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12th International Symposium on District Heating and Cooling

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>iaNote that the annual flow-compensated meantemperature in Table 2 is based <strong>on</strong> results from the fieldstudy where measured values for low relative heat loadare missing, which makes the values in the tablesomewhat underestimated.CONCLUSION AND DISCUSSIONBy installing the add-<strong>on</strong>-fan blower applicati<strong>on</strong> <strong>on</strong>existing radiators the temperature level in the heatingsystem can be substantially reduced. This will also haveimpacts <strong>on</strong> the DH network <strong>and</strong> DH producti<strong>on</strong> units.The impact <strong>on</strong> the DH network can be applied based <strong>on</strong>two principles:1) DH supply temperature kept at the same level aswithout the add-<strong>on</strong>-fan blowers. This will result inreduced primary flow rate.2) Reduced DH supply temperature while primary flowrate is kept c<strong>on</strong>stant.The first strategy could be applied immediately, sincethe primary supply temperature is kept as the samelevel as before. This means that not all heating systemsc<strong>on</strong>nected to the DH network need to be modified inorder to apply this method. The lowered sec<strong>on</strong>darytemperature level results not <strong>on</strong>ly in reduced DH-returntemperature, but also in a reducti<strong>on</strong> of the DH flow rate.The reduced flow rate could be used to increase thenumber of buildings c<strong>on</strong>nected to the DH network, or toavoid bottlenecks in the DH network. The magnitude ofthe reducti<strong>on</strong> of the DH supply temperature is between9 <strong>and</strong> 12 °C at DOT <strong>and</strong> at the same time the flow rateis decreased with more than 10 %. On annual basis thepossible reducti<strong>on</strong> of temperature level in the DHnetwork is in the magnitude of several degrees Celsius.In order to apply the sec<strong>on</strong>d strategy the dem<strong>and</strong> for ahigh temperature level in the DH network needs to bereduced for all the c<strong>on</strong>nected buildings. Otherwise theDH flow rate will increase. Calculati<strong>on</strong>s based <strong>on</strong> theresults from the field study in this paper shows that theDH supply temperature can be reduced with about10 °C at DOT without affecting the DH flow rate. At thesame time the DH return temperature will be reducedwith as much as 10 °C at DOT.The performance of the tested add-<strong>on</strong>-fan blowerscorresp<strong>on</strong>ds to the pattern of theoretical calculati<strong>on</strong>s.However, the results are not comparable since the airflow in the pilot project has not been measured.The results presented here are an important part in theevaluati<strong>on</strong> of effects of improvements in c<strong>on</strong>sumerheating systems <strong>on</strong> primary energy efficiency in DHsystems including producti<strong>on</strong> plants, especially CHP.ACKNOWLEDGEMENTThis work is part of the Primary Energy Efficiencyproject of Nordic Energy Research.NOMECLATUREAbbreviati<strong>on</strong>sCHPDHDHWDOTHEXVariablesCombined heat <strong>and</strong> power stati<strong>on</strong><strong>District</strong> heatingDomestic hot waterDesign outdoor temperatureHeat exchanger (DH substati<strong>on</strong>)α Heat transfercoefficient (W/m 2. K)β coefficient ofexpansi<strong>on</strong> (K-1)δ Thickness (m)λ C<strong>on</strong>ductivity (W/m . K)Gr Grashof number (-)h Height (m)k Heat transfercoefficient (W/m 2. K)L Length (m)ε Emissisivity (-) m mass flow (kg/s)ν Kinematic viscosity(m 2 /s)ζ Stephan-Boltzmanc<strong>on</strong>stantΔθ Logarithmic meantemperaturedifference (K)A Area (m 2 )Nu Nusselt number (-)P Electric power (W orkW)Pr Pr<strong>and</strong>tl number (-)Q Heat output (W or kW)c p Heat capacity (J/kgK) Ra Rayleigh number (-)C C<strong>on</strong>stant Re Reynolds number (-)g Gravity force (N/s 2 ) T Temperature (ºC or K)Subscripts0 Design c<strong>on</strong>diti<strong>on</strong>(without fan)Fan Add-<strong>on</strong>-fan blower inoperati<strong>on</strong>prPrimary (side)Returni indoor rad radiati<strong>on</strong>m Mean rel Relativeout outdoor s Sec<strong>on</strong>dary (side) orSupply29

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