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Novel Study for Energy Recovery from the Cooling–Solidification Stage of Synthetic Slag Manufacturing: Estimation of the Potential Energy Recovery

Abstract

Herein, a novel method for energy recovery from molten synthetic slags is analyzed. In this work, the potential energy that could be recovered from the production of synthetic slag is estimated by means of an integrated experimental–theoretical study. The energy to be recovered comes from the cooling–solidification stage of the synthetic slag manufacturing. Traditionally, the solidification stage has been carried out through quick cooling with water, which does not allow the energy recovery. In this paper, a novel cooling method based on metal spheres is presented, which allows the energy recovery from the molten slags. Two points present novelty in this work: (1) the method for measuring the metal spheres temperature (2) and the estimation of the energy that could be recovered from these systems in slag manufacturing. The results forecasted that the temperature achieved by the metal spheres was in the range of 295–410 ◦C in the center and 302–482 ◦C on the surface. Furthermore, we estimated that 325–550 kJ/kg of molten material could be recovered, of which 15% of the energy consumption is in the synthetic slag manufacturing process. Overall, the results obtained confirmed the potential of our proposal for energy recovery from the cooling–solidification stage of synthetic slag manufacturing.

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Novel Study for Energy Recovery from the Cooling–Solidification Stage of Synthetic Slag Manufacturing: Estimation of the Potential Energy Recovery

Author: Baena-Moreno, Francisco M.; Rodríguez Galán, Mónica; Navarrete Rubia, Benito; Vilches Arenas, Luis Francisco
Publisher: MDPI
Year: 2020
DOI: 10.3390/pr8121590
Source: https://idus.us.es/bitstreams/f6b43ab7-dbae-46fd-bf19-62d7fd595ca0/download
p ocesses
A icle
No el S udy o Ene gy Reco e y om he
Cooling–Solidi ica ion S age o Syn he ic Slag
Manu ac u ing: Es ima ion o he Po en ial
Ene gy Reco e y
F ancisco M. Baena-Mo eno * , Mónica Rod íguez-Galán, Beni o Na a e e and Luis F. Vilches
Chemical and En i onmen al Enginee ing Depa men , Technical School o Enginee ing, Uni e si y o Se ille,
C/Camino de los Descub imien os s/n, 41092 Se illa, Spain; [email p o ec ed] (M.R.-G.);
[email p o ec ed] (B.N.); [email p o ec ed] (L.F.V.)
*Co espondence: [email p o ec ed]
Recei ed: 6 No embe 2020; Accep ed: 25 No embe 2020; Published: 2 Decembe 2020


Abs ac :
He ein, a no el me hod o ene gy eco e y om mol en syn he ic slags is analyzed. In his
wo k, he po en ial ene gy ha could be eco e ed om he p oduc ion o syn he ic slag is es ima ed
by means o an in eg a ed expe imen al– heo e ical s udy. The ene gy o be eco e ed comes om he
cooling–solidi ica ion s age o he syn he ic slag manu ac u ing. T adi ionally, he solidi ica ion s age
has been ca ied ou h ough quick cooling wi h wa e , which does no allow he ene gy eco e y.
In his pape , a no el cooling me hod based on me al sphe es is p esen ed, which allows he ene gy
eco e y om he mol en slags. Two poin s p esen no el y in his wo k: (1) he me hod o measu ing
he me al sphe es empe a u e (2) and he es ima ion o he ene gy ha could be eco e ed om hese
sys ems in slag manu ac u ing. The esul s o ecas ed ha he empe a u e achie ed by he me al
sphe es was in he ange o 295–410
◦
C in he cen e and 302–482
◦
C on he su ace. Fu he mo e,
we es ima ed ha 325–550 kJ/kg o mol en ma e ial could be eco e ed, o which 15% o he ene gy
consump ion is in he syn he ic slag manu ac u ing p ocess. O e all, he esul s ob ained con i med
he po en ial o ou p oposal o ene gy eco e y om he cooling–solidi ica ion s age o syn he ic
slag manu ac u ing.
Keywo ds:
sus ainable syn he ic slag p oduc ion; ene gy eco e y; me al sphe es; ixed bed egene a o ;
was e and ene gy nexus
1. In oduc ion
1.1. Backg ound
The u u e challenges ela ed o he known ci cula economy policy need o in ensi y he esea ch
o mo e en i onmen al p ocesses and less ene gy-in ensi e indus ial p ocesses [
1
,
2
]. In his sense,
one o he key poin s is he de elopmen o new p oduc manu ac u ing h ough he eco e y o
was e/by-p oduc s in applica ions wi h high added alue and easy echnology ans e o he indus ial
sec o [
3
,
4
]. The use o was e o o m new i eous ma e ials o e a po en ial possibili y o was e
alo iza ion. E en hough he idea o alo izing was e as cons i uen s o cemen s is documen ed in
he li e a u e h ough pa en s and esea ch wo ks [
5
–
10
], no el ies can be s udied in di e en ways
such as (1) explo ing new ma e ials and seeking simila p ope ies o hose p esen ed by blas u nace
slags; (2) he ob aining o syn he ic slags exclusi ely om was e mix u es ha could be managed in
non-haza dous was e land ills; and (3) he ene gy-e icien p oduc ion o syn he ic slag manu ac u ing.
P ocesses 2020,8, 1590; doi:10.3390/p 8121590 www.mdpi.com/jou nal/p ocesses
P ocesses 2020,8, 1590 2 o 20
The i s and second op ions poin ed ou abo e seek o p o ide alue-added p oduc s om
was e based on compliance wi h egula o y equi emen s. Ne e heless, he hi d one is conside ed
associa ed o he iabili y o he manu ac u ing p ocess o hese new ma e ials om an ene gy
pe spec i e. The e o e, he ene gy-e iciency s udy o he p oduc ion p ocess is conside ed one o
he keys o ob ain i s echnical–economic iabili y, oge he wi h he minimiza ion o was e anspo
cos s. In a p e ious wo k o his esea ch g oup, cemen subs i u i e wi h p ope ies simila o blas
u nace slags (syn he ic slags) was ob ained. The ypical composi ion o blas u nace slag can be seen
in Table 1. In his p ocess, a mix o was e was p oposed o ob ain he syn he ic slag ma e ial [
11
].
As announced in p e ious wo k, a deep ene gy eco e y s udy is needed o es ima e he iabili y o
his no el p oduc ion me hod.
Table 1. Typical composi ion anges o blas u nace slags. Own elabo a ion based on [12–14].
Composi ion Range SiO2CaO Al2O3MgO Fe2O3SO3Na2O K2O
27–40 30–50 5–15 1–15
0.2–2.5
1–2.5 0.1–3 0.1–3
In acco dance wi h EN 15167-1 [
15
], g anula ed blas u nace slag is a i i ied ma e ial p oduced
by apid cooling o a mol en slag o sui able composi ion. This kind o slag is ob ained by mel ing
i on o e in a blas u nace, con aining a leas wo- hi ds o c ys alline slag mass and ha ing hyd aulic
p ope ies when ac i a ed p ope ly. The pa ame e s ha in luence he hyd aulic beha io o he inal
slag a e he i eous phase con en , he chemical composi ion, he ineness, he addi i es, and he
me hods and/o subs ances o he ac i a ion s age, p esen ing wha is called la en o po en ial
hyd aulic capaci y [
16
]. The chemical composi ion o he blas u nace slags is one o he p ope ies
ha ma ks i s hyd aulic po en ial, since he g ea e he basici y o he slags, he be e he hyd aulic
beha io . Howe e , he main cha ac e is ic ela ed o hyd aulic beha io is he p opo ion o he
i eous phase o he slag, which mus exceed 70% o gua an ee he hyd aulic beha io [17].
The e icien p oduc ion o he manu ac u e o syn he ic slags needs a s udy o he ene gy eco e y
in i s manu ac u ing p ocess. These s udies ha e been conduc ed in dep h by nume ous au ho s [
18
–
22
],
ocusing especially on he ene gy ha can be eco e ed in he cooling s age o he mol en ma e ial.
Slag cooling sys ems can be classi ied acco ding o he cooling luid o ma e ial used o hei impac
on he ene gy e iciency o he p ocess (ene gy eco e y in he o m o s eam and/o wa m gases). Thus,
basically, all cooling sys ems consis o a hea exchange be ween he mol en ma e ial and he selec ed
luid (wa e and/o ai ) o solid ma e ial (me allic ma e ial). In any case, he echnologies applicable
o he de elopmen o he cooling sys ems mus pe o m a quick cooling, as well as being capable
o ha nessing he po en ial ene gy con ained in mol en ma e ial du ing he cooling p ocess. Below,
some me hods o ene gy eco e y om he mol en ma e ial a e explained, which a e mainly based on
we sys ems (wa e as cooling luid) o d y sys ems (whe e he cooling luid used is ai /gases).
Cooling wi h wa e achie es he objec i es ega ding he i eous p ope ies o he ma e ial.
Howe e , he disad an ages o wa e -based sys ems a e ela ed o hei low ene gy e iciency and
con amina ion wi h pa icles and o he pollu an s, gene a ing a highly co osi e apo due o he
p esence o acid gases ha inc ease ea men , equipmen main enance, and ene gy eco e y cos s.
In he d y cooling sys em, a ansmission occu s o hea om he mol en ma e ial o a s eam o ai ,
which is in con ac wi h eco e y boile s. In many o he ai -cooling echniques, a p io a omiza ion
o he mol en solid could be pe o med. Subsequen ly, a con ac ing s age wi h a s eam o ai in a
luidized o non- luidized bed is ca ied ou , which abso bs he hea , achie ing solidi ica ion o he
mel . O he g anula ion op ions a ise when he mol en ma e ial is agmen ed by o a ing de ices [
23
].
Ano he possibili y o cooling could be by con ac o he mol en ma e ial wi h solid ma e ials such as
sphe ical bodies. This op ion equi es ha he solid ma e ial ha no eac chemically wi h he mol en
slag (i.e., me al sphe es [
24
] o cooling on o a ing me al d ums [
25
–
27
]). Wi h hese example sys ems,
he ene gy eco e y om he mol en slag is possible. In addi ion, combining he ene gy e iciency o
P ocesses 2020,8, 1590 3 o 20
hese ene gy eco e y sys ems wi h he imp o emen o slag p ope ies, he o e all ene gy eco e y
e iciency o cooling p ocesses can be inc eased [28].
This pape s udies he po en ial ene gy eco e y o he cooling p ocess o syn he ic slags p oduc ion
by means o a mass cooling sys em wi h me al sphe es. Concep ually, he mass cooling sys em by
means o he mal egene a ion wi h me al sphe es achie es apid cooling o he mol en ma e ial as a
consequence o he ans e o ene gy om he mol en ma e ial o he me al sphe es. Subsequen ly,
he e is he possibili y o a eco e y o he ene gy con ained in he sphe es by means o an ai cu en .
In addi ion, he cha ac e is ics associa ed wi h he p ope ies o he solid elemen s and he solidi ied
ma e ial, gene ally o low he mal esis ance, allow hea o dissipa e apidly. Once he me al sphe es
and he ma e ial ha e been cooled by he ai low in he egene a o and a pos e io sepa a ion s age o
he solidi ied ma e ial om he balls, he me al sphe es would come back in o con ac wi h he syn he ic
slags in a con inuous cycle. The concep ual scheme o he ene gy eco e y sys em is p esen ed in
Figu e 1. In his sys em, he slag is sepa a ed om he me al sphe es a e cooling h ough sc eening
by he size o he sphe es and solidi ied slags. This sepa a ion is possible as he slag a e no adhe ed o
he su ace o he me al sphe es.
P ocesses2020,8,xFORPEERREVIEW3o 21
Thispape s udies hepo en ialene gy eco e yo  hecoolingp ocesso syn he icslags
p oduc ionbymeanso amasscoolingsys emwi hme alsphe es.Concep ually, hemasscooling
sys embymeanso  he mal egene a ionwi hme alsphe esachie es apidcoolingo  hemol en
ma e ialasaconsequenceo  he ans e o ene gy om hemol enma e ial o heme alsphe es.
Subsequen ly, he eis hepossibili yo a eco e yo  heene gycon ainedin hesphe esbymeans
o anai cu en .Inaddi ion, hecha ac e is icsassocia edwi h hep ope ieso  hesolidelemen s
and hesolidi iedma e ial,gene allyo low he mal esis ance,allowhea  odissipa e apidly.Once
heme alsphe esand hema e ialha ebeencooledby heai  lowin he egene a o andapos e io 
sepa a ions ageo  hesolidi iedma e ial om heballs, heme alsphe eswouldcomebackin o
con ac wi h hesyn he icslagsinacon inuouscycle.Theconcep ualschemeo  heene gy eco e y
sys emisp esen edinFigu e1.In hissys em, heslagissepa a ed om heme alsphe esa e 
cooling h oughsc eeningby hesizeo  hesphe esandsolidi iedslags.Thissepa a ionispossible
as heslaga eno adhe ed o hesu aceo  heme alsphe es.

