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Synthesis and characterization of belite calcium sulfoaluminate cements produced by oxyfuel combustion residues

Abstract

In this work, the possibility of reusing ashes issued by an oxyfuel combustion process (OC) as a source of material in the production of belite calcium sulfoaluminate BCSA cements has been investigated. OF process is one of the most promising combustion technologies for CO2 reduction from power plants. Combustion tests were carried out in an oxyfuel bubbling fluidized bed pilot plant. Four BCSA clinker-generating raw mixes were heated in a laboratory electric oven in the temperatures range 1150°-1350°C: one included only natural materials (limestone, clay, bauxite and gypsum), the others contained OC ashes as total substitute for clay. X-ray diffraction (XRD) analysis on the burning products showed high conversion of reactants toward the main BCSA clinker components (C2S and C4A3$), especially at 1200° or 1250°C. Moreover, physical-mechanical tests associated with XRD and differential thermal-thermogravimetric analyses accomplished on all the cements (obtained by adding natural gypsum to the clinkers produced at the best synthesis temperatures) generally displayed a similar hydration behaviour. Telesca, A.; Marroccoli, M.; Ibris, N.; Naik, T.R.; Lupiáñez, C.; Díez, L.I.; Romeo, L.M.; Montagnaro, F.

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Synthesis and characterization of belite calcium sulfoaluminate cements produced by oxyfuel combustion residues

Author: Telesca, A.; Naik, T.R.; Romeo, L.M.; Marroccoli, M.; Díez, L.I.; Montagnaro, F.; Ibris, N.; Lupiáñez, C.
Year: 2019
DOI: 10.18552/2019/IDSCMT5116
Source: https://zaguan.unizar.es/record/99384/files/texto_completo.pdf
Syn hesis and cha ac e iza ion o beli e calcium
sul oalumina e cemen s p oduced by oxy uel combus ion
esidues
A. Telesca*1, M. Ma occoli2, N. Ib is3,
T. R., Naik4, C. Lupiáñez5, L. I. Díez6, L. M. Romeo7 and F. Mon agna o8
1-3School o Enginee ing, Uni e si à degli S udi della Basilica a, ITALY.
(E-mail: an onio. [email protected] , milena.ma [email protected] , nelu a.ib[email p o ec ed] )
4Depa men o Ci il Enginee ing and Mechanics, Uni e si y o Wisconsin, USA
(E-mail: a [email protected])
5-7Mechanical Enginee ing Depa men , Uni e sidad de Za agoza, SPAIN.
(E-mail: ca los.lupianez@uniza .es, luisig@uniza .es, luismi@uniza .es)
4 Depa men o Chemical Sciences, Uni e si à degli S udi di Napoli Fede ico II, ITALY.
(E-mail: abio.mon agna [email protected] )
ABSTRACT
In his wo k, he possibili y o eusing ashes issued by an oxy uel combus ion p ocess
(OC) as a sou ce o ma e ial in he p oduc ion o beli e calcium sul oalumina e BCSA
cemen s has been in es iga ed. OF p ocess is one o he mos p omising combus ion
echnologies o CO2 educ ion om powe plan s. Combus ion es s we e ca ied ou
in an oxy uel bubbling luidized bed pilo plan . Fou BCSA clinke -gene a ing aw
mixes we e hea ed in a labo a o y elec ic o en in he empe a u es ange 1150°-
1350°C: one included only na u al ma e ials (limes one, clay, bauxi e and gypsum),
he o he s con ained OC ashes as o al subs i u e o clay.
X- ay di ac ion (XRD) analysis on he bu ning p oduc s showed high con e sion o
eac an s owa d he main BCSA clinke componen s (C2S and C4A3$), especially a
1200° o 1250°C. Mo eo e , physical-mechanical es s associa ed wi h XRD and
di e en ial he mal- he mog a ime ic analyses accomplished on all he cemen s
(ob ained by adding na u al gypsum o he clinke s p oduced a he bes syn hesis
empe a u es) gene ally displayed a simila hyd a ion beha iou .
Keywo ds: Oxy uel combus ion esidues, clinke , beli e calcium sul oalumina e.
