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Investigation on Relative Heat Losses and Gains of Heating and Cooling Networks

Abstract

The integration of district heating (DH) and cooling (DC) in the sustainable energy system of the future requires a significant reduction in operating temperatures. Supply temperatures below 70 °C are required for new 4th Generation DH. Main benefits are the use of low exergy heat sources and the reduction of heat losses. The reduction of heat losses is achieved by reducing the driving temperature difference between the medium pipe and the ground. The decrease of the return temperature level is limited by the consumer behaviour and the ground temperature level. As a consequence, the reduction of the supply temperature is accompanied by a reduction of the maximum transmittable heat flow. For energy efficiency and economic reasons, the relative heat losses are therefore an important design value for DH networks. The study proposes an approach to estimate the relative heat losses by using steady-state heat loss models and analyses the values for different DH generations. In particular, due to the rising of the near-surface soil temperature, the relative cold losses are also studied.

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Investigation on Relative Heat Losses and Gains of Heating and Cooling Networks

Author: Madan, Violeta,Weidlich, Ingo
Publisher: RTU Press
DOI: 10.2478/rtuect-2021-0035
Source: https://repos.hcu-hamburg.de/bitstream/hcu/659/1/10.2478_rtuect-2021-0035.pdf
En i onmen al and Clima e Technologies
2021, ol. 25, no. 1, pp. 479–490
h ps://doi.o g/10.2478/ uec -2021-0035
h ps://con en .sciendo.com
479
©2021 Viole a Madan, Ingo Weidlich.
This is an open access a icle licensed unde he C ea i e Commons A ibu ion License (h p://c ea i ecommons.o g/
licenses/by/4.0).
In es iga ion on Rela i e Hea Losses and Gains o
Hea ing and Cooling Ne wo ks
Viole a MADAN1*, Ingo WEIDLICH2
1, 2 Ha enCi y Uni e si y, Henning-Vosche au-Pla z 1, Hambu g, 20457, Ge many
Abs ac – The in eg a ion o dis ic hea ing (DH) and cooling (DC) in he sus ainable ene gy
sys em o he u u e equi es a signi ican educ ion in ope a ing empe a u es. Supply
empe a u es below 70 °C a e equi ed o new 4 h Gene a ion DH. Main bene i s a e he use
o low exe gy hea sou ces and he educ ion o hea losses. The educ ion o hea losses is
achie ed by educing he d i ing empe a u e di e ence be ween he medium pipe and he
g ound. The dec ease o he e u n empe a u e le el is limi ed by he consume beha iou
and he g ound empe a u e le el. As a consequence, he educ ion o he supply empe a u e
is accompanied by a educ ion o he maximum ansmi able hea low. Fo ene gy e iciency
and economic easons, he ela i e hea losses a e he e o e an impo an design alue o DH
ne wo ks. The s udy p oposes an app oach o es ima e he ela i e hea losses by using s eady-
s a e hea loss models and analyses he alues o di e en DH gene a ions. In pa icula , due
o he ising o he nea -su ace soil empe a u e, he ela i e cold losses a e also s udied.
Keywo ds – Cold losses; dis ic cooling; dis ic hea ing; hea losses
Nomencla u e
A C oss-sec ional a ea m²
cp Hea capaci y J/(kgK)
D Hal o he dis ance be ween he pipe axes m
di, do Inne and ou e insula ion diame e m
h Hea loss ac o –
T Tempe a u e K
Q