Figu e1.Concep ualschemeo  heene gy eco e yp ocessp oposedin hiswo k.
1.2.GoalandScope
Basedon heno elconcep o de elopingsyn he icslags omwas e,asexplainedinou 
p e iouswo k[11], hemainobjec i eo  hiss udyis oe alua e hep ope ieso syn he icslags
and heene gy eco e ycapaci yo  hea o emen ionedcoolingsys emdesc ibedinFigu e1.
Likewise, heene gy eco e edin hecoolingai s eamwases ima edin ela ion o heene gy
possessedby hemol enma e ialino de  oanalyze hepossibleene gysa ings ha would esul 
in hemanu ac u eo slags.Twomainpoin sp esen no el yin hiswo k.The i s oneis heme hod
o measu ing he empe a u es ha  heme alsphe esachie e.To heknowledgeo  heau ho s, his
is he i s  ime ha bo h heme hodologyand he eal empe a u eda aa epublished.Thesecond
no el yo  hiswo kis ha knowing he eal empe a u eachie edin heme alsphe es,i was
possible oes ima e heene gy ha couldbe eco e edby hesesys emsinslagmanu ac u ing.
Thees ima iono ene gy eco e y om hemol enma e ialconsis edinse e als eps,which
a eindica edbelow:
‐ Jus i ica iono  he empe a u e eachedby heme alsphe esa  a iousmol enmass(m
m
)/me al
sphe es(m
s
)mass a io.
Figu e 1. Concep ual scheme o he ene gy eco e y p ocess p oposed in his wo k.
1.2. Goal and Scope
Based on he no el concep o de eloping syn he ic slags om was e, as explained in ou p e ious
wo k [
11
], he main objec i e o his s udy is o e alua e he p ope ies o syn he ic slags and he ene gy
eco e y capaci y o he a o emen ioned cooling sys em desc ibed in Figu e 1. Likewise, he ene gy
eco e ed in he cooling ai s eam was es ima ed in ela ion o he ene gy possessed by he mol en
ma e ial in o de o analyze he possible ene gy sa ings ha would esul in he manu ac u e o
slags. Two main poin s p esen no el y in his wo k. The i s one is he me hod o measu ing he
empe a u es ha he me al sphe es achie e. To he knowledge o he au ho s, his is he i s ime ha
bo h he me hodology and he eal empe a u e da a a e published. The second no el y o his wo k is
ha knowing he eal empe a u e achie ed in he me al sphe es, i was possible o es ima e he ene gy
ha could be eco e ed by hese sys ems in slag manu ac u ing.
The es ima ion o ene gy eco e y om he mol en ma e ial consis ed in se e al s eps, which a e
indica ed below:
P ocesses 2020,8, 1590 4 o 20
-
Jus i ica ion o he empe a u e eached by he me al sphe es a a ious mol en mass (m
m
)/me al
sphe es (ms) mass a io.
-
Co obo a ion o he indus ial easibili y o he p oposed sys em in Figu e 1by means o ixed
bed (o egene a o ) heigh calcula ion. Fo his pu pose, he calcula ion o he con ec i e hea
ans e coe icien by solid–ai con ec ion is needed. The de ini ion o his s ep is c ucial o
checking ha he p ocess p oposed is o indus ial in e es .
- Es ima ion o he po en ial ene gy eco e ed pe kg o mol en ma e ial.
To mee his end, his wo k is o ganized as ollows. Fi s , expe imen s o measu ing he maximum
empe a u e ha could be eached by he me al sphe es we e pe o med. Inasmuch han he s udy
aims o be use ul o indus ial pu poses, he expe imen s we e pe o med a di e en m
m
/m
s
a ios
o ep oduce eal indus ial scena ios. Subsequen ly, he mol en ma e ial ha was pou ed o e
he me al sphe es was analyzed by means o X- ay di ac ion (XRD) o e i y he o ma ion o he
cha ac e is ic i eous phase. A e wa ds, be o e es ima ing he po en ial ene gy eco e y, he echnical
easibili y o he p oposed cooling p ocess was cha ac e ized. To his end, he ixed bed heigh was
calcula ed ollowing he me hodology explained in Sec ion 2.2.4. Fo i s es ima ion, he p e ious
de e mina ion o he con ec i e hea ans e coe icien (h) was necessa y. The me hodology employed
o h es ima ion can be seen in Appendix A. Two expe imen s we e pe o med o es ima e he me al
sphe es—ai low empe a u e p o iles in a eal ixed bed. The expe imen s allowed he es ima ion
o h ollowing he assump ions explained in Sec ion 2.2.4. Once he indus ial ixed bed heigh was
ob ained and analyzed as easible, he ene gy eco e y pe kg o mol en ma e ial was es ima ed.
To es ima e he app oxima e pe cen age o he ene gy eco e y in he o e all slag manu ac u ing
p ocess, a compa ison o he i eous–mine al phases be ween ou mol en ma e ial and adi ional
clinke was done. This compa ison allowed ensu ing ha no signi ican di e ences a e ound and
hence ha he o al ene gy consump ion o ou mol en ma e ial can be app oxima e o he one o
clinke p oduc ion.
2. Ma e ials and Me hods
In o de o s udy he ene gy eco e y e iciency o he cooling and solidi ica ion sys em o he
mol en syn he ic slags, a h ee-s age labo a o y expe imen was p oposed:
(1)
Mel he was e mix u e in an o en in app op ia e p opo ions o achie e a composi ion simila o
blas u nace slags. This s age was add essed in dep h in ou p e ious wo k [11].
(2)
Ob ain he empe a u e eached by he me al sphe es when he mol en ma e ial is pou ed wi h
di e en mel ing/me al mass a ios. De e mina ion o he cha ac e is ics o he i eous phase
ob ained in o de o ensu e he i eous p ope ies o he ma e ial solidi ied.
(3)
E alua e he ene gy ha can be ex ac ed om a ixed bed o me al sphe es a he empe a u e
eached in he p e ious phase by exchanging ene gy wi h an ai cu en .
Below, he ma e ials and me hods employed o ul ill his scheme a e explained in dep h.
2.1. Ma e ials
The mix o was e o manu ac u ing syn he ic slags was de ined in a p e ious wo k o ou
g oup [
11
]. Th ee di e en was es we e selec ed as aw ma e ials, which we e cons uc ion and
demoli ion was e, he solid was e s eam gene a ed in an aluminum eco e y plan , and mussel shell
was e om he aquicul u e indus y. Fo mo e in o ma ion, please see [11].
2.2. Expe imen al Se up
2.2.1. Mel ing Fu nace
The mix o was e was mel ed by employing he mel ing u nace (4 kW powe ) schemed in Figu e 2,
which was he same one employed in ou p e ious wo k [
11
]. In b ie , he mel ing u nace consis s
P ocesses 2020,8, 1590 5 o 20
o six elec ical esis ances loca ed inside a hexagonal usion chambe . The discha ge o he mol en
ma e ial is ca ied ou om he bo om o he u nace.
P ocesses2020,8,xFORPEERREVIEW5o 21

