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<strong>ceramic</strong> <strong>pigments</strong> <strong>for</strong> <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> <strong>produced</strong> <strong>with</strong> chromite ores and<br />

<strong>Black</strong><br />

oxide waste<br />

iron<br />

b Anadolu University, Department of Material Science and Engineering, Iki Eylül Campus 26550, Eskisehir, Turkey<br />

this study, two different natural chromite ores and iron oxide waste from the steel rolling industry were used as less expensive<br />

In<br />

raw materials <strong>for</strong> the synthesis of black <strong>ceramic</strong> <strong>pigments</strong> to be used in <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong>. The effects of chromite<br />

alternative<br />

oxide waste ratios and calcination temperature on the pigment properties were investigated. It was found that<br />

ore-iron<br />

ore <strong>with</strong> a higher Cr 2 O 3 /FeO ratio can be used to synthesise black <strong>ceramic</strong> <strong>pigments</strong> when combined <strong>with</strong> the iron<br />

chromite<br />

waste. However, their color intensity was not as strong as commercial black <strong>pigments</strong> due to the presence of other phases<br />

oxide<br />

impurities coming from the chromite ores. When these <strong>pigments</strong> were used in combination <strong>with</strong> commercial black <strong>pigments</strong>,<br />

and<br />

natural and synthetic <strong>pigments</strong> find applications<br />

Inorganic<br />

coloring agents in glazes, <strong>ceramic</strong> <strong>bodies</strong> and <strong>porcelain</strong><br />

as<br />

[1]. Most of the synthetic <strong>pigments</strong> are prepared<br />

enamels<br />

metallic oxides or salts of the desired metals and<br />

<strong>with</strong><br />

must be of industrial chemical purity. However, this<br />

they<br />

them rather expensive. There<strong>for</strong>e, current trends are<br />

makes<br />

the use of less expensive natural raw materials<br />

towards<br />

and/or industrial wastes [6-9].<br />

[2-5]<br />

containing structures have been widely studied<br />

Chromium<br />

<strong>ceramic</strong> <strong>pigments</strong> [10, 11] <strong>for</strong> coloring glazes and <strong>ceramic</strong><br />

as<br />

due to their interesting properties including high<br />

<strong>bodies</strong><br />

resistance and chemical stability combined<br />

temperature<br />

suitable optical properties. Chromium-containing black<br />

<strong>with</strong><br />

<strong>pigments</strong> are either in the spinel or hematite<br />

<strong>ceramic</strong><br />

<strong>Black</strong> <strong>pigments</strong> based on the spinel system are<br />

structures.<br />

used to decorate glazed wall and floor <strong>tile</strong>s, since<br />

widely<br />

remain stable when mixed <strong>with</strong> glazes during high<br />

they<br />

firing. Spinel-based black <strong>pigments</strong> are based on<br />

temperature<br />

ferrochromite, (Fe,Co)(Fe,Cr) 2<br />

O 4<br />

or nickel ferrochromite,<br />

cobalt<br />

(Ni,Fe)(Fe,Cr) 2<br />

O 4<br />

compounds. <strong>Black</strong> <strong>pigments</strong> based<br />

the hematite system are synthesised by a traditional<br />

on<br />

state reaction method to obtain a (Fe,Cr) 2<br />

O 3<br />

solid<br />

solid<br />

and are mainly used in coloring <strong>porcelain</strong>-stoneware<br />

solution<br />

<strong>bodies</strong>. They are not suitable <strong>for</strong> glazes due to their<br />

<strong>tile</strong><br />

[12-14].<br />

instability<br />

many minerals contain chromium, chromite is<br />

Although<br />

author:<br />

*Corresponding<br />

: +90-222-2393750<br />

Tel<br />

+90-222-2393613<br />

Fax:<br />

btanisan@ogu.edu.tr<br />

E-mail:<br />

has a spinel crystalline structure and the theoretical<br />

ore<br />

composition is FeCr 2<br />

O 4<br />

(or FeO·Cr 2<br />

O 3<br />

as oxides).<br />

chemical<br />

the composition of chromite ores<br />

However, 2+ chemical<br />

be more generally written as (Mg,Fe )O·<br />

also could<br />

3+ 2 3<br />

owing to the partial natural substitution<br />

(Cr,Al,Fe 2+ ) 2+ 3+ O +3 , +3 , and Cr by Fe and Al in a lower<br />

Mg by Fe of<br />

[15, 16].<br />

proportion<br />

far as <strong>ceramic</strong> <strong>pigments</strong> are concerned, chromite is a<br />

As<br />

inexpensive natural pigment or a raw material<br />

potential<br />

of its high thermal and chemical stability among<br />

because<br />

oxides and is available on the market in a large<br />

natural<br />

[2]. Natural chromite has been used as a pigment<br />

amount<br />

coloring <strong>porcelain</strong> <strong>tile</strong>s, producing dark gray shades<br />