Hea low a e W
q Leng h ela ed hea low W/m
ν Flow eloci y m/s
λg, λi Hea conduc i i y o he g ound and insula ion W/(mK)
H Bu ial dep h m
R The mal Resis ance mK/W
1. INTRODUCTION
Dis ic hea ing (DH) and dis ic cooling (DC) can mainly con ibu e o a sus ainable
ene gy sys em based on enewable ene gy p oduc ion. The empo al and local uncoupling o
*Co esponding au ho .
E-mail add ess: iole a.madan@hcu-hambu g.de
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he demand and supply a e ad an ageous o he in eg a ion o enewable ene gy sou ces and
he sec o coupling app oach [1]. O he bene i s a e he signi ican imp o emen o he ene gy
e iciency o high popula ion densi y a eas and mo e lexible exchange o he ene gy sou ce.
The de elopmen o DH ex ends o e ou gene a ions and includes he op imiza ion o
ma e ials, hea sou ces, pipe design and ope a ing condi ions. Dec easing o he ope a ing
empe a u e is one o he main objec i es o newe DH gene a ions, as a lowe empe a u e
le el a ou s he in eg a ion o low empe a u e hea sou ces and he educ ion o hea losses.
Lund e al. de ine a supply empe a u e le el below 100 °C o he 3 d and 30–70 °C o he
4 h Gene a ion DH [1].
The hea losses and gains a e he main in luencing pa ame e s o design and e iciency o
a DH o DC sys em. I is a majo in e es o minimize he hea losses (and gains in case o
DC) o ene gy sa ings and economic easons. Addi ional app oaches o dec ease hea losses
a e he imp o emen o he pipe insula ion and he applica ion o win o iple pipes [2].
Howe e , lowe ope a ion empe a u es p omise he highe impac compa ed o ma e ial
changes in he pipe sys ems.
Fo he de e mina ion o s eady–s a e hea losses, analy ic solu ions [3] and explici
solu ions o speci ic geome ies a e a ailable [4], [5]. The explici solu ion o Wallen én is
implemen ed in DIN EN 13941–1, which ep esen s he s a e o he a o he hea loss
calcula ion in dis ic hea ing [6]. Wallen én p oposes an explici solu ion o one o wo
insula ed pipes and win pipes in he g ound by applying he mul ipole me hod [5]. K isgaa d
and Had ig in oduce a co ec ed dep h o he pipe axis o conside he hea ans e
coe icien a he g ound su ace [4]. This assump ion is also adap ed in DIN EN 13941–1
[6]. The model o K isgaa d and Had ig has been e alua ed by Oppel e al. o DH and DC
alica ion. In [7] a maximum de ia ion o 2.0–2.7 % o DH and 3.8–6.2 % o DC was
epo ed o he K isgaa d/Had ig model compa ed o simula ions wi h he ini e olume
me hod in he case o wo insula ed single pipes.
Bøhm e iewed di e en me hods o he calcula ion o s eady–s a e hea losses and
obse ed he undis u bed empe a u e o he g ound as a c i ical alue o he exis ing s eady–
s a e models. In his s udy, he did expe imen s and FEM simula ions o ind he loca ion o an
undis u bed g ound empe a u e ha can be applied in he s eady-s a e heo y o achie e
accep able accu acy. He ound he loca ion o his empe a u e app oxima ely a he op o
he casing o p einsula ed pipes [8]. Howe e , o he esea che s showed a measu able
inc ease o he empe a u e nea o DH pipes in he ield [9], [10]. Ano he ac o is he change
in he nea –su ace empe a u e ield due o clima e change, u baniza ion and he mal
exposu e o he soil. Henning and Limbe g ound a g ound empe a u e ise o mo e han 4 K
