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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

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