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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>iashell <strong>and</strong> surrounding soil is less than 0.005 °C for twoc<strong>on</strong>secutive calculati<strong>on</strong>s. The‖st<strong>and</strong>ard‖ <strong>and</strong>―advanced‖ model are available <strong>on</strong>line [14]. In the―FEM advanced‖ model we directly implementedequati<strong>on</strong> (1) in the insulati<strong>on</strong> domain, instead. Theresults indicate that in case of low-temperatureoperati<strong>on</strong>, lower total heat losses are calculated if thetemperature-dependency of the insulati<strong>on</strong> lambdavalueis taken into account. Moreover the heat transferbetween the pipes in twin or triple pipes can beproperly evaluated.Total Heat Loss [W/m]7.06.05.04.03.02.01.00.0DN 14 DN 16 DN 20 DN 26 DN 32 DN 40St<strong>and</strong>ard 3.61 4.24 4.62 5.71 6.45FEM St<strong>and</strong>ard 3.34 3.68 4.33 4.80 6.02 6.76Advanced 2.86 3.36 3.69 4.55 5.10FEM Advanced 3.19 3.51 4.14 4.59 5.75 6.47(Aluflex: ≤ DN 26, steel: ≤ DN 50) the best design is toput the supply pipe in the centre of the casing, assuringthe best possible insulati<strong>on</strong> for the supply pipe. Thisstrategy guarantees also the lowest temperature dropin the supply side, which is a critical figure inlow-temperature applicati<strong>on</strong>s.For bigger sizes (Aluflex: ≥ DN 26, steel: ≥ DN 50) thebest design is achieved by ―moving up‖ the media pipelayout <strong>and</strong> at the same time by keeping the samedistance between the media pipes as in thesymmetrical case.Double pipesA double pipe c<strong>on</strong>sists of a pair of media pipes ofdissimilar size, co-insulated in the same casing. It is afurther development of the twin pipe c<strong>on</strong>cept. A sketchof a possible applicati<strong>on</strong> of the double pipe c<strong>on</strong>cept isshown in Figure 7. Though these measures, networkheat loss reducti<strong>on</strong> is possible, in case of operati<strong>on</strong>during low heating load periods.Figure 6: Comparis<strong>on</strong> of 4 different approaches for steadystateheat loss calculati<strong>on</strong>. Aluflex twin pipe series,supply/return/ ground temperatures: 55/25/8 °C.Asymmetrical insulati<strong>on</strong> in twin pipesThe results show that improvements are possible,thanks to asymmetrical insulati<strong>on</strong> (see Table 3). Weproved that a better design leads to lower heat lossesfrom the supply pipe (leading to a lower temperaturedrop); next, the heat loss from the return pipe can beclose to zero, maintaining isothermal c<strong>on</strong>diti<strong>on</strong>s in thereturn line. If commercial available casing sizes arekept, we suggest two design strategies, depending <strong>on</strong>the size of the pipes. For small pipe sizesTable 3: Comparis<strong>on</strong> between asymmetrical <strong>and</strong> symmetrical insulati<strong>on</strong> in twin pipes.The centre of the casing is the origin of the Cartesian system.Size(DN)14Coordinates(x; y) [mm]Heat loss[W/m]86Figure 7: Sketch of the possible applicati<strong>on</strong> of the doublepipe c<strong>on</strong>cept in a simple district heating network.The space heating dem<strong>and</strong> in summer is diminished,except for the energy requirement in bath roomheating. According to the energy balance, the reducedasymm.-symm. [%]Mat. Sup. Ret. Sup. Ret. Tot. Sup. Tot.(0; 0) (0; 27) 3.24 0.01 3.25 -7.6 2.016 (0; 0) (0; 28) 3.56 -0.01 3.55 -5.1 1.120Alx.(0; 0) (0; 30) 4.16 -0.04 4.12 -4.2 -0.326 (0; 0) (0; 36) 4.67 0.00 4.67 -5.1 1.932 (0; -16) (0; 28) 5.54 0.00 5.54 -5.8 -2.550(0; -25) (0; 55) 5.69 -0.03 5.66 -7.7 -2.4Steel65 (0; -36) (0; 60) 6.70 -0.02 6.68 -7.8 -3.2heating load requires lessnetwork flow rate as far as thedesigned building temperaturedrop is sustained. However, thereducti<strong>on</strong> of network flow ratewill increase the supply watertemperature drop al<strong>on</strong>g thepipeline due to heat loss. As ac<strong>on</strong>sequence, the supplytemperature at the end usermay lower down below theminimum requirement. Thisproblem is relevant to towenergyDH systems with analready low supply temperature.This design is based <strong>on</strong> the factthat the supply line acts also asre-circulati<strong>on</strong> line during low

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