in u ban egions compa ed o u al egions in Be lin [11].
Rega ding low empe a u e DH, wo e ec s ha e o be conside ed: The dec ease o he
supply (and e u n) empe a u e on he one hand and he dec ease o empe a u e g adien
be ween he e u n and supply pipe on he o he hand. The educ ion o he supply empe a u e
le el goes along wi h a signi ican educ ion o he absolu e hea losses o he sys em. The
dec ease o empe a u e g adien be ween he supply and e u n pipe educes he ans e ed
hea ene gy o he consume . This loss o pe o mance could be compensa ed by he end o
low ene gy buildings [1]. S a egies o supply exis ing buildings wi h empe a u es below
70 °C a e desc ibed in [12]. In his con ex he ela i e hea losses may be he main design
alue o new DH gene a ions.
The ela i e hea losses a e usually calcula ed depending on he annual hea consump ion
[13] o by a de ailed modelling o he speci ic ne wo k [14], [15]. I no measu emen s o he
consump ion da a a e a ailable, he es ima ion o he annual demand o space hea ing and
domes ic ho wa e is p one o e o s [13], [14]. The s udy p oposes an app oach o es ima e
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ela i e hea losses and gains by applying s eady–s a e hea loss models. The calcula ion
me hod can easily be adap ed by he ne wo k ope a o o ge a i s imp ession o he ne wo k
e iciency and capaci y equi ed o he hea p oduc ion. In he ollowing s udy, he ela i e
hea losses a e calcula ed wi h he p oposed me hod and he esul s a e compa ed o di e en
gene a ions DH ne wo ks and DC. Hea ing and cooling ne wo ks in Hambu g and
su oundings ha e been selec ed o c ea e ealis ic bounda y condi ions o he calcula ions.
2. METHODOLOGY
In he ollowing, he da abase, he hea loss models and he model pa ame e s applied o
he calcula ions will be desc ibed.
2.1. Da abase
Hambu g’s DH ne wo k and se e al o he local hea ing ne wo ks a e co e ing abou a
qua e o he hea ing demand o he ci y. The he mal egis e o Hambu g p o ides an
o e iew o he hea ing ne wo ks and ope a o s [16]. Fo he in es iga ion o he hea losses,
di e en hea ne wo ks a e selec ed ha mee he empe a u e equi emen s o he second,
hi d and ou h DH gene a ions [1]. Hambu g’s DH ne wo k p o ides a supply empe a u e
o 133 °C o he s anda d ou e empe a u e o −12 °C o Hambu g acco ding o he na ional
annex o DIN EN 12831 [17]. Due o his high empe a u e le el, Hambu g’s DH ne wo k is
classi ied as 2nd Gene a ion DH. To ep esen he 4 h Gene a ion DH (TS < 70 °C), he supply
and e u n empe a u es o a new esiden ial a ea ‘Waisengä en’ in Schwe in, a ci y in
no he n Ge many, ha e been selec ed o he s udy. The new esiden ial buildings in he a ea
o ‘Waisengä en’ is ope a ed by S ad we ke Schwe in GmbH, he public u ili y p o ide o
Schwe in [18]. The ene gy concep o he new buildings combines geo he mal hea supply
wi h home s a ions o egula e he domes ic ho wa e empe a u e [19].
The empe a u es o he dis ic and local hea ing ne wo ks selec ed o his s udy a e aken
om he o icial echnical connec ion condi ions o he ne wo k ope a o s [18], [20]–[22] and
a e summa ized in Table 1. The e u n empe a u es in he o icial echnical connec ion
condi ions a e maximum e u n empe a u es allowed by he ope a o s. Fo he ollowing