INTRODUCTION
The apid g ow h o Wo ld popula ion, he ene gy demand inc ease, he global
wa ming (GW) ha e pushed go e nmen s and in e na ional au ho i ies o se on he
pa h owa ds sus ainable de elopmen . The e is no doub ha GW ep esen s he mos
signi ican challenge o achie ing sus ainable de elopmen ; his phenomenon is
caused by he emission and accumula ion in he a mosphe e o g eenhouse gases
* Co esponding au ho . T: +39 0971 205225. E-mail: an o[email p o ec ed].
Fi h In e na ional Con e ence on Sus ainable Cons uc ion Ma e ials and
Technologies. h p://www.claisse.in o/P oceedings.h m
(GHGs) which a e mainly eleased by he bu ning o ossil uels, land clea ing,
ag icul u e- ela ed and o he human ac i i ies [Benhelal e al., 2013; De Rich e e al.,
2016; Szulejko e al., 2017; Telesca e al., 2017]. Ca bon dioxide is blamed o be he
main esponsible o GW; he e o e, sea ching o p omising app oaches o mi iga e
CO2 emissions ep esen s he p io i y o s udies aimed a alle ia ing he h ea o
clima e change. In his ega d, he ca bon cap u e and s o age (CCS) echnology has
he po en ial o almos comple ely elimina e CO2 [Boo -Hand o d e al., 2014; Leung
e al., 2014; Telesca e al., 2014a; Telesca e al., 2017]. CCS indica es a g oup o
echnologies de eloped o ob ain CO2- ich lue gases eady o be s o ed by injec ion
in o geological s a a wi h speci ic ea u es. Among he di e en CCS p ocesses (e.g.,
chemical abso p ion, chemical and calcium looping), oxy uel combus ion (OC) is o
g ea in e es due o i s concep ual simplici y [Diez e al., 2015]. In OC a blend o
nea ly pu e oxygen and pa o exhaus gas (employed as O2 diluen o sa e y easons),
is used o combus ion, hus lowe ing bo h N2 and NOx con en s in he exhaus gas
[Buh e e al., 2005; Lupiáñez e al., 2013a; Lupiáñez e al., 2014]. In absence o he
mos ele an diluen o CO2 and a e u he ea men s, i is possible o ob ain
s eams >90% CO2- ich. The CO2- ich s eam is hus eady o inal p ocessing and
geological s o age.
Cemen p oduc ion is one o he mos la ge-scale aw ma e ials consuming as well as
ene gy-in ensi e manu ac u ing p ocesses and ep esen s one o he majo indus ial
sec o s gi ing ise o CO2 emission. In ac , he Wo ld’s annual cemen p oduc ion
cu en ly accoun s o abou 4.7 billion ons [Ac i i y epo 2016, 2017] and i s
con ibu ion o he global an h opogenic CO2 emission is es ima ed as high as 7%
(abou 26% o he indus ial CO2 emission) [T egambi e al., 2018]. I is he e o e
widely accep ed he need o inc ease he sus ainabili y o cemen mainly o ien ed a
mi iga ing he CO2 impac .
Po land cemen (PC) is he mos widely used binde all o e he Wo ld; i is ob ained
by in e g inding PC clinke (PCC) wi h a ew pe cen o calcium sul a es (mos ly
gypsum). Fo each kg o PCC p oduced, abou 0.87 kg o CO2 a e eleased [Ba celo
e al., 2014]; ca bon dioxide comes om bo h limes one he mal decomposi ion (abou
60% o he o al CO2 emission) and uel combus ion. The e o e, one app oach o lowe
CO2 emissions is ela ed o he limes one educ ion in he clinke -gene a ing aw meal
[Telesca e al., 2016]. In his ega d, beli e ich-cemen s a e conside ed
en i onmen ally iendly binde s inasmuch as hey can allow a CO2 educ ion as much
as 10% [Pim aksa e al., 2009; Cube os e al., 2010]; mo eo e , he p esence o
calcium sul oalumina e (C4A3$) in he cemen clinke can bo h compensa e he lowe
eac i i y o beli e ( ela i e o ali e) and u he educe he limes one equi emen in
he aw eed [Quillin, 2001]. Beli e calcium sul oalumina e (BCSA) cemen s gene ally
display physical and mechanical p ope ies compa able o OPC [Selçuk e al., 2010];
in ac , hei echnical beha iou mos ly depends on he abili y o C4A3$ and C2S, o
espec i ely gene a e, upon hyd a ion, C6A$3H32, e ingi e (a ea ly ages) and CSH
(a medium and longe ages). Mo eo e , BCSA cemen s a e in e es ing hyd aulic
binde s om he en i onmen al poin o iew inasmuch as hei manu ac u ing
p ocess, compa ed o ha o OPC, displays a p onounced en i onmen ally iendly
cha ac e mainly associa ed o (a) he ela i ely low syn hesis empe a u e, (b) he
dec eased speci ic uel consump ion [Ma occoli e al., 2010a], (c) he easie
g indabili y and (d) he g ea e usabili y o indus ial was es and by-p oduc s whose
u iliza ion is gene ally complica ed [Ma occoli e al., 2009; Ma occoli e al., 2010b;
Ma e al., 2014; Shen and Qian, 2015]. BCSA cemen s a e gene ally p oduced by
bu ning a aw mix composed by limes one (L), bauxi e (B), clay (C) and gypsum (G)
a empe a u es anging om 1250°-1350°C [Xue e al., 2016].
In his pape , esidues gene a ed du ing an OC p ocess, ca ied ou in a pilo -scale
luidized bed (FB) eac o , we e es ed as subs i u es o clay in he BCSA clinke -
gene a ing aw mix.
Fou mix u es we e hea ed in a labo a o y elec ic o en in he empe a u es ange
1150°-1350°C: one included only na u al ma e ials ( aken as a e e ence e m), he
o he s con ained OC esidues in a measu e comp ised be ween 24.5 and 56.0% by
mass. The con e sion o eac an s owa ds C2S and C4A3$ was in es iga ed by means
o X- ay di ac ion (XRD) analysis. XRD and di e en ial he mal− he mog a ime ic
(DT−TG) analyses oge he wi h physical and mechanical es s we e employed as
main cha ac e iza ion echniques o ca y ou he in es iga ion.
EXPERIMENTAL
Ma e ials and Oxy uel Pilo Plan
The na u al ma e ials (L, C, B and G) used in his in es iga ion we e aken om
qua ies loca ed in I aly. The OC ashes came om a 95 kW h pilo -scale bubbling
oxy uel luidized bed (FB) eac o (2.5 m high wi h an inne diame e o 21 cm); i is
schema ically epo ed in Figu e 1 and desc ibed elsewhe e [Lupiáñez e al., 2013b].
Figu e 1. Oxy uel luidized bed pilo plan .
The FB eac o (R), cooled by means o a wa e jacke placed a i s bo om and ou
wa e -cooled p obes uni o mly dis ibu ed, was cha ged wi h a bed in en o y o 5 kg
silica sand, luidized a 0.8 ms–1 (wi h a 65% CO2–35% O2 mix u e) and hea ed up o
850°C o 925°C; i was equipped wi h wo di e en de ices o he emo al o ly ash
(ba le chambe , BC, and cyclone, CY, in he o de ) om he lue gas s eam.
A blend o ligni e and biomass co n s o e ed he appa a us in a 70:30 ene gy a io;
mo eo e , o cap u e he SO2 gene a ed du ing he combus ion h ough he in si u
desul u iza ion (calcium, Ca (in he so ben ): sul u , S (in he uel)), wo di e en
limes ones (A and B) we e al e na i ely injec ed in o FBR.
Th ee di e en es s we e pe o med: hei ope a ing condi ions, o he sake o cla i y,
a e summa ized in Table 1. Du ing each es , h ee kind o combus ion esidues we e
collec ed: a bo om ash (BA), ex ac ed om he bo om o FBR, and wo ly ashes
(BCFA, CYFA) wi hd awn along he lue gas ea men line.
Table 1. Ope a ing condi ions o he es s ca ied ou in he in he FBR.
Tes no.
Fuel
Limes one
Ca:S
FBR Tempe a u e, °C
1
Ligni e+Co n s o e
A
2
925
2
“
A
6
850
3
“
B
6
925
The esidues o each es we e hen mixed o p epa e h ee blends (B1, B2 and B3),
p opo ioned consis en wi h he co esponding amoun gene a ed du ing he
expe imen al ac i i y (40%BA-50%BCFA-10%CYFA).
The chemical composi ion (in e ms o majo oxides) o he aw ma e ials, de e mined
by X- ay luo escence echnique (wa eleng h dispe si e BRUKER Explo e S4
appa a us), is shown in Table 2.
