Presentation - Third International Slag Valorisation Symposium
Presentation - Third International Slag Valorisation Symposium
Presentation - Third International Slag Valorisation Symposium
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IMPROVED SLAG<br />
QUALITIES BY LIQUID SLAG<br />
TREATMENT<br />
D. MUDERSBACH,<br />
P. DRISSEN, H. MOTZ
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Introduction<br />
2 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Production of Iron and Steel <strong>Slag</strong> in Europe<br />
2008: 45.6 million tonnes<br />
BOS<br />
20 %<br />
EAF S<br />
2 %<br />
EAF C<br />
12 %<br />
SecMS<br />
4 %<br />
BFS<br />
62%<br />
Internal use for<br />
metallurgical<br />
purposes<br />
3%<br />
Fertilizer<br />
2%<br />
Hydraulic<br />
engineering<br />
1%<br />
Road<br />
construction<br />
38 %<br />
3 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Use of Iron and Steel <strong>Slag</strong> in Europe<br />
2008: 46.9 million tonnes<br />
Interim storage<br />
5 % Final deposit<br />
2% Others<br />
1 %<br />
Cement<br />
production<br />
48 %<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
6,6 %<br />
2,3 8,0 % %<br />
7,7 mio. t Blast Furnace <strong>Slag</strong>s in Germany 2010<br />
5,4 9,3 %<br />
504515<br />
178765<br />
714126<br />
70,0 %<br />
11,8 %<br />
903922<br />
5365115<br />
4 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
ABS<br />
GBS cement<br />
GBS other<br />
internal use<br />
stock<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
31.3 %<br />
14.3 %<br />
29.4 %<br />
19.6 %<br />
Cement production and CO 2 emissions<br />
- Benefits of slag cements -<br />
Calcination:0.55 t / t Cl<br />
CEM I 32.5 R (= 100 %) CEM II/B-S with 30 % slag (= 72 %)<br />
1011<br />
kg/t<br />
539<br />
kg/t<br />
51.0 %<br />
54.4 %<br />
30.4 %<br />
16.9 %<br />
CEM III/A with 50 % slag (= 53 %) CEM III/B with 75 % slag (= 30 %)<br />
Electr.energy:651 g/kWh<br />
26.4 %<br />
27.8 %<br />
5 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
730<br />
kg/t<br />
45.8 %<br />
52.8 %<br />
300<br />
kg/t<br />
Therm.energy:331 g/kWh<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
3,9 %<br />
8,0 8,0 % %<br />
231171<br />
1508238<br />
5,4 %<br />
472603<br />
6 mio. t Steel <strong>Slag</strong>s in Germany 2010<br />
320959<br />
25,4 %<br />
13512<br />
57,1 %<br />
3388050<br />
6 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
BOF-S<br />
EAF-C-S<br />
EAF-S-S<br />
LF-S<br />
AOD-/VOD-S-S<br />
other<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Increasing the quality<br />
of water granulated<br />
blast furnace slags<br />
7 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
8 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Druckfestigkeit in N/mm 2<br />
60<br />
50<br />
40<br />
30<br />
20<br />
10<br />
0<br />
original<br />
HOS D<br />
Mörtel-Druckfestigkeit (Zement: Mischung HS/Kl 75/25, 4200 cm 2 /g)<br />
Versuche mit SEKS: 51% CaO; 36% Al2O3<br />
Al2O3=11,4%<br />
C/S=1,10<br />
+3%<br />
SEKS<br />
+6%<br />
SEKS<br />
Al2O3=14,8%<br />
+10%<br />
SEKS<br />
C/S=1,39<br />
+20%<br />
SEKS<br />
Al2O3=11,8%<br />
C/S=1,17<br />
HOS D HOS C<br />
original<br />
HOS C<br />
+3%<br />
SEKS<br />
9 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
+6%<br />
SEKS<br />
Al2O3=15,3%<br />
C/S=1,40<br />
+10%<br />
SEKS<br />
2d<br />
7d<br />
28d<br />
+20%<br />
SEKS<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
low basicity CaO/SiO 2 �<br />
low compressive strength of<br />
mortar/concrete<br />
low concentration of Al 2O 3 �<br />
retarded development of (early) strength<br />
Injection of lime/Al 2O 3<br />
into the main runner<br />
10 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH 28/04/2011<br />