in es iga ion, a win e and summe case a e conside ed o in es iga e he ela i e hea losses
and gains o he sys ems.
TABLE 1. SELECTED HEATING AND COOLING NETWORKS
Sys em ope a o
Supply/ e u n
empe a u e win e case
(−12 °C)
Supply and e u n
empe a u e summe case
(20 °C)
Dis ic Hea ing
Gene a ion acco ding o
Lund e al. [1]
Wä me Hambu g GmbH 133/60 °C 90/20 °C 2nd
Innogy SE 100/55 °C 69/20 °C 3 d
HanseWe k Na u GmbH 80/45 °C 70/45 °C 3 d
S ad we ke Schwe in GmbH 56/35 °C 56/35 °C 4 h
Wä me Hambu g GmbH
(Cooling ne wo k) 8/15 °C 6/12 °C –
A highe accu acy o de e mina ion o hea losses and gains can be ob ained by knowing
he g ound empe a u e p o ile [23]. The e o e, his o ical wea he da a o Hambu g lis ed in
DIN 4710:2003–01 [24] has been applied in he s eady s a e hea loss models p esen ed in
sec ion 2.2. The g ound empe a u es in Janua y and July a e ep esen a i e o he win e
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and summe case. Fo he sake o a classi ica ion he esul ing empe a u e p o iles o
Hambu g we e d awn oge he wi h gene alized cu es acco ding o Dahlem in Fig. 1.
I is impo an o poin ou ha he wea he da a summa ized in DIN 4710:2003–01 [24] is
he a e age empe a u e o he yea s 1961–1990. Cu en wea he da a om he Ge man
Wea he Se ice (Deu sche We e diens ) [25] sugges s ha he g ound empe a u es sligh ly
inc eased in he las decades and he ambien empe a u e can ise up o 35 °C du ing he
summe season.
Fig. 1. G ound empe a u e p o iles o he ci y o Hambu g compa ed wi h cu es acco ding o Dahlem wi hou g ound
wa e [23], [24].
2.2. Model o S eady-S a e Hea Loss
Dis ic hea ing ne wo ks usually consis o wo insula ed symme ical bu ied pipes wi h a
ci cula c oss–sec ion as shown in Fig. 2. Fo he calcula ion o he s eady–s a e hea losses,
pu e hea conduc ion is usually assumed, while con ec ion, mois u e anspo and phase
changes a e neglec ed. O he assump ions a e homogeneous ma e ial p ope ies and no
he mal esis ances o he medium pipe and casing [10]. Radial hea conduc ion h ough he
insula ion o he g ound and be ween he pipes is he p ocess desc ibed by he mos s eady–
s a e hea loss models o DH applica ion. In he ollowing, he e m ‘hea loss’ e e s o he
leng h- ela ed hea loss in W/m i no o he wise speci ied in he ex .
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Fig. 2. Geome y o wo insula ed pipes in he g ound.
Wallen én desc ibes he hea loss o each DH pipe as a supe posi ion o symme ical and
an i–symme ical hea losses e e ing o he mul ipole me hod [3]. Thus, he hea losses o
he supply and e u n pipe can be calcula ed acco ding o Eq. (1) and Eq. (2).
,,
s sym s a s
qq q= +
(1)
,,
sym a
qq q= −
(2)
The symme ical and an i–symme ical hea losses (3) and (4) can be calcula ed by applying
he empe a u es Tsym and Ta de ined in Eq. (5) and Eq. (6).
( )2
sym sym g g sym
q TT h= − ⋅ πλ ⋅
(3)
2
a a ga
qT h= ⋅ πλ ⋅
(4)
2
s
sym
TT
T+
=
(5)
2
s
a
TT
T−
=
(6)
The i s –o de mul ipole o mula o calcula e he ecip ocal o he hea loss ac o o he
symme ical p oblem is de ined in Eq. (7). The o mula o he an i–symme ical hea loss
ac o is gi en in [5]. The dimensionless he mal esis ance pa ame e β is de ined in Eq. (8).
22 2
00 0
222
1
2
0
4416( )
4
ln ln 1 1
14
sym
o
dd d
D H DH
HH
hdD d
D
−

