Circular Steel: Enablers for a circular economy of climate-neutral steel

Ger­man Rese­arch Foun­da­ti­on (DFG), 1 April 2026 — 31 March 2031

Project description

The DFG Rese­arch Trai­ning Group Cir­cu­lar Steel is a struc­tu­red doc­to­ral rese­arch pro­gram­me fun­ded by the Ger­man Rese­arch Foun­da­ti­on. It brings tog­e­ther doc­to­ral rese­ar­chers and super­vi­sors from dif­fe­rent disci­pli­nes through a coor­di­na­ted rese­arch and qua­li­fi­ca­ti­on pro­gram­me. The Rese­arch Trai­ning Group pro­mo­tes inter­di­sci­pli­na­ry col­la­bo­ra­ti­on, the exch­an­ge of methods and data, and the deve­lo­p­ment of inte­gra­ted solu­ti­ons that extend bey­ond indi­vi­du­al rese­arch projects.

Within this frame­work, Cir­cu­lar Steel inves­ti­ga­tes the sci­en­ti­fic and tech­no­lo­gi­cal foun­da­ti­ons requi­red for a cir­cu­lar and cli­ma­te neu­tral steel indus­try. Its rese­arch spans pri­ma­ry and secon­da­ry steel pro­duc­tion, pro­cess tech­no­lo­gy, alloy and mate­ri­al design, pro­duct per­for­mance, recy­cling, mate­ri­al flows, and sus­taina­bi­li­ty assess­ment. By con­nec­ting the­se per­spec­ti­ves, the pro­gram­me aims to address the enti­re steel cycle rather than iso­la­ted pro­duc­tion or mate­ri­al rela­ted challenges.

Within the over­all pro­gram­me, Area I focu­ses on pro­cess tech­no­lo­gies for cli­ma­te neu­tral steel pro­duc­tion. Topic I‑2 inves­ti­ga­tes the inte­gra­ted ope­ra­ti­on of hydro­gen based direct reduc­tion and elec­tric arc fur­nace steel­ma­king, inclu­ding the effects of DRI pro­per­ties and char­ging con­di­ti­ons as well as the inte­gra­ti­on of hydro­gen pro­duc­tion and was­te-heat recovery.

Cou­pled Pro­cess Simu­la­ti­on of Hydro­gen-Based DRI-EAF Steelmaking

Hydro­gen-based direct reduc­tion fol­lo­wed by elec­tric arc fur­nace (EAF) steel­ma­king is a key rou­te for repla­cing coke-based pri­ma­ry steel pro­duc­tion while retai­ning the fle­xi­bi­li­ty to use recy­cled scrap. Its per­for­mance depends on inter­faces that can­not be resol­ved when hydro­gen pro­duc­tion, direct reduc­tion and EAF steel­ma­king are simu­la­ted as iso­la­ted units.

The tem­pe­ra­tu­re, metal­liza­ti­on, resi­du­al oxy­gen and car­bon, gang­ue com­po­si­ti­on and impu­ri­ty con­tent of direct redu­ced iron (DRI) deter­mi­ne the EAF mel­ting ener­gy, slag volu­me and com­po­si­ti­on, flux demand, foa­ming con­di­ti­ons, refrac­to­ry expo­sure, emis­si­ons and steel qua­li­ty. Char­ging mode is equal­ly important: con­ti­nuous hot char­ging of hydro­gen-redu­ced DRI must be com­pared with cold or pre­hea­ted hot bri­quet­ted iron (HBI) and with dif­fe­rent scrap/DRI ratios.

Topic I‑2 deve­lo­ps a cou­pled dyna­mic pro­cess model for an inte­gra­ted rou­te com­pri­sing high-tem­pe­ra­tu­re solid oxi­de elec­tro­ly­sis (SOEC), hydro­gen-based shaft-fur­nace direct reduc­tion, DRI/HBI hand­ling and EAF steel­ma­king. A lite­ra­tu­re-based DR model will pro­vi­de the mass, com­po­si­ti­on and ther­mal sta­te of the pro­duct to an enhan­ced RWTH dyna­mic EAF model. The EAF model will resol­ve mel­ting and heat trans­fer as well as the dis­tri­bu­ti­on of C, O, P, S and N among steel, slag and gas. Was­te heat reco­very and inter­me­dia­te sto­rage of steam, hydro­gen and oxy­gen will be inte­gra­ted to quan­ti­fy sys­tem-level ener­gy and resour­ce efficiency.

