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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>ia6. TOTAL SYSTEM HEAT LOSSTo calculate the total system heat loss, pipe lengths asshown in the pipe length histograms are to bemultiplied by the respective heat losses per pipe pair,as shown in the heat loss value histograms.Fig. 15 ―multiplied‖ by Fig. 6 leads to the total systemheat losses in Fig. 16.Heat Loss [kW]80.070.060.050.040.030.020.010.00.0ST.PUR.PE RefPB as measured std eng.PB increased insulati<strong>on</strong> thicknessPB increased insulati<strong>on</strong> thickness all SDR11system [-]Fig. 16, Total system heat loss, current insulati<strong>on</strong> qualityThe graphs in Fig. 16 show the reference heat loss forsteel-PUR-PE in red <strong>and</strong> the currently measured heatloss for PB-PE-PE with n<strong>on</strong>-optimized insulati<strong>on</strong>thickness in orange. In green, total system heat loss isshown for current insulati<strong>on</strong> quality but with optimizedinsulati<strong>on</strong> thickness. The exclusive use of SDR11(blue) has a rather small effect.Improving insulati<strong>on</strong> quality, as described in paragraph5 <strong>and</strong> shown in Fig. 7, leads to slightly lower totalsystem heat loss for freshly produced PB-PE-PE whencompared to the reference, see Fig. 17.Heat Loss [kW]60.050.040.030.020.010.00.0ST.PUR.PE RefPB impr. insulati<strong>on</strong> thickness/qualitysystem [-]There is currently no experimental data <strong>on</strong> the rate ofageing of PB-PE-PE as a result of the exchange ofblowing agent with air. However, it is possible tocalculate a worst case situati<strong>on</strong> (see fig. 18), using thepredicted values plotted in fig. 8.Heat Loss [kW]70.060.050.040.030.020.010.00.0ST.PUR.PE RefPB impr. insulati<strong>on</strong> thickness/qualityPB impr. Insulati<strong>on</strong> thickness/quality degassedsystem [-]Fig. 18, Total system heat loss, including worst caseIn practice <strong>and</strong> over time, the predicted total systemheat loss will slowly shift from the fresh value in purpleto the worst case value in blue. Average heat lossduring lifetime will be somewhere in-between.FUTURE RESEARCHHydraulic calculati<strong>on</strong>s in combinati<strong>on</strong> with insulati<strong>on</strong>thickness form an interesting optimizati<strong>on</strong> problem:what diameter to select <strong>and</strong> which insulati<strong>on</strong> thicknessto choose?Current design strategies for hydraulic networks,aiming at linear pressure drop with distance, seem tooadventitious to be optimal. In additi<strong>on</strong>, heat losscalculati<strong>on</strong>s using st<strong>and</strong>ard casing dimensi<strong>on</strong>s showrapidly diminishing yields with each step up ininsulati<strong>on</strong> thickness, suggesting the optimum issomewhere in-between.First attempts have been made to use Pipelab [6] in adouble optimizati<strong>on</strong> routine, trying to find optimalhydraulic performance in combinati<strong>on</strong> with optimalinsulati<strong>on</strong> thickness distributi<strong>on</strong> over the network.Given the specific hydraulic properties of PB (high fluidvelocities permitted) <strong>and</strong> the specific insulati<strong>on</strong>properties of PE foam (better at small size), this maylead to rather different design strategies whencompared to c<strong>on</strong>venti<strong>on</strong>al rigid piping systems fordistrict heating <strong>and</strong> cooling.Fig. 17, Total system heat loss, reference <strong>and</strong> predicti<strong>on</strong>for improved insulati<strong>on</strong> quality316

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