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>iaDESIGN OF LOW TEMPERATURE DISTRICT HEATING NETWORK WITH SUPPLYWATER RECIRCULATIONH<strong>on</strong>gwei Li 1 , Aless<strong>and</strong>ro Dalla Rosa 1 , Svend Svendsen 11 Civil Engineering Department, Technical University of DenmarkABSTRACTThe focus <strong>on</strong> c<strong>on</strong>tinuing improving building energyefficiency <strong>and</strong> reducing building energy c<strong>on</strong>sumpti<strong>on</strong>brings the key impetus for the development of the newgenerati<strong>on</strong> district heating (DH) system. In the newgenerati<strong>on</strong> DH network, the supply <strong>and</strong> returntemperature are designed low in order to significantlyreduce the network heat loss. Meanwhile, the lownetwork operati<strong>on</strong>al temperature can make a betterutilizati<strong>on</strong> of renewable energy <strong>and</strong> further improve theCHP plant efficiency.Though the designed return temperature is low, it mayincrease c<strong>on</strong>siderably when the heating load becomeslow <strong>and</strong> the by-pass system starts to functi<strong>on</strong>. The aimof this paper is to investigate the influence of by-passwater <strong>on</strong> the network return temperature <strong>and</strong> introducethe c<strong>on</strong>cept of supply water recirculati<strong>on</strong> into thenetwork design so that the traditi<strong>on</strong>al by-pass systemcan be avoided. Instead of mixing the by-pass waterwith return water, the by-pass water is directed to aseparated circulati<strong>on</strong> line <strong>and</strong> returns back to the plantdirectly. Different pipe design c<strong>on</strong>cepts were tested <strong>and</strong>the annual thermal performances for a selectedresidential area were evaluated with the commercialprogram TERMIS. The simulati<strong>on</strong> program calculatesthe heat loss in the twin pipe as that in the single pipe.The influence of this simplificati<strong>on</strong> <strong>on</strong> the supply/returnwater temperature predicti<strong>on</strong> was analyzed by solvingthe coupled differential energy equati<strong>on</strong>s.INTRODUCTIONIn European Uni<strong>on</strong>, <strong>on</strong>e of the major energydevelopment targets is to reduce the building energyc<strong>on</strong>sumpti<strong>on</strong> <strong>and</strong> increase the supply of renewableenergy. The introducti<strong>on</strong> of European EnergyPerformance of Building Directive (EPBD) posesstringent requirement for the member countries toeffectively reduce their building energy c<strong>on</strong>sumpti<strong>on</strong>.According to the nati<strong>on</strong>al energy policy, the buildingenergy c<strong>on</strong>sumpti<strong>on</strong> in Denmark will drop to 25% ofcurrent level by the year 2060, while the renewableenergy share will increase from 20% to 100% at themeantime [1].<strong>District</strong> heating (DH) benefits from ec<strong>on</strong>omic of scalewith mass producti<strong>on</strong> of heat from central heatingplants. The significant reducti<strong>on</strong> of building energyc<strong>on</strong>sumpti<strong>on</strong> <strong>and</strong> wide exploitati<strong>on</strong> of waste heat <strong>and</strong>renewable energy, however, makes the current DH73technologies become barriers to further increase themarket share [2]. In order to sustain the ec<strong>on</strong>omiccompetiveness <strong>and</strong> realize the l<strong>on</strong>g term sustainabledevelopment, the c<strong>on</strong>cept of design <strong>and</strong> operati<strong>on</strong> ofDH system needs to be re-examined under the newenergy regulati<strong>on</strong> <strong>and</strong> development trends. This is themain impetus for the development of the newgenerati<strong>on</strong> DH system. Based <strong>on</strong> previous studies, in aproperly designed in-house substati<strong>on</strong> system, thenetwork supply temperature at 55oC <strong>and</strong> returntemperature at 20oC can meet the c<strong>on</strong>sumer spaceheating <strong>and</strong> domestic hot water dem<strong>and</strong> [3].The low return temperature has the advantages toreduce the network heat loss, increase CHP plantpower generati<strong>on</strong> capability, <strong>and</strong> utilize direct flue gasc<strong>on</strong>densati<strong>on</strong> for waste heat recovery. However, thereturn temperature can become much higher than thedesigned value when the heating load becomes low<strong>and</strong> the by-pass system at the critical user starts tofuncti<strong>on</strong>. In this paper, the influence of by-pass water<strong>on</strong> network return temperature was examined for areference residential area. The c<strong>on</strong>cept of supply waterrecirculati<strong>on</strong> was introduced to avoid the mixing of bypasswater <strong>and</strong> the return water. Three network designmethods were tested. The annual thermal performancewas evaluated with the commercial district heatingnetwork hydraulic <strong>and</strong> thermal simulati<strong>on</strong> softwareTERMIS [4]. The simulati<strong>on</strong> program calculates theheat loss in the twin pipe as that in the single pipe. Theinfluence of this simplificati<strong>on</strong> <strong>on</strong> the supply/returnwater temperature predicti<strong>on</strong> was analyzed by solvingthe coupled differential energy equati<strong>on</strong>s.SUPPLY WATER RECIRCILUATIONThe soluti<strong>on</strong> to overcome the excessive temperaturedrop al<strong>on</strong>g the supply pipe due to reduced flow rate isto install by-pass system at the critical user in thenetwork. Figure 1 shows the principle of supply waterby-pass. Extra flow is called based <strong>on</strong> the temperaturemeasurement at the critical user until the minimumsupply temperature requirement is met. This extra flowis then ―by-passed‖ <strong>and</strong> sends back to the return pipe.As the by-pass flow rate may be c<strong>on</strong>siderable <strong>and</strong> itstemperature is high, the mixing with return water willsignificantly increase the return water temperaturewhich causes both increased heat loss in the returnpipeline <strong>and</strong> decreased power generati<strong>on</strong> capability inthe CHP plant.
