The values presented do of course largely depend <strong>on</strong>the actual physical lambdas (in W/m.K) of the insulati<strong>on</strong>material, but the underlying measurement data suggestthat other factors come into play as well, such as thegeometry of foam in combinati<strong>on</strong> with the temperaturedependence of the ―physical‖ lambda of the foam.Therefore, the values in Table 1 are valid <strong>on</strong>ly forcalculati<strong>on</strong> / predicti<strong>on</strong> purposes, in exactly the samecalculati<strong>on</strong> model from which they were derived (alsoaccording to EN15632). The values in Table 1 aresupported by experimental data <strong>on</strong> four samples at thetime of writing this paper.When all parameters are known, equati<strong>on</strong> 1 can beused to calculate heat loss: i Where:1ln sd 2d 1 2 T probe T casing1 ln id 3d 21 ln cT probe, T casing represent probe (medium) <strong>and</strong> casingtemperatured 1 to d 4 represent inner/outer diameters of servicepipe <strong>and</strong> casingλ s , λ i , λ c = heat coefficient of service pipe,insulati<strong>on</strong> <strong>and</strong> casingIn this case, λ s <strong>and</strong> λ c are known: λ s = 0.19 W/m.K<strong>and</strong> λ c = 0.40 W/m.K. On a test rig, T probe , T casing <strong>and</strong>heat loss are measured, so for specific test samples,eq. 1 can be used backwards to calculate ―synthetic‖values for λ i in Table 1.For the Steel-PUR-PE reference, see [1], values canbe determined in a similar fashi<strong>on</strong>. ―Synthetic‖ λ ivalues for PUR foam, determined frommeasurement of samples, were typically in the rangeof 0.030 to 0.032 W/m.K, with λ s for steel 50 W/m.KHeat Loss [W/m]50454035302520151050St stdPB std insulati<strong>on</strong> thicknessPB extended insulati<strong>on</strong> thicknessPB impr. freshd 4d 316 20 25 32 40 50 63 75 90 110Nominal diameter [mm]Fig. 7, Heat loss per pair, including improved insulati<strong>on</strong>quality(1)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>ia313The red graph in Fig. 7 represents the predicted heatloss values for the combined effect of both increasedinsulati<strong>on</strong> thickness <strong>and</strong> insulati<strong>on</strong> qualityimprovement. For most diameters, these are <strong>on</strong> parwith or slightly better than the reference in Steel-PUR-PE. These data are valid <strong>on</strong>ly for the recently producedor ―fresh‖ product. As there is no experimental dataavailable <strong>on</strong> the rate of degassing <strong>and</strong> therefore therate of ageing, it is difficult to predict heat loss over thelife time of the product.However, it is possible to speed up the process ofageing artificially, until all the foaming agent has beenreplaced by air. The predicted values for this c<strong>on</strong>diti<strong>on</strong>are also presented in Table 1, as lambda degassed.These are ―synthetic‖ as well, <strong>and</strong> suitable forcalculati<strong>on</strong> purposes <strong>on</strong>ly. Calculated heat loss resultswith these values are presented in Fig. 8.Pump I, power: 16 kWHeat Loss [W/m]454035302520151050St std PB impr fresh PB impr degassed84 %14 %2 %16 20 25 32 40 50 63 75 90 110Nominal diameter [mm]Fig. 8, Heat loss per pair, including improved insulati<strong>on</strong>quality, fully degassedIn Fig. 8, the purple graph represents the reference,Steel-PUR-PE as measured, see Smits et al. 2010 [1].The red graph represents the predicti<strong>on</strong> of improved,fresh PB-PE-PE <strong>and</strong> green the predicti<strong>on</strong> of fullydegassed PB-PE-PE. The values vary a bit, but aregenerally in the same range. During the lifetime of theproduct, heat loss is expected to increase from the redvalues to the green values.Of course, ageing is also applicable to the referenceproduct, but not included here for two reas<strong>on</strong>s. First,the ageing process for rigid systems is expected to besignificantly slower than for flexible systems, <strong>and</strong>sec<strong>on</strong>d, the reference samples were not fresh, as couldbe judged by the gas c<strong>on</strong>tent. Therefore, it is not likelythat the values presented for the reference system willdeteriorate much further during lifetime.Ageing can be slowed down c<strong>on</strong>siderably if measuresare taken to prevent the exchange of blowing agentwith the envir<strong>on</strong>ment. If successful, these measures
