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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>iaAverage cell size [mm]60504030201001,81,51,20,90,60,30,0- 5.000 10.000 15.000 20.000 25.000Cross secti<strong>on</strong> of foam [mm²]Graph 1: Density <strong>and</strong> cell size in relati<strong>on</strong> to foam crosssecti<strong>on</strong>Heat loss of buried piping [W/m]40,035,030,025,020,015,03050 100 150 200Outer diameter pipesystem [mm]Graph 2: 50,calculated <strong>and</strong> calculated heat loss of buriedpipe in relati<strong>on</strong> to outer pipe size8070605040C<strong>on</strong>ductivity [mW/m.K]Density [kg/m³]Graph 3 shows the relati<strong>on</strong>ship between outer pipesystem diameter size <strong>and</strong> the percentage of foamingagent directly from producti<strong>on</strong>. With increasingdiameter the foaming agent increases, possibly to anasymptotic value.An additi<strong>on</strong>al interesting factor is the <strong>on</strong>going processin the foam during <strong>and</strong> after producti<strong>on</strong>. As describedbefore the final step in the producti<strong>on</strong> is a 5-day curingstage.During the curing stage the foam exp<strong>and</strong>s <strong>and</strong> part ofthe foaming agent releases from the foam. As the foamis locked by a hard outer shell, expansi<strong>on</strong> is directedinwards. By this the gap between the foam <strong>and</strong> the PBmedium pipe, typical for our producti<strong>on</strong> method, isdecreased.Table 2 shows the effect of curing <strong>and</strong> degassing <strong>on</strong>both the c<strong>on</strong>tents of foaming agent <strong>and</strong> the calculatedheat loss.Even when forced, degassing takes time. The numberof degassed samples manufactured in the same wayas the fresh samples is therefore limited. Table 2 isshort due to a lack of adequate <strong>and</strong> comparablesamples.Table 2: The effect of time <strong>on</strong> curing <strong>and</strong> degassingFresh6 days curing DegassedProduct AgentHeatHeatHeatAgent AgentLossLossLoss% W/m % W/m % % W/m %63 A 32 52 15 23 17,5 15 0 17,1 1275 A 40 46 18 40 16,9 -5 0 20,1 1390 A 40 64 17 53 18 5 0 18,5 8Graph 2 shows the influence of outer pipe size tocalculated c<strong>on</strong>ductivity 50 <strong>and</strong> heat loss of buried pipesystems.It also shows that part of the increase of the heat losswith the diameter is caused by increase of c<strong>on</strong>ductivity.Percentage foaming agent90807060504050 100 150 200Outer diameter pipesystem [mm]Graph 3: Foaming agent c<strong>on</strong>tent in relati<strong>on</strong> to outerdiameter sizeHeat loss of buried piping [W/m]2019181716150 10 20 30 40 50 60Percentage of foaming agentGraph 4: Relati<strong>on</strong>ship between heat loss <strong>and</strong> foamingagentGraph 4 shows that there is a tendency of decreasingheat loss with increasing foaming agent. This tendencyhas seems weak. The spread is large over the entiregraph.116

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