  
++

  

 ⋅+
  
 

= +β+ + −
 

 +β 
  +
−β 
(7)
ln
go
ii
d
d
λ
β= 
λ
(8)
Wallen én quan i ies he ela i e e o s o he calcula ed hea losses as less han 0.5 %,
when he i s o de o mulae a e used [5]. Fo he ollowing analysis, he Wallen én and
Tg, λg

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K isgaa d/Had ig model a e applied o calcula e he sys em hea losses. The wo models
di e in he calcula ion o he he mal soil esis ance and in he alue o he g ound
empe a u e. The co ec ed bu ied dep h implemen ed by K isgaa d and Had ig o conside
he hea ans e coe icien a he soil su ace is de ined in Eq. (9). Fo a de ailed desc ip ion
o he K isgaa d/Had ig model e e o [4].
*
0.0685
g
HH= + ⋅λ
(9)
The g ound empe a u e applied o he hea loss calcula ions is a key di e ence be ween
he Wallen én and K isgaa d/Had ig model. Wallen én p oposes he empe a u e on he
g ound su ace, while K isgaa d and Had ig apply he empe a u e a he g ound le el o he
pipe axis a ins alla ion dep h. To in es iga e he in luence o he g ound empe a u e on
calcula ed hea losses, he esul s ob ained by using he o iginal models a e p esen ed among
he esul s in sec ion 3. Bøhm in es iga ed he loca ion o an undis u bed g ound empe a u e
o s eady–s a e hea loss calcula ion o achie e accu a e esul s. The undis u bed g ound
empe a u e posi ion o p einsula ed pipes ound by Bøhm co esponds o he g ound
empe a u e a he op o he casing and is applied in his s udy. Fo his pu pose, he unc ion
equa ion o he ci y o Hambu g de i ed using he wea he da a in DIN 4710:2003–01 is
applied [24].
To calcula e he ela i e hea losses, he sum o he leng h ela ed hea losses (1) and (2) is
di ided by he maximum amoun o hea anspo ed in he ne wo k acco ding o he basic
equa ion o he modynamics (10). The ele an c oss–sec ional a ea A is he c oss–sec ional
a ea o he wa e pipe. Due o he s a iona y condi ion, only he ull load case is conside ed.
Acco ding o he AGFW (Ge man Dis ic Hea ing Associa ion), he s eady–s a e condi ion
is only applicable o ne wo k leng hs below 10 km [26].
()
p s
Q A c T T=ρ⋅ ⋅ ⋅ ⋅ −

(10)
The esul ing pa ame e p oposed in his s udy o es ima e ela i e hea losses is a
pe cen age hea loss pe me e o pipe leng h acco ding o Eq. (11). The co esponding uni
is %/m.