Table 2. Chemical analysis o he na u al and was e aw ma e ials, w %
L
B
G
C
B1
B2
B3
CaO
55.16
-
30.10
10.40
49.92
27.13
16.84
SiO2
-
7.20
3.00
54.10
21.35
37.70
44.38
Al2O3
-
56.30
0.90
11.50
4.23
8.62
10.67
Fe2O3
-
6.30
0.30
4.50
3.86
10.54
11.63
SO3
-
-
36.20
-
7.26
6.87
5.51
O he s
-
2.30
3.70
6.40
1.89
3.28
2.97
L.o.i.*
43.40
27.50
24.60
13.10
11.48
5.85
8.00
*Loss on igni ion a 950°C
Mix u es Design and Cemen s P epa a ion
Fou BCSA clinke -gene a ing aw mix u es we e designed acco ding o he modi ied
Bogue equa ions [I in e al., 2011], assuming ha C2S, C4A3$, C4AF and C$ amoun
ell in he ange 45%-60%, 20%-30%, 8%-20% and 4%-10%, espec i ely; mo eo e ,
a ee CaO concen a ion alue lowe han 1.5% was also conside ed. All he mix u es
con ained L, B and G; a e e ence mix (MR) included also clay (C), whe eas he
emaining h ee mix u es (M1, M2 and M3) al e na ely con ained B1, B2 o B3 as o al
subs i u e o C. Table 3 and 4 espec i ely epo he modi ied Bogue po en ial
mine alogical composi ion o he ou clinke s (CLIR, CLI1, CLI2 and CLI3) and he
aw meals p opo ion.
Table 3. Bogue po en ial mine alogical composi ion o he clinke s, w %
C2S
C4A3$
C4AF
C$
C
CLIR
56.0
25.9
8.3
5.1
0.1
CLI1
48.7
23.9
12.4
9.7
1.4
CLI2
52.6
20.7
17.9
4.9
0.1
CLI3
50.2
22.8
16.4
7.1
0.1
The aw mix u es we e hea ed in co e ed pla inum c ucibles in a labo a o y elec ic
o en o wo hou s a 1200°, 1250°, 1300° and 1350°C and hen apidly cooled o
oom empe a u e; he ob ained BCSA clinke s we e inely g ound in a F i sch
Pul e ise e 6 (FP6) labo a o y plane a y mill o pass a 90 m sie e and a e wa ds
submi ed o XRD analysis in o de o assess he bes empe a u e o maximizing bo h
C2S and C4A3$ concen a ion.
Table 4. Composi ion o he aw meals, w %
L
B
G
C
B1
B2
B3
MR
53.0
13.0
12.0
22.0
-
-
-
M1
50.0
13.0
5.0
-
56.0
-
-
M2
20.0
16.0
8.0
-
-
32.0
-
M3
52.0
13.5
10.0
-
-
-
24.5
BCSA cemen s (CEMR, CEM1, CEM2 and CEM3) we e hen p epa ed by g inding
he bes ob ained clinke s wi h G in he FP6 labo a o y mill always o pass he 90 m
sie e. The amoun o he added gypsum was de e mined conside ing bo h he C$
al eady p esen in he clinke (calcula ed wi h he modi ied Bogue equa ion) and he
eac ion s oichiome y o he gene a ion o e ingi e (C6A$3H32, he main hyd a ion
p oduc egula ing he echnical beha io a ea ly ages) and aluminium hyd oxide
(AH3) [Manzano e al., 2012; Telesca e al., 2014c], namely:
C4A3$+2C$+38H⇒C6A$H32 +2AH3 (1)
XRD analysis was also employed o he e alua ion o BCSA cemen s hyd a ion
p oduc s; i was pe o med wi h a B uke D2 Phase di ac ome e (CuKα adia ion
and 0.02°2θs-1 scanning a e).
Measu emen s on Mo a s
BCSA mo a p isms we e p epa ed acco ding o he Eu opean S anda d EN 196-1 and
cu ed a e demolding unde wa e a 20°±1°C; hey we e submi ed o comp essi e
s eng h measu emen s a cu ing pe iods anging om 1 o 56 days.
Measu emen s on Pas es
BCSA cemen s we e pas e hyd a ed wi h a wa e /cemen a io equal o 0.5 by mass.
