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>iaComfort level is increased by applying a higher bypassthermostat setting <strong>and</strong>/or a ―hot‖ heat exchanger duringidle. Fig. 5 shows an example of flat stati<strong>on</strong> with ―hot‖heat exchanger <strong>and</strong> thermostatic c<strong>on</strong>trolled heatexchanger [7]. Idle temperature is approx. 50 °Ccorresp<strong>on</strong>ding to dhw tapping temperature.For simulati<strong>on</strong>s a branch pipe flow (Q1) of 800 l/h isassumed. This represents a situati<strong>on</strong> where thethermostat is fully open until the desired set temperatureis reached. Further a step vice flow change from zero toQ1 or zero to Q2 is assumed. Tapping flow is assumedto be <strong>on</strong> a high level flow for <strong>on</strong>e tap, which is typicallyapplied when opening the dhw. Q2=400 l/h for allsimulati<strong>on</strong>s.161412Delay until reaching 45°CL2=5m & 10m (internal ø10mm) - Heat Exchanger hot & cold at idlehot - dt at T2 - L2=5mhot - dt at T4 - L2=5mcold - dt at T3 - L2=5mcold - dt at T4 - L2=10mhot - dt at T3 - L2=5mhot - dt at T4 - L2=10mcold - dt at T4 - L2=5mdT [sec]10864Fig. 5. Dynamic c<strong>on</strong>trol performance (idle recovery) forthermostatic c<strong>on</strong>trolled heat exchanger for dhw producti<strong>on</strong>.Heat exchanger is warm during idle. [7]Fig. 5 shows a flat system with ―hot‖ heat exchanger atidle. Bypass temperature setting corresp<strong>on</strong>ds to aprimary supply temperature (T11) of 58 °C <strong>and</strong> primaryreturn temperature (T12) of 44 °C. This setting is thehigh end, meaning in ―high‖ end regarding comfort. Forthis system there are no primary delays, <strong>and</strong> dhwtapping temperature at the flat stati<strong>on</strong> is available afterapprox. 2 sec. Additi<strong>on</strong>al delay due to dhw pipingtowards tap would be similar to previous example.In many practical matters a compromise between thetwo examples regarding idle temperature setting fulfilsdem<strong>and</strong>s for good comfort with reas<strong>on</strong>able energyc<strong>on</strong>sumpti<strong>on</strong>.In the following a general trade off is included betweenbranch pipe length, dhw pipe length, idle c<strong>on</strong>diti<strong>on</strong> forheat exchanger <strong>and</strong> temperature delay <strong>on</strong> dhw, based<strong>on</strong> dynamic simulati<strong>on</strong>s. Pipes are simplified by simpledelay models with no heat loss. Heat exchanger isbased <strong>on</strong> a lumped capacity model described in [5].200 1 2 3 4 5 6L1 [m] (internal ø20mm)Fig. 7. Dynamic simulati<strong>on</strong> for hot <strong>and</strong> cold heat exchangerduring idle. Delay (dt) for dhw temp. of 45 °C.Heat exchanger simulated is Danfoss XB06H-40 [6]. Itcan be seen from figure 7, that influence <strong>on</strong> hot or coldheat exchanger is in the range of 2 sec. delay. Branchpipe length (L1) has minor impact <strong>on</strong> time delay. This isdue to the fact that temperature is maintained with atemperature gradient al<strong>on</strong>g pipe during idle, reflectingT1 to T2. Basically water in branch pipe is heated to acertain level already before tapping. Anyhow, due toenergy loss <strong>and</strong> return temperature, idle bypasstemperature is lower than dhw tapping temperature inthis case.Main influence <strong>on</strong> time delay is dhw pipe diameter <strong>and</strong>length (L2). C<strong>on</strong>necti<strong>on</strong> in flats shall be of ―starcoupling‖ principle where every tap has its own supplypipe with a small inner diameter. Temperature in dhwpipe water is assumed to be room temperature prior totapping. In general, additi<strong>on</strong>al delays of typically 3 to 6sec<strong>on</strong>ds shall be expected due to thermal interacti<strong>on</strong>with thermal capacities al<strong>on</strong>g the way to tap <strong>and</strong>hydraulic dynamics <strong>on</strong> branch pipe side <strong>and</strong> hydraulicdynamics <strong>on</strong> dhw side.Simulated waiting time for a dhw temperature of 40 °Cis included in figure below:Fig. 6. Basic applicati<strong>on</strong> for flat stati<strong>on</strong>, including boundaryc<strong>on</strong>diti<strong>on</strong>s for dynamic simulati<strong>on</strong>s.19
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>iadT [sec]1614121086420Delay until reaching 40°CL2=5m & 10m (internal ø10mm) - Heat Exchanger hot & cold at idlehot - dt at T4 - l"=5mcold - dt at T4 - l2=5mcold - dt at T4 - L2=10mhot - dt at T4 - L2=10mcold - dt at T3 - L2=5m0 1 2 3 4 5 6L1 [m] (internal ø20mm)Fig. 7. Dynamic simulati<strong>on</strong> results for hot <strong>and</strong> cold heatexchanger during idle. Delay (dt) for dhw temp. of40 °C.First of all it can be seen that time delay for reaching40 °C at tap is <strong>on</strong>ly a bit shorter than reaching 45 °C.This is due to the fact that the T4 temperature profilehas an almost step vice nature, i.e. if temperature goesup after the dhw pipe is flushed through, it goes almostlike a step.Different dhw c<strong>on</strong>trollers have different performanceregarding time delay. In case of pure proporti<strong>on</strong>alc<strong>on</strong>trol for dhw system, time delay is