergy supply system would be greatly hindered.2. Applicable technologies for the realisati<strong>on</strong>2.1. Phase Change SlurriesThe most used heat transfer fluid in district heating <strong>and</strong>cooling networks is water. In supply networks, the heatis transferred as sensible heat with a temperaturedifference between forward <strong>and</strong> backward flow. Theheat transfer capacity of a network is determined by thetemperature difference, the mass flow <strong>and</strong> the heatcapacity of the heat transfer fluid. The temperaturedifference <strong>and</strong> the temperature level of the network arelimited by technical restricti<strong>on</strong>s <strong>and</strong> determine thenecessary mass flow of the heat transfer fluid. Toovercome these restricti<strong>on</strong>s, fluids with higher heatcapacities than the heat capacity of water are underdevelopment. An alternative to water could be PCS.PCS are mixtures of dispersed phase change material<strong>and</strong> a c<strong>on</strong>tinuous liquid phase, which possess anincreased heat capacity due to the additi<strong>on</strong>al latentheat of fusi<strong>on</strong> occurring during the phase transiti<strong>on</strong> ofthe phase change material. The PCS remainspumpable even when the phase change material isfrozen. Thus, the PCS can be used as heat transferfluid in supply networks. A promising PCS for heat orcold supply networks is paraffin/water dispersi<strong>on</strong>.Figure 3 is a photograph of a paraffin/water dispersi<strong>on</strong>.Paraffin is the phase change material, which can bechosen according to the desired temperature of thephase transiti<strong>on</strong>, <strong>and</strong> water is the c<strong>on</strong>tinuous phase ofthe dispersi<strong>on</strong>. In [4] paraffin/water dispersi<strong>on</strong>s areinvestigated <strong>and</strong> their properties presented42Figure3. Photograph of a paraffin/water dispersi<strong>on</strong>The increase of the heat transport capacity of a supplynetwork using a PCS instead of water can be describedby a thermal capacity enhancement factor (TCEF),which is calculated according to equati<strong>on</strong> (2).TCEF PCSwh c T wcf, PCM p,PCM1p,w T(2) c Twp,wThe TCEF is a functi<strong>on</strong> of the densities of the PCS ρ PCS<strong>and</strong> water ρ w , the mass c<strong>on</strong>centrati<strong>on</strong> of the PCM w,the specific heat capacity of PCM c p,PCM <strong>and</strong> water c p,wthe heat of fusi<strong>on</strong> of the PCM Δh f,PCM <strong>and</strong> thetemperature change ΔT of the fluids. The TCEF iscalculated <strong>and</strong> plotted in the diagram figure 4 fortemperature differences ΔT between the forward <strong>and</strong>backward flow of 10 <strong>and</strong> 15 K as functi<strong>on</strong> of the massc<strong>on</strong>centrati<strong>on</strong> w.TCEF [-]3.532.521.51delta T = 10 Kdelta T = 15 K0 0.2 0.4 0.6 0.8 1w [-]Figure 4. TCEF – PCS compared to water for temperaturedifferences 10 <strong>and</strong> 15 K, diagram calculated with theproperties of water <strong>and</strong> RT-42 of the companyRubitherm [5]Using PCS with a mass c<strong>on</strong>centrati<strong>on</strong> w of 0.4 wouldincrease the heat transport capacity of the supplynetwork to 1.5 times of the value compared to water, if
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academic access is facilitated as t
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produce heat and electricity. Fluct
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