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Flexible dynamic model of PHEX for transient simulations in Matlab/Simulink using finite control volume method

Abstract

In order to improve the energy efficiency and control of heat pump systems, it is necessary to develop dynamic models that accurately simulate their real performance. In addition, these models will help to carry out future works of research, such as new low carbon refrigerant testing. Physics-based models follow a set of physics laws that characterize the model as the most accurate, versatile and robust to simulate different heat pump systems. Taking into account the fact that the dynamics of the elements that regulate mass flow (compressors and valves) are much faster than the dynamics of the components that regulate heat transfer (heat exchangers), the model complexity usually resides in the latter. This paper provides a detailed explanation of the physics-based dynamic model in Matlab/Simulink using the finite-control volume approach applied to a refrigerant-to-liquid plate heat exchanger. Dynamic experimental tests were developed to validate the model under four possible situations: condenser and evaporator heat exchangers working in both counter- and parallel-flow. In addition, an approximation of the number of finite control volumes required to reach a good accuracy, while maintaining a reasonable simulation time is presented. Simulation results show great accuracy when compared to experimental tests. It was proved by calculating the Normalized Residual Error, which is between 1.1 E-04 and 1.0 E-03 in all cases. It was also concluded that using twenty finite control volumes, there is good agreement between the accuracy of the results and the computational time.

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Flexible dynamic model of PHEX for transient simulations in Matlab/Simulink using finite control volume method

Author: Salazar Herrán, Erik,Martín Escudero, Koldobika,Del Portillo Valdés, Luis Alfonso,Flores Abascal, Iván,Romero Antón, Naiara
Publisher: Elsevier
Year: 2020
DOI: 10.1016/j.ijrefrig.2019.11.003
Source: https://addi.ehu.eus/bitstream/10810/65304/4/Manuscript%20before%20printing.pdf
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Flexible dynamic model o PHEX o ansien simula ions in
Ma lab/Simulink using ini e con ol olume me hod
E ik Salaza -He an, Koldobika Ma in-Escude o, Luis A. del Po illo-Valdes, I an
Flo es-Abascal, Naia a Rome o-An on
ENEDI Resea ch g oup, Depa men o The mal Enginee ing, Uni e si y o he Basque
Coun y (UPV/EHU), Plaza To es Que edo 1, 48013 Bilbao, Spain
Email: e ik.salaza @ehu.eus
Telephone numbe : + (34) 94 601 7322
ABSTRACT
In o de o imp o e he ene gy e iciency and con ol o hea pump sys ems, i is
necessa y o de elop dynamic models ha accu a ely simula e hei eal pe o mance.
In addi ion, hese models will help o ca y ou u u e wo ks o esea ch, such as new low
ca bon e ige an es ing.
Physics-based models ollow a se o physics laws ha cha ac e ize he model as he
mos accu a e, e sa ile and obus o simula e di e en hea pump sys ems. Taking in o
accoun he ac ha he dynamics o he elemen s ha egula e mass low (comp esso s
and al es) a e much as e han he dynamics o he componen s ha egula e hea
ans e (hea exchange s), he model complexi y usually esides in he la e .
This pape p o ides a de ailed explana ion o he physics-based dynamic model in
Ma lab/Simulink using he ini e-con ol olume app oach applied o a e ige an - o-liquid
pla e hea exchange . Dynamic expe imen al es s we e de eloped o alida e he model
unde ou possible si ua ions: condense and e apo a o hea exchange s wo king in
bo h coun e - and pa allel- low. In addi ion, an app oxima ion o he numbe o ini e
con ol olumes equi ed o each a good accu acy, while main aining a easonable
simula ion ime is p esen ed.
Simula ion esul s show g ea accu acy when compa ed o expe imen al es s. I was
p o ed by calcula ing he No malized Residual E o , which is be ween 1.1 E-04 and 1.0
E-03 in all cases. I was also concluded ha using wen y ini e con ol olumes, he e is
good ag eemen be ween he accu acy o he esul s and he compu a ional ime.
Keywo ds: Pla e hea exchange s; Dynamic modeling; Expe imen al alida ion; Fini e
con ol olume app oach; Re e sible hea pump sys ems; Ma lab/Simulink.
This is he accep ed manusc ip o he a icle ha appea ed in inal o m in In e na ional Jou nal o Re ige a ion 110 : 83-94
(2020) , which has been published in inal o m a h ps://doi.o g/10.1016/j.ij e ig.2019.11.003. © 2019 Else ie L d and IIR.
unde CC BY-NC-ND license (h p://c ea i ecommons.o g/licenses/by-nc-nd/4.0/)
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Nomencla u e
Symbols
A a ea [m2]
c speci ic hea [kJ kg-1 K-1]]
h en halpy [kJ kg-1]
ℎ󰇗 en halpy ime de i a i e [kJ kg-1 s-1]
L wid h o he pla es [m]
m mass [kg]
𝑚󰇗 mass low a e [kg s-1]
N numbe o ini e olumes [-]
P p essu e [kPa]
𝑃󰇗 p essu e ime de i a i e [kPa s-1]
𝑞󰇗 hea ans e a e [kW s-1]
ime [s]
T empe a u e [K]
V olume [m3]
x leng h o he pla es in he low di ec ion [m]
G eek le e s
𝛼 con ec ion hea ans e coe icien [kW m-2 K-1]
𝜕 pa ial de i a i e
𝜌 densi y [kg m-3]
𝜌󰇗 densi y ime de i a i e [kg m-3 s-1]
Subsc ip s
a e a e age p ope y
c c oss-sec ional a ea
h a cons an en halpy
i con ol olume index
in inle
ou ou le
p a cons an p essu e
R e ige an
s hea ans e a ea
S seconda y luid
W wall/pla e
Ac onyms
COP coe icien o pe o mance [-]
FCV Fini e Con ol Volume
GSHP G ound-Sou ce Hea Pump sys ems
HEX Hea Exchange s
HTC Hea T ans e Coe icien [kW m-2 K-1]
MB Mo ing Bounda y
NRE No malized Residual E o
PHEX Pla e Hea Exchange
RTF Real Time Fac o
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1. In oduc ion
Ene gy sus ainabili y is a global challenge ha needs o be achie ed in he coming yea s.
Di e en s eps ha e been aken owa ds his goal o e he las ew yea s, such as he
Pa is Ag eemen [1] and he Ho izon 2020 p og am [2]. Wi hin his challenge, Hea Pump
sys ems a e des ined o be one o he sys ems ha will help o achie e hese
in e na ionally p oposed goals. In ac , since 2009 in he Eu opean Union, a pa o he
ene gy p oduced by hese sys ems can be conside ed enewable [3].
G ound sou ce hea pump sys ems (GSHP) a e a ype o apo comp ession sys em
ha , d i en by elec ic ene gy, can hea o cool wa e o ai h oughou he yea by
ans e ing hea om o o a sou ce, such as he subsoil o a wa e ese oi [4]. These
sys ems ha e been p o ed o ha e be e ene gy pe o mance han ai sou ce hea pump
sys ems [5].
Imp o ing he pe o mance and con ol o hese sys ems is a key issue in making GSHP
an inc easingly compe i i e echnology as compa ed o con en ional hea ing and cooling
sys ems, as well as o eaching he abo e-men ioned ene ge ic sus ainabili y. In his
issue, hea pump manu ac u e s play a e y impo an ole in de eloping inno a i e
GSHP wi h upg aded p edic i e con ol sys ems and be e pe o mance. Ne e heless,
hea pump p o o ypes and expe imen al es s wi h new equipmen equi e a high
in es men and his is ime-consuming. Dynamic simula ion models and so wa e, which
could educe he cos s o new p oduc s and imp o e hei pe o mance [6], would be
bene icial all o e he wo ld, bu such models need o be accu a e, e sa ile and obus .
In his line, physics-based models a e an app op ia e solu ion. These kinds o model use
physical laws and pa ial de i a i es o simula e he dynamic beha io o he sys em,
p o iding g ea accu acy and he oppo uni y o simula e di e en componen s and
con igu a ions. Unde wood [7] e iewed GSHP simula ions, compa ing models based on
ans e unc ions and physics-based models, emphasizing he accu acy o he la e .
Simila ly, Rasmussen [8] compa ed physics-based and da a-based models, highligh ing
he e sa ili y o he o me .
The challenge when modeling a dynamic sys em usually lies in modeling he
componen s wi h as dynamics. In he case o hea pump sys ems, he hea exchange s
ha e much slowe dynamics han he componen s ha egula e he mass low a e, such
as comp esso s o al es.
Fo modeling hea exchange s (HEX) wi h physics-based models, di e en app oaches
and esolu ion me hods can be ound. Among o he s, wo o he mos commonly used
app oaches a e he mo ing-bounda y (MB) [9] and ini e-con ol olume (FCV) [10].
While FCV di ides he o al leng h o he HEX in o a ini e numbe o olumes o equal
size; he MB app oach di ides i in o a educed numbe o unequal and a iable size
ini e olumes. The sizes o hose ini e olumes a ies along he simula ion and depends
on a chosen p ope y, such as he mean oid ac ion [11].
Some compa isons be ween bo h app oaches ha e been p esen ed o e he las ew
yea s. Bendapudi e al. [12] compa ed hem in a shell-and- ube hea exchange o a
cen i ugal chille sys em. The esul s we e compa ed wi h expe imen al da a and i was
concluded ha , du ing s eady-s a es, MB was as e eaching equal accu acy.
Ne e heless, du ing ansien -s a es, he FCV o mula ion was ound o be mo e obus .
He schel e al. [13] made a compa ison be ween modeling an ai - o-liquid HEX wi h bo h
FVC and MB app oaches, concluding ha he compu a ional ime o MB was lowe han
4
ha o FCV, main aining a good o de o accu acy in bo h cases. Deside i e al. [14]
compa ed MB and FCV app oaches o simula e a pla e hea exchange (PHEX)
concluding he simila good g ade o accu acy o bo h model and highligh ing he lowe
compu a ional ime o he MB app oach. Simila conclusions we e eached by Bonilla e
al. [15] simula ing an e apo a o o a di ec sola s eam acili y. Rod iguez e al. [16]
compa ed ou di e en dynamic modeling pa adigms o an ai - o- e ige an e apo a o .
I was compa ed FCV app oach wi h h ee MB me hods: en halpy, oid ac ion and
densi y based MB. They highligh ed he ad an ages o he FCV me hod due o he no
need o swi ching igge s, h esholds o ole ances o each an accu a e esul s,
al hough i is done a he expenses o a highe compu a ional ime.
The MB app oach has been widely used in ai - o- e ige an HEX dynamic modeling, as
desc ibed in [8,17,18]. Fo ins ance, Ib ahim e al. [19] used i o p edic he ene gy
pe o mance o an ai sou ce hea pump wa e hea e . Simila ly, MB app oach has been
used o simula e liquid- o- e ige an HEX, such as [14,20]. Bell e al. [20] de eloped an
MB model o coun e low HEX aking in o accoun he luid phase change, bu was only
able o p edic s a iona y s a es. Chu e al. [21] we e able o model a coun e low PHEX
by using a MB-FCV coupling algo i hm.
Rega ding FCV app oach, Ozana e al. [22] implemen ed a dynamic model o a s eam
supe hea e HEX o an indus ial boile using he FCV app oach. I was alida ed o bo h
pa allel and coun e low connec ions. Ne e heless, as o a supe hea ed HEX, i was
no necessa y o model he phase change o he luids. Bendapudi e al. [23] de eloped
a cen i ugal chille sys em model using he FCV app oach o he shell-and- ube hea
exchange , ocusing on such aspec s as mesh dependence, in eg a o o de and s ep-
size. I was concluded ha an inc ease in he numbe o ini e con ol olumes inc eases
he simula ion accu acy up o a limi . S iha i e al. [24] analyzed he e ec o a bad
dis ibu ion o he low in o he pla e hea exchange (PHEX) channels o single-phase
luids using an FCV model. The ansien pe o mance o he ai side hea exchange o
an ai -wa e hea pump sys em unde condi ions o os ing was analyzed using a
dynamic FCV model by Gao e al. [25].
Two o he mos common modeling en i onmen s o physic-based models o HEX a e
Modelica [26] and Ma lab/Simulink [27]. In Modelica many esea ches ha e been ca ied
ou , bo h wi h MB and FCV app oach [14,15,28,29]. Mo eo e , some d awbacks o FCV
such as cha e ing [30] ha e been s udied concluding ha ha phenomenon would be
educed by using MB app oach [31].
Rega ding Ma lab/Simulink, among o he s [32,33], one o he mos known he mal
sys ems simula ion models a e in he oolbox The mosys [34]. I allows he use o
simula e di e en e ige a ion sys ems wi h di e en componen s such as ai - o-
e ige an condense s and e apo a o s o liquid- o- e ige an condense s and
e apo a o s. Howe e , his las ones only in pa allel low con igu a ion. These
componen s a e de eloped by using MB app oach, which make di icul o de elop a
liquid- o- e ige an HEX wi h coun e - low con igu a ion.
Taking all his in o conside a ion and o he bes o au ho s knowledge, a e ige an - o-
liquid HEX dynamic model ha includes phase-change phenomena (bo h condensa ion
and e apo a ion) and ha can be used indis inc ly o bo h coun e - low and pa allel- low
con igu a ions in Ma lab/Simulink en i onmen canno be ound in he li e a u e. This kind
o model allows calcula ions o be ca ied ou in GSHP, ha ing he possibili y o simula e
swi ching mode ope a ion. In addi ion, he ex ensi e use o Ma lab/Simulink so wa e
5
mus be aken in o accoun in he wo ld o he mal acili ies manu ac u e s, especially o
he de elopmen o con ol loops.
The main goal o his documen is o p esen a high accu acy dynamic model o simula e
ansi o y changes in PHEX ha can be connec ed in bo h pa allel and coun e - low.
Addi ionally, he model allows he same PHEX o wo k as a condense o e apo a o .
The go e ning equa ions o he model and i s ma ix o m a e de eloped in de ail.
Mo eo e , an example o he o mula ion o a h ee ini e con ol olumes PHEX o bo h
coun e and pa allel- low is p esen ed. Finally, he alida ion o he model unde di e en
expe imen al si ua ions is ca ied ou and a pa ame ic analysis o assess he in luence
o he numbe o FVC in he simula ion speed is done.
2. Model de elopmen
The model p esen ed is a dynamic model based on physical equa ions using a
dis ibu ed-pa ame e ini e olume modeling me hod de eloped in a Ma lab/Simulink
en i onmen . As we ha e al eady said, he de eloped model is able o simula e he
beha io o a e ige an - o-liquid PHEX unde di e en si ua ions. All hese si ua ions
a e g ouped unde he cases shown in Table 1. The go e ning equa ions p esen ed and
deal wi h he e a e equal o all o he said cases. Ne e heless, when he equa ions a e
disc e ized in o di e en ini e con ol olumes and b ough oge he in a ma ix o m,
depending on whe he he PHEX connec ions a e in coun e - low o pa allel- low, he
esul ing ma ices a e di e en . As he di ec ion o he e ige an is in e ed, wha was
he inle po o he e ige an becomes he ou le po and ice e sa, changing he sign
o some a iables o he ma ix. Addi ionally, he co ela ions o calcula ing he hea
ans e coe icien (HTC) o ob ain he hea ans e a es a e subo dina e o he wo king
mode o he PHEX, and hese a e di e en o he condense o e apo a o wo king
modes.
Table 1. Cases analyzed o PHEX wo king modes and connec ions
Case numbe
PHEX connec ions and wo king mode
Case 1
Coun e - low condense
Case 2
Pa allel- low condense
Case 3
Coun e - low e apo a o
Case 4
Pa allel- low e apo a o
2.1. Model equa ions
The equa ions used o desc ibe he dynamic, physical beha io o he luids inside he
PHEX a e now p esen ed. The ollowing assump ions ha e been aken in o accoun o
modeling he PHEX.
• P essu e d ops h ough he PHEX a e negligible.
• The maldis ibu ion o he luids is neglec ed.
• Axial hea conduc ion is negligible, so he p ope ies inside each ini e olume a e
conside ed o be uni o m.
• The PHEX is supposed o be pe ec ly insula ed om he su ounding
en i onmen .
• The luid low is modeled as one-dimensional in he longi udinal di ec ion.

6
The FCV app oach is used o ca y ou he simula ions. This model can cap u e he
beha io and dynamics inside hea exchange s in g ea de ail. The he mo-physical
g adien s and dis ibu ed pa ame e s o each small disc e iza ion o he hea exchange
can be ob ained.
2.1.1. Re ige an equa ions
The e ige an luid unde goes a phase change when i ci cula es h ough he PHEX. I
can be condensed, going om supe hea ed gas o sub-cooled liquid, o e apo a ed,
going om wo-phase luid o supe hea ed gas. Addi ionally, i can lea e he PHEX as a
wo-phase luid i he hea ans e ed be ween luids is insu icien o conclude he
condensa ion o e apo a ion p ocesses.
Du ing ansien s a es, he p ope ies o he e ige an luid change o e ime. In o de
o model he changes in he luid p ope ies, ene gy and mass conse a ion equa ions
a e applied o he e ige an luid. The momen um equa ion is no applied because, as
said be o e, he p essu e d op h ough he PHEX is negligible.
Eq. (1) and (2) p esen he mass and ene gy conse a ion equa ion applied o he
e ige an luid espec i ely.
The ollowing s eps a e ollowed o ans o m bo h equa ions:
• Apply 𝑐𝑅𝑇𝑅=ℎ𝑅 equali y o calcula e he en halpy a ia ion ins ead o empe a u e
a ia ion.
• In eg a e o e he leng h o he con ol olume, which in his case is he o al leng h o
he hea exchange .
• Apply he Leibniz in eg al ule [36].
• Assume a e age alues o luid and pla e p ope ies inside he PHEX.
• Sol e ime de i a i es.
• Take he en halpy and he p essu e as he independen a iables o calcula e he
densi y ime de i a i e.
Now, he mass conse a ion equa ion and ene gy conse a ion equa ion applied o he
e ige an luid has been modi ied in o de o be implemen ed in a simula ion code.
whe e |𝜕𝜌
𝜕𝑃|ℎ ep esen s he e ige an densi y a ia ion wi h espec o he p essu e
a ia ion a cons an en halpy and |𝜕𝜌
𝜕ℎ|𝑃 ep esen s he e ige an densi y a ia ion wi h
espec o he en halpy a ia ion a cons an p essu e [37].
𝜕(𝜌𝑅𝐴𝑐)
𝜕𝑡 +𝜕(𝑚󰇗𝑅)
𝜕𝑥 =0
(1)
𝜕(𝜌𝑅𝑐𝑅𝐴𝑐𝑇𝑅)
𝜕𝑡 −𝜕(𝐴𝑐𝑃𝑅)
𝜕𝑡 +𝜕(𝑚󰇗𝑅𝑐𝑅𝑇𝑅)
𝜕𝑥 =𝛼𝑅𝐿(𝑇𝑅−𝑇𝑊)
(2)
(|𝜕𝜌
𝜕𝑃|ℎ𝑉)𝑃󰇗𝑅+(|𝜕𝜌
𝜕ℎ|𝑃𝑉)ℎ󰇗𝑅+𝑚󰇗𝑅,𝑜𝑢𝑡−𝑚󰇗𝑅,𝑖𝑛=0
(3)
(|𝜕𝜌
𝜕𝑃|ℎℎ𝑅,𝑎𝑣𝑒−1)𝑉𝑃󰇗𝑅+(|𝜕𝜌
𝜕ℎ|𝑃ℎ𝑅,𝑎𝑣𝑒+𝜌𝑅,𝑎𝑣𝑒)𝑉ℎ󰇗𝑅+𝑚󰇗𝑅,𝑜𝑢𝑡ℎ𝑅,𝑜𝑢𝑡−𝑚󰇗𝑅,𝑖𝑛ℎ𝑅,𝑖𝑛
= 𝛼𝑅𝐴𝑠(𝑇𝑅−𝑇𝑊)
(4)
7
Implemen ing Eq. (3) and Eq. (4) oge he in a simula ion code, he a ia ion o he
e ige an p ope ies du ing ansien s a es can be p edic ed.
2.1.2. Seconda y luid equa ions
The eloci y and he densi y o he seconda y luid, gene ally wa e , a e assumed o be
cons an all along he hea exchange . This means he equa ion o he mass conse a ion
does no need o be applied o he seconda y luid.
Eq. (5) p esen s he ene gy conse a ion equa ion o he seconda y luid. Unlike he
e ige an luid, he seconda y luid will emain in a liquid phase h oughou he PHEX.
The e o e, he empe a u e a ia ion can be di ec ly calcula ed ins ead o en halpy
a ia ion.
Since he seconda y luid is assumed o be an incomp essible luid, he a ia ion in he
p essu e is neglec ed. The e o e, he pa ial de i a i e o he p essu e in e ms o he
ime does no appea in Eq. (5).
𝜕(𝜌𝑆𝐴𝑐𝑐𝑆𝑇𝑆)
𝜕𝑡 +𝜕(𝑚󰇗𝑆𝑐𝑆𝑇𝑆)
𝜕𝑥 =𝛼𝑆𝐿(𝑇𝑊−𝑇𝑆)
(5)
In eg a ing each e m o he equa ion o e he leng h o he PHEX, assuming a e age
p ope ies inside he PHEX and sol ing he ime de i a i es, Eq (6) is ob ained.
𝑉𝜌𝑆,𝑎𝑣𝑒𝑐𝑆,𝑎𝑣𝑒𝑇󰇗𝑆+𝑚󰇗𝑆𝑐𝑆,𝑎𝑣𝑒(𝑇𝑆,𝑜𝑢𝑡−𝑇𝑆,𝑖𝑛)= 𝛼𝑆𝐴𝑠(𝑇𝑊−𝑇𝑆)
(6)
By implemen ing Eq. (6) in a simula ion code, he seconda y luid empe a u e a ia ion
in a HEX can be calcula ed wi h espec o he ime.
2.1.3. Hea exchange pla e equa ions
The empe a u e a ia ion o he hea exchange pla e is desc ibed by applying he
ene gy conse a ion equa ion. I is p esen ed in Eq. (7) and no ans o ma ions a e
needed.
𝑐𝑊𝑚𝑊𝑇󰇗𝑊=𝛼𝑅𝐴𝑠(𝑇𝑅−𝑇𝑊)−𝛼𝑆𝐴𝑠(𝑇𝑆−𝑇𝑊)
(7)
The empe a u e o he pla e depends on he mass, he he mal p ope ies o he pla e
ma e ial and he hea ans e ed o o om bo h e ige an and seconda y luids.
2.2. Model implemen a ion
Once he necessa y equa ions ha e been ans o med in o empo al de i a i e
equa ions, hey a e hen disc e ized o use wi h he FCV app oach. Fo an 𝑁 ini e
numbe o con ol olumes, Eqs. (3), (4), (6) and (7) a e ans o med in o Eqs. (8) - (11).
𝑉𝑐𝑣[(|𝜕𝜌
𝜕𝑃|ℎ)𝑖ℎ𝑅,𝑖−1]𝑃󰇗𝑅+𝑉𝑐𝑣[(|𝜕𝜌
𝜕ℎ|𝑃)𝑖ℎ𝑅,𝑖+𝜌𝑅,𝑖]ℎ󰇗𝑅,𝑖+𝑚󰇗𝑅,𝑜𝑢𝑡,𝑖ℎ𝑅,𝑜𝑢𝑡,𝑖
−𝑚󰇗𝑅,𝑖𝑛,𝑖ℎ𝑅,𝑖𝑛,𝑖= 𝛼𝑅,𝑖𝐴𝑠,𝑐𝑣(𝑇𝑅,𝑖−𝑇𝑊,𝑖)
(8)
𝑉𝑐𝑣(|𝜕𝜌
𝜕𝑃|ℎ)𝑖𝑃󰇗𝑅+𝑉𝑐𝑣(|𝜕𝜌
𝜕ℎ|𝑃)𝑖ℎ󰇗𝑅,𝑖+𝑚󰇗𝑅,𝑜𝑢𝑡,𝑖−𝑚󰇗𝑅,𝑖𝑛,𝑖=0
(9)
𝑉𝑐𝑣𝜌𝑆,𝑖𝑐𝑆,𝑖𝑇󰇗𝑆,𝑖+𝑚󰇗𝑆,𝑖𝑐𝑆,𝑖(𝑇𝑆,𝑜𝑢𝑡,𝑖−𝑇𝑆,𝑖𝑛,𝑖)= 𝛼𝑆,𝑖𝐴𝑠,𝑐𝑣(𝑇𝑊,𝑖−𝑇𝑆,𝑖)
(10)
8
𝑐𝑊,𝑐𝑣𝑚𝑊,𝑐𝑣𝑇󰇗𝑊,𝑖=𝛼𝑅,𝑖𝐴𝑠,𝑐𝑣(𝑇𝑅,𝑖−𝑇𝑊,𝑖)−𝛼𝑆,𝑖𝐴𝑠,𝑐𝑣(𝑇𝑆,𝑖−𝑇𝑊,𝑖)
(11)
Then, in o de o implemen hem in a Ma lab code, hey a e eo ganized in o a ma ix
equa ion.
[
𝑉𝑐𝑣[(|𝜕𝜌
𝜕𝑃|ℎ)𝑖ℎ𝑅,𝑖−1]𝑉𝑐𝑣[(|𝜕𝜌
𝜕ℎ|𝑃)𝑖ℎ𝑅,𝑖+𝜌𝑅,𝑖]0 0
𝑉𝑐𝑣(|𝜕𝜌
𝜕𝑃|ℎ)𝑖𝑉𝑐𝑣(|𝜕𝜌
𝜕ℎ|𝑃)𝑖0 0
0 0 𝑉𝑐𝑣𝜌𝑆,𝑖𝑐𝑝,𝑆,𝑖 0
00 0 𝑐𝑊𝑚𝑊,𝑐𝑣
]
×
[
𝑃󰇗𝑅
ℎ󰇗𝑅,𝑖
𝑇󰇗𝑆,𝑖
𝑇󰇗𝑊,𝑖
]
=
[
𝑚󰇗𝑅,𝑖𝑛,𝑖ℎ𝑅,𝑖𝑛,𝑖−𝑚󰇗𝑅,𝑜𝑢𝑡,𝑖ℎ𝑅,𝑜𝑢𝑡,𝑖+2𝑞󰇗𝑅,𝑖
𝑚󰇗𝑅,𝑖𝑛,𝑖−𝑚󰇗𝑅,𝑜𝑢𝑡,𝑖
−𝑚󰇗𝑆,𝑖𝑐𝑆,𝑖(𝑇𝑆,𝑜𝑢𝑡,𝑖−𝑇𝑆,𝑖𝑛,𝑖)+2𝑞󰇗𝑆,𝑖
𝑞󰇗𝑅,𝑖−𝑞󰇗𝑆,𝑖
]
(12)
Bo h hea ans e a es (𝑞󰇗𝑅 and 𝑞󰇗𝑆) a e mul iplied by wo because, in he ac ual PHEX,
e e y e ige an o seconda y luid a e in con ac wi h wo in e media e pla es, excep
o he bounda y seconda y luid channels. Empi ical co ela ions a e used in he
calcula ion o he hea ans e a es. Fo he one-phase con ec ion HTC, he Di us-
Boel e co ela ion is used [38]. In addi ion, he co ela ions p esen ed in Han e al.
[39,40] a e used o he wo-phase con ec ion HTC.
In o de o sol e Eq. (12), he inle and ou le mass low a es o he e ige an luid mus
be known. When a s eady-s a e is calcula ed, bo h a e equal. Ne e heless, du ing a
ansien -s a e, expansion and comp ession de ices egula e he e ige an mass low
and he one can be di e en om he o he . On he o he hand, he inle en halpy o he
e ige an luid and he inle empe a u e and mass low a e o he seconda y luid mus
also be known.
As will be shown la e , when Eq. (12) is ex ended o an a bi a y numbe o con ol
olumes and he e ige an inle and ou le mass low a es a e known, he in e media e
mass low a es mus be calcula ed a each ime s ep. These in e media e e ige an
mass low a es will be mo ed o he second e m o he ma ix equa ion, o ming ano he
s a e ec o .
In he agg ega e, o each ime s ep, 4𝑁 de i a i e s a es and in eg a ions mus be
sol ed. Ne e heless, only he e ige an ene gy and mass equa ions ha e o be sol ed
oge he . The ene gy equa ion o pla es and seconda y luid can be emo ed om he
ma ix and sol ed sepa a ely, hus educing he compu a ional ime.
On he o he hand, a he ime o applying he p esen ed o mula ion o a ixed numbe
o FCV, coun e - low and pa allel- low connec ions mus be di e en ia ed. Figu e 1 and
Figu e 2 show a g aph desc ip ion o a PHEX disc e ized in N numbe o FCV o coun e -
low and pa allel- low connec ions, espec i ely.
9
Figu e 1. Fini e con ol olume coun e - low PHEX model.
Figu e 2. Fini e con ol olume pa allel- low PHEX model.
As can be seen, he ou le s and inle s o he e ige an luid a e in e ed when he
connec ion o he PHEX is in coun e - low o pa allel- low. The in e sion o he e ige an
luid allows he model o be used in e e sible hea pump sys ems which can hea and
cool-down wa e , depending on he use demand.
2.3. Th ee FCV example cases
Eq. (12) will now be ex ended o a h ee con ol olume o mula ion o bo h a coun e -
low and a pa allel- low connec ion. The di e ences in he o mula ion be ween bo h
connec ions a e shown below.
Eqs. (13) and (14) show he ma ix equa ions ha sol e he e ige an ene gy and mass
equa ions o coun e - low and pa allel- low PHEX, espec i ely. As he ene gy equa ion
o seconda y luid and pla es can be sol ed sepa a ely and a e equal ega dless o he
connec ion o he PHEX, hey ha e been emo ed om he main ma ix. Eq. (15) shows
he seconda y luid ene gy ma ix equa ion and Eq. (16) shows he in e media e pla e
ene gy ma ix equa ion o he h ee con ol olume example.
Seconda y
luid
Re ige an
luid
Pla e
Con ol
olumen 1 Con ol
olumen 2 Con ol
olumen n-1 Con ol
olumen n
. . .
𝑚󰇗𝑆𝑚󰇗𝑆
𝑚󰇗𝑅,𝑜𝑢𝑡 𝑚󰇗𝑅,𝑖𝑛
𝑞󰇗𝑅,
𝑞󰇗𝑆, 𝑇𝑆,𝑜𝑢𝑡
ℎ𝑅,𝑜𝑢𝑡
𝑇𝑆,𝑖𝑛
ℎ𝑅,𝑖𝑛
𝑇𝑆, 𝑇𝑆,𝑛 𝑛
𝑇𝑆, 𝑇𝑆, 𝑇𝑆,𝑛 𝑇𝑆,𝑛
ℎ𝑅, ℎ𝑅,𝑛 𝑛
ℎ𝑅, ℎ𝑅, ℎ𝑅,𝑛 ℎ󰇗𝑅,𝑛
𝑞󰇗𝑅, 𝑞󰇗𝑆, 𝑞󰇗𝑅,𝑛
𝑞󰇗𝑆,𝑛 𝑞󰇗𝑅,𝑛
𝑞󰇗𝑆,𝑛
𝑞󰇗𝑆, 𝑞󰇗𝑆, 𝑞󰇗𝑆,𝑛 𝑞󰇗𝑆,𝑛
𝑞󰇗𝑅, 𝑞󰇗𝑅, 𝑞󰇗𝑅,𝑛 𝑞󰇗𝑅,𝑛
Pla e
Pla e
𝑚󰇗𝑅, 𝑚󰇗𝑅,𝑛 𝑛
Seconda y
luid
Re ige an
luid
Pla e
Con ol
olumen 1 Con ol
olumen 2 Con ol
olumen n-1 Con ol
olumen n
. . .
𝑚󰇗𝑆𝑚󰇗𝑆
𝑚󰇗𝑅,𝑜𝑢𝑡
𝑚󰇗𝑅,𝑖𝑛 𝑞󰇗𝑅,
𝑞󰇗𝑆, 𝑇𝑆,𝑜𝑢𝑡
ℎ𝑅,𝑜𝑢𝑡
𝑇𝑆,𝑖𝑛
ℎ𝑅,𝑖𝑛
𝑇𝑆, 𝑇𝑆,𝑛 𝑛
𝑇𝑆, 𝑇𝑆, 𝑇𝑆,𝑛 𝑇𝑆,𝑛
ℎ𝑅, ℎ𝑅,𝑛 𝑛
ℎ𝑅, ℎ𝑅, ℎ𝑅,𝑛 ℎ𝑅,𝑛
𝑞󰇗𝑅, 𝑞󰇗𝑆, 𝑞󰇗𝑅,𝑛
𝑞󰇗𝑆,𝑛 𝑞󰇗𝑅,𝑛
𝑞󰇗𝑆,𝑛
𝑞󰇗𝑆, 𝑞󰇗𝑆, 𝑞󰇗𝑆,𝑛 𝑞󰇗𝑆,𝑛
𝑞󰇗𝑅, 𝑞󰇗𝑅, 𝑞󰇗𝑅,𝑛 𝑞󰇗𝑅,𝑛
Pla e
Pla e
𝑚󰇗𝑅, 𝑚󰇗𝑅,𝑛 𝑛
16
(a)
(b)
(c)
Figu e 8. Pa allel- low condense (Case 2) esul s o e ige an p essu e (a), wa e
empe a u es (b) and empe a u e dis ibu ion a ime 800 seconds (c).
Figu e 8(c) depic s he empe a u e dis ibu ion in he pa allel- low condense . As can be
seen, he e ige an luid jus eaches he sub-cooled sa u a ion line in he inal pa o
he PHEX.
On he o he hand, Figu e 9(c) and Figu e 10(c) ep esen he empe a u e dis ibu ion
when he PHEX wo ks as an e apo a o o he coun e - low and he pa allel- low,
espec i ely. As can be seen, he e ige an luid goes in o he PHEX as a wo-phase
luid. Inside he PHEX, i is e apo a ed and supe hea ed.
(a)
(b)
2400
2500
2600
2700
2800
2900
0 200 400 600 800 1000
Condensa ion p essu e [kPa]
Time [s]
Tes da a
Model esul s
25
30
35
40
45
0 200 400 600 800 1000
Wa e empe a u e [ºC]
Time [s]
Ou le (model)
Ou le ( es )
Inle
30
40
50
60
70
80
010 20 30 40 50
Tempe a u e [ºC]
PHEX leng h [cm]
Re ige an
In e media e pla e
Wa e
700
800
900
1000
1100
0 200 400 600 800 1000
E apo a ion p essu e [kPa]
Time [s]
Tes da a
Model esul s
0
5
10
15
20
0 200 400 600 800 1000
Wa e empe a u e [ºC]
Time [s]
Ou le (model)
Ou le ( es )
Inle

17
(c)
Figu e 9. Coun e - low e apo a o (Case 3) esul s o e ige an p essu e (a), wa e
empe a u es (b) and empe a u e dis ibu ion a ime 800 seconds (c).
(a)
(b)
(c)
Figu e 10. Pa allel- low e apo a o (Case 4) esul s o e ige an p essu e (a), wa e
empe a u es (b) and empe a u e dis ibu ion a ime 800 seconds (c).
Rega ding he PHEX connec ions, in bo h Case 2 and Case 3, he wa e inside he PHEX
is cooled down by a ound 5 ºC. Ne e heless, in Case 2, he e ige an luid goes ou
om he PHEX wi h a supe hea ing o a ound 5ºC, while in Case 3, he supe hea ing is
o app oxima ely 2 ºC. Such a di e ence is ela ed o he PHEX connec ion, he hea
ans e being highe in a coun e - low connec ion han in a pa allel- low connec ion.
In Table 6, he maximum and mean nume ical di e ences be ween he model esul s
and he da a om he es s o e ige an p essu e and wa e ou le empe a u e a e
p esen ed.
