scieee Science in your language
[en] (orig)

Importance of the experimental investigation of a concasting technology

Abstract

The solidification and cooling of a continuously cast billet, slab cylinder, generally of a concasting and the simultaneous heating of the mold is a very complicated problem of three-dimensional (3D) transient heat and mass transfer. The solving of such a problem is impossible without numerical models of the temperature field of the concasting itself hich it is being processed through the concasting machine (caster). The application of the numerical model requires systematic experimentation and measurement of operational parameters on a real caster as well as in the laboratory. The measurement results, especially temperatures, serve not only for the verification of the exactness of the model, but mainly for optímization of the process procedure: real process input data numerical analyses optimization correction of real process. The most important part of the investigation is the measurement of the temperatures in the walls of the mold and the surface of the slab in the zones of secondary and tertiary cooling.

Read accessible full text

Importance of the experimental investigation of a concasting technology

Author: Štětina, Josef; Kavička, František; Katolický, Jaroslav; Mauder, Tomáš; Klimeš, Lubomír
Year: 2018
DOI: 10.1051/matecconf/201816807009
Source: https://dspace.vut.cz/bitstreams/b71e416b-7841-4068-8a09-5688d0cc1295/download
Impo ance o he expe imen al in es iga ion o
a concas ing echnology
Jose Š ě ina1, F an išek Ka ička1,*, Ja osla Ka olický1, Tomáš Maude 1, and Lubomí
Klimeš1
1B no Uni e si y o Technology, Facul y o Mechanical Enginee ing, Czech Republic
Abs ac . The solidi ica ion and cooling o a con inuously cas bille , slab
o cylinde , gene ally o a concas ing and he simul aneous hea ing o he
mold is a e y complica ed p oblem o h ee-dimensional (3D) ansien
hea and mass ans e . The sol ing o such a p oblem is impossible
wi hou nume ical models o he empe a u e ield o he concas ing i sel
which i is being p ocessed h ough he concas ing machine (cas e ).
The applica ion o he nume ical model equi es sys ema ic
expe imen a ion and measu emen o ope a ional pa ame e s on a eal
cas e as well as in he labo a o y. The measu emen esul s, especially
empe a u es, se e no only o he e i ica ion o he exac ness o he
model, bu mainly o op ímiza ion o he p ocess p ocedu e: eal p ocess
 inpu da a  nume ical analyses  op imiza ion  co ec ion o eal
p ocess. The mos impo an pa o he in es iga ion is he measu emen o
he empe a u es in he walls o he mold and he su ace o he slab in he
zones o seconda y and e ia y cooling.
1 In oduc ion
The p oduc ion o s eels, alloys and me allu gical p oduc s in gene al is cons an ly
de eloping. Ma e ials wi h high u ili y pa ame e s a e mo e in demand and adi ional
p oduc ion is being eplaced by highe quali y s eel. Mo e and mo e sophis ica ed
agg ega es using mo e sophis ica ed echnological p ocedu es a e being implemen ed.
In o de o main ain compe i i eness, di e si y p oduc ion and expand o o he ma ke s, i is
necessa y o moni o echnological de elopmen .
In he case o concas ing, i is no possible o ul ill hese equi emen s wi hou he
applica ion o models o all cas e p ocesses dependen on he mal-mechanical
ela ionships. The success ul applica ion o a nume ical model ( o example o a s eel slab)
and i s con inuous imp o emen is necessa ily condi ioned by ca ying ou demanding
expe imen s and hei e alua ion [1-3]. The measu ed pa ame e s se e ei he as di ec
inpu da a o he nume ical model o hey a e used o he c ea ion o his inpu da a. This
is, o example, he case o de e mining he hea ans e coe icien s benea h he cooling
je s ha has o be ca ied ou in he labo a o y (see below). The ange o he measu emen s
ca ied ou and applied was ela i ely conside able. They can he e o e be di ided in o
* Co esponding au ho : ka icka@ me. u b .cz
© The Au ho s, published by EDP Sciences. This is an open access a icle dis ibu ed unde he e ms o he C ea i e Commons
A ibu ion License 4.0 (h p://c ea i ecommons.o g/licenses/by/4.0/).
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018
expe imen al esea ch ca ied ou on an ope a ional de ice (cas e ) and expe imen al
esea ch ca ied ou in labo a o y condi ions [4]. Resea ch conduc ed on he ope a ional
de ice comp ises pe manen moni o ing o he necessa y physical and echnological
quan i ies du ing he en i e p ocess. Some o hem a e pa o a so-called b eakou sys em.
This en ails ela i ely ex ensi e iles o alues con aining indi idual da a as well as ime
eco ds – o example empe a u e in he walls o he mould, su ace empe a u es o he
slab in he place o he bend, he pou ing empe a u e, he cas ing speed, he empe a u e o
he cooling wa e , e c. Fu he mo e, o he expe imen s we e also conduc ed o he
pu poses o esea ch. This includes, o example, measu emen o he su ace empe a u es
in o he places o he seconda y-cooling zone (i.e. he cage), a e exi ing he cage (in he
so-called e ia y-cooling zone) [5] and mo e.
2 An o iginal o -line model o he empe a u e ield o he
concas s eel slab 1 530 × 250 mm (wid h × hickness)
The 3D model had i s been designed as an o -line e sion and la e as an on-line e sion
so ha i could wo k in eal ime. The nume ical model akes in o accoun he empe a u e
ield o he en i e slab ( om he meniscus o he le el o he mel in he mould o he
cu ing o ch) using a 3D mesh con aining mo e han a million nodal poin s.
The solidi ica ion and cooling o a concas slab 1 530 x 250 mm is a global p oblem o
3D ansien hea and mass ans e . I hea conduc ion wi hin he hea ans e in his
sys em is decisi e, he p ocess is desc ibed by he Fou ie -Ki chho equa ion. I desc ibes
he empe a u e ield o he solidi ying slab in all h ee o i s s a es: a he empe a u es
abo e he liquidus (i.e. he mel ), wi hin he in e al be ween he liquidus and solidus
(i.e. in he mushy zone) and a he empe a u es below he solidus (i.e. he solid s a e).
In o de o sol e hese i is con enien o use he explici nume ical me hod o ini e
di e ences. Nume ical simula ion o he elease o la en hea s o phase o s uc u al
changes is ca ied ou by in oducing he en halpy unc ion dependen on empe a u e T,
p e e ably in he o m o en halpy ela ed o uni olume H . The la en hea s a e con ained
he e. A e he au oma ed gene a ion o he mesh (p e-p ocessing) ies on he en y o he
he mophysical ma e ial p ope ies o he in es iga ed sys em, including hei dependence
on empe a u e – in he o m o ables o using polynomials. They a e namely he hea
conduc i i y k, he speci ic hea capaci y c and densi y