Figu e2.Mel ing u nacescheme.
2.2.2.Me alSphe es:Coolingo  heMol enMa e ial
Thecoolings age oene gy eco e y om hemol enma e ialwasbasedonme alsphe es.The
i s s agewas hes udyo  he empe a u ee olu ioninsideasingleme alsphe e.To hisend, he
sys emshowninFigu e3wasdesigned.In hissys em,asingleme alsphe ewelded oapla ewas
buil .Thesphe ewasdesignedwi h wope o a ionsin helowe pa inwhich wo he mocouples
we einse ed ha allowmeasu ing he empe a u eda ain hecen e andon hesu aceo  he
sphe e.All he mocoupleswe econnec ed o heco espondingda aacquisi ionsys em.Fo sakeo 
sa e y, hesphe ewasassemblediname alcon aine andinsula edbya e ac o yma e ial,ascan
beseeninFigu e3.Thesys emwasplacedunde  hemel ing u nace,and hemol enma e ialwas
pou eddi ec ly om he u naceon o hesphe e.Ino de  o ep oduceanindus ialen i onmen 
close o ealcases, wosizeso sphe eso 40and50mmdiame e we eused.Figu e3shows he
cha ac e is icdimensionso  he50mmdiame e me alsphe eand heduc sinwhich he
he mocoupleswe einse ed.Fu he mo e,pho oso  hepla esa o emen ionedwi h hesphe es
coupledcanbeseen.Ade ailedexplana iono p ope iesandcomposi iono  hesphe escanbe
oundin e e ence[29].
Figu e 2. Mel ing u nace scheme.
2.2.2. Me al Sphe es: Cooling o he Mol en Ma e ial
The cooling s age o ene gy eco e y om he mol en ma e ial was based on me al sphe es.
The i s s age was he s udy o he empe a u e e olu ion inside a single me al sphe e. To his end,
he sys em shown in Figu e 3was designed. In his sys em, a single me al sphe e welded o a pla e was
buil . The sphe e was designed wi h wo pe o a ions in he lowe pa in which wo he mocouples
we e inse ed ha allow measu ing he empe a u e da a in he cen e and on he su ace o he sphe e.
All he mocouples we e connec ed o he co esponding da a acquisi ion sys em. Fo sake o sa e y,
he sphe e was assembled in a me al con aine and insula ed by a e ac o y ma e ial, as can be seen
in Figu e 3. The sys em was placed unde he mel ing u nace, and he mol en ma e ial was pou ed
di ec ly om he u nace on o he sphe e. In o de o ep oduce an indus ial en i onmen close o eal
cases, wo sizes o sphe es o 40 and 50 mm diame e we e used. Figu e 3shows he cha ac e is ic
dimensions o he 50 mm diame e me al sphe e and he duc s in which he he mocouples we e
inse ed. Fu he mo e, pho os o he pla es a o emen ioned wi h he sphe es coupled can be seen.
A de ailed explana ion o p ope ies and composi ion o he sphe es can be ound in e e ence [29].
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Figu e2.Mel ing u nacescheme.
2.2.2.Me alSphe es:Coolingo  heMol enMa e ial
Thecoolings age oene gy eco e y om hemol enma e ialwasbasedonme alsphe es.The
i s s agewas hes udyo  he empe a u ee olu ioninsideasingleme alsphe e.To hisend, he
sys emshowninFigu e3wasdesigned.In hissys em,asingleme alsphe ewelded oapla ewas
buil .Thesphe ewasdesignedwi h wope o a ionsin helowe pa inwhich wo he mocouples
we einse ed ha allowmeasu ing he empe a u eda ain hecen e andon hesu aceo  he
sphe e.All he mocoupleswe econnec ed o heco espondingda aacquisi ionsys em.Fo sakeo 
sa e y, hesphe ewasassemblediname alcon aine andinsula edbya e ac o yma e ial,ascan
beseeninFigu e3.Thesys emwasplacedunde  hemel ing u nace,and hemol enma e ialwas
pou eddi ec ly om he u naceon o hesphe e.Ino de  o ep oduceanindus ialen i onmen 
close o ealcases, wosizeso sphe eso 40and50mmdiame e we eused.Figu e3shows he
cha ac e is icdimensionso  he50mmdiame e me alsphe eand heduc sinwhich he
he mocoupleswe einse ed.Fu he mo e,pho oso  hepla esa o emen ionedwi h hesphe es
coupledcanbeseen.Ade ailedexplana iono p ope iesandcomposi iono  hesphe escanbe
oundin e e ence[29].
Figu e 3. Con .

