Argon oxygen decarburization: Difference between revisions

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{{RefimproveMore citations needed|date=November 2010}}

[[File:AOD (Argon, oxygen decarburisation) vessel.jpg|thumb|Refining of a 9.5%CrMoWVNbN steel in an argon, oxygen decarburisation (AOD) vessel]]

'''Argon oxygenArgonoxygen decarburization''' ('''AOD''') is a process primarily used in [[stainless steel]] [[steel making|making]] and other high grade alloys with oxidizable elements such as [[chromium]] and [[aluminium]]. After initial melting the metal is then transferred to an AOD vessel where it will be subjected to three steps of refining; [[decarburization]], [[Reduction (chemistry)|reduction]], and [[desulfurization]].

The AOD process was invented in 1954 by the Lindé Division of The [[Union Carbide Corporation]]<ref name=krivsky73>{{cite journal | doi = 10.1007/BF02667991| bibcode = 1973MT......4.1439K| title = The linde argon-oxygen process for stainless steel; A case study of major innovation in a basic industry| journal = Metallurgical Transactions| volume = 4| issue = 6| pages = 1439–1447| last1 = Krivsky| first1 = W. A.| year = 1973| s2cid = 135951136|url=https://link.springer.com/article/10.1007/BF02667991| url-access = subscription}}</ref><ref name=jalkanen14>{{cite journal |last1=Jalkanen |first1=Heikki |last2=Holappa |first2=Lauri |editor1-last=Seetharaman |editor1-first=Seshadri |title=Converter Steelmaking |journal=Treatise on Process Metallurgy: Industrial Processes |date=2014 |doi=10.1016/C2010-0-67121-5 |publisher=Elsevier|isbn=9780080969886 }}</ref> (which became known as [[Praxair]] in 1992).<ref name=uchist>[http://www.unioncarbide.com/History History] {{Webarchive|url=https://web.archive.org/web/20170609104241/http://www.unioncarbide.com/history |date=2017-06-09 }}. Unioncarbide.com (1917-11-01). Retrieved on 2013-12-28.</ref>

==Process==

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=== Decarburization ===

Prior to the decarburization step, one more step should be taken into consideration: ''de-siliconization'', which is a very important factor for refractory lining and further refinement.

The decarburization step is controlled by ratios of [[oxygen]] to [[argon]] or [[nitrogen]] to remove the [[carbon]] from the metal bath. The ratios can be done in any number of phases to facilitate the reaction. The gases are usually blown through a top lance (oxygen only) and tuyeres[[tuyere]]s in the sides/bottom (oxygen with an inert gas shroud). The stages of blowing remove carbon by the combination of oxygen and carbon forming [[carbon monoxide|CO]] gas.

:4 Cr_(bath) + 3 O₂ → 2 Cr₂O_3([[slag]])

:Cr₂O_3(slag) + 3 C_(bath) → 3 CO_(gas) + 2 Cr_(bath)

To drive the reaction to the forming of CO, the [[partial pressure]] of CO is lowered using argon or nitrogen. Since the AOD vessel is not externally heated, the blowing stages are also used for temperature control. The burning of carbon increases the bath temperature. By the end of this process around 97% of Cr is retained in the steel.

=== Reduction ===

After a desired carbon and temperature level have been reached the process moves to reduction. Reduction recovers the oxidized elements such as chromium from the slag. To achieve this, alloy additions are made with elements that have a higher affinity for oxygen than chromium, using either a silicon alloy or aluminium. The reduction mix also includes [[Lime (material)|lime]] (CaO) and [[fluorspar]] (CaF₂). The addition of lime and fluorspar help with driving the reduction of Cr₂O₃ and managing the slag, keeping the slag fluid and its volume small.

=== Desulfurization ===

Desulfurization is achieved by having a high lime concentration in the slag and a low oxygen activity in the metal bath.

:S_(bath) + CaO_(slag) → CaS_(slag) + O_(bath)

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So, additions of lime are added to dilute sulfur in the metal bath. Also, aluminium or silicon may be added to remove oxygen. Other trimming alloy additions might be added at the end of the step. After sulfur levels have been achieved the slag is removed from the AOD vessel and the metal bath is ready for tapping. The tapped bath is then either sent to a stir station for further chemistry trimming or to a caster for casting.

UsuallyThe desulfurization step is usually the first step of the process.

