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>ia1200(1) ST.PUR.PE Ref (2) PB as measured std eng.1000Pipe Length [m]800600400200Fig. 12, Pressure drop steel network with increasedservice pipe flowThere is not a lot of difference between both graphs inFig. 10 <strong>and</strong> Fig. 12. The reas<strong>on</strong> for this is that thedesign maximum fluid velocity is rather low for steel.This may prove different for the PB network, which isdesigned with smaller diameters in the periphery. SeeFig. 13, which can be compared to Fig. 11.The graph in Fig. 13 indeed shows an increasedpressure drop in the service pipes c<strong>on</strong>necting thehouses, when the flow in those pipes is artificiallyincreased to 100% of the installed power. However, thetotal pressure drop stays within the same limits as doesthe steel network under similar c<strong>on</strong>diti<strong>on</strong>s (Fig. 12).016 20 25 32 40 50 63 75 90 110Nominal diameter [mm]Fig. 14, Pipe length histogram Steel <strong>and</strong> PBAs a result of the use of smaller diameters with PB, thedistributi<strong>on</strong> of pipe lengths generally shifts to the left inthe pipe histogram. As heat loss increases withdiameter (see Fig. 8) this should have a positive effect<strong>on</strong> the total distributi<strong>on</strong> system heat loss.This shift to the left may be taken <strong>on</strong>e step further,since the wall thickness of the smallest PB mediumpipes currently is chosen a bit larger than the strengthclass (SDR11) requires. This is d<strong>on</strong>e for ease ofinstallati<strong>on</strong>. If the thickness of these pipes is chosen nolarger than SDR11, there is a slight additi<strong>on</strong>al shift tothe left, see Fig. 15.(1) ST.PUR.PE Ref (2) PB as measured std eng.(3) PB impr. Fresh all SDR1112001000Pipe Length [m]800600400200Fig. 13, Pressure drop PB network with increased servicepipe flowThe result of both design calculati<strong>on</strong>s is plotted inFig. 14, steel in red <strong>and</strong> PB in green.016 20 25 32 40 50 63 75 90 110Nominal diameter [mm]Fig. 15, Pipe length histogram steel, PB <strong>and</strong> PB SDR11networks315
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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academic access is facilitated as t
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