10
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
11 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
CaO/SiO2-ratio<br />
1,50<br />
1,45<br />
1,40<br />
1,35<br />
1,30<br />
1,25<br />
1,20<br />
1,15<br />
1. Start<br />
< 1t slag/min<br />
2. Start<br />
CaO/SiO2-ratio = f(CaO-injection) [spoon sample]<br />
08:25<br />
08:33<br />
08:39<br />
08:42<br />
08:48<br />
08:54<br />
08:57<br />
09:03<br />
09:06<br />
09:12<br />
09:18<br />
3. Start<br />
09:27<br />
09:30<br />
09:36<br />
09:42<br />
09:51<br />
09:57<br />
10:00<br />
10:06<br />
12 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
4. Start<br />
5. Start<br />
time<br />
6. Start<br />
10:15<br />
7. Start<br />
10:24<br />
8. Start<br />
10:33<br />
10:36<br />
10:42<br />
10:45<br />
9. Start<br />
10:54<br />
11:03<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
compressive strength [N/mm2]<br />
50<br />
45<br />
40<br />
35<br />
30<br />
25<br />
20<br />
15<br />
10<br />
5<br />
0<br />
compressive strength of mortar prisms as function of gbfs's<br />
basicity CaO/SiO2<br />
unbehandelt 2 4<br />
C/S = 1,17 C/S = 1,25<br />
C/S = 1,29<br />
13 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
2d<br />
7d<br />
28d<br />
C/S<br />
1,30<br />
1,25<br />
1,20<br />
1,15<br />
1,10<br />
C/S= Basicity CaO/SiO2<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Increasing the quality<br />
of basic oxygen<br />
furnace slags for the<br />
use in road<br />
construction<br />
14 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
BOF/EAF slag might have some free CaO<br />
(free lime) & free MgO (periclase). In the<br />
presence of humidity the hydration of<br />
both minerals causes 100 % increase in<br />
volume of the crystals.<br />
15 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
The hydration is a<br />
serious problem in<br />
using steel slag as<br />
construction material !<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
16 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
O 2 + 2 FeO Fe 2O 3 + energy<br />
2 CaOfree + SiO2 2 CaOxSiO2 2 CaOfree + Fe2O3 2 CaOxFe2O3 by injection of sand and oxygen:<br />
� additional heat is generated<br />
- to keep slag liquid<br />
- to heat up and dissolve the sand<br />
� CaO/SiO 2 is reduced<br />
� free lime is dissolved and chemically bound<br />
17 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
18 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Increasing the quality<br />
of basic oxygen<br />
furnace slags for the<br />
use as fertiliser<br />
19 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
Vermartung in Tonnen<br />
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
3.000.000<br />
2.500.000<br />
2.000.000<br />
1.500.000<br />
1.000.000<br />
500.000<br />
0<br />
1945 1955 1965 1975 1985 1995 2005 2015<br />
Jahr<br />
20 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Thomasphosphat<br />
Konverterkalk<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Aim:<br />
sewage sludge ash + BOFS �� „Thomasphosphate 2 nd Generation“<br />
~ 20 % P 2O 5 ~ 1,5 % P 2O 5 ~ 10 % P 2O 5<br />
with ~ 40 % ~ 95 % ~ 99 % available for plants<br />
Whitlockite + Dicalciumsilicate � Calcium-Phosphate-Silicate<br />
Ca 3(PO 4) 2 + 6 Ca 2Si 1-xP xO 4 � Ca 15(PO 4) 2(SiO 4) 6<br />
Approach:<br />
dissolution of the ash in the liquid slag<br />
21 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Problems<br />
with the<br />
physical<br />
properties<br />
of the<br />
liquid slag<br />
Homogeneous<br />
mixture of<br />
sewage sludge<br />
ash and liquid<br />
BOF slag<br />
22 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Zugabe in t<br />
16<br />
14<br />
12<br />
10<br />
8<br />
6<br />
4<br />
2<br />
0<br />
Zugabe zu 20 t LDS mit 1,1 M.-% P2O5<br />
Zugabe Klärschlammasche mit<br />
21,8 M.-% P2O5 in t<br />
4,7<br />
2,5<br />
Problems<br />
with<br />
handling<br />
and<br />
dust<br />
Zugabe<br />
Tierkörperverbrennungsasche mit<br />
37,0 M.-% P2O5 in t<br />
9,9<br />
Mixture:<br />
20t BOFS + 8t ash<br />
(liquid) 4,7(solid)<br />
3 4 5 6 7 8 9 10 11<br />
M.-% P 2O 5 im Produkt<br />
15,1<br />
6,7<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
23 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Converter lime:<br />
rich in lime but<br />
pure in P 2O 5<br />
Sewage sludge<br />
ash: rich in P 2O 5<br />
but P 2O 5 only 40 %<br />
available for plants<br />
24 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Thomasphosphate<br />
of 2 nd generation<br />
Rich in lime and in<br />
P 2O 5 with 99 %<br />
available for plants<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Optimising the<br />
metallurgical work of<br />
electric furnace slags<br />
25 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
hoch<br />
legiert<br />
Stahlerzeugung<br />
Fe 2O 3 SiO 2 CaO Cr 2O 3 NiO ZnO PbO<br />
niedrig<br />
legiert<br />
Steel EAF-<strong>Slag</strong><br />
25 - 40 3 - 7 3 - 5 5 - 15 0,5 - 3 5 - 30 0,1 - 0,2<br />
Staubzusammensetzung<br />
25 - 45 3 - 7 3 - 5 1 - 5 0,1 - 1 15 - 35 0,1 - 1,5<br />
Recycling/Utilisation:<br />
Scandust/Valera<br />
26 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Internal Recycling<br />
Stope filling<br />
Waelz<br />
Oxide<br />
Waelz kiln<br />
Waelz<br />
<strong>Slag</strong><br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
filterhouse<br />
dustsilo<br />
for external<br />
recycling<br />
dusttransmitter<br />
27 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
caol<br />
O 2<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
wt.-% Zn in dust;<br />
kg dust/t liquid steel<br />
35<br />
30<br />
25<br />
20<br />
15<br />
10<br />
5<br />
Zn-content in dust [wt.-%]<br />
External output of dust in kg/t liquid steel<br />
Recycled dust quantity in %<br />
1994 1995 1996 1997 1998 1999 2000 2001 2002 2003<br />
28 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
70<br />
60<br />
50<br />
40<br />
30<br />
20<br />
10<br />
0<br />
28/04/2011<br />
Recycled dust quantity in %
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
ratio (Cr 2O 3)/[Cr]<br />
1,2<br />
1,0<br />
0,8<br />
0,6<br />
0,4<br />
0,2<br />
0,0<br />
w/o dust-Recycling,<br />
only stirring with N 2<br />
Chrome scorification as function of treatment<br />
only dust-Recycling<br />
with C<br />
additional FeSi<br />
with air injection<br />
29 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
additional FeSi<br />
with N 2 injection<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Increasing the quality<br />
of stainless steel<br />
slags<br />
30 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Mineral:<br />
Idealisied<br />
Formula:<br />
% of<br />
Mineral:<br />
Compared to 19 wt.-% Cr2O3 in solid<br />
material, the leaching of 0.7 mg Cr/liter<br />
slag is surprisingly low.<br />
95 % of the total Cr is fixed as chromite, a<br />
Spinel-type mineral.<br />
(Me 2+ Me 2 3+ O4, with Me 2+ = Fe 2+ , Mg 2+ , Ni 2+<br />
and Me 3+ = Fe 3+ , Al 3+ , Cr 3+ ) are known to be<br />
very stable under environmental conditions.<br />
Further progress is possible by stimulating<br />
the formation of spinels.<br />
Electron Microprobe Analyses of Minerals [wt.-%]<br />
SiO 2 Al 2 O 3 CaO MgO Cr 2 O 3 MnO Fe 2 O 3 NiO MoO 2 P 2 O 5 S<br />
Factor SP = 0.2 MgO + 1.0 Al 2O 3 + n Fe total + 0.5 Cr 2O 3<br />
Spinel Me 3+<br />
2Me2+ O4 35 0,3 6,9 1,6 14,6 51,4 5,8 4,5 0,10 0,04 0,03 0,01<br />