o he cas me al.
The empe a u e dis ibu ion in he slabs desc ibed by he en halpy balance equa ion.
The simpli ied equa ion, sui able o applica ion on adial-cas e s wi h a g ea adius, whe e
only he speed (o he mo emen o he slab) componen w in he z-di ec ion is conside ed,
is:
z
H
w
z
T
y
T
x
T
k
τ
H
ν
2
2
2
2
2
2
ν






















(1)
En halpy H as a he modynamic unc ion o empe a u e mus be known o each speci ic
s eel. I is dependen on he composi ion o he s eel and on he a e o cooling.
The expe imen was conduc ed on a 1530 x 250 mm s eel slab, whe e he pou ing
condi ions we e cha ac e ised by he empe a u e in he undish (1 550 C), he empe a u e
o he liquid (1 521 C), and he shi a e o he slab (0.82 m.min-1). The liquidus and
solidus empe a u es a e de i ed om he composi ion o he s eel.
The exac ness o he p esen ed nume ical model depends no only on he spa ial and
empo al disc e iza ion, bu also on he accu acy wi h which he he mophysical p ope ies
o he ma e ials o all pa s o he sys em a e de e mined. I also depends on he de i a ion
o bounda y condi ions, i.e. he alues o he hea ans e coe icien on all cas e
bounda ies.
2
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018
expe imen al esea ch ca ied ou on an ope a ional de ice (cas e ) and expe imen al
esea ch ca ied ou in labo a o y condi ions [4]. Resea ch conduc ed on he ope a ional
de ice comp ises pe manen moni o ing o he necessa y physical and echnological
quan i ies du ing he en i e p ocess. Some o hem a e pa o a so-called b eakou sys em.
This en ails ela i ely ex ensi e iles o alues con aining indi idual da a as well as ime
eco ds – o example empe a u e in he walls o he mould, su ace empe a u es o he
slab in he place o he bend, he pou ing empe a u e, he cas ing speed, he empe a u e o
he cooling wa e , e c. Fu he mo e, o he expe imen s we e also conduc ed o he
pu poses o esea ch. This includes, o example, measu emen o he su ace empe a u es
in o he places o he seconda y-cooling zone (i.e. he cage), a e exi ing he cage (in he
so-called e ia y-cooling zone) [5] and mo e.
2 An o iginal o -line model o he empe a u e ield o he
concas s eel slab 1 530 × 250 mm (wid h × hickness)
The 3D model had i s been designed as an o -line e sion and la e as an on-line e sion
so ha i could wo k in eal ime. The nume ical model akes in o accoun he empe a u e
ield o he en i e slab ( om he meniscus o he le el o he mel in he mould o he
cu ing o ch) using a 3D mesh con aining mo e han a million nodal poin s.
The solidi ica ion and cooling o a concas slab 1 530 x 250 mm is a global p oblem o
3D ansien hea and mass ans e . I hea conduc ion wi hin he hea ans e in his
sys em is decisi e, he p ocess is desc ibed by he Fou ie -Ki chho equa ion. I desc ibes
he empe a u e ield o he solidi ying slab in all h ee o i s s a es: a he empe a u es
abo e he liquidus (i.e. he mel ), wi hin he in e al be ween he liquidus and solidus
(i.e. in he mushy zone) and a he empe a u es below he solidus (i.e. he solid s a e).
In o de o sol e hese i is con enien o use he explici nume ical me hod o ini e
di e ences. Nume ical simula ion o he elease o la en hea s o phase o s uc u al
changes is ca ied ou by in oducing he en halpy unc ion dependen on empe a u e T,
p e e ably in he o m o en halpy ela ed o uni olume H . The la en hea s a e con ained
he e. A e he au oma ed gene a ion o he mesh (p e-p ocessing) ies on he en y o he
he mophysical ma e ial p ope ies o he in es iga ed sys em, including hei dependence
on empe a u e – in he o m o ables o using polynomials. They a e namely he hea
conduc i i y k, he speci ic hea capaci y c and densi y

o he cas me al.
The empe a u e dis ibu ion in he slabs desc ibed by he en halpy balance equa ion.
The simpli ied equa ion, sui able o applica ion on adial-cas e s wi h a g ea adius, whe e
only he speed (o he mo emen o he slab) componen w in he z-di ec ion is conside ed,
is:
z
H
w
z
T
y
T
x
T
k
τ
H
ν
2
2
2
2
2
2
ν






