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Figu e3.Schemeo  hede ice o coolingmol enma e ialwi hme alsphe esand iewso  he
con ainmen  essel.
Figu e4showsa ealpho oinwhich hecouplingbe ween hemel ing u naceou le and he
coolingde icewi h heme alsphe ecanbeobse ed.

Figu e4.Couplingo  hemel ing u naceou le and hecoolingde ice.
2.2.3.Me alSphe esPackingDe ice o Ene gyReco e y
Toes ima e hepo en ialene gy eco e y om heme alsphe eswi hai ,a ixedbedcomposed
by wobaske s illedwi hme alsphe eswasdesigned.Thebaske sa emadeo s ainlesss eeland
ha eamesh ha allows hegas opass h ough hebed.Theneeded he mocouples( o  empe a u e
measu emen s)we econnec ed o heda aacquisi ionsys em.Figu e5showsanimageo  he ixed
bedandme alsphe ebaske s.
Figu e 3.
Scheme o he de ice o cooling mol en ma e ial wi h me al sphe es and iews o he
con ainmen essel.
Figu e 4shows a eal pho o in which he coupling be ween he mel ing u nace ou le and he
cooling de ice wi h he me al sphe e can be obse ed.
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Figu e3.Schemeo  hede ice o coolingmol enma e ialwi hme alsphe esand iewso  he
con ainmen  essel.
Figu e4showsa ealpho oinwhich hecouplingbe ween hemel ing u naceou le and he
coolingde icewi h heme alsphe ecanbeobse ed.

Figu e4.Couplingo  hemel ing u naceou le and hecoolingde ice.
2.2.3.Me alSphe esPackingDe ice o Ene gyReco e y
Toes ima e hepo en ialene gy eco e y om heme alsphe eswi hai ,a ixedbedcomposed
by wobaske s illedwi hme alsphe eswasdesigned.Thebaske sa emadeo s ainlesss eeland
ha eamesh ha allows hegas opass h ough hebed.Theneeded he mocouples( o  empe a u e
measu emen s)we econnec ed o heda aacquisi ionsys em.Figu e5showsanimageo  he ixed
bedandme alsphe ebaske s.
Figu e 4. Coupling o he mel ing u nace ou le and he cooling de ice.
2.2.3. Me al Sphe es Packing De ice o Ene gy Reco e y
To es ima e he po en ial ene gy eco e y om he me al sphe es wi h ai , a ixed bed composed
by wo baske s illed wi h me al sphe es was designed. The baske s a e made o s ainless s eel and
ha e a mesh ha allows he gas o pass h ough he bed. The needed he mocouples ( o empe a u e
measu emen s) we e connec ed o he da a acquisi ion sys em. Figu e 5shows an image o he ixed
bed and me al sphe e baske s.
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Figu e5.Me alsphe espackingde ice.
Theme alsphe epacking,a e beinghea edinano en o hedesi ed empe a u e,was
deposi edina he mallyinsula ed essel ha canbeseeninFigu e6.

Figu e6.The mallyinsula ed essel(dimensionsinmm).
Mo eo e , hedesignedde iceinco po a esanai p ehea e bymeanso elec ical esis ance,
whichallowedpe o ming es sa di e en ini ialai  empe a u es.All heelemen sdesc ibedin his
sec iona ein eg a edin he inalexpe imen alse upshowninFigu e7.
Figu e 5. Me al sphe es packing de ice.
The me al sphe e packing, a e being hea ed in an o en o he desi ed empe a u e, was deposi ed
in a he mally insula ed essel ha can be seen in Figu e 6.
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Figu e5.Me alsphe espackingde ice.
Theme alsphe epacking,a e beinghea edinano en o hedesi ed empe a u e,was
deposi edina he mallyinsula ed essel ha canbeseeninFigu e6.

Figu e6.The mallyinsula ed essel(dimensionsinmm).
Mo eo e , hedesignedde iceinco po a esanai p ehea e bymeanso elec ical esis ance,
whichallowedpe o ming es sa di e en ini ialai  empe a u es.All heelemen sdesc ibedin his
sec iona ein eg a edin he inalexpe imen alse upshowninFigu e7.
Figu e 6. The mally insula ed essel (dimensions in mm).
Mo eo e , he designed de ice inco po a es an ai p ehea e by means o elec ical esis ance,
which allowed pe o ming es s a di e en ini ial ai empe a u es. All he elemen s desc ibed in his
sec ion a e in eg a ed in he inal expe imen al se up shown in Figu e 7.
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Figu e7.Comple eme alsphe espackingde ice o ene gy eco e y.
2.2.4.FixedBedHeigh Es ima ion
Theconcep ualidea o  he ixedbedo me alsphe eshe einappliedconsis so  he ollowing
s eps.Fi s , hemol enma e ialispou edon heme alsphe es.A e  ha , hesphe es oge he wi h
he i i iedma e iala eloca edina ixedbedinwhich hesphe esmo ebyg a i yslowly
( ollowingaplug luxmodel).Thus, hesphe esgo om heuppe pa o  he ixedbed o hebo om,
coolingwi hcoun e cu en ai  om400°C o oom empe a u e.AswillbeexplainedinSec ion3.1,
a empe a u eo 400°Ccanbe eachedin hesphe es, o examplewi hanm
m
/m
s
 a ioo 0.4and
wi hasphe ediame e o 50mm.
Thees ima iono  hepo en ialene gy eco e y om hep oposedp ocessneeds hep e ious
calcula ionso somepa ame e s.The e o e, hepu poseo  hissec ionwas oes ima e he esidence
imeo  hesphe es op oducea empe a u edec ease om400°C o oom empe a u e,aswellas
henecessa yai  lowand he empe a u e ha wouldbe eachedin heai .Thep oposedme hod
oob ain hese esul sisasemi‐empi icalmodel a ia iono  he empe a u eo  hesphe esin he
bed.PleaseseeAppendixA o mo ein o ma ion.Thisallowedes ima ingh’,whichisa a ia iono 
heo iginalhunde  heassump ionsimposed,whicha eexplainedinAppendixA.
Onceh’wasknown,i waspossible oes ima e hedimensionso  heequipmen .To hisend,a
s eady‐s a ebalancewaspe o medin he ixedbed egene a o showninFigu e8.Equa ions(1)
and(2)collec  hecomponen so  hesebalanceequa ions.The esidence imenecessa y o achie ing
adec easein heme alsphe es empe a u e om400 o40°Cwascalcula edalsobymeanso  hese
balanceequa ions.Thiscalcula ionallowedob aining he empe a u ep o ilealong he ixedbed
egene a o (Figu e8).
Figu e 7. Comple e me al sphe es packing de ice o ene gy eco e y.
2.2.4. Fixed Bed Heigh Es ima ion
The concep ual idea o he ixed bed o me al sphe es he ein applied consis s o he ollowing
s eps. Fi s , he mol en ma e ial is pou ed on he me al sphe es. A e ha , he sphe es oge he
wi h he i i ied ma e ial a e loca ed in a ixed bed in which he sphe es mo e by g a i y slowly
( ollowing a plug lux model). Thus, he sphe es go om he uppe pa o he ixed bed o he bo om,
cooling wi h coun e cu en ai om 400
◦
C o oom empe a u e. As will be explained in Sec ion 3.1,
a empe a u e o 400
◦
C can be eached in he sphe es, o example wi h an m
m
/m
s
a io o 0.4 and
wi h a sphe e diame e o 50 mm.
The es ima ion o he po en ial ene gy eco e y om he p oposed p ocess needs he p e ious
calcula ions o some pa ame e s. The e o e, he pu pose o his sec ion was o es ima e he esidence
ime o he sphe es o p oduce a empe a u e dec ease om 400
◦
C o oom empe a u e, as well as
he necessa y ai low and he empe a u e ha would be eached in he ai . The p oposed me hod o
ob ain hese esul s is a semi-empi ical model a ia ion o he empe a u e o he sphe es in he bed.
Please see Appendix A o mo e in o ma ion. This allowed es ima ing h
0
, which is a a ia ion o he
o iginal h unde he assump ions imposed, which a e explained in Appendix A.
Once h
0
was known, i was possible o es ima e he dimensions o he equipmen . To his end,
a s eady-s a e balance was pe o med in he ixed bed egene a o shown in Figu e 8. Equa ions (1)
and (2) collec he componen s o hese balance equa ions. The esidence ime necessa y o achie ing
a dec ease in he me al sphe es empe a u e om 400 o 40
◦
C was calcula ed also by means o hese
balance equa ions. This calcula ion allowed ob aining he empe a u e p o ile along he ixed bed
egene a o (Figu e 8).
ms· kg
h!·cs kJ
kg·K!·(Ts(x−∆x)−Ts(x))(K)=ma kg
h!·ca kJ
kg·K!·(Ta(x−∆x)−Ta(x))(K)(1)
h0(x)kJ
h·m2·K·A(∆x)(m2)·Ts(x−∆x)+Ts(x)
2−
Ta(x−∆x)+Ta(x)
2(K)=makg
h·cakJ
kg·K·(Ta(x−∆x)−Ta(x))(K)(2)
P ocesses 2020,8, 1590 9 o 20
P ocesses2020,8,xFORPEERREVIEW9o 21