The pas e samples we e cas in o 15-mm-high and 30-mm-diame e cylind ical molds,
and inally placed in polye hylene bags inside a he mos a ic ba h (a 20°C and 95%
ela i e humidi y) o cu ing imes anging om 4 hou s o 56 days. A he end o each
aging pe iod he specimens we e i s c ushed and hen ea ed wi h ace one ( o s op
hyd a ion) and die hyl e he ( o emo e wa e ); he pul e ized samples we e
subsequen ly s o ed in a desicca o o e silica gel–soda lime ( o ensu e p o ec ion

agains H2O and CO2) and inally submi ed o simul aneous DT-TG (NETZSCH-Tasc
414/3 appa a us, hea ing a e 10°C min–1, ope a ing be ween oom empe a u e and
1000°C) and XRD analyses.
Fo he expansion–sh inkage measu emen s, eigh pas e samples, shaped as small
p isms (15X15X78 mm), we e i s ai cu ed a 20°C o 4 hou s and hen demolded.
La e on, one se o samples was aged a 20°C unde ap wa e , he o he s o ed in a
con olled humidi y (H) chambe a 70% R.H. and 20°C. The leng h changes we e
de e mined as a e age alues o ou measu emen s wi h a calipe accu a e o ±1 m;
he e e ence leng h o hem was ha e alua ed jus a e demolding [Telesca e al.,
2014b; Valen i e al., 2012].
RESULTS AND DISCUSSION
The in ensi y o he main XRD peaks o C2S and C4A3$ we e aken as a con e sion
index o he BCSA clinke -gene a ing aw mixes owa d hese p oduc s. The “ex e nal
s anda d me hod” [Culli y e al., 2001] was used and, as a e e ence line, he same
e lec ion om pu e C2S and C4A3$ p epa a ions (gene a ed by high- empe a u e
syn hesis o analy ical g ade calcium ca bona e and qua z o he o me and calcium
ca bona e, alumina and gypsum o he la e ) was aken [Telesca e al., 2015]. The
XRD in ensi y (cps) o he C2S and C4A3$ lines is plo ed as a unc ion o he hea ing
empe a u e (Figu e 2 (a) and 2 (b), espec i ely); each cu e displays a maximum
occu ing, o C2S, a abou 1200 °C (MR and M2) o 1250°C (M1 and M3).
Conce ning calcium sul oalumina e, he bes syn hesis empe a u e was he same as
ha o beli e o mix u es M1 and M2, while highe o MR (1250°C) and M3
(1300°C).
Figu e 2. XRD in ensi y (coun s pe second, cps) o he C2S and C4A3$ main peak o
he BCSA clinke s as a unc ion o he syn hesis empe a u e.
F om an o e all examina ion o he XRD da a abou he syn he ic BCSA clinke s i
was ound ha ha , a e e y in es iga ed empe a u e, he con e sion o eac an s was
comple e and C2S and C4A3$ we e he main bu ning p oduc s. Fu he mo e, C4AF,
C2AS and C$ equen ly occu ed as seconda y componen s.
Tempe a u e, °C
1150 1200 1250 1300 1350
Peak in ensi y, cps
0
500
1000
1500
2000
2500
CLIR
CLI1
CLI2
CLI3
Tempe a u e, °C
1150 1200 1250 1300 1350
Peak in ensi y, cps
500
1000
1500
2000
2500
3000
3500
4000
4500
CLIR
CLI1
CLI2
CLI3
Figu e 3 illus a es he XRD pa e ns o mix u es MR, M1, M2 and M3 hea ed a he
bes syn hesis empe a u es. The ou BCSA cemen s ob ained om he syn he ic
clinke s gene a ed by RM, M1, M2 and M3 a hei bes syn hesis empe a u e we e
espec i ely deno ed wi h he symbols CEMR, CEM1, CEM2 and CEM3.
Figu e 3. XRD pa e ns o he BCSA clinke s ob ained om MR, M1, M2 and M3 a
hei bes syn hesis empe a u e. Legend o symbols: Y=C4A3$, A=C$, B=C2S,
G=C2AS, B =C4AF.
Table 5 epo s he comp essi e s eng h de elopmen o BCSA-based mo a s as a
unc ion o cu ing ime; a all he in es iga ed pe iods, he comp essi e s eng h alues
o CEMR, CEM2 and CEM3 based-mo a s we e simila o each o he ; on he
con a y, he comp essi e s eng h alues o CEM1 we e cons an ly lowe han hose
o he o he cemen s.
Table 5. Resul s o comp essi e s eng h measu emen s o CEMR, CEM1, CEM2 and
CEM3 a a ious aging pe iods.