Ope­ra­ting sce­na­ri­os will compa­re elec­tri­ci­ty, natu­ral gas, hydro­gen, oxy­gen and bio­ge­nic or other alter­na­ti­ve car­bon car­ri­ers. Hydro­gen is con­side­red for pro­cess heat, while alter­na­ti­ve car­bon car­ri­ers are asses­sed for car­bu­riza­ti­on and slag foa­ming. The cou­pled model will iden­ti­fy ope­ra­ting win­dows that redu­ce direct fos­sil CO2 emis­si­ons wit­hout com­pro­mi­sing steel, slag or pro­cess performance.

Cen­tral rese­arch ques­ti­on: How do DRI pro­per­ties, scrap share and char­ging tem­pe­ra­tu­re pro­pa­ga­te through EAF ener­gy demand, slag che­mis­try, emis­si­ons and pro­duct quality?

Project goals

  • Imple­ment a DR shaft-fur­nace model, inclu­ding rele­vant side pro­ces­ses, in Python using mass and ener­gy balan­ces, reduc­tion kine­tics and heat-trans­fer rela­ti­ons from the literature.
  • Extend the available dyna­mic EAF pro­cess model for hydro­gen-redu­ced DRI/HBI, fle­xi­ble scrap/DRI mix­tures, con­ti­nuous hot char­ging, cold or pre­hea­ted char­ging and hydro­gen-based pro­cess heat.
  • Repre­sent steel slag gas reac­tions and the dis­tri­bu­ti­on of C, O, P, S and N, inclu­ding desul­fu­riza­ti­on, dephos­pho­riza­ti­on and nitro­gen pick­up or removal.
  • Pre­dict slag amount and com­po­si­ti­on, flux requi­re­ments, MgO satu­ra­ti­on and con­di­ti­ons rele­vant to slag foa­ming and refrac­to­ry protection.
  • Cou­ple EAF was­te-heat reco­very with high-tem­pe­ra­tu­re SOEC elec­tro­ly­sis and buf­fer sto­rage, and use sce­na­rio and sen­si­ti­vi­ty ana­ly­ses to mini­mi­ze ener­gy use, direct fos­sil CO2 emis­si­ons and mate­ri­al los­ses while mee­ting pro­duct-qua­li­ty constraints.

Evaluation criteria

Ener­gy and integration

Elec­tri­ci­ty, che­mi­cal ener­gy, hydro­gen and oxy­gen demand; reco­vera­ble heat; sto­rage requirements.

Metall­ur­gy and quality

Metal tem­pe­ra­tu­re and com­po­si­ti­on; P, S, N, O and C dis­tri­bu­ti­on; steel yield and impu­ri­ty control.

Slag and refractories

Slag amount and com­po­si­ti­on; flux demand; MgO satu­ra­ti­on; con­di­ti­ons rele­vant to slag foa­ming and refrac­to­ry protection.

Cli­ma­te and resources

Direct fos­sil CO2 emis­si­ons, alter­na­ti­ve car­bon use, by-pro­duct qua­li­ty, mate­ri­al los­ses and over­all resour­ce efficiency.

Contact

Mohamed Abouayana, M.Sc.

 

+49 241 80–28926

Dr.-Ing. Thomas Echterhof
 

+49 241 80–25958

Funding

Fun­ded by the Ger­man Rese­arch Foun­da­ti­on (DFG) within Rese­arch Trai­ning Group GRK 3139 “Cir­cu­lar Steel — Enablers for a cir­cu­lar eco­no­my of cli­ma­te-neu­tral steel”, Pro­ject ID 546471228.