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>iaFig. 4 In-house heat exchanger (HE) in DH systemTable 1 Simultaneous Factors<strong>District</strong> <strong>Heating</strong> NetworkThe DH network <strong>and</strong> the c<strong>on</strong>necti<strong>on</strong> to the end usersare shown in Fig. 6. The house is designed to c<strong>on</strong>nectto the plant directly through different diameter pipeswhich were optimized with the simulati<strong>on</strong> program. Thedirect c<strong>on</strong>necti<strong>on</strong> allows the primary DH network tocirculate water directly into the end user installati<strong>on</strong>. Itis suitable for a moderate pressure level network <strong>and</strong>the differential pressure of DH network is sufficient tocirculate water to the house installati<strong>on</strong>. The networks<strong>and</strong> house installati<strong>on</strong>s are assumed to withst<strong>and</strong>maximum pressure 10 bar. The c<strong>on</strong>sumer differentialpressure is set as 0.5 bar. It is c<strong>on</strong>trolled at the enduser al<strong>on</strong>g the network critical route which is shown ingreen color.Three network design scenarios were investigated foreach house installati<strong>on</strong>:Case 1: It is the reference case. The totalnetwork length is 3080 m <strong>and</strong> the network lineheat density is 177 kWh/year. Network wasdesigned in the traditi<strong>on</strong>al way for two pipeswith <strong>on</strong>e supply <strong>and</strong> <strong>on</strong>e return, respectively.The differential pressure is c<strong>on</strong>trolled at userA. Twin pipes were selected for theDH network. They are called ―reference pipe‖in this paper.Case 2: By-pass water recirculati<strong>on</strong>. A thirdpipeline (Fig. 6 grey color line) was introducedto separate the by-pass water with returnwater <strong>and</strong> re-circulate the by-pass water backto the plant. The third pipeline was sizedbased <strong>on</strong> the summer by-pass water flow rate.The differential pressure is c<strong>on</strong>trolled at pointB.Case 3: Double pipeline supply. The main pipe(from plant to the juncti<strong>on</strong> point at each street)in the third pipeline which was sized in case 2functi<strong>on</strong>s all year round. It acts as supply pipeduring winter seas<strong>on</strong> <strong>and</strong> functi<strong>on</strong>s as supplywater recirculati<strong>on</strong> pipe when there has bypasswater dem<strong>and</strong>. In this case, the mainpipe in the reference case was resized as aporti<strong>on</strong> of supply water is shared by therecirculati<strong>on</strong> pipe. The c<strong>on</strong>necti<strong>on</strong> ofrecirculati<strong>on</strong> pipe to the reference pipe isshown with red color.Fig. 5 Domestic hot water storage (DHWS) in DH systemThe thermal by-pass temperature was set as 50 °C forHE <strong>and</strong> 60 °C for DHWS with dead b<strong>and</strong> 2 °C. The bypassis placed <strong>on</strong> the end user at each street in case 1,while at the virtual point adjacent to the end user incase 2.75
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>iaNetwork Heat Loss Calculati<strong>on</strong>The reference network was designed with twin pipes byplacing the supply <strong>and</strong> return pipe in the same casing.Two types of twin pipes were c<strong>on</strong>sidered in thesimulati<strong>on</strong>: AluFlex multilayer flexible pipe <strong>and</strong> straightsteel pipe. The pipes were selected with c<strong>on</strong>tinuousdimensi<strong>on</strong> ranging from Alx14 to 32 for AluFlex pipe<strong>and</strong> DN 32 to DN40 for steel pipe, based <strong>on</strong> the marketavailable products [8]. Single AluFlex pipe is selectedfor the 3rd recirculati<strong>on</strong> line. This 3rd pipeline can beassumed being placed in the same trench al<strong>on</strong>g thetwin pipes. The thermal interacti<strong>on</strong> between the twin<strong>and</strong> the single pipe is assumed negligible.The heat loss in the twin pipe was calculated accordingto the reference [7,9][1][2]coefficients corresp<strong>on</strong>ding to the temperaturedifference between the flow <strong>and</strong> the ground.The temperature variati<strong>on</strong> al<strong>on</strong>g the pipeline wascalculated as internal flow with isothermal boundaryc<strong>on</strong>diti<strong>on</strong>. The downstream temperature in the pipe isexpressed as [4]:T d , T u <strong>and</strong> T a represent the downstream fluidtemperature, upstream fluid temperature, <strong>and</strong> ambienttemperature respectively. M <strong>and</strong> K are parametersinclude the overall heat transfer coefficient. As theoverall heat transfer coefficients have to be calculatedbeforeh<strong>and</strong>, the influence of flow temperature variati<strong>on</strong><strong>on</strong> U s <strong>and</strong> U r al<strong>on</strong>g the pipeline is neglected. It is areas<strong>on</strong>able assumpti<strong>on</strong> when the thermal by-passtemperature is set close to the plant temperature,however, may cause appreciable errors if thetemperature drop al<strong>on</strong>g the network is high.It is worth to be noted that though the design returntemperature (22 o C) is higher than ground temperature,the net heat transfer in the return pipe may absorb heatfrom surrounding which makes U r negative. However,negative U r has to be set to zero as the simulati<strong>on</strong>program cannot h<strong>and</strong>le negative heat transfercoefficient.[3]RESULTS AND DISCUSSIONFig. 6 <strong>District</strong> heating networkThe supply <strong>and</strong> return pipe are assumed identical <strong>and</strong>placed horiz<strong>on</strong>tally in the same depth from the ground.The linear thermal transmittance U ij reduces toU 11 =U 22 =U 1 <strong>and</strong> U 12 =U 21 =U 2 . In additi<strong>on</strong>, the thermalc<strong>on</strong>ductivity of insulati<strong>on</strong> foam was assumed c<strong>on</strong>stant.U 1 <strong>and</strong> U 2 were then calculated with the analyticalsoluti<strong>on</strong> developed from the multi-pole method [10].The simulati<strong>on</strong> program cannot h<strong>and</strong>le two heattransfer coefficients in the same pipe, U s <strong>and</strong> U r werederived to represent the overall heat transferHeat ExchangerNetwork simulati<strong>on</strong> starts from proper selecti<strong>on</strong> of pipedimensi<strong>on</strong>, based <strong>on</strong> the design c<strong>on</strong>diti<strong>on</strong> <strong>and</strong> thedesign criteria introduced in the previous secti<strong>on</strong>.Table 2 shows the selected pipe types <strong>and</strong>corresp<strong>on</strong>ding length for three different cases. Case 1is the reference case. Flexible twin pipe Alx 20 to 32<strong>and</strong> steel twin pipe DN32 <strong>and</strong> DN 40 were selected.The third recirculati<strong>on</strong> pipe was designed in case 2based <strong>on</strong> the summer by-pass flow rate. Pressuregradient 1500 pa/m for street pipes <strong>and</strong> 500 pa/m formain pipes were set as the dimensi<strong>on</strong> criteria. Thoughsmaller pipe was suggested by the program, the Alx16single pipe was selected as the minimum diameter pipeavailable <strong>on</strong> the market. It was assumed that therecirculati<strong>on</strong> pipe can be used as water supply in winterin case 3. Therefore, the main pipes in the referenceline were re-designed with c<strong>on</strong>sidering that a porti<strong>on</strong> ofsupply water goes through the recirculati<strong>on</strong> line. It canbe seen that the supply pipe has smaller diameter thanreturn pipe in some secti<strong>on</strong>s in the twin pipe line.76
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academic access is facilitated as t
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produce heat and electricity. Fluct
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