Electric Arc Furnace (EAF) modeling has been a common research area to date. This thesis work proposes a new field-data based EAF-specific model. The data used in developing the proposed model is obtained from field measurements of instantaneous voltages and currents of EAF the plants. This model presents the dynamic behavior of the EAF system including all its parts, which are the EAF transformer, the secondary circuit, the electrodes moving and the arc itself. It consists of a cascade connected variable-resistance and &ndash / inductance combination to represent the variation in time of the fundamental frequency, and a current source in parallel with it to inject the harmonics and interharmonics content of the EAF current. The proposed model is capable of representing both AC and DC EAFs, whose controllers&rsquo / set points are the impedance values seen from the low voltage (LV) side of the EAF transformer. The validity of the proposed model has been verified by comparing EMTDC/PSCAD simulations of the model with the field measurements. The results obtained have shown quite satisfactory correlation between the behavior of the proposed model and v the actual EAF operation. To show the advantages of the model while developing FACTS solutions for power quality (PQ) problem mitigation of a given busbar supplying single- or multi-EAF installations, various applications are presented.

In this work, feasibility of utilizing municipal incinerator fly ash (MIFA) of different sources as a substitute of raw materials for steel-making in a mini-mill was studied. Also studied included the efficacy of this mode of melting treatment and recycling. Under the condition of adding 1 wt% MIFA to scrap iron/scrap steel for partial replacement of lime, the L9 orthogonal arrays of Taguchi methods were utilized to investigate the effects of MIFA melting treatment of different sources by an electric arc furnace (EAF). Four experimental factors (i.e., scrap iron mass, lime mass, coke mass, and MIFA mass) were selected to study their effects on Pb leaching of EAF dust and slag. Test results for MIFA obtained from Plants K1, K2, and K3 show that EAF dust remains hazardous as it is originally a listed waste. On the other hand, slag so generated remains nonhazardous based on the TCLP results. The experimental results of EAF dust and slag were further subjected to the analysis of variance (ANOVA) and regular analysis. Using this process, the optