Current Work on PCM Fins
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Transcript of Current Work on PCM Fins
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8/16/2019 Current Work on PCM Fins
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1. Analysis of geometrical and operational parameters of PCM in a fin and
tube heat exchanger (2014(!eat and mass "ransfer
#ote$ %xperimental &or'.
1. Fin and tube heat exchanger 2. solidification and melting
3. PCM = R35
4. HF= !ater
5. "n#estigate the effect of flo$ rate% inlet tem&erature and geometrical &arameter 'fin &itch(
on charging and discharging &rocesses of the &hase change material.
). he shell side is a rectangular and a continuous spiral tube that carries the
$ater inside the shell.
2. Analysis of !"s) PCMs and fins effects on the thermal performance
of shell*tube thermal energy storage units (201+ (,olar %nergy
#ote$ #umerical -or' (/
*. PCMs = including &ure +a+,3 and a com&osite
of +a+,3-ex&anded gra&hite '/(
2. HF= s0nthetic oil and molten salts.
3. charging-discharging &rocess%
4. ffects of the extended fin%
5. his stud0 is ex&ected to &ro#ide an a&&rehensi#e inter&retation of thermal trans&ort
mechanism and rational ad#ices in o&timi1ing the s0stem o&eration.
. An effectieness#" techni3ue for characterising a finned tubes PCM
system using a C/ model (Applied %nergy(201+
#ote$ #umerical -or' (2/
*. $o dimensional mathematical model% based on the effecti#enessnumber of transfer units
techniue.
2. Radial Fins.
3. he model a&&lies an em&iricall0 deri#ed P factor $hich defines the &ro&ortion of the heat
flo$ $hich is &arallel and isothermal.
4.P factor $as determined using a #alidated com&utational fluid d0namics model. his
method is used to design and o&timise tubeintan salt based &hase change thermal storage
units $ith finned tubes.
5. PCM = !ater and salt h0drate.
4. A numerical method for PCMbased pin fin heat sin's optimiation (energy
conersion and management(201+
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#ote$ #umerical -or' (/
*. /eometric o&timi1ation of PCMbased &in fin heat sins.
2. Paraffin R44HC is used as PCM
3. Fins are made of aluminium.
4. aguchi method $ith numerical simulations is utili1ed for this &ur&ose. +umber of fins%
fins height% fins thicness and the base thicness are &arameters $hich are studied for
o&timi1ation.
5. Results sho$ that a com&lex relation exists bet$een PCM and C #olume &ercentages.
he o&timal case strongl0 de&ends on the fins6 number% fins height and thicness and also the
critical tem&erature.
+. Closecontact melting in a horiontal cylindrical enclosure &ith longitudinal plate
fins$ /emonstration) modeling and application to thermal storage.(!eat and mass
transfer(201+
#ote$
1. closecontact melting 'CCM( ($hich ma0 significantl0 increase the melting rate% has not
been ex&lored(.
2. "n the &resent ex&eriments% a laborator0scale threefin unit is trans&arent and thus the
&rocesses inside it are obser#ed and recorded. Closecontact melting is achie#ed b0 su&&l0ing
heat to the outer shell of the unit7 the solid &hase is detached from the shell and mo#es in the
liuid &hase.
3.8 no#el theoretical model includes gra#it0induced rotational motion of the solid% &rimar0
melting on a #ertical fin $ith nonuniform tem&erature distribution% secondar0 melting at the
shell% and frictional resistance at the latter.
4. he model is #alidated using the ex&erimental results% and then used for a
&arametric in#estigation and dimensional anal0sis.
5. "t is re#ealed that the melt fraction de&ends on the Fourier and tefan numbers combined.
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5. Constructal design of horiontal fins to improe the performance of phase change
material rectangular enclosures (Applied thermal %ngineering(201+
#ote$
*. he &ur&ose of the current stud0 is to determine the effect of adding hori1ontal fins to
im&ro#e the efficienc0 of a heat sin. he reuired time for the maximum tem&erature of the
heat sin to reach its critical #alue is maximi1ed in#oing constructal theor0.
2. 9egrees of freedom are the number of enclosures% hori1ontal fins number and heat sin
as&ect ratio% $hile the entire surface area and the PCM content are constraints.
3. he results indicate that the best maximum safe o&eration time occurs in an o&timum #alue
for the hori1ontal fins number.
4. he results sho$ that for lo$ number of enclosures% heat sins $ith high as&ect ratios are
su&erior: $hile% for high number of enclosures% heat sins $ith lo$ as&ect ratios ha#e better
&erformance.
5. 8dding geometrical com&lexities to the heat sin $ill not necessaril0 im&ro#e the
&erformance of the enclosure.
6. 7P accelerated numerical study of PCM melting process in an enclosure &ith
internal fins using lattice 8oltmann method
*.he gra&hics &rocessing units '/P;( com&uting
2.he melting &rocess in PCMs $as in#estigated for different materials of
fins and $alls% number of fins% fin configurations% hot $all tem&erature% thermal boundar0
conditions% and inclination angle of the PCM ca#it0.
3.
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10. Maximiation of performance of a PCM latent heat storage system
&ith innoatie fins (Applied %nergy(201+
#ote$ #umerical
*. "n this &a&er the use of tree sha&ed fins is &ro&osed to enhance the &erformance of a shell
andtube
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)."nserting fins leads to the significant enhancement of the melting and solidification rate.
A."t is more efficient during the solidification &rocess due to the su&&ression of the natural
con#ection effect during the melting &rocess.
12. #umerical inestigation of PCM melting process in sleee tube &ith internal fins
(%nergy conseration and management(2015
#ote $ #umerical
*. o anal01e the im&act of fin geometr0 'including finlength% finratio and the angle bet$een neighbor fins( and outer tube conducti#it0 on PCM melting &rocess:
2. he influence of the natural con#ection in the hori1ontal slee#etube unit $ithin the
longitudinal fins is further examined.
3. Results sho$s that small finratio can reduce melting time% but not remarabl0: the angle
bet$een neighbor fins has little im&act on melting &rocess%
4. ,&timi1ation of the angle bet$een neighbor fins to reduce melting time in the fullscale
unit.
5.he outer tube conducti#it0 has great im&act on melting &rocess $hether considering the
natural con#ection or not.
1."hermal performance enhancement of shell and tube
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'HF(.
3.x&erimental results sho$ that the heat transfer augmentation is more sensiti#e to increase
in
HF inlet tem&erature as com&ared to increase in mass flo$ rate of HF. olidification time
has been obser#ed to reduce u& to 43.) b0 installation of three fins.