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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>iaRESULTS AND CORRELATIONSIt is again the company´s philosophy that paves theway for innovati<strong>on</strong>s. One of these innovati<strong>on</strong>s is thedevelopment of an in-house device for testing pipesystems, directly from producti<strong>on</strong>, cured <strong>and</strong> degassed.This proved to be a suitable device for producti<strong>on</strong>c<strong>on</strong>trol, but also for gaining more insights into productparameters.The objective of testing is to improve the knowledge ofthe produced pipe systems in order to optimize:Producti<strong>on</strong> methods:Machine data can be adjusted based <strong>on</strong> test results.Test results may lead to new producti<strong>on</strong> methods withnew equipment.Chemical <strong>and</strong> physical compositi<strong>on</strong> of layer material:Knowledge of various compositi<strong>on</strong> materials may leadto an improvement of insulating values.Cell structure <strong>and</strong> gap between insulating foam <strong>and</strong>medium pipe:Cell size influences values, test result basedimprovements are possible. The gap is a bad insulator.The quest for a minimal gap started with testing.Improvement <strong>and</strong> minimizati<strong>on</strong> of this gap was anachieved challenge in the testing period.Thermaflex is a lean <strong>and</strong> mean organisati<strong>on</strong> thatresp<strong>on</strong>ds quickly to new insights. Therefore newinsights were applied even before the complete rangeof producti<strong>on</strong> testing was performed.For the company, improvements of product <strong>and</strong>producti<strong>on</strong> have the highest priority. Although theproducti<strong>on</strong> range is wide, the insight into specific <strong>and</strong>general parameters increased c<strong>on</strong>siderably.The research provides the prominent variables toimprove insulati<strong>on</strong> performance. Practical heat lossdeterminati<strong>on</strong>, in combinati<strong>on</strong> with analytical studies,results in a clear underst<strong>and</strong>ing of heat loss behaviourin single <strong>and</strong> twin flexible pipe systems during theirentire lifetime.As a result of the tests the manufacturing process isimproved in two steps.The emphasis of the first step was to diminish the cellsize of the foam. This succeeded in a decrease of cellsize by some 20%.DISCUSSION OF PARAMETERSTable 1 summarises the results of measurements <strong>and</strong>calculati<strong>on</strong>s of tests <strong>on</strong> Flexalen 600 pipes directly fromproducti<strong>on</strong>. Various diameters are tested <strong>and</strong>calculated according to EN 15632 for a surfacetemperature of 10 °C <strong>and</strong> a comm<strong>on</strong> mediumtemperature of 70 °C (Instead of the maximum mediumtemperature of 95 °C).The table indicates the relati<strong>on</strong>ships between product,cross secti<strong>on</strong>al area of the foam, foam density, cell sizeof the foam, remaining foaming agent, calculatedthermal c<strong>on</strong>ductivity <strong>and</strong> the calculated heat loss of aburied piping system.The products 50A25, 63A32, 75A40 <strong>and</strong> 90A50 arenewly developed. These products are not necessarily<strong>District</strong> <strong>Heating</strong> products. However, they are producedusing the same process <strong>and</strong> have their applicati<strong>on</strong> inthe c<strong>on</strong>necti<strong>on</strong> between the district heating network<strong>and</strong> the building or house. It is also applicable in caseof low temperature differences, cooling or in-househeating or cooling.Table 1: Test results of fresh, uncured piping systemsProductFoamsecti<strong>on</strong> density cell size agent 50,calc Heat Loss*mm² kg/m³ (mm) % mW/m.K W/m50 A 25 1.473 50,0 0,47 52 39 15,363 A 32 2.313 34,0 0,50 52 38 15,275 A 40 3.044 38,0 0,40 46 44 17,890 A 40 5.105 42,0 0,80 64 51 17,190 A 50 4.398 39,0 0,80 62 55 23,0125 A 63 9.155 39,0 0,88 70 56 22,0160 A 75 15.688 40,3 1,20 81 54 21,0160 A 90 13.745 35,0 1,30 85 61 25,2200 A 110 21.913 45,0 1,60 81 68 27,4*) calculated heat loss of buried system at temperature difference of 60 KIn Graph 1 foam density <strong>and</strong> cell size are related to thecross secti<strong>on</strong>al surface.In Table 1 the foam density varies from about 35 kg/m³to about 50 kg/m³. Graph 1 shows hardly anyrelati<strong>on</strong>ship with the surface of the cross secti<strong>on</strong>.Table 1 shows that cell size varies from 0.47 to 1.60mm. Graph 1 shows that cell size is directly related tothe cross secti<strong>on</strong>al surface, however less than 1 to 1.This relati<strong>on</strong>ship is influenced by physical producti<strong>on</strong>parameters.The latest step is altering producti<strong>on</strong> such that thec<strong>on</strong>tent of anti-radiati<strong>on</strong> agent increases. The initialresults are promising but are not yet c<strong>on</strong>clusive as theanti-radiati<strong>on</strong> agent is also a good heat c<strong>on</strong>ductor.115

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