Figu e8.Fixedbed egene a o scheme.
m

·kg
h·c
s
kJ
kg·K·󰇛T

(x−∆x)−T

(x)󰇜󰇛K󰇜=m

kg
h·c
a
kJ
kg·K·󰇛T
a
(x−∆x)−T
a
(x)󰇜󰇛K󰇜
(1)
hʹ󰇛x󰇜kJ
hm
2
·K·A󰇛∆x󰇜m
2
·󰇧T

󰇛x−∆x󰇜+T

󰇛x󰇜
2-
T
a
󰇛x−∆x󰇜+T
a
󰇛x󰇜
2󰇨󰇛K󰇜=m

kg
h·c
a
kJ
kg·K·󰇛T
a
󰇛x-∆x󰇜−T
a
(x)󰇜󰇛K󰇜
(2)
Theequa ionswe esol ed ollowingas andalonepa h.Imposing ha Ts(x),Ts(x–“∆”x),and
Ta(x−“∆”x)a eknown,i ispossible oob ainTa(x) omEqua ion(1),aswellas“∆”x om
Equa ion(2).
2.3.PhysicochemicalCha ac e iza ion
Thephysicochemicalcha ac e iza ionwasca iedou bymeansXRDanalysis,modelAXIOS
omPanaly ical.The2θanglewasinc easedby0.05°,wi ha450 imepe s epo e a angeo 10–
90°.Then,di ac ionpa e nswe e eco deda 40mAand45kVin hecasesinwhichi was
necessa y,usingCuKα adia ion(λ=0.154nm).
2.4.Expe imen alPlan
To ul ill hescopeo  hewo kp e iouslyde ined, he ollowingexpe imen alplanwas
designed.Thewholeexpe imen al es swe edi idedin o womaing oupso expe imen s,
co esponding o hesamep e iousdi isionbe ween hejus i ica iono  he empe a u e ha me al
sphe escanachie eand hemeasu emen o  heai  empe a u ein he ixedbedpacking o 
es ima ing hepo en ialene gy eco e y.Table2shows he es spe o medinbo hs ages.The
objec i eo  he i s s agewas oco e all hepossibili ies ega dingme alsphe esdiame e sand
mol enquan i y.Howe e , hedesigno  heseconds agewasaimed oacqui eda a o ene gy
eco e yes ima ion.All heexpe imen sincludedinTable2we econduc ed wice,ensu ing ha  he
esul sa e ep oduciblewi hano e allexpe imen ale o o ±2%.
Figu e 8. Fixed bed egene a o scheme.
The equa ions we e sol ed ollowing a s andalone pa h. Imposing ha Ts(x), Ts(x – “
∆
” x), and Ta
(x
−
“
∆
” x) a e known, i is possible o ob ain Ta(x) om Equa ion (1), as well as “
∆
” x om Equa ion (2).
2.3. Physicochemical Cha ac e iza ion
The physicochemical cha ac e iza ion was ca ied ou by means XRD analysis, model AXIOS
om Panaly ical. The 2
θ
angle was inc eased by 0.05
◦
, wi h a 450 ime pe s ep o e a ange o 10–90
◦
.
Then, di ac ion pa e ns we e eco ded a 40 mA and 45 kV in he cases in which i was necessa y,
using Cu Kα adia ion (λ=0.154 nm).
2.4. Expe imen al Plan
To ul ill he scope o he wo k p e iously de ined, he ollowing expe imen al plan was designed.
The whole expe imen al es s we e di ided in o wo main g oups o expe imen s, co esponding o he
same p e ious di ision be ween he jus i ica ion o he empe a u e ha me al sphe es can achie e and
he measu emen o he ai empe a u e in he ixed bed packing o es ima ing he po en ial ene gy
eco e y. Table 2shows he es s pe o med in bo h s ages. The objec i e o he i s s age was o
co e all he possibili ies ega ding me al sphe es diame e s and mol en quan i y. Howe e , he design
o he second s age was aimed o acqui e da a o ene gy eco e y es ima ion. All he expe imen s
included in Table 2we e conduc ed wice, ensu ing ha he esul s a e ep oducible wi h an o e all
expe imen al e o o ±2%.
P ocesses 2020,8, 1590 16 o 20
3.4. Po en ial Use o he Ene gy Reco e ed in he Regene a o in he Manu ac u e o Syn he ic Slags
A possible i eous ma e ial p oduc ion scheme could co espond o a ypical clinke manu ac u ing
p ocess [
31
], in which, a e he o a y kiln, an o en is included whe e he comple e usion o he
ma e ial occu s. The p ocess would consis o a p ehea e , in which pa o he calcina ion eac ions
would occu ; a o a y kiln, in which he deca bona ion o he ma e ial would be inished and ha
would ake he ma e ial o 1300
◦
C; and inally, a mel ing o e e be a ing u nace, whe e he ma e ial
ha a i es om he o a y kiln would be mol en and hea up o 1500
◦
C o gua an ee i s luidi y.
A e mel ing, he ma e ial would be cooled quickly in he ixed bed o me al sphe es o achie e he
desi ed i eous p ope ies.
To con i m he p oposed p oduc ion p ocess, an XRD analysis o he mixed ma e ial was pe o med
in he p opo ions indica ed in Sec ion 2.1 and hea ed o empe a u es p io o he mel ing poin
(1250–1280
◦
C). As shown in Figu e 16 in which he XRD esul s a e p esen ed, a hose empe a u es,
c ys alline phases appea simila o hose ha occu in he clinke iza ion p ocess (C2S—Dicalcium
Silica e, C3S—T icalcium Alumina e, C3A—T icalcium Silica e, CAF—Te acalcium Alumino e i e).
P ocesses2020,8,xFORPEERREVIEW17o 21
poin (1250–1280°C).AsshowninFigu e16inwhich heXRD esul sa ep esen ed,a  hose
empe a u es,c ys allinephasesappea simila  o hose ha occu in heclinke iza ionp ocess
(C2S—DicalciumSilica e,C3S—T icalciumAlumina e,C3A—T icalciumSilica e,CAF—
Te acalciumAlumino e i e).