<strong>for</strong><br />

the fired <strong>tile</strong>. A mixture of 95 wt.% chromite and 5 wt.%<br />

on<br />

additions to a body at a certain amount was used to<br />

CoO<br />

black shades on the fired <strong>tile</strong> [17]. It is also reported<br />

get<br />

natural chromite combined <strong>with</strong> commercial black<br />

that<br />

reduced the cost of black coloring <strong>porcelain</strong>-<br />

pigment<br />

<strong>tile</strong>s [4]. However, chromite used in these studies<br />

stoneware<br />

neither calcined nor combined <strong>with</strong> hematite. Recent<br />

was<br />

on producing less expensive Fe-Cr <strong>pigments</strong><br />

investigations<br />

natural raw materials have shown that limonite and<br />

<strong>with</strong><br />

ores could be used to obtain brown <strong>pigments</strong><br />

chromite<br />

transparent and opaque glazes <strong>for</strong> wall <strong>tile</strong>s [2, 14].<br />

<strong>for</strong><br />

from dark brown to light brown, depending on the<br />

Colors<br />

temperature and chromite-limonite content,<br />

calcination<br />

obtained and present a good alternative to commercial<br />

were<br />

<strong>produced</strong> from pure oxides.<br />

<strong>pigments</strong><br />

oxides are the most widely used raw materials <strong>for</strong><br />

Iron<br />

production. The continually increasing importance<br />

pigment<br />

iron oxide-based <strong>pigments</strong> is due to their non-toxicity,<br />

of<br />

stability, wide variety of colors ranging from<br />

chemical<br />

orange, red, brown to black and low price [18].<br />

yellow,<br />

is reported that hundreds and thousands of tons of<br />

It<br />

J O U R N A L O F<br />

Journal of Ceramic Processing Research. Vol. 12, No. 4, pp. 462~467 (2011)<br />

Ceramic<br />

Processing Research<br />

Tanisan a, * and Servet Turan b<br />

a Belgin<br />

Osmangazi University, Department of Metallurgical and Materials Engineering, Meselik Campus 26480, Eskisehir, Turkey<br />

Eskisehir<br />

the consumption of the commercial <strong>pigments</strong> can be reduced, providing cost savings <strong>for</strong> coloration of <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong>.<br />

Key words: <strong>Black</strong> <strong>ceramic</strong> pigment, Chromite, Iron oxide waste, Spinel, Color.<br />

Introduction<br />

the only commercial ore mineral of chromium. Pure chromite<br />

462


unusable solid waste containing from less<br />

practically<br />

15 to more than 90% iron are <strong>for</strong>med annually by<br />

than<br />

chemical, mechanical engineering and other<br />

metallurgical,<br />

plants [19]. There are several studies on the<br />

industrial<br />

of iron-chromium brown and/or black <strong>ceramic</strong><br />

synthesis<br />

<strong>for</strong> glazes and <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> from Fe-rich<br />

<strong>pigments</strong><br />

wastes. For example, cast iron foundry grinding<br />

industrial<br />

together <strong>with</strong> chromite [20], copper slag flotation<br />

waste<br />

<strong>with</strong> chromite, Cr 2 O 3 , ZnO and CoO [21], Fe-rich<br />

waste<br />

sludge generated during steel wiredrawing<br />

galvanizing<br />

Cr/Ni-rich sludge [22, 23] generated from Cr/Ni<br />

<strong>with</strong><br />

have been used.<br />

plating<br />

aim of this study is to produce (Fe,Cr) 2 O 3 black<br />

The<br />

<strong>pigments</strong> by using natural chromite ores and iron<br />

<strong>ceramic</strong><br />

waste from the steel rolling industry and to investigate<br />

oxide<br />

suitability <strong>for</strong> coloring <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> as a way<br />