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>iawould result in the ―red‖ heat loss values duringlifetime. Moreover, a new generati<strong>on</strong> of blowing agentsis under development. These new agents aim at lowerc<strong>on</strong>ductivity values for the gas <strong>and</strong> larger molecules.This may result in lower c<strong>on</strong>ductivity values for theproduct as well as a slower ageing process.6. HYDRAULIC CALCULATIONSThe pipe per pipe comparis<strong>on</strong> between Steel-PUR-PE<strong>and</strong> PB-PE-PE as dem<strong>on</strong>strated in Fig. 8, gives anindicati<strong>on</strong> of field results, but is not c<strong>on</strong>clusive. Internaldiameters differ, as do fricti<strong>on</strong> coefficients. Therefore,for the comparis<strong>on</strong> between distributi<strong>on</strong> systems fittedwith either pipe, hydraulic calculati<strong>on</strong>s are needed. Tothis end, a reference network is introduced in Korsmanet al. 2008 [2]. The same network is used here. It isinstalled in a housing estate near Arnhem, theNetherl<strong>and</strong>s, <strong>and</strong> has been designed using Pipelab,developed by Prof. Dr. Pàll Valdimarss<strong>on</strong> in 1995 [6].See www.pipelab.nl. St<strong>and</strong>ard design criteria wereused. A total of 247 houses are c<strong>on</strong>nected by 3.02 kmof DH network (6.05 km of pipe), 12.2 m per house.The graph in Fig. 10 represents the pressure in thesupply network (in m water column), as a functi<strong>on</strong> ofthe distance from the source. For st<strong>and</strong>ard symmetricalnetworks, the return network is similar, but mirroredover a horiz<strong>on</strong>tal axis.Using the flexible <strong>and</strong> smooth PB pipes allows forsmaller diameters, mainly because PB is less pr<strong>on</strong>e tothe transmissi<strong>on</strong> of hydraulic noises. This is due to thelow modulus of elasticity of PB when compared tosteel. In c<strong>on</strong>trast, a steel pipe filled with water is quite agood c<strong>on</strong>ductor of sound. To prevent noise caused byhigh flow velocities, these are limited in the design forsteel networks to 1 m/s.A network, specifically designed for PB, is shown inFig. 11. Smaller diameters in the periphery of thenetwork as a result of a higher permitted fluid velocitycauses higher pressure drops. This has to becompensated by bigger pipes closer to the source toreach the same overall pressure drop.Fig. 9, Aerial photograph of reference housing estateFig. 11, Design pressure drop PB networkFig. 10 shows an output graph of Pipelab.Fig. 10, Design pressure drop steel networkIn the design of district heating networks, the maximumdesign point is chosen c<strong>on</strong>siderably below the sum ofthe installed power in the c<strong>on</strong>nected buildings. It is notuncomm<strong>on</strong> to have a design point of 50% of the totalinstalled power for larger numbers of c<strong>on</strong>necti<strong>on</strong>s,depending <strong>on</strong> the experience <strong>and</strong> the courage of thedesigner. A design point of 50% of the total installedpower was used in both designs in this paper. Inpractice, no problems have arisen with this designpoint, partly because not all installed power is used atthe same time. However, this statistical effect does notapply to individual c<strong>on</strong>necti<strong>on</strong>s. Therefore, a designtrick is used in the periphery of the network, to preventproblems in the service pipes c<strong>on</strong>necting the buildings.The flow in these pipes is raised artificially above thedesign point, up to 100% load. The result of thiscalculati<strong>on</strong> is shown in Fig. 12, which can be comparedto Fig. 10.314
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P-1P-4P-9P-7E-5P-14P-8The 1
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academic access is facilitated as t
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1. CHP system operation in A2. Ther
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is covered by operating HOB. In oth
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produce heat and electricity. Fluct
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