Figu e16.Di ac og amwi hc ys allinephaseso  hewas emix u e(1250–1280°C).
The e o e,i canbeconcluded ha syn he icslagsha echa ac e is icsandmine alphases ha 
a e ypically oundin he awma e ialsusedin hemanu ac u eo  heclinke .Fu he mo e,i can
bea i med ha  heene gyconsump ion o i smanu ac u ewillbeo  hesameo de as ha 
consumedin hemanu ac u eo clinke .In hiscon ex , heene gy eco e edin he ixedbed
egene a o p esen edin hiswo kcouldbeusedasai a abou 350–400°C.Fo example,sa ingsin
uelconsump ioncouldoccu i  he egene a o ai s eamwasusedas hecombus ionai inle 
s eam.B oadly,i 10%highe  han heene gyconsump iono clinke p oduc ion(abou 3800kJ/kg
clinke [32])is akenasa e e ence o  heene gyconsump iono syn he icslags, he egene a o ’s
ai  lowcould esul inene gysa ingsin hemanu ac u eo syn he icslags ha couldbea ound
15%o  heene gyneeded o i sp oduc ion.
4.Conclusions
In hiswo k,ano elme hod o ene gy eco e y om hecooling–solidi ica ions ageo a
syn he icslagmanu ac u ingp ocesswassa is ac o ys udied.Thes udywase alua edbymeanso 
anexpe imen als udy ha wascomplemen edby heo e icalcalcula ions oclose heo e all
pe o mance.
Theexpe imen als agewasdi idedin o wodi e en ia edg oupo  es s.The i s g oupaimed
oob ain he empe a u e alueo  heme alsphe eswhen hemol enma e ialwaspou edo e 
hem.Thesecondexpe imen alwasca iedou  oe alua e heme alsphe es–ai  low empe a u e
p o ilesina eal ixedbed.Du ing heexpe imen al es s, hescopewas oanalyze he empe a u es
ob ainedin hecen e andon hesu aceo  heme alsphe es.Thanks o hisexpe imen als udy,i 
waspossible omeasu ea empe a u ein he angeo 295–410°Cin hecen e o  hesphe eand302–
482°Co e  hesu ace.Thus,i allowedse ingupa empe a u e alue o  hesecondexpe imen al
s age,whichconsequen lyallowed he heo e icalcalcula iono  heene gy eco e ype kgo mol en
slag.Mo eo e , hemol enma e ial ha waspou edo e  heme alsphe eswasanalyzedbymeans
o XRD,and he o ma iono  hecha ac e is ic i eousphasewas e i ied.
Themainpu poseo  he heo e icalapp oachwas oachie ea ixedbed egene a o heigh ,
whichp o ed ha  hep ocessis iableindus ially.Tomee  hisend,hwasp e iouslyes ima ed
wi h hehelpo  he aluesob ainedin hesecondexpe imen als age.The ixedbedheigh calcula ed
p o ed obeindus iallyachie able.Once hepo en ialindus ial ixedbedheigh wasob ainedand
Figu e 16. Di ac og am wi h c ys alline phases o he was e mix u e (1250–1280 ◦C).
The e o e, i can be concluded ha syn he ic slags ha e cha ac e is ics and mine al phases ha
a e ypically ound in he aw ma e ials used in he manu ac u e o he clinke . Fu he mo e, i can be
a i med ha he ene gy consump ion o i s manu ac u e will be o he same o de as ha consumed in
he manu ac u e o clinke . In his con ex , he ene gy eco e ed in he ixed bed egene a o p esen ed
in his wo k could be used as ai a abou 350–400
◦
C. Fo example, sa ings in uel consump ion could
occu i he egene a o ai s eam was used as he combus ion ai inle s eam. B oadly, i 10% highe
han he ene gy consump ion o clinke p oduc ion (abou 3800 kJ/kg clinke [
32
]) is aken as a e e ence
o he ene gy consump ion o syn he ic slags, he egene a o ’s ai low could esul in ene gy sa ings
in he manu ac u e o syn he ic slags ha could be a ound 15% o he ene gy needed o i s p oduc ion.
4. Conclusions
In his wo k, a no el me hod o ene gy eco e y om he cooling–solidi ica ion s age o a
syn he ic slag manu ac u ing p ocess was sa is ac o y s udied. The s udy was e alua ed by means o an
expe imen al s udy ha was complemen ed by heo e ical calcula ions o close he o e all pe o mance.
The expe imen al s age was di ided in o wo di e en ia ed g oup o es s. The i s g oup aimed
o ob ain he empe a u e alue o he me al sphe es when he mol en ma e ial was pou ed o e
hem. The second expe imen al was ca ied ou o e alua e he me al sphe es–ai low empe a u e
p o iles in a eal ixed bed. Du ing he expe imen al es s, he scope was o analyze he empe a u es
ob ained in he cen e and on he su ace o he me al sphe es. Thanks o his expe imen al s udy, i was