their<br />

reduce their coloring cost. It is to be noted that (Fe,Cr) 2 O 3<br />

to<br />

<strong>ceramic</strong> pigment is the most extensively used pigment<br />

black<br />

materials<br />

Raw<br />

ores <strong>with</strong> different chemical compositions;<br />

Chromite<br />

chromite I (Kumas A.S., Turkey) and chromite II<br />

namely<br />

Chimica Mineraria S.P.A, Italy) and iron oxide<br />

(Laviosa<br />

and characterisation of <strong>pigments</strong><br />

Preparation<br />

chromite ores and iron oxide waste was<br />

As-received<br />

separately to the required particle-size by planetary<br />

ground<br />

ball-milling using distilled water and dried. Then,<br />

wet<br />

ores and iron oxide waste containing 30-100 wt.%<br />

chromite<br />

I ore and chromite II ore were mixed by wet<br />

chromite<br />

<strong>for</strong> 20 minutes and the slurries were dried<br />

ball-milling<br />

110 o C. This was followed by calcination firstly at 1200 o C<br />

at<br />

5 hours dwell time. This temperature was selected<br />

<strong>for</strong><br />

the previous studies on a similar system [24]. In<br />

from<br />

to see the effect of the calcination temperature on<br />

order<br />

products, a selected composition was also calcined<br />

reaction<br />

1100 o C and 1300 o C using the same dwell time. The<br />

at<br />

<strong>pigments</strong> were ground by planetary wet ball-<br />

calcined<br />

<strong>for</strong> 2 hours, filtered and dried at 110 o C in an oven.<br />

milling<br />

order to evaluate the color development, 3 wt.% ground<br />

In<br />

was added to a <strong>porcelain</strong> <strong>tile</strong> body composition,<br />

pigment<br />

from a <strong>ceramic</strong> factory (Toprak A.S, Eskisehir,<br />

supplied<br />

Table 1. Chemical composition of raw materials obtained by using XRF analysis (wt.%)<br />

was pressed into 4 cm diameter pellets at 40 MPa<br />

mix<br />

fired in an electric furnace at 1190 o C in 45 minutes<br />

and<br />

cold to cold.<br />

from<br />

compositions of the raw materials were determined<br />

The<br />

an X-ray fluorescence spectrometer (XRF, RIGAKU<br />

using<br />

Primus). A laser diffraction particle size analyser<br />

ZSX<br />

MASTERSIZER 2000G) was used to find<br />

(MALVERN<br />

the particle size distribution of the raw materials and<br />

out<br />

The crystalline phases in the samples were<br />

<strong>pigments</strong>.<br />

using an X-ray diffractometer (XRD, RIGAKU<br />

identified<br />

2200-Series). In the XRD analysis, metallic silicon<br />

Rint<br />

powder was used as a reference to determine the exact<br />

(Si)<br />

of the phases present and also to compare their<br />

d-spacings<br />

amounts.<br />

relative<br />

color parameters of fired <strong>porcelain</strong> <strong>tile</strong> samples<br />

L*a*b*<br />

<strong>with</strong> the <strong>pigments</strong> <strong>produced</strong> in this study were<br />

colored<br />

<strong>with</strong> an UV-Vis spectrophotometer (MINOLTA<br />

measured<br />

d). Measurements were recorded <strong>with</strong> a small<br />

3600<br />

and a standard D 65 light source. The color<br />

aperture<br />

L*, a* and b*, were measured according to<br />

coordinates,<br />

CIE-L*a*b* trichromatic system recommended by the<br />

the<br />

(Commission Internationale del’Eclairage) [25]. In<br />

CIE<br />

system, L* is the degree of lightness and darkness<br />

this<br />

the color in relation to the scale extending from white<br />

of<br />

= 100) to black (L* = 0). a* is the scale extending<br />

(L*<br />

green (−a*) to red (+a*) axis and b* is the scale<br />

from<br />

from blue (−b*) to yellow (+b*) axis. The<br />

extending<br />

difference (∆E*) was calculated according to<br />

color<br />

[(∆L*) 2 +(∆a*) 2 +(∆b*) 2 ] 1/2 . The values ∆L*, ∆a*<br />

∆E*=<br />

∆b* correspond to the difference of each parameter<br />

and<br />

of raw materials<br />

Characterisation<br />

compositions of the raw materials determined<br />

Chemical<br />

the XRF technique are given in Table 1. When<br />

using<br />

I and chromite II ores were compared, they both<br />

chromite<br />

similar amounts of Cr 2 O 3 , chromite I was<br />

contained<br />

to contain less FeO and consequently the Cr 2 O 3 /FeO<br />

found<br />

was higher <strong>for</strong> chromite I. There were also differences<br />

ratio<br />

MgO, Al 2 O 3 and SiO 2 contents in that chromite I was<br />

in<br />

in MgO and SiO 2 whereas chromite II was rich in<br />

rich<br />

2 O 3. The iron oxide waste was determined to contain<br />

Al<br />

97 wt.% Fe 2 O 3 (Table 1). XRD analysis showed that<br />

over<br />

iron oxide waste contained only the hematite phase<br />

the<br />

1(a)) and thus the iron oxide waste will be named<br />

(Fig.<br />

the “hematite waste” hereafter. XRD analysis also showed<br />

as<br />

<strong>Black</strong> <strong>ceramic</strong> <strong>pigments</strong> <strong>for</strong> <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> <strong>produced</strong> <strong>with</strong> chromite ores and iron oxide waste 463<br />