Days
CEMR
CEM1
CEM2
CEM3
1
12.70.4
8.70.5
10.90.3
12.20.3
2
19.20.3
14.50.2
16.10.5
19.70.2
7
26.40.2
20.40.6
24.50.5
27.90.5
14
32.50.1
24.60.3
30.50.8
33.50.2
28
37.10.5
26.90.1
34.50.7
36.80.4
56
36.90.7
28.40.5
35.10.8
37.10.3
The comp essi e s eng h esul s e e o h ee p isms (six de e mina ions)
The esul s o he expansion–sh inkage es s a e illus a ed in Figu e 4.
Figu e 4: Dimensional s abili y cu es o BCSA-based cemen s (ai and wa e cu ed).
They indica e ha all he in es iga ed BCSA cemen s di e ed e y li le om each
o he , bo h when subme ged unde wa e and cu ed in ai . In pa icula , unde wa e
he maximum expansion alues, eached a e abou 14 days o cu ing, a e comp ised
in he na ow ange o 0.17-0.23%. When cu ed in ai , he in es iga ed pas es showed
a con inuous sh inkage ill 14 days when a minimum leng h change is eached (-0.06%,
-0.05%, -0,08 and -0.07% o CEMR, CEM1, CEM2 and CEM3, espec i ely); since
ha pe iod he alues emained cons an o all he in es iga ed sys ems.
The change o mine alogical phases wi h ongoing hyd a ion was de e mined h ough
XRD and DT-TG in es iga ions. The XRD analysis o all he BCSA cemen s e ealed,
as expec ed, ha a e 4 hou s o hyd a ion e ingi e had al eady o med a he expense
o pa o calcium sul oalumina e and calcium sul a es. A 28 days o cu ing e ingi e
was s ill he main c ys alline phase o hyd a ed cemen s which also e ealed he
p esence o some aces o C4A3$ and ine phases (e.g. gehleni e). A he same cu ing
pe iod, s ä lingi e (C2ASH8), which s a ed o ming al eady a e 1 day o cu ing in
CEMR and CEM1, was e iden oge he wi h ka oi e (C3AH6) in all he in es iga ed
sys ems. These compounds had espec i ely o med om beli e (as silicon sou ce) and
AH3 (as aluminium sou ce) and om he emaining beli e and C2ASH8 acco ding o
he ollowing equa ions [Winne eld e al., 2016]:
C2S+AH3+5H ⇒C2ASH8 (2)
C2S+ C2ASH8 ⇒ CSH2+C3AH6 (3)
Mo eo e , AH3 was no de ec ed a any cu ing pe iod due o i s amo phous na u e. No
signi ican changes we e obse ed a 56 days o cu ing in he ou hyd a ed sys ems.
As an example, XRD pa e ns o CEMR, CEM1 and CEM3 hyd a ed a 4 hou s, 1
and 56 days a e epo ed in Figu e 5.
Tempe a u e (°C)
010 20 30 40 50
Leng h change (%)
-0,10
-0,05
0,00
0,05
0,10
0,15
0,20
0,25
CEMR ai cu ed
CEM1 ai cu ed
CEM2 ai cu ed
CEM3 ai cu ed
CEMR wa e cu ed
CEM1 wa e cu ed
CEM2 wa e cu ed
CEM3 wa e cu ed
Figu e 5. XRD pa e ns o CEMR (le ), CEM1 (middle) and CEM3 ( igh ) hyd a ed o
4 hou s, 1 and 56 days. Legend o symbols: E=C6A$3H32, Y=C4A3$, S=C2ASH8,
K=C3AH6, B=C2S.
The DT−TG analyses almos con i med he mine alogical e alua ions made by XRD.
Th ee endo he mal e ec s we e obse ed and a ibu ed, on he basis o li e a u e da a
[Taylo , 1997], o he ollowing compounds: e ingi e (E) and, con a y o XRD da a,
calcium silica e hyd a e (CSH) and aluminum hyd oxide (AH3); in pa icula , CSH, E
and AH3 we e espec i ely de ec ed h ough he ollowing dehyd a ion endo he mal
peaks: 103°±4 °C, 152°±5°C, 277°±3°C. S ä lingi e could no be iden i ied inasmuch
as i s DT peak was o e lapped by he e ingi e one.
(a)
c
(b)