Melilithe Ca 2 Al 2 SiO 7 20 33,3 14,1 37,9 2,2 0,1 10,9 0,1 0,03 0,00 0,10 0,53<br />
Bredigite Ca 7 MgSi 4 O 8 45 34,3 0,1 46,5 10,4 1,4 2,4 2,5 0,01 0,01 0,08 0,02<br />
31 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Crtotal (leachate) in mg/l<br />
0,30<br />
0,25<br />
0,20<br />
0,15<br />
0,10<br />
0,05<br />
0,00<br />
EAF-slags: original and laboratory modified<br />
(original slag: Fe total -parts < 1,0 %-wt.)<br />
XRD-investigation:<br />
point: no (Mg,Fe)-(Fe,Al,Cr)-spinel and<br />
square: (Mg,Fe)-(Fe,Al,Cr)-spinel<br />
sp 0,05 mg/l<br />
operational test: without bauxite-addition<br />
operational test: with bauxite-addition<br />
0 5 10 15 20 25 30 35 40 45<br />
factor sp = (0,2xMgO + 1,0xAl 2O 3 [+ 4,0xFe total] lab.- 0,5xCr 2O 3) in %-wt.<br />
32 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
sp >25 %-wt. : Crtotal in leachate
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
33 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
Operational tests<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Spent refractories<br />
34 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Increasing the quality<br />
and optimising the<br />
recycling<br />
of secondary<br />
metallurgy slags<br />
35 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
During solidification of secondary steelmaking slag<br />
some dicalciumsilicate (C 2S) is built, mostly. By<br />
further cooling C 2S transforms from � - to � -<br />
modification. The transformation is accompanied by<br />
an increase in volume of 11 % of the crystals. The<br />
increase in volume destroys the structure of slag.<br />
The transformation causes several problems:<br />
� formation of dust,<br />
� fine grained materials are hardly used in<br />
civil engineering,<br />
� progressive leaching according to<br />
the high specific surface area.<br />
36 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
37 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
� Solution 1 : rapid cooling of the slag<br />
SiO2 8,5<br />
Al2O3 32,7<br />
CaO 45,1<br />
CaO frei 1 - 5<br />
porous<br />
< 1<br />
amorphous<br />
Periclase<br />
(MgO)<br />
beta-C2S<br />
X X<br />
*<br />
(Ca2SiO4) gamma-C2S<br />
X<br />
fine X X X<br />
X<br />
X<br />
(Ca2SiO4) Mayenite<br />
(Ca12Al14O33) X<br />
X<br />
X<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
39 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
40 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Borgehalt im Feststoff [mg/kg]<br />
15000<br />
13500<br />
12000<br />
10500<br />
9000<br />
7500<br />
6000<br />
4500<br />
3000<br />
1500<br />
0<br />
02399<br />
02406<br />
Abhängigkeit der Borkonzentration im S4-Eluat vom Borgehalt im Feststoff<br />
02407<br />
02397<br />
02405<br />
02394<br />
02398<br />
02408<br />
02393<br />
02411<br />
02412<br />
02409<br />
02410<br />
02400<br />
02414<br />
02401<br />
02416<br />
02403<br />
�-C 2S<br />
Borgehalt Feststoff<br />
Borkonzentration Eluat<br />
Trendlinie der Eluatkonzentration<br />
45 kg Glassrock (B-&P-haltig)<br />
60 kg Glassrock (B-&P-haltig)<br />
02404<br />
02402<br />
02413<br />
02424<br />
02415<br />
02422<br />
02417<br />
02418<br />
02420<br />
02421<br />
02423<br />
02425<br />
02419<br />
41 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
30<br />
25<br />
20<br />
15<br />
10<br />
5<br />
0<br />
Borkonzentration im S4-Eluat [mg/l]<br />
GFS Bor<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
Conclusion<br />
42 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011
IMPROVED SLAG QUALITIES BY LIQUID SLAG TREATMENT<br />
43 Second <strong>International</strong> <strong>Slag</strong> <strong>Valorisation</strong> <strong>Symposium</strong> │ D. MUDERSBACH<br />
28/04/2011