in <strong>porcelain</strong> <strong>tile</strong> production.<br />

Experimental<br />

waste from the steel rolling industry (Eregli Demir-Celik<br />

I<br />

Fabrikalar T.A.S., Turkey) were used as raw materials.<br />

recorded <strong>for</strong> the two samples that are being compared.<br />

Results and Discussion<br />

Turkey) by wet ball-milling. The dried <strong>porcelain</strong> powder<br />

Raw materials Fe 2 O 3 Cr 2 O 3 Al 2 O 3 SiO 2 FeO MgO CaO Others LOI<br />

Iron oxide waste 97.5 0.8 0.9 0.4 0.5<br />

Chromite I ore 42.5 8.4 7.4 17.7 17.8 1.8 1.0 3.4<br />

Chromite II ore 40.9 13.4 3.4 31.1 8.9 1.3 0.9<br />

(LOI is loss of ignition at 1000 o C)


oth chromites contained only spinel type phases<br />

that<br />

that chromite I also contained a minor amount<br />

except<br />

quartz (Fig. 1(b)). It is rather difficult to differentiate<br />

of<br />

composition spinel phases in chromites. However,<br />

different<br />

et al. [26] demonstrated that the iron present<br />

Sanchez-Ramos<br />

the spinel phase of chromite had a +2 valency and thus<br />

in<br />

the phase as the generic magnesiochromite<br />

identified 2+ spinel<br />

)(Cr,Al) 2<br />

O 4<br />

]. For this reason, the content<br />

[(Mg,Fe ferroan<br />

iron oxide is given as FeO in Table 1.<br />

of<br />

2 gives the particle-size distribution of each raw<br />

Table<br />

after planetary ball milling. The average particlesize<br />

material<br />

was around 7 µm and 90% of the particles are below<br />

25 µm. It is known that solid state reactions between<br />

about<br />

components primarily depend on the particle size: the<br />

two<br />

the particle size, the easier is the reaction between the<br />

finer<br />

However, milling into lower particle sizes by<br />

components.<br />

milling requires prolonged milling time that increases<br />

ball<br />

cost of processing.<br />

the<br />

of <strong>pigments</strong><br />

Characterisation<br />

XRD patterns of <strong>pigments</strong> <strong>produced</strong> <strong>with</strong> the use<br />

The<br />

different of chromite I and hematite waste<br />

of o amounts<br />

at 1200 C are shown in Fig. 2. When<br />

calcined mixtures<br />

I was calcined alone, the occurrence of a free<br />

chromite<br />

2<br />

O 3<br />

phase was evident together <strong>with</strong> predominant spinel<br />

Cr<br />

The free Cr 2<br />

O 3<br />

phase was not seen in the XRD<br />

phases.<br />

of the as-received raw material (Fig. 1(b)). This<br />

pattern<br />

Raw materials d 10 d 50 d 90<br />

patterns of <strong>pigments</strong> <strong>produced</strong> by calcining different<br />

XRD<br />

of chromite I-hematite waste mixtures at a constant<br />

amounts<br />

2+ the chromium-containing spinel [(Mg,Fe )·<br />

reveals that<br />

O 4<br />

] was separating to Cr 2<br />

O 3<br />

and another type<br />

2<br />

(Cr,Al)<br />

spinel at high temperatures. This phenomenon was also<br />

of<br />

by Sanchez-Ramos et al. [26] who demonstrated<br />

observed<br />

the Cr 2<br />

O 3<br />

segregates as a differentiable compound,<br />

that<br />

removed from the chromite spinel and remaining<br />

being<br />

in as magnesium, aluminium and iron oxides<br />

only o spinels<br />

C. In the compositions containing hematite<br />

800 above<br />

in addition to the presence of the spinel phases, the<br />

waste,<br />

free Cr 2<br />

O 3<br />

reacts <strong>with</strong> the hematite (Fe 2<br />

O 3<br />

) to<br />

generated<br />

a solid solution phase (Fe 1-x<br />

Cr x<br />

) 2<br />

O 3<br />

(Fig. 2). In the<br />

produce<br />

diagram of Fe 2<br />

O 3<br />

and Cr 2<br />

O 3<br />

, these oxides can be<br />

phase<br />

to a complete (Fe,Cr) 2<br />

O 3<br />

solid solution<br />

observed o generate<br />

the range of compositions up to 1400 C [27]. As<br />

all <strong>for</strong><br />

same amount of silicon (Si) was used in the samples<br />

the<br />

an internal standard, the intensity ratio of the solid<br />

as<br />

phase (Fe 1−xCr x<br />

) 2<br />

O 3<br />

(F) and Si (F/Si) can be used<br />

solution<br />

follow the development of the solid solution phase.<br />

to<br />

Fig. 2, F 110<br />

/Si 111<br />

ratio is 0.0, 0.48, 0.75 and 1.16 <strong>for</strong> the<br />

In<br />

of 100% chromite I, 80% chromite I-20% hematite<br />

mixtures<br />

60% chromite I-40% hematite waste and 40%<br />

waste,<br />

I-60% hematite waste, respectively. The highest<br />

chromite<br />

is observed in the 40% chromite I-60% hematite waste<br />

ratio<br />

indicating that this sample contains the largest<br />

sample,<br />

of the solid solution phase.<br />

amount<br />

XRD patterns of <strong>pigments</strong> <strong>produced</strong> <strong>with</strong> the use<br />

The<br />

different of chromite II and hematite waste<br />

of o amounts<br />

at 1200 C are presented in Fig. 3. The<br />

calcined mixtures<br />

phases were spinels and the solid solution phase<br />

main<br />

1−xCr<br />

x<br />

) 2<br />

O 3<br />

in all compositions. No free Cr 2<br />

O 3<br />

phase<br />

(Fe<br />

464 Belgin Tanisan and Servet Turan<br />

Table 2. Particle size distribution of ball milled raw materials (µm)<br />

Iron oxide waste 1.1 7.8 24.9<br />

Chromite I ore 0.9 7.1 23.0<br />

Chromite II ore 1.0 6.7 20.2<br />

Fig. 2.<br />

temperature of 1200 o C (CI : chromite I, H : hematite waste).<br />

Fig. 1.<br />

XRD patterns of iron oxide waste (a) and chromite ores (b).


3. XRD patterns of <strong>pigments</strong> <strong>produced</strong> by calcining different<br />

Fig.<br />

of chromite II-hematite waste mixtures at a constant<br />

amounts<br />

was observed in the pure chromite II after<br />

<strong>for</strong>mation<br />

in contrast to pure chromite I. This may be due<br />

calcination<br />

the higher amount of FeO content of chromite II which<br />

to<br />

the solid solution phase directly upon calcination.<br />

<strong>for</strong>ms<br />

the F 110 /Si 111 ratio (~0.8) was not changed substantially<br />

Although<br />

<strong>with</strong> the addition of hematite waste, the solid solution<br />

became rich in iron (see the shift of the solid solution<br />

phase<br />

to lower 2θ values, indicated by a dotted line in<br />

peaks<br />

3). Similar shift of 2θ values of the solid solution phase<br />

Fig.<br />

Fe 2 O 3 was also observed by Munoz et al. [24].<br />

<strong>with</strong><br />

both chromite I and chromite II containing compositions,<br />

In<br />

the highest amount of solid solution phase was<br />

when 40% chromite I and 60% hematite waste<br />

obtained<br />

used. There<strong>for</strong>e, to see the effect of temperature on<br />

were<br />

solid solution phase <strong>for</strong>mation, this composition was<br />

the<br />

constant and also calcined at 1100 o C and 1300 o C.<br />

kept<br />

XRD patterns of <strong>pigments</strong> <strong>produced</strong> from 40%<br />

The<br />

I and 60% hematite waste mixtures calcined<br />

chromite<br />

between 1100 o C and 1300 o C are compared in Fig. 4.<br />

at<br />

the same figure, a diffraction pattern of the commercial<br />

In<br />

pigment (Coded as CP-2) is also shown <strong>for</strong> comparison.<br />

black<br />

The XRD results showed that the samples calcined<br />

all temperatures contained (Fe 1−x Cr x ) 2 O 3 solid solution<br />

at<br />

spinel phases. The F 110 /Si 111 intensity ratios in Fig. 4<br />

and<br />

0.58, 1.16 and 0.86 at 1100 o C, 1200 o C and 1300 o C,<br />

is<br />

This indicates that the highest amount of<br />

respectively.<br />

solid solution phase was obtained at 1200 o C which was<br />

the<br />

at the beginning of the study to find out the<br />

selected<br />

composition <strong>for</strong> the <strong>for</strong>mation of the highest<br />

optimum<br />

of the solid solution phase. While the lower amount<br />

amount<br />

the solid solution phase at 1100 o C may be due to<br />

of<br />

reactions, its decreased amount at 1300 o C may<br />

incomplete<br />

due to the decomposition of the solid solution phase<br />

be<br />

by an increased vapour pressure of Cr 2 O 3 .<br />

possibly<br />

measurement<br />

Color<br />

measured L*a*b* values of colored <strong>porcelain</strong> <strong>tile</strong>s<br />

The<br />

4. XRD patterns of <strong>pigments</strong> containing 40% chromite I-<br />

Fig.<br />

hematite waste mixture calcined at different temperatures<br />

60%<br />

1100 o C and 1300 o C. An XRD pattern of black commercial<br />

between<br />

(CP-2) is also included <strong>for</strong> comparison purposes.<br />

pigment<br />

3 wt.% <strong>pigments</strong> (<strong>produced</strong> at 1200 o C according<br />

containing<br />

the procedure given above) are shown in Fig. 5. The<br />

to<br />

prepared <strong>with</strong> pure chromite I gives a yellowbrown<br />

pigment<br />

color which has L*a*b* values of 41.6, 3.0 and 5.2.<br />

an increasing hematite waste percentage in chromite<br />

With<br />

waste mixtures, L*a*b* values were all decreased<br />

I-hematite<br />

the lowest L*a*b* values of 35.9, 1.4 and 1.1, which<br />

and<br />

better black coloring, were obtained <strong>with</strong> the use<br />

indicate<br />

the 40% chromite I and 60% hematite waste composition.<br />

of<br />

These results are in line <strong>with</strong> the XRD spectra that<br />

use of 40% chromite I and 60% hematite waste gave<br />

the<br />

largest amount of the (Fe 1−x Cr x ) 2 O 3 solid solution phase<br />

the<br />

a concurrent decrease of the spinel phase intensity.<br />

<strong>with</strong><br />

commercial black <strong>pigments</strong>, coded as CP-1<br />

However,<br />

CP-2 (Itaca, Spain) both gave L*, a* and b* values of<br />

and<br />

33, < 1 and < 0.5, respectively (Table 3). This indicates<br />

<<br />

even the lowest L*a*b* giving composition (40%<br />

that<br />

I-60% hematite waste) is not good enough to be<br />

chromite<br />

as a replacement <strong>for</strong> a commercial black pigment.<br />

used<br />

may be attributed to the dilution effect of impurity<br />

This<br />

The other reason might be the difference in the<br />

oxides.<br />

size distribution of the pigment. However, please<br />

particle<br />

note that the particle size distribution of the synthesised<br />

also<br />

used in this study was very similar to the com-<br />

pigment<br />

black <strong>pigments</strong> (Table 4). In order to increase the<br />

mercial<br />

coloring, that is, to decrease L*a*b* values, 0.5 and<br />

black<br />

wt.% of a commercial black pigment (CP-2) was used<br />

1<br />

<strong>with</strong> 3 wt.% the pigment (40% chromite I-60%<br />

together<br />

waste composition) in a <strong>porcelain</strong> <strong>tile</strong> body.<br />

hematite<br />

was selected as the commercial black pigment to<br />

CP-2<br />

used together <strong>with</strong> the synthesised pigment in this<br />

be<br />

due to its better L*a*b* values (Table 3). The addition<br />

study<br />

the commercial pigment reduced the L*a*b* values as<br />

of<br />

in Table 3, approaching those of the pure commercial<br />

given<br />

This indicates that chromite I and hematite waste<br />

pigment.<br />

can be a cost-effective complementary to the<br />

mixtures<br />

<strong>Black</strong> <strong>ceramic</strong> <strong>pigments</strong> <strong>for</strong> <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> <strong>produced</strong> <strong>with</strong> chromite ores and iron oxide waste 465<br />

temperature of 1200 o C (CII : chromite II, H : hematite waste).<br />

commercial black <strong>pigments</strong> and help to reduce their usage.