P ocesses 2020,8, 1590 17 o 20
possible o measu e a empe a u e in he ange o 295–410
◦
C in he cen e o he sphe e and
302–482 ◦C
o e he su ace. Thus, i allowed se ing up a empe a u e alue o he second expe imen al s age,
which consequen ly allowed he heo e ical calcula ion o he ene gy eco e y pe kg o mol en slag.
Mo eo e , he mol en ma e ial ha was pou ed o e he me al sphe es was analyzed by means o XRD,
and he o ma ion o he cha ac e is ic i eous phase was e i ied.
The main pu pose o he heo e ical app oach was o achie e a ixed bed egene a o heigh ,
which p o ed ha he p ocess is iable indus ially. To mee his end, h was p e iously es ima ed
wi h he help o he alues ob ained in he second expe imen al s age. The ixed bed heigh calcula ed
p o ed o be indus ially achie able. Once he po en ial indus ial ixed bed heigh was ob ained and
analyzed as easible, he ene gy eco e y pe kg o mol en ma e ial was es ima ed. We es ima ed
ha be ween 325 and 550 kJ/kg o mol en ma e ial could be eco e ed, which is 15% o he ene gy
consump ion in syn he ic slag manu ac u ing p ocess.
O e all, he esul s ob ained con i med he po en ial o ou p oposal o ene gy eco e y om he
cooling–solidi ica ion s age o syn he ic slag manu ac u ing. Ou wo k he ein s udied p o ed o be o
g ea in e es o he indus ial scale. The ene gy eco e y o high-ene gy consump ions indus ies is
one o he key poin s o achie e a mo e sus ainable indus ial model.
Au ho Con ibu ions:
Concep ualiza ion, L.F.V., B.N. and M.R.-G.; me hodology, M.R.-G., F.M.B.-M.; so wa e,
M.R.-G., F.M.B.-M.; alida ion, M.R.-G., F.M.B.-M.; o mal analysis, F.M.B.-M.; in es iga ion, L.F.V., B.N., M.R.-G.,
F.M.B.-M.; esou ces, L.F.V., B.N.; da a cu a ion, M.R.-G.; w i ing—o iginal d a p epa a ion, L.F.V., F.M.B.-M.;
w i ing— e iew and edi ing, L.F.V., M.R.-G., F.M.B.-M.; isualiza ion, M.R.-G., F.M.B.-M., X.X.; supe ision, L.F.V.,
F.M.B.-M.; p ojec adminis a ion, L.F.V., B.N.; unding acquisi ion, L.F.V., B.N. All au ho s ha e ead and ag eed
o he published e sion o he manusc ip .
Funding:
This wo k was suppo ed by Uni e si y o Se ille h ough V PPIT-US. Financial suppo o his wo k
was also p o ided by MAVIT p ojec (FEDER-INNTERCONECTA).
Con lic s o In e es : The au ho s decla e no con lic o in e es .
Abb e ia ions
mmmol en mass
mssphe es mass
Tsi sphe es empe a u e inle
Tso sphe es empe a u e ou le
Tai ai empe a u e inle
Tao ai empe a u e ou le
Ts sphe es empe a u e
Ta ai empe a u e
H ixed bed egene a o heigh
D ixed bed egene a o diame e
h con ec i e hea ans e coe icien
h0con ec i e hea ans e coe icien a ia ion
Cs sphe es calo i ic alue
Ca ai calo i ic alue
A(“∆” x) ans e a ea me al sphe es–ai
Appendix A
Exis ing models o he mal egene a o s equi e a e y igo ous adjus men o a ious pa ame e s such
as speed, Reynolds numbe , P and l numbe , o he cha ac e is ic diame e o he sphe es. In addi ion, when
conside ing he balance equa ions ha allow de e mining he beha io o he equipmen , i is necessa y o
sol e a nonlinea equa ion sys em ha equi es app oxima e nume ical echniques o i s esolu ion. Howe e ,
semi-empi ical bed models a e usually esol ed unde he conside a ion ha he sphe e in e nal esis ance is
negligible o hea conduc ion [
33
]. This hypo hesis allows easily es ima ing he cooling empe a u e along he
ixed bed wi h an exponen ially unc ion as ollows (Equa ion (A1)):
T( ) = T∞+ (Ti−T∞)·e
−h
ρs·cs·Dp· (A1)
P ocesses 2020,8, 1590 18 o 20
whe e T( ) is he sphe e empe a u e a ime (
◦
C); T is he ambien empe a u e ha su ounds he sphe e (
◦
C); T
i
is he sphe e empe a u e in =0 (
◦
C);
ρs
is he sphe e densi y (kg/m
3
); c
s
is he speci ic hea o he sphe e (J/kg
·
K);
h is he con ec i e hea ans e coe icien by solid–ai con ec ion (W/m
2·
K); and D
p
is he sphe e diame e (m).
A a cons an descen a e o he sphe es along he ixed bed and in a s eady s a e, Equa ion (1) can be
exp essed as ollows (Equa ion (A2)):
T(x) = A(x) + B(x)·eC(x). (A2)
Thus, o a coo dina e x in he bed, T(x) is he empe a u e o he sphe es; A(x) is he empe a u e o he
ai su ounding he sphe es inside he bed; B(x) is a cons an unc ion o A(x); and C(x) has he exp ession he
ollowing exp ession (Equa ion (A3)):
C(x)=h0(x)
ρs·cs·Dp(A3)
whe e h
0
(x) is he con ec i e hea ans e coe icien a coo dina e x. Since
ρs
, c
s
, and D
p
a e cons an , i can
be a i med ha C(x) only depends on h
0
(x). This allows inding exp essions ha explain he a ia ion o h
0
(x)
knowing he empe a u es o he sphe e and he su ounding ai . Fu he mo e, h
0
(x) depends on bo h ai
p ope ies– low condi ions and he geome y o he me al sphe es o he bed.
S ic ly, he h coe icien should be calcula ed unde a comple e expe imen al design in a s eady s a e o
he empe a u es o he sphe es and a ying he ollowing pa ame e s: Reynolds numbe (Re), P and l numbe
(P ), and sphe e diame e o bed diame e a io. Ne e heless, due o he es ima i e pu poses o his wo k, he
calcula ion o h
0
(x) was done wi h a ixed bed o me al sphe es simila o he one shown in Figu e A1. In his
sys em, he ollowing pa ame e s we e measu ed: he empe a u e o he sphe es (T
s
) and he ai empe a u es a
he inle and ou le o he bed (Tai and Tao, espec i ely), as well as he mass ai low.
P ocesses 2020, 8, x FOR PEER REVIEW 19 o 21
T󰇛x󰇜=A(x)+B(x)·eC(x). (A2)
Thus, o a coo dina e x in he bed, T(x) is he empe a u e o he sphe es; A(x) is he empe a u e
o he ai su ounding he sphe es inside he bed; B(x) is a cons an unc ion o A(x); and C(x) has he
exp ession he ollowing exp ession (Equa ion (A3)):
C󰇛x󰇜=h’(x)
ρs·cs·Dp (A3)
whe e h’(x) is he con ec i e hea ans e coe icien a coo dina e x. Since ρs, cs, and Dp a e cons an ,
i can be a i med ha C(x) only depends on h’(x). This allows inding exp essions ha explain he
a ia ion o h’(x) knowing he empe a u es o he sphe e and he su ounding ai . Fu he mo e, h’(x)
depends on bo h ai p ope ies– low condi ions and he geome y o he me al sphe es o he bed.
S ic ly, he h coe icien should be calcula ed unde a comple e expe imen al design in a s eady
s a e o he empe a u es o he sphe es and a ying he ollowing pa ame e s: Reynolds numbe
(Re), P and l numbe (P ), and sphe e diame e o bed diame e a io. Ne e heless, due o he
es ima i e pu poses o his wo k, he calcula ion o h’(x) was done wi h a ixed bed o me al sphe es
simila o he one shown in Figu e A1. In his sys em, he ollowing pa ame e s we e measu ed: he
empe a u e o he sphe es (Ts) and he ai empe a u es a he inle and ou le o he bed (Tai and Tao,
espec i ely), as well as he mass ai low.
Figu e A1. Scheme o he expe imen al sys em used o es ima e h’(x).
Wi h his sys em, he ene gy ans e balance o a ime o expe imen a ion app oxima es he
exp ession indica ed by Equa ion (A4):
h’·A·󰇛T

