1
M e t a l l u r g i e P r o z e s s t e c h n i k Recycling Synthesis of Ti-Al-V alloys by Aluminothermic Reduction to Produce Pressed Electrodes for ESR Dipl.-Ing Siran Hassan Pour IME Process Metallurgy and Metal Recycling RWTH Aachen University, 52056 Aachen, Germany Prof. A.D. Ryabtsev, Prof. A.A. Troyansky Department of Electrometallurgy Donetsk National Technical University, Ukraine 3 2 2 3 2 3 4 O Al Ti Al TiO 3 2 5 2 6 5 3 5 2 1 O Al V Al O V 3 2 4 3 4 3 8 O Al KCl Al KClO Booster reaction Vanadium oxide reduction Titanium dioxide reduction ATR - production ESR - refining Pressing Electrodes ATR Master Alloy Electroslag Remelting 1 2 3 Motivation reactor lining based on Al 2 O 3 charged material as powder electrical ignition from mixture surface self-propagating reaction through entire mixture settling of metal phase at reactor bottom due to high material and production costs alternative production processes are highly demanded aluminothermic reduction offers a least expensive process through: high temperatures short reaction times self-propagating reaction behavior direct synthesis of titanium alloy by co-reduction of alloying element oxides reduced production costs via decreasing amount of Titanium sponge reactor reaction front propagation slag metal reactor metal slag separation ATR Process determination of β for master alloy Ti-6βAl-4βV definition of process window by adjusting adiabatic reaction temperature reaction enthalpy phys. properties of input material TiO 2 Al CaO ATR product metal cross section chrushed ATR metal Titanium sponge Ti-6Al-4V compact Process Idea kJ H R Ti 1 , 184 kJ H R O V 1 , 621 5 2 kJ H R KClO 3 , 2241 4 0 2 4 6 8 10 0 10 20 30 40 50 0,8 1,2 1,6 2 2,4 2,8 O in wt.-% Al in wt% Al/TiO2 (molar ratio) Al O Al-O-interaction in TiO 2 reduction Vanadium decreases oxygen content in ATR metal to 2900 ppm ESR slag system CaF 2 -CaO-Ca V 2 O 5 KClO 4 adding Ti-sponge to obtain Ti-6Al-4V Ti-sponge acts as binder high binder content required high ATR metal input favored lab-scale ESR unit power supply: 724 kW electrode weight: 1,0 kg protective argon atmosphere used slag system CaF 2 -CaO-Ca monitoring of metal droplet transfer during remelting process deoxidation target < 500ppm β = 4: Ti-26Al-16V β = 5: Ti-30Al-20V TiAl produced via ATR 0 5000 10000 15000 20000 4 5 O in wt.% β in Ti-6βAl-4βV TiAl β 107 TiAl

Synthesis of Ti-Al-V alloys by Aluminothermic Reduction to Produce Pressed ... · M e t a l l u r g i e P r o z e s s t e c h n i k Recycling Synthesis of Ti-Al-V alloys by Aluminothermic

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Page 1: Synthesis of Ti-Al-V alloys by Aluminothermic Reduction to Produce Pressed ... · M e t a l l u r g i e P r o z e s s t e c h n i k Recycling Synthesis of Ti-Al-V alloys by Aluminothermic

Me

tall

urg

ie

Pro

ze

ss

tec

hn

ik

Recycling

Synthesis of Ti-Al-V alloys by Aluminothermic Reduction

to Produce Pressed Electrodes for ESR

Dipl.-Ing Siran Hassan Pour

IME Process Metallurgy and Metal Recycling

RWTH Aachen University, 52056 Aachen, Germany

Prof. A.D. Ryabtsev, Prof. A.A. Troyansky

Department of Electrometallurgy

Donetsk National Technical University, Ukraine

3223

2

3

4OAlTiAlTiO

32526

5

3

5

2

1OAlVAlOV

3243

4

3

8OAlKClAlKClO

Booster reaction

Vanadium oxide reduction

Titanium dioxide reduction

Text

ATR - production ESR - refining

Pressing

Electrodes ATR Master Alloy Electroslag Remelting 1 2 3

Motivation

reactor lining based on Al2O3

charged material as powder

electrical ignition from

mixture surface

self-propagating reaction

through entire mixture

settling of metal phase at

reactor bottom

due to high material and production costs alternative production processes

are highly demanded

aluminothermic reduction offers a least expensive process through:

high temperatures

short reaction times

self-propagating reaction behavior

direct synthesis of titanium alloy by co-reduction of alloying element oxides

reduced production costs via decreasing amount of Titanium sponge

reactor

reaction front propagation

slag

metal

reactor

metal slag separation

ATR Process

determination of β

for master alloy

Ti-6βAl-4βV

definition of process

window by adjusting

adiabatic reaction

temperature

reaction enthalpy

phys. properties of

input material

TiO2

Al

CaO

ATR product

metal cross section

chrushed ATR metal

Titanium sponge

Ti-6Al-4V compact

Process Idea

kJH R

Ti 1,184

kJH R

OV 1,62152

kJH R

KClO 3,22414

0

2

4

6

8

10

0

10

20

30

40

50

0,8 1,2 1,6 2 2,4 2,8

O in

wt.

-%

Al in

wt%

Al/TiO2 (molar ratio)

AlO

Al-O-interaction in TiO2 reduction

Vanadium decreases

oxygen content in ATR

metal to 2900 ppm

ESR slag system

CaF2-CaO-Ca

V2O5

KClO4

adding Ti-sponge

to obtain

Ti-6Al-4V

Ti-sponge acts as

binder

high binder

content required

high ATR metal

input favored

lab-scale ESR unit

power supply: 724 kW

electrode weight: 1,0 kg

protective argon atmosphere

used slag system CaF2-CaO-Ca

monitoring of metal droplet

transfer during remelting

process

deoxidation target < 500ppm

β = 4: Ti-26Al-16V

β = 5: Ti-30Al-20V

TiAl produced

via ATR 0

5000

10000

15000

20000

4 5

O in

wt.

%

β in Ti-6βAl-4βV

TiAl

β

107

TiAl