5. The L*a*b* values of colored and fired <strong>porcelain</strong> <strong>tile</strong><br />

Fig.<br />

containing 3 wt.% pigment, prepared by calcining different<br />

samples<br />

of chromite I-hematite waste and chromite II-hematite<br />

amounts<br />

mixtures at a constant temperature of 1200 o C.<br />

waste<br />

3. CIE-L*a*b* and calculated DE* values of colored<br />

Table<br />

<strong>tile</strong> samples<br />

<strong>porcelain</strong><br />

Reference<br />

pigment<br />

Pigment<br />

(wt.%)<br />

CP-2<br />

(wt.%)<br />

a* b* DE*(1) DE*<br />

L*<br />

(2)<br />

and CP-2 : commercial black <strong>pigments</strong>, 40CI-60H designates<br />

(CP-1<br />

chromite I and 60% of hematite waste derived pigment)<br />

40%<br />

Pigment d 10 d 50 d 90<br />

and CP-2 : commercial black <strong>pigments</strong>, 40CI-60H designates<br />

(CP-1<br />

chromite I and 60% of hematite waste derived pigment)<br />

40%<br />

measured L*a*b* values of <strong>pigments</strong> containing<br />

The<br />

chromite I and 60% hematite waste calcined at<br />

40%<br />

between 1100 o C and 1300 o C are given in<br />

temperatures<br />

6. The L*a*b* values of <strong>pigments</strong> were influenced by<br />

Fig.<br />

calcination temperature. L* values decrease <strong>with</strong> a<br />

the<br />

calcination temperature, whereas the values<br />

decreasing<br />

a* and b* were considerably lower at a calcination<br />

of<br />

of 1200 o C in comparison to 1100 o C and<br />

temperature<br />

o C. These coloring observations are in line <strong>with</strong> XRD<br />

1300<br />

given in Fig. 4.<br />

data<br />

prepared <strong>with</strong> chromite II resulted in darker<br />

Pigments<br />

than those <strong>with</strong> chromite I where the chromite<br />

colors<br />

was higher (> 80%) (Fig. 5). This is due to the<br />

content<br />

of the solid solution phase even in the pure<br />

<strong>for</strong>mation<br />

II containing sample. However, at lower chromite<br />

chromite<br />

L*a*b* values of chromite II derived <strong>pigments</strong><br />

contents,<br />

not as low as chromite I derived <strong>pigments</strong>. The<br />

were<br />

black coloring of chromite I and hematite waste<br />

better<br />

6. The L*a*b* values of colored <strong>porcelain</strong> <strong>tile</strong> samples<br />

Fig.<br />

3 wt.% pigment, synthesised by calcining a 40%<br />

containing<br />

I-60% hematite waste mixture at temperatures between<br />

chromite o C and 1300 o C.<br />

1100<br />

466 Belgin Tanisan and Servet Turan<br />

CP-1 3 - 33.0 1.0 0.4 - 1.9<br />

CP-2 3 - 31.4 0.3 -0.3 1.9 -<br />

40CI-60H 3 - 35.9 1.4 1.1 3.0 4.8<br />

40CI-60H 3 0.5 34.5 1.4 0.9 1.6 3.5<br />

40CI-60H 3 1.0 33.8 1.0 0.2 0.8 2.5<br />

4. Particle size distribution of <strong>pigments</strong> (µm)<br />

Table<br />

CP-1 2.4 6.0 14.6<br />

CP-2 1.5 4.7 10.4<br />

40CI-60H 1.9 5.6 12.8


evidenced by lower L* and a* values, may be<br />

mixtures,<br />

to somewhat higher solid solution phase <strong>for</strong>mation in<br />

due<br />

I and hematite waste mixtures. This may be due<br />

chromite<br />

the exsolution of Cr 2 O 3 from chromite I, readily reacting<br />

to<br />

using less expensive chromite ores and hematite<br />

By<br />

black <strong>ceramic</strong> <strong>pigments</strong> suitable <strong>for</strong> <strong>porcelain</strong> <strong>tile</strong><br />

waste,<br />

coloring can be <strong>produced</strong>. A black color close to<br />

body<br />

black <strong>pigments</strong> was obtained after calcination<br />

commercial<br />

40% chromite I and 60% hematite waste mixture at<br />

of o C. The black coloring phase is the (Fe 1−x Cr x ) 2 O 3 solid<br />

1200<br />

phase. However, due to the presence of impurity<br />

solution<br />

of Al 2 O 3 , SiO 2 and MgO the color intensity is not<br />

oxides<br />

strong as commercial black <strong>pigments</strong> which are generally<br />

as<br />

<strong>with</strong> higher purity oxides. These <strong>pigments</strong>, when<br />

prepared<br />

<strong>with</strong> a small amount of commercial black<br />

combined<br />

can reduce the consumption of the more expensive<br />

<strong>pigments</strong>,<br />

<strong>pigments</strong>, providing cost savings <strong>for</strong> black<br />