S-T

a󰇜=m·cg·󰇛T

ai-T

ao󰇜. (A4)
whe e h’ is he con ec i e hea ans e coe icien (W/m2·K); A is he ans e a ea (m2); T
s is he
a e age sphe es empe a u e in he expe imen a ion ime (°C); T
a is he a e age empe a u e
be ween he inle ai and ou le ai in he expe imen a ion ime (°C); T
ao is he a e age ou le ai
empe a u e in he expe imen a ion ime (°C); T
ai is he a e age inle ai empe a u e in he
expe imen a ion ime (°C); ma is he inle ai mass low (kg/s); and Cg is he ai -speci ic hea
(J/kg·K).
Re e ences
1. Royo, P.; Ace edo, L.; Fe ei a, V.J.; Ga cía-A mingol, T.; López-Sabi ón, A.M.; Fe ei a, G. High-
empe a u e PCM-based he mal ene gy s o age o indus ial u naces ins alled in ene gy-in ensi e
indus ies. Ene gy 2019, 173, 1030–1040, doi:10.1016/j.ene gy.2019.02.118.
2. Baena-Mo eno, F.M.; Rod íguez-Galán, M.; Vega, F.; Reina, T.R.; Vilches, L.F.; Na a e e, B. Regene a ion
o sodium hyd oxide om a biogas upg ading uni h ough he syn hesis o p ecipi a ed calcium
ca bona e: An expe imen al in luence s udy o eac ion pa ame e s. P ocesses 2018, 6, 205,
doi:10.3390/p 6110205.
Figu e A1. Scheme o he expe imen al sys em used o es ima e h0(x).
Wi h his sys em, he ene gy ans e balance o a ime o expe imen a ion app oxima es he exp ession
indica ed by Equa ion (A4):
h0·A·TS−Ta=ma·cg·Tai −Tao(A4)
whe e h
0
is he con ec i e hea ans e coe icien (W/m
2·
K); A is he ans e a ea (m
2
);
Ts
is he a e age sphe es
empe a u e in he expe imen a ion ime (
◦
C);
Ta
is he a e age empe a u e be ween he inle ai and ou le ai
in he expe imen a ion ime (
◦
C);
Tao
is he a e age ou le ai empe a u e in he expe imen a ion ime (
◦
C);
Tai
is he a e age inle ai empe a u e in he expe imen a ion ime (
◦
C);
ma
is he inle ai mass low (kg/s); and C
g
is he ai -speci ic hea (J/kg·K).
Re e ences
1.
Royo, P.; Ace edo, L.; Fe ei a, V.J.; Ga c
í
a-A mingol, T.; L
ó
pez-Sabi
ó
n, A.M.; Fe ei a, G. High- empe a u e
PCM-based he mal ene gy s o age o indus ial u naces ins alled in ene gy-in ensi e indus ies. Ene gy
2019,173, 1030–1040. [C ossRe ]
2.
Baena-Mo eno, F.M.; Rod
í
guez-Gal
á
n, M.; Vega, F.; Reina, T.R.; Vilches, L.F.; Na a e e, B. Regene a ion o
sodium hyd oxide om a biogas upg ading uni h ough he syn hesis o p ecipi a ed calcium ca bona e:
An expe imen al in luence s udy o eac ion pa ame e s. P ocesses 2018,6, 205. [C ossRe ]
3.
Peceño, B.; Lei a, C.; Alonso-Fa iñas, B.; Gallego-Schmid, A. Is ecycling always he bes op ion?
En i onmen al assessmen o ecycling o seashell as agg ega es in noise ba ie s. P ocesses
2020
,8, 776.
[C ossRe ]
P ocesses 2020,8, 1590 19 o 20
4.
Gonz
á
lez-A ias, J.; S
á
nchez, M.E.; Ma
í
nez, E.J.; Co alski, C.; Alonso-Sim
ó
n, A.; Gonz
á
lez, R.; Ca a-Jim
é
nez, J.
Hyd o he mal ca boniza ion o oli e ee p uning as a sus ainableway o imp o ing biomass ene gy po en ial:
E ec o eac ion pa ame e s on uel p ope ies. P ocesses 2020,8, 1201. [C ossRe ]
5.
Philip, P.T.; Hanna o d, A.L.; Konick, E. Me hods o Making Cemen i ious Composi ions om Was e P oduc s.
U.S. Pa en 4756761A, 16 June 1986.
6.
Iglesias, J.; Tuya, A.; Peña, F. P ocedu e o Ob aining Calcium Alumina e F om Was e Ob ained Following
T ea men o Saline D oss F om he P oduc ion o Seconda y Aluminium. U.S. Pa en 20110293494A1, 18
July 2011.
7.
Akiyama, K. P ocess o he Manu ac u e o Aluminous Cemen F om Aluminum Smel ing Residue. U.S.
Pa en 4071373, 6 July 1976.
8.
Lei a, C.; A enas, C.; Alonso-Fa iñas, B.; Vilches, L.F.; Peceño, B.; Rod iguez-Gal
á
n, M.; Baena, F.
Cha ac e is ics o i ed b icks wi h co-combus ion ly ashes. J. Build. Eng. 2016,5. [C ossRe ]
9. Ka ellas, S.; Leon a i is, A.D.; Panousis, G.; Bellos, E.; Kaka as, E. Ene ge ic and exe ge ic analysis o was e
hea eco e y sys ems in he cemen indus y. Ene gy 2013,58, 147–156. [C ossRe ]
10.
Ha a, T.; Shima, H.; Yoshida, Y.; Ma suhashi, R. Model analysis o an in e -indus ial and in e - egional
was e ecycling sys em in Japan. Ene gy 2007,32, 609–618. [C ossRe ]
11.
Rod
í
guez-Gal
á
n, M.; Alonso-Fa iñas, B.; Baena-Mo eno, F.M.; Lei a, C.; Na a e e, B.; Vilches, L.F. Syn he ic
slag p oduc ion me hod based on a solid was e mix i i ica ion o he manu ac u ing o slag-cemen .
Ma e ials 2019,12, 208. [C ossRe ]
12.
Mo z, H.; Geisele , J. P oduc s o s eel slags an oppo uni y o sa e na u al esou ces. Was e Manag.
2001
.
[C ossRe ]
13.
Zhu, J.; Zhong, Q.; Chen, G.; Li, D. E ec o pa iclesize o blas u nace slag on p ope ies o Po land cemen .
P ocedia Eng. 2012,27, 231–236. [C ossRe ]
14.
Pue as, F. Esco ias de al o ho no: Composici
ó
n y compo amien o hid
á
ulico. Ma e . Cons ucci
ó
n
1993
,
43, 37–48. [C ossRe ]
15.
BSI. G anula ed Slag G ound om High Blas Fu nace o Use in Conc e e, Mo a and Pas e; B i ish S anda ds
Ins i u ion: London, UK, 2006.
16.
Wang, K.S.; Lin, K.L.; Tzeng, B.Y. La en hyd aulic eac i i y o blended cemen inco po a ing slag made
om municipal solid was e incine a o ly ash. J. Ai Was e Manag. Assoc. 2003. [C ossRe ] [PubMed]
17.
Reino Ga c
í
a, H. Supe cem
®
. Expe iencia de Holcim (España) con cemen os con esco ias de al o ho no
al amen e adicionados. Pa ol. Cim. Es uc . Ho mig. 2013.
18.
Li, J.; Mou, Q.; Zeng, Q.; Yu, Y. Expe imen al s udy on p ecipi a ion beha io o spinels in s ainless
s eel-making slag unde hea ing ea men . P ocesses 2019,7, 487. [C ossRe ]
19.
Zhang, H.; Wang, H.; Zhu, X.; Qiu, Y.J.; Li, K.; Chen, R.; Liao, Q. A e iew o was e hea eco e y echnologies
owa ds mol en slag in s eel indus y. Appl. Ene gy 2013,112, 956–966. [C ossRe ]
20.
Xiong, B.; Chen, L.; Meng, F.; Sun, F. Modeling and pe o mance analysis o a wo-s age he moelec ic
ene gy ha es ing sys em om blas u nace slag wa e was e hea . Ene gy 2014,77, 562–569. [C ossRe ]
21.
Wang, Q.; Wang, Q.; Tian, Q.; Guo, X. Simula ion s udy and indus ial applica ion o enhanced a senic
emo al by egula ing he p opo ion o concen a es in he SKS coppe smel ing p ocess. P ocesses
2020
,
8, 385. [C ossRe ]
22.
Ishaq, H.; Dince , I.; Na e e , G.F. Exe gy and cos analyses o was e hea eco e y om u nace cemen slag
o clean hyd ogen p oduc ion. Ene gy 2019,172, 1243–1253. [C ossRe ]
23.
Ba a i, M.; Es ahani, S.; U iga d, T.A. Ene gy eco e y om high empe a u e slags. Ene gy
2011
,36, 5440–5449.
[C ossRe ]
24.
Company, N. Me odo Pa a En ia Ma e ial Ab asi o Aluminoso Fundido. ES Pa en ES399446, 3 Feb ua y
1972.
25.
Hulek, A.; Ri zbe gue , F. Me hod o Con inuously P oducing Vi eous Blas Fu nace Slag. U.S. Pa en
6250109B1, 10 July 1998.
26.
Ji ou, K.; Yasu o, T.; Ohkoshi, K. Appa a us o Manu ac u ing Vi eous Slag. U.S. Pa en 4330264A,
18 May 1982.
27.
Naka ani, G.; Kanai, K.; I oh, H.; Takasaki, Y.; Ohkoshi, K.; Yanagida, Y. Appa a us o Manu ac u ing
Rapidly Cooled Solidi ied Slag. U.S. Pa en 4420304A, 13 Decembe 1983.
28. Uni , A.G. Low Ene gy Slag and Cemen P oduc ion. U.S. Pa en 9233485B1, 12 Janua y 2016.
P ocesses 2020,8, 1590 20 o 20
29.
G esesqui-Lobaina, E.; Rod
í
guez-Gonz
á
lez, I.; Fe n
á
ndez-Columbi
é
, T. Cha ac e iza ion o s eel 70XL
used in he manu ac u e o balls o he clinke ’s milling. Min. Geol.
2017
. A ailable online: h ps:
//www. edalyc.o g/ja sRepo/2235/223553249009/h ml/index.h ml (accessed on 24 No embe 2020).
30.
Shaku o , A.G.; Shkol’nik, Y.S.; Pa shin, V.M.; Che o , A.D.; Zhu a le , V.V. Cooling and solidi ica ion o
slag mel in sphe ical packing. S eel T ansl. 2012. [C ossRe ]
31.
Mills, K.C. The es ima ion o slag p ope ies. In P oceedings o he Sou he n A ican Py ome allu gy
In e na ional Con e ence, Johannesbu g, Sou h A ica, 6–9 Ma ch 2011.
32.
Cas illo Ney a, P. Manual P
á
c ico de Combus i
ó
n y Clinke izaci
ó
n. 1990. A ailable online:
h ps://dl-manual.com/download/manual-p ac ico-de-combus ion-y-clinke izacion-6 j3xe k20oe?
hash=168 d0ddbedc13b8ad71e8ec972e7a70 (accessed on 30 No embe 2020).
33.
Inc ope a, F.P.; deWi , D.P. Fundamen os de T ans e encia de Calo ; Pea son P en ice Hall: Uppe Saddle Ri e ,
NJ, USA, 1999; ISBN 970-17-0170-4.
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