(1)
En halpy H as a he modynamic unc ion o empe a u e mus be known o each speci ic
s eel. I is dependen on he composi ion o he s eel and on he a e o cooling.
The expe imen was conduc ed on a 1530 x 250 mm s eel slab, whe e he pou ing
condi ions we e cha ac e ised by he empe a u e in he undish (1 550 C), he empe a u e
o he liquid (1 521 C), and he shi a e o he slab (0.82 m.min-1). The liquidus and
solidus empe a u es a e de i ed om he composi ion o he s eel.
The exac ness o he p esen ed nume ical model depends no only on he spa ial and
empo al disc e iza ion, bu also on he accu acy wi h which he he mophysical p ope ies
o he ma e ials o all pa s o he sys em a e de e mined. I also depends on he de i a ion
o bounda y condi ions, i.e. he alues o he hea ans e coe icien on all cas e
bounda ies.
3 Expe imen al measu emen o he applica ion o he model o
he empe a u e ield o a s eel slab 1 530 × 250 mm
3.1 Measu ing empe a u es in he mould (c ys allize ) and in he seconda y
cooling zone
Figu e 1 illus a es he posi ions o 44 he mo-couples in wo lines along all walls o he
mould [6] (so called he b eakou sys em). The esul s o hese measu emen s a e indica ed
in Figu e 2, oge he wi h he cou se o he mean alue and dis ibu ion, and a e en e ed
in o he nume ical model o he mould. Figu e 2 shows an example o eal immedia e
empe a u es on he mould.
In o de o make he model o he empe a u e ield o he mould mo e accu a e and o
e i y i , i is use ul o ca y ou expe imen al measu emen o he su ace empe a u es
immedia ely below he mould, i.e. in he a ea o he e aining olle s. The measu emen is
ca ied ou using op ical py ome e s posi ioned a he cen e o he slab, hal -way be ween
he cen e and he edge and nea he co ne (Figu e 1). This measu emen also makes i
possible o assess whe he he empe a u e ield is symme ical along he axis o he c oss-
sec ion. Figu e 3 shows he measu emen o he su ace empe a u es along he la ge adius
in he a ea o he e aining olle s. The g aph illus a es ha i is necessa y o p ocess he
da a be o e i is used, i.e. i is necessa y o ind a sui able me hod o il e ing. The gene ally
used me hod o il e ing is loa ing a e aging. I s disad an age is ha la ge de ia ions a e
sp ead along a la ge a ea. The median ecu si e il e b ings he s onges il a ion – i s
ou pu is, o example, usable o he egula ion o he seconda y cooling. I is possible o
conside ha in e e ence o he signal om he py ome e is caused by a quali y su ace o
he slab (scales and solidi ied cas ing powde ). Tha is why he maximal alues p o ided by
he maximum il e a e conside ed as co ec [7].
The expe imen al empe a u es could be used om he b eakou sys em (and no he
da a om he py ome e s), which, wi h espec o he densely a anged he mocouples in
wo ho izon al planes (Figu e 1) co e s he asymme y be e . In o de o apply he dynamic
model o he empe a u e ield, he in es iga ion o only one hal o he slab is su icien .
Figu e 3 illus a es he a ou able compa ison o empe a u es measu ed by h ee
py ome e s wi h a calcula ed cu e o he su ace empe a u es o he slab a e 4 000 s.
In o de o make he model o he empe a u e ield mo e accu a e and o e i y i , i was
necessa y o use wo pe manen ly ins alled py ome e s wi h bo h measu ing he uppe
su ace o he slab along he small adius. The i s was ins alled by Mannesmann Demag
al eady a he s age o s a ing up he cas e . I is posi ioned jus be o e he unbending poin .