commercial<br />

of <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong>.<br />

coloration<br />

would like to thank Eregli Demir-Celik Fabrikalari<br />

We<br />

Kumas A.S. and Laviosa Chimica Mineraria S.P.A<br />

T.A.S,<br />

the supply of raw materials. One of us (B. Tanisan)<br />

<strong>for</strong><br />

likes to thank Anadolu University, Material Science<br />

also<br />

Engineering Dept. <strong>for</strong> the use of their facilities and<br />

and<br />

Pervin Dag <strong>for</strong> her help.<br />

Miss<br />

T. Manfredini and F. Bondioli, Ceramic Ind. 150[2] (2000)<br />

1.<br />

53-58.<br />

E. Ozel, I. Küçük and S. Turan, Silicates Ind. 68 (2003) 25-28.<br />

2.<br />

A.B. Corradi, C. Leonelli, T. Manfredini, P. Pozzi and M.<br />

3.<br />

American Ceram. Soc. Bull. 72[5] (1993) 63-69.<br />

Romagnoli,<br />

F. Bondioli, A.M. Ferrari, C. Leonelli and T. Manfredini,<br />

4.<br />

Eng. Proc. 18[2] (1997) 44-58.<br />

Ceram.<br />

V.M. Pogrebenkov and M.B. Sedel’nikova, Glass and<br />

5.<br />

59(2002) 396-399.<br />

Ceramics.<br />

G. Costa, M.J. Ribeiro, T. Trindate and J.A. Labrincha, Bol.<br />

6.<br />

(1994) 63-69.<br />

73[12]<br />

F.J. Berry, N. Costantini and L.E. Smart, Waste Manage.<br />

8.<br />

(2002) 761-772.<br />

22<br />

R.I. Lazau, C. Pacurariu, D. Becherescu and R. Ianos, J.<br />

9.<br />

Ceram. Soc. 27 (2007) 1899-1903.<br />

Eur.<br />

T.S. Lyubenova, M. Ocana and J. Carda, Dyes and Pigments.<br />

10.<br />

(2008) 265-269.<br />

79<br />

R. Munoz, N. Maso, B. Julian, F. Marquez, H. Beltran, P.<br />

11.<br />

and E. Cordoncillo, J. Eur. Ceram. Soc. 24[7]<br />

Escribano<br />

2087-2094.<br />

(2004)<br />

J. Calbo, M.A. Tena, G. Monros, M. Llusar, R. Galindo and<br />

12.<br />

Badenes, American Ceram. Soc. Bull. 84[12] (2005)<br />

J.A.<br />

10-14.<br />

J. Calbo, S. Sorli, M. Llusar, M.A. Tena and G. Monros,<br />

13.<br />

Ceram. Trans. 103[1] (2004) 3-9.<br />

Brith.<br />

E. Ozel and S. Turan, J. Eur. Ceram. Soc. 23 (2003) 2097-2104.<br />

14.<br />

H.B. Xu, Y. Zhang, Z.H. Li, S.L. Zheng, Z.K. Wang, T. Qi<br />

15.<br />

H.Q. Li, J. Cleaner Production. 14 (2006) 211-219.<br />

and<br />

M.F. Gazulla, A. Barba, M.P. Gomez and M. Orduna,<br />

16.<br />

and Geoanalytical Research. 30[3] (2006)<br />

Geostandards<br />

237-243.<br />

G. Biffi, “Porcelain Stoneware Production Manual Method<br />

17.<br />

Use” (Gruppo Editoriale Faenza Editrice S.p.A. Italy, 1999).<br />

of<br />

O.K.R. Montedo, F.M. Bertan, R. Picolli, D. Hotza and A.P.<br />

18.<br />

de Oliveria, Qualicer. (2004) 11-13.<br />

Novaes<br />

A.N. Epikhin and A.V. Krylova, Russian Journal of Applied<br />

19.<br />

76[1] (2003) 20-22.<br />

Chem.<br />

S. Turan, Y. Inceefe and E. Ozel, Key Eng. Mater. 264-268<br />

20.<br />

2473-2476.<br />

(2004)<br />

E. Ozel, S. Turan, S. Çoruh and O.N. Ergun, Waste Manage.<br />

21.<br />

24 (2006) 125-133.<br />

Res.<br />

G. Costa, V.P. Della, M.J. Ribeiro and J.A. Labrincha, American<br />

22.<br />

Soc. Bull. 87[7] (2008) 9101-9107.<br />

Ceram.<br />

G. Costa, V.P. Della, M.J. Ribeiro, A.P.N. Oliveria, G. Monros<br />

23.<br />

J.A. Labrincha, Dyes and Pigments. 77 (2008) 137-144.<br />

and<br />

R. Munoz, M. Martos, C.M. Rotaru, H. Beltran, E. Cordoncillo<br />

24.<br />

P. Escribano, J. Eur. Ceram. Soc. 26[8] (2006) 1363-1370.<br />

and<br />

C.I.E (1978) Recommendations on uni<strong>for</strong>m color spaces,<br />

25.<br />

difference equations, psychometric color terms.<br />

color<br />

No.2 to CIE publication No.15 1971.<br />

Supplement<br />

S. Sanchez-Ramos, A. Domenech-Carbo, J.V. Gimeno-<br />

26.<br />

J. Peris-Vicente and F.M. Valle-Algarra,<br />

AdelantadoÅ,<br />

Acta. 476 (2008) 11-19.<br />

Thermochimica<br />

A. Muan and S. Somiya, J. Am. Ceram. Soc. 57 (1960)<br />

27.<br />

<strong>Black</strong> <strong>ceramic</strong> <strong>pigments</strong> <strong>for</strong> <strong>porcelain</strong> <strong>tile</strong> <strong>bodies</strong> <strong>produced</strong> <strong>with</strong> chromite ores and iron oxide waste 467<br />

Soc. Esp. Ceram V. 46[1] (2007) 7-13.<br />

7. N. Ay, M. Çak and A. Kara, American Ceram. Soc. Bull.<br />

I<br />

<strong>with</strong> the hematite waste to <strong>for</strong>m the solid solution phase.<br />

Conclusions<br />

Acknowledgements<br />

References<br />

204-209.

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