== History ==

The AOD process has a significant place in the history of steelmaking, introducing a transformative method for refining stainless steel and shaping the industry's landscape. <ref>{{cite book |last1=Cobb |first1=Harold |title=History of Steel Making |date=2010}}</ref>

=== 1960s ===

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== Additional uses ==

In additional to its primary application in the production of stainless steel, many various additional uses have been found for AOD across different industries and materials.

=== Carbon Capture and Utilization ===

=== Carbon Capture and Utilization <ref>{{cite journal |last1=Moon, Choi |first1=E.-J, Y.C |title=Development of carbon-capture binder using stainless steel argon oxygen decarburization slag activated by carbonation |journal=Journal of Cleaner Production |date=2018 |volume=180 |page=642-654}}</ref> ===

AOD slag has shown promising potential for usage as a carbon-capture construction material due to its high capacity for CO2CO₂ and its low cost. Carbonation curing, a process utilizing CO2CO₂ as a curing agent in concrete manufacturing, enhances the chemical properties of stainless steel slag by stabilizing it. During carbonation, g-C2SC₂S (di-calcium silicate) in the slag reacts with CO2CO₂ to produce compounds like calcite and silica gel, resulting in increased compressive strength and improved durability of cementitious materials. The incorporation of AOD slag as a replacement material in ordinary Portland cement (OPC) during carbonation curing has been studied, demonstrating positive effects on strength and reduced porosity.<ref>{{cite journal |last1=Moon|first1= Choi |first2=E.J.|last2= Y.C |title=Development of carbon-capture binder using stainless steel argon oxygen decarburization slag activated by carbonation |journal=Journal of Cleaner Production |date=2018 |volume=180 |pages=642–654|doi=10.1016/j.jclepro.2018.01.189 |bibcode= 2018JCPro.180..642M }}</ref>

=== Cementitious Activity and Modifiers ===

=== Cementitious Activity and Modifiers <ref>{{cite journal |last1=Baciocchi, Costa, Di Bartolomeo, Polettini, Pomi |first1=R., G., E., A. R. |title=Carbonation of Stainless Steel Slag as a Process for CO2 Storage and Slag Valorization. |journal=Waste and Biomass Valorization |date=2010 |volume=1 |issue=4 |page=467-477}}</ref> ===

AOD slag exhibits cementitious activity, but its properties can be changed by modifiers. Studies have focused on the impact of modifiers, such as B2O3 and P2O5 on preventing the crystal transition of β-C2S and improving the cementitious activity of the slag. Addition of B2O3 and P2O5 has shown curing effects and increased compressive strength. These findings suggest that proper selection of modifiers can enhance the performance of stainless steel slag in cementitious applications.<ref>{{cite journal |last1=Baciocchi|first1=Renato|last2= Costa|first2=Giulia|last3= Di Bartolomeo|first3=Elisabetta|last4= Polettini|first4=Alessandra|last5= Pomi|first5=Raffaella|doi=10.1007/s12649-010-9047-1 |title=Carbonation of Stainless Steel Slag as a Process for CO2 Storage and Slag Valorization. |journal=Waste and Biomass Valorization |date=2010 |volume=1 |issue=4 |pages=467–477}}</ref>

=== Chromium Leachability and Carbonation ===

=== Chromium Leachability and Carbonation <ref>{{cite journal |last1=Wang, Zeng, Zhang, Zhang, Zhao |first1=Y., Li, Y., Y. |title=Carbonation of argon oxygen decarburization stainless steel slag and its effect on chromium leachability. |journal=Journal of Cleaner Production |date=2020 |volume=256}}</ref> ===

Another aspect of AOD slag research is its carbonation potential and its impact on chromium leachability. Carbonation of the dicalcium silicate in AOD slag leads to the formation of various compounds, including amorphous calcium carbonate, crystalline calcite, and silica gel. The carbonation ratio of the slag affects the mineral phases, which subsequently influence chromium leachability. Optimal carbonation ratios have been identified to minimize chromium leaching risks during carbonation-related production activities.<ref>{{cite journal |last1=Wang|first1=Ya-Jun|first2=Ya-Nan|last2=Zeng|first3=Jun-Guo|last3=Li|first4=Yu-Zhu|last4=Zhang|first5=Ya-Jing|last5=Zhang|first6=Oing-Zhang|last6=Zhao |title=Carbonation of argon oxygen decarburization stainless steel slag and its effect on chromium leachability. |journal=Journal of Cleaner Production |date=2020 |volume=256|doi=10.1016/j.jclepro.2020.120377 |bibcode=2020JCPro.25620377W }}</ref>

== References ==

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{{Iron and steel production}}