This py ome e was o iginally used o checking he unc ion o he p ocess seconda y
cooling. Du ing he in eg a ion o he on-line model in o he sys em, i is now used o
compa ing he empe a u es calcula ed by he model wi h he eal ones. Fu he mo e, i was
joined by ano he py ome e o he same ype a he exi om he cage. This a angemen o
bo h models also includes a p ocessing uni ha il e s he measu ed da a. This acili a es
hei u ilisa ion because he so wa e o he empe a u e model no longe has o deal wi h
he il e ing o he signal. The py ome e s measu e wi hin he ange om 750 o 1 200 °C
and in he case o a measu emen ailu e i shows a empe a u e o 700 °C. The posi ioning
o he py ome e s in he wo men ioned poin s is necessa y o he pu poses o checking.
The empe a u e o he slab in he poin o he i s py ome e a he beginning o he
unbending (poin ) mus be highe han he empe a u e p esc ibed o his poin (i.e. a slab
ha is oo cold mus no be s aigh ened ou ). On he o he hand, he empe a u e a he exi
o he cage should be lowe han he p esc ibed empe a u e.
3
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018
Fig. 1. A angemen o measu emen senso s.
Fig. 2. Immedia e empe a u es o he b eakou sys em ( ed – uppe line, yellow – bo om line).
Fig. 3. A compa ison o he cou se o he calcula ed and measu ed empe a u es a e 4 000 s.
3.2 Measu ing o cooling e ec o nozzles
A eal cas e con ains a o al o 8 ypes o ai -je s and geome ical layou s. Since i is no
possible o de e mine he in ensi y o he ai -wa e je s on an ac ual cas e , i is necessa y o
4
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018
Fig. 1. A angemen o measu emen senso s.
Fig. 2. Immedia e empe a u es o he b eakou sys em ( ed – uppe line, yellow – bo om line).
Fig. 3. A compa ison o he cou se o he calcula ed and measu ed empe a u es a e 4 000 s.
3.2 Measu ing o cooling e ec o nozzles
A eal cas e con ains a o al o 8 ypes o ai -je s and geome ical layou s. Since i is no
possible o de e mine he in ensi y o he ai -wa e je s on an ac ual cas e , i is necessa y o
ans e he in es iga ion – o each je indi idually – o he expe imen al labo a o y de ice
(Figu e 4), which is capable o simula ing he su ace o a concas slab [8-11]. This de ice
also allows he measu emen o empe a u es benea h he su ace wi hin he slab.
The empe a u es measu ed a e con e ed o cooling in ensi ies by means o an in e se
ask, which, in u n, a e con e ed o he cou ses o he hea ans e coe icien s using an
expanded nume ical model. The nume ical model also de e mines he e ec o adia ion
which is dependen on he su ace empe a u e.
3.3 Measu ing o slab su ace empe a u es in he e ia y cooling zone
Th ee 2 mm insula ed he mocouples had been used o he measu emen . The ho end o
each he mocouple was ixed inside he hollow ip o a s ud, ca e ully posi ioned on he
su ace o he slab a e cooling (Figu e 5) and all we e hamme ed in o he same dep h
du ing he o ch-cu ing p ocess [12]. The measu emen was ini ia ed on a sepa a ed slab, 5-
o-6 m om he exi o he cage, and con inued un il he slab was cold – in he cooling ield.
The co ec ion o he e o o he measu emen esul , om he hea ans e h ough he
he mocouple insula ion and he p o uding end, is conduc ed ia compa ison
measu emen s. The measu ed empe a u es o h ee su ace poin s a e in Figu e 5.
Fig. 5. Tempe a u es o he h ee su ace poin s.
Fig. 4. The labo a o y de ice in use.
5
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018