l<strong>on</strong>ger at part load.This is because primary flow is proporti<strong>on</strong>al tosec<strong>on</strong>dary flow, <strong>and</strong> the lower the flow the l<strong>on</strong>ger thewaiting time. Looking at the example for Q1=800l/h,Q2=400 l/h, L1=4 m, L2=5 m then time delay (dt) at T4is 6.9 sec to reach 45 °C dhw temperature. In case ofproporti<strong>on</strong>al c<strong>on</strong>troller with parameters Q1=400 l/h,Q2=400 l/h, L1=4m, L2=5 m then dt=11.0 sec to reach45 °C. This has c<strong>on</strong>siderable effect <strong>on</strong> time delay as L1gets l<strong>on</strong>ger. In case of a thermostatically c<strong>on</strong>trolled dhwsystem or a combinati<strong>on</strong> of a thermostatically <strong>and</strong>proporti<strong>on</strong>ally c<strong>on</strong>trolled dhw system, time delay isshorter because no matter how small tapping is, as l<strong>on</strong>gas the desired set point temperature is not reached, theprimary valve will be fully or almost fully open resultingin high primary flow. Regarding delay to reach a dhwtemperature of 40 °C this is <strong>on</strong>ly related to dhw pipedimensi<strong>on</strong> since 40 °C is the bypass temperature if heatexchanger is hot during idle. In case the heat exchangeris cold during idle, then this introduces an additi<strong>on</strong>altime delay as described above. In all cases, time delayis dependent <strong>on</strong> dhw flow, resulting in delay in the dhwpipe.Hygienic c<strong>on</strong>siderati<strong>on</strong>sLegi<strong>on</strong>ella is a well-known bacterial risk for dhwsystems. Normally it is not the questi<strong>on</strong> whetherLegi<strong>on</strong>ella is present in the dhw system or not, butrather Legi<strong>on</strong>ella bacteria c<strong>on</strong>centrati<strong>on</strong> in the dhw.Facts influencing <strong>on</strong> potential for Legi<strong>on</strong>ellac<strong>on</strong>centrati<strong>on</strong> growth are dhw temperature, exchangerate of hot water in distributi<strong>on</strong> pipes, <strong>and</strong> volume ofdhw water in the entire hot system. Also other factorsare influencing, e.g. systematic cleaning of showeroutlets, but this will be not addressed to here, since theeffect is similar for c<strong>on</strong>cepts compared.Comparing volumes of dhw in pipes for c<strong>on</strong>cepts, theflats stati<strong>on</strong> soluti<strong>on</strong> has significantly lower volumecompared to the traditi<strong>on</strong>al system. Furthermore dhwpipes should be ―star‖ c<strong>on</strong>nected, meaning <strong>on</strong>e small(diameter) pipe from the flat stati<strong>on</strong> to each individualhot tap. This eliminates problematic dead end or lowflow areas.Typically volume of heat exchanger is 0.25 to 0.50 litre.Typical dhw pipe volume is 0.10 l/m, equal to 1.0 litre for10 m pipe. In total this is a volume of 1.5 to 2 litrepr. flat. The comparable centrally placed dhw systemwith dhw distributi<strong>on</strong> will have a volume of 5–7 litre pr.flat. By installing a dhw storage tank this will increasesignificantly. The German DVGW regulati<strong>on</strong>s states thatheating dhw up to 60 °C, due to e.g. Legi<strong>on</strong>ella, is notrequired if volumes of heat exchanger or volume of dhwpipes is less than 3 litres [8]. Based <strong>on</strong> those physicalc<strong>on</strong>cept differences Legi<strong>on</strong>ella bacteria risk is reducedfor the flat stati<strong>on</strong> c<strong>on</strong>cept.Future energy supply/dem<strong>and</strong> perspectiveOne important challenge for DH is to c<strong>on</strong>vert to 4thgenerati<strong>on</strong> DH systems. Intenti<strong>on</strong> is to realise efficientDH systems for urban areas where heat dem<strong>and</strong>s willdecrease due to modernisati<strong>on</strong> <strong>and</strong> new building energysaving codes. In this c<strong>on</strong>text <strong>on</strong>e way to go is to reducetemperatures in DH networks [9]/[10]. This allows forcost effective geothermal sources as well as otherrenewable low temperature sources. For dhw, normaltemperature level is 45 to 60°, where highertemperatures typically are based <strong>on</strong> c<strong>on</strong>siderati<strong>on</strong>stowards Legi<strong>on</strong>ella. A way to reduce temperature levelsin DH networks is to set dhw temperature at 45 °C. Bythis a primary temperature at sub stati<strong>on</strong> of 50 to 55 °Cwill be sufficient. A prec<strong>on</strong>diti<strong>on</strong> for this is to use heatexchangers for dhw producti<strong>on</strong>, like the flat stati<strong>on</strong>c<strong>on</strong>cept.CONCLUSIONThe two pipe flat stati<strong>on</strong> c<strong>on</strong>cepts, c<strong>on</strong>sisting ofdecentralised instantaneous dhw producti<strong>on</strong>, open thepossibility of reducing general DH net work temperature,which for the future will be even more relevant due todecreasing building heat dem<strong>and</strong> <strong>and</strong> increasedavailability of renewable energy. For building owners,the investigated case shows that the flat stati<strong>on</strong> c<strong>on</strong>ceptis <strong>on</strong> brake-even investment level compared to20
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