Table 6. Maximum and mean nume ical di e ences be ween model esul s and es s da a o
he ou s udied cases.
Re ige an p essu e [kPa]
Wa e ou le empe a u e [ºC]
5
7
9
11
13
15
17
010 20 30 40 50
Tempe a u e [ºC]
PHEX leng h [cm]
Re ige an In e media e pla e Wa e
900
950
1000
1050
1100
1150
0 200 400 600 800 1000
E apo a ion p essu e [kPa]
Time [s]
Tes da a
Model esul s
0
5
10
15
20
0 200 400 600 800 1000
Wa e empe a u e [ºC]
Time [s]
Ou le (model)
Ou le ( es )
Inle
4
6
8
10
12
14
010 20 30 40 50
Tempe a u e [ºC]
PHEX leng h [cm]
Re ige an
In e media e pla e
Wa e
18
Maximum
Mean
Maximum
Mean
Case 1
51.5
20.3
1.1
0.3
Case 2
52.6
30.4
1.3
0.6
Case 3
46.9
12.4
0.5
0.1
Case 4
51.9
21.8
0.8
0.2
The esul s show ha he maximum nume ical di e ence o he e ige an p essu e is
a ound 50 kPa o any s udied case. Rega ding he compa ison o he wa e ou le
empe a u e, he g ea es di e ence is ound in Case 2. He e, he maximum di e ence
inc eases up o 1.3 ºC.
Addi ionally, he NRE o he e ige an p essu es and wa e ou le empe a u es o he
ou cases a e shown in Table 7. As can be seen, in all he cases s udied, he NRE is
smalle han he accep ed alue o 0.05.
Table 7. No malized Residual E o o he ou s udied cases.
Re ige an
p essu e
Wa e ou le
empe a u e
Case 1
1.1 E-04
1.2 E-04
Case 2
1.6 E-04
2.5 E-04
Case 3
2.2 E-04
2.5 E-04
Case 4
5.8 E-04
1.0 E-03
4.3. FVC numbe s simula ion speed
Finally, he simula ion speed and accu acy ha e been s udied by inc easing he numbe
o FCV used o simula e he desc ibed model om i e o one hund ed. The coun e - low
condense (Case 1) has been simula ed o 20 minu es and he Real Time Fac o (RTF)
o he simula ion has been calcula ed, di iding he compu a ional ime by he simula ed
ime.
Figu e 11 (a) shows he di e ences in he condensing p essu e calcula ion using a
di e en numbe o ini e olumes. Al hough he simula ion ime was 1200 seconds, in
he image only he pe iod whe e he ansien occu s has been shown, so he di e ences
can be be e pe cei ed. Figu e 11 (b) shows he RTF o di e en numbe s o FCV.
As can be app ecia ed in Figu e 11 (a), he shape o he sys em dynamic is well ollowed,
e en wi h a low numbe o FCV. Ne e heless, he nume ical esul s do no accu a ely i
wi h a low numbe o FCV. Wi h en FCV, he esul s can be imp o ed. The nume ical
esul s a e accu a e enough once he numbe o FCV is equal o o highe han wen y.
Rega ding he compu a ional ime, he RTF emains low up o 20 FCV and inc eases
g ea ly wi h 100 FCV. These esul s ag ee wi h he conclusions gi en in [42], whe e i is
s a ed ha a leas 15 FCV a e equi ed o achie e good accu acy.
19
(a)
(b)
Figu e 11. Condensing p essu e wi h di e en numbe s o ini e con ol olumes (a) and Real
Time Fac o o di e en numbe s o ini e con ol olumes (b).
5. Conclusions
In o de o imp o e he con ol sys ems o e e sible hea pump sys ems, models ha
can p edic he dynamic beha io and ansien s a es o hese sys ems a e needed. In
his ask, physics-based models a e he mos accu a e ones.
In his pape , a physics-based model using he ini e olume con ol app oach o simula e
a PHEX is p esen ed. The model has been de eloped in Ma lab/Simulink en i onmen .
This kind o hea exchange is commonly used in esiden ial e e sible g ound sou ce
hea pump sys ems. As i is based on physical equa ions, his model can be used o
model di e en ypes o PHEX, achie ing a good le el o accu acy. The model has been
alida ed wi h expe imen al dynamic es s o a PHEX wo king as condense and as
e apo a o . Mo eo e , o each wo king mode, i has been simula ed unde coun e - low
and pa allel- low a angemen s.
The accu acy o he model has been p o ed by calcula ing he NRE o he simula ed
esul s wi h espec o he es da a o he e ige an p essu e and he wa e ou le
empe a u e. The minimum alue o he NRE was 1.1 E-04, while he maximum was 1.0
E-03, which is lowe han he accep ed alue o his kind o model. I has also been
demons a ed ha disc e izing he model in wen y ini e olumes allows a high deg ee
o accu acy o be eached, while main aining he compu a ional ime low.
This pape p o ides a use ul ool o hea pump sys ems and PHEX design as i allows
he pe o mance o a PHEX o be compa ed, a ying he wo king mode o he PHEX, he
luid connec ions, he PHEX size, he numbe o PHEX pla es, he wo king luids, e c.
Addi ionally, as he model can simula e a PHEX wo king as a condense and as an
e apo a o , i can be used o simula e he beha io o e e sible hea pump sys ems.
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Condensing p essu e [kPa]
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