4 Conclusion
Resea ch in o he he mokine ics o solidi ica ion and cooling o concas slabs equi es
sys ema ic expe imen al measu emen on a eal cas e . I s esul s a e u ilised no only o
imp o ing he nume ical model o he empe a u e ield bu also o assessing he exac ness
o his model. This dynamic model, which wo ks non-s op in eal ime, ensu es con inuous
co ec ion o he eal p ocess o he cas e in ques ion. The main measu ed quan i ies a e
he empe a u e in he walls o he mould, he su ace empe a u es o he slab upon exi
om he mould, a he unbending poin o he slab and upon exi om he cage o he
seconda y cooling. Fu he mo e, i is he cas ing empe a u e, he cas ing speed, he
empe a u e o he cooling wa e , he me allu gical leng h, e c. A specialised labo a o y
conduc s measu emen s o he sp aying cha ac e is ics o indi idual cooling nozzles. I s
ou pu es ablishes he hea ans e coe icien s benea h each o he wa e o wa e -ai
nozzles.
This esea ch was suppo ed h ough NETME CENTRE PLUS (LO1202) by he Minis y o
Educa ion, You h and Spo s o he Czech Republic unde he „Na ional Sus ainabili y P og amme
I“.
Re e ences
1. J.K. B imacombe, Me all. and Ma e . T ans. B, 30B, 553 (1999)
2. J. Mie inen, S. Louhenkilpi, J. Laine, P oc. o Gen. COST 512 Wo kshop (1996)
3. R.A. Richa d, R. Ha ding, Ch. Becke mann, Me all. & Ma e . T ansac ions, 34B,
297 (2003)
4. J. Š ě ina, Ph.D. Thesis, TU Os a a, Czech Rep. (2007)
5. B.G.Thomas, R.J. O’Malley, D.T. S one, Model. O Cas . Weld., Solidi . P oc. VIII,
San Diego, CA, TMS (1998)
6. F.Ka ička, e al., P oc. o 4 h In e . Con . on Compu . Fluid Dyn. in he Oil, Gas,
Me all. and P oc. Ind., T ondheim, No way (2005)
7. F. Ka ička, e al., Communica ions, 4A2012, 14, 13 (2012)
8. J. Ho ský, M. Raudenský, P oc. o 14 h In e . Me al. & Ma e . Con . METAL, H adec
n/M., Czech Rep. (2005)
9. J. Ho ský, e al., AISTech, I on&S eel Techn. Con . & exp., Cha lo e, USA (2005)
10. M. Raudenský, J. Ho ský, I onm. & S eelm. 32, 2 (2005)
11. J .Š ě ina, Assoc. p o esso . & habili . hesis, TU Os a a, Czech Rep. (2008)
12. J. Š ě ina, e al., Comp. Me h. & Exp. Meas. XII, 749, WIT P ess (2005)
13. F. Ka ička e al., P oc. o 5 h Pac. Rim In e . Con . on Ad . Ma e . & and P oces.,
Zue ich, T ans Tech Pub. (2004)
6
MATEC Web o Con e ences 168, 07009 (2018) h ps://doi.o g/10.1051/ma eccon /201816807009
XXI. AEaNMiFMaE-2018