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>iaA desirable design approach is to maintain the by-passsystem as the flow rate adjuster, while avoids themixing of the by-pass water <strong>and</strong> the return water. Thisdesign c<strong>on</strong>cept is schematically shown in Fig. 2, whichis realized through adding a third pipeline for supplywater re-circulati<strong>on</strong>. When the by-pass water is called,the circulati<strong>on</strong> line will transfer the extra supply waterback to the plant where it is re-heated up to the supplytemperature again. On the other h<strong>and</strong>, the additi<strong>on</strong> ofthe 3rd pipeline provides the possibility to supply waterin two supply lines when the heat dem<strong>and</strong> is high. Thenetwork, therefore, can be designed as two supplylines with reduced diameter together with <strong>on</strong>e returnline.Fig. 3 Annual heating load (blue columns) <strong>and</strong> durati<strong>on</strong>hours (red curve) at different ground temperatureNETWORK SIMULATIONFig. 1 Schematic for hot water by-pass systemFig. 2 Schematic for by-pass water recirculati<strong>on</strong><strong>Heating</strong> LoadThe simulati<strong>on</strong> was performed for a reference area with81 low energy dem<strong>and</strong> houses. The house wasdesigned based <strong>on</strong> the building st<strong>and</strong>ard Class 1,following the Danish Building Regulati<strong>on</strong>. The domestichot water draw-off profile was designed similar to theDanish st<strong>and</strong>ard DS439 [5]. Detailed space heating<strong>and</strong> domestic hot water heating load simulati<strong>on</strong> can befound from [6, 7]. Figure 4 shows the averaged heatingload <strong>and</strong> the corresp<strong>on</strong>ding durati<strong>on</strong> hours. The annualheating load is divided into 8 intervals, varying as afuncti<strong>on</strong> of undisturbed ground temperatures whichranges from 0 to 15 ºC. The summer seas<strong>on</strong> lasts 3281hours <strong>and</strong> the heating load comes <strong>on</strong>ly from thedomestic hot water dem<strong>and</strong>. The space heating isrequired for the rest of the year.House Installati<strong>on</strong>sTwo house installati<strong>on</strong>s were c<strong>on</strong>sidered in this study.Figure 4 shows the instantaneous heat exchanger (HE)in the DH system. Without a buffer tank, the branchpipe which c<strong>on</strong>nects directly to the HE installati<strong>on</strong> musthave the capability to supply the instantaneous hotwater dem<strong>and</strong> without causing significant pressuredrop, which otherwise can be compromised byinstalling a booster pump. The HE design load is 32kWper houses at the network supply temperature 55oC<strong>and</strong> return temperature 22 ºC. On the other h<strong>and</strong>,simultaneous factors which are the probabilities formultiple users‘ c<strong>on</strong>current use of hot water arec<strong>on</strong>sidered for the design of street pipes <strong>and</strong> mainpipes, as shown in Table 1 [3]. Fig. 5 shows thedomestic hot water storage tank (DHWS) in the DHsystem. The DHWS design load is 8 kW per house. Toavoid the legi<strong>on</strong>ella problem, the design temperaturefor DHWS is higher than HE, at 65 ºC /30 ºC for supply<strong>and</strong> return respectively.74
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academic access is facilitated as t
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1. CHP system operation in A2. Ther
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is covered by operating HOB. In oth
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produce heat and electricity. Fluct
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