100%
s
qq
q
Q
+
= ⋅

(11)
2.3. Model Pa ame e s
The calcula ion pa ame e s a e selec ed acco ding o ypical ope a ing condi ions o DH
ne wo ks. Key pa ame e s a e summa ized in Table 2. The s eel pipe dimension o DN 200
can be applied o dis ic hea ing and cooling; he dimensions o he pipe and insula ion
comply wi h he s anda ds DIN EN 253 and DIN EN 17415–1 [27], [28].
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TABLE 2. CALCULATION PARAMETERS
Pa ame e Symbol Value
Hea conduc i i y o he g ound λg 1.2 W/(mK)
Hea conduc i i y o he insula ion λi 0.027 W/(mK)
C oss-sec ional a ea A 0.0346 m²
Hea capaci y o wa e cp 4190 J/(kgK)
Inne insula ion diame e di 0.219 m
Ou e insula ion diame e do 0.315 m
Dis ance be ween he pipe axes 2D 0.565 m
Bu ied dep h H 0.9575 m
Flow eloci y ν 1 m/s
3. RESULTS
Fo he ne wo ks lis ed in Table 1 he absolu e hea losses and gains calcula ed wi h he
Wallen én and K isgaa d/Had ig model a e isualized in Fig. 3 and Fig. 4, each o win e
and summe case. The esul s p esen ed in Fig. 2 and Fig. 3 a e ob ained by applying he
g ound empe a u es p oposed by he o iginal au ho s o isualize he in luence o he selec ed
g ound empe a u e on he hea losses. Fo he Wallen én model, a g ound su ace empe a u e
o 0.8 °C (win e ) and 18.5 °C (summe ) and o he K isgaa d/Had ig model 4.6 °C (win e )
and 14.9 °C (summe ) a e applied [24].
Fig. 3. Calcula ed hea losses – win e case.
0
10
20
30
40
50
60
70
80
0
10
20
30
40
50
60
70
80
133/60 100/55 80/45 56/35 8/15
Del a |supply- e u n|, K
Hea losses and cold gains, W/m
Ne wo k supply/ e u n empe a u e, °C
Win e
Wallen en model K isgaa d/Had ig model del aT supply- e u n
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Fig. 4. Calcula ed hea and cold losses – summe case.
Fig. 5. Calcula ed ela i e hea losses – win e case.
The esul ing hea losses ob ained wi h he Wallen én and K isgaa d/Had ig model show a
cons an de ia ion o abou 3 W/m. The ela i e de ia ion be ween he calcula ed hea losses
inc eases wi h dec easing empe a u e g adien be ween he wa e pipe and g ound
empe a u e. The ela i e de ia ion has a ange o 4–12 % o he DH and eaches he
maximum alue o 38 % o DC. The ela i e de ia ion be ween he wo models is less han
0.5 % i he same alue is applied o he g ound empe a u e.
-20
0
20
40
60
80
-10
-5
0
5
10
15
20
25
30
35
40
90/20 69/20 70/45 56/35 6/12
Del a |supply- e u n|, K
Hea -and cold losses, W/m
Ne wo k supply/ e u n empe a u e, °C
Summe
Wallen en model K isgaa d/Had ig model del aT supply- e u n
0
10
20
30
40
50
60
70
80
0
0.2
0.4
0.6
0.8
1
1.2
133/60 100/55 80/45 56/35 8/15
Del a |supply- e u n|, K
Rela i e hea losses and cold gains, %/km
Ne wo k supply/ e u n empe a u e, °C
Win e
el. hea losses el. cold gains del a T supply- e u n
a
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The Wallen én model wi h he undis u bed g ound empe a u e p oposed by Bøhm is
applied o de e mine he ela i e hea losses. The g ound le el o he op o he pipe casing
co esponds o a dep h o 0.8 m. The undis u bed g ound empe a u e esul s in 4 °C o he
win e case and 15.5 °C o he summe case. The esul ing ela i e hea losses pe kilome e
pipe leng h a e p esen ed in Fig. 5 and Fig. 6.
Fig. 6. Calcula ed ela i e hea - and cold losses – summe case.
4. DISCUSSION
In he p e ious sec ion he esul s ob ained by he Wallen én and K isgaa d/Had ig model
o s eady–s a e hea losses o di e en hea ing and one cooling ne wo k ha e been p esen ed
in Fig. 3 and Fig. 4. A cons an de ia ion o abou 3 W/m occu s be ween he esul s due o
di e en g ound empe a u es implemen ed in he o iginal models. As he hea losses a e
cons an ly dec easing wi h dec easing empe a u e g adien be ween he medium pipe and
g ound empe a u e, he ela i e de ia ion o he hea losses ises up o 38 % o he DC case.
These esul s o he di e en s eady–s a e models o low empe a u e DH and DC show he
signi icance o an accu a e selec ion o he undis u bed g ound empe a u e o hese
applica ions. In his con ex , an op imized g ound empe a u e posi ion o he 4 h Gene a ion
DH and o DC should be u he in es iga ed. The o e all end o dec easing hea losses o
newe DH gene a ions due o he dec ease o he d i ing empe a u e g adien be ween he
pipe and he g ound is con i med in he esul s o he win e and summe case. The ou line s
o he 90/20 °C and 69/20 °C ne wo ks in he summe can be explained by he lowe e u n
empe a u e o 20 °C compa ed o he o he in es iga ed hea ing ne wo ks.
In his wo k, he pe cen age hea loss pe me e o pipe leng h is p oposed as a pa ame e
o es ima e he ela i e hea losses and gains o a sys em. In Fig. 5 and Fig. 6 he ela i e hea
losses a e p esen ed o a win e and summe case.
In he win e case, he ela i e hea losses o he in es iga ed hea ing ne wo ks inc ease,
while he empe a u e le el is dec easing. As he absolu e hea losses dec ease as shown in
Fig. 3, he in luence o he slope o he anspo ed hea lux 𝑄𝑄󰇗 causes he ising end. Fo
0
20
40
60
80
100
0
0.2
0.4
0.6
0.8
1
90/20 69/20 70/45 56/35 6/12
Del aT |supply- e u n|, K
Rela i e hea -and cold losses, %/km
Ne wo k supply/ e u n empe a u e, °C
Summe
el. hea losses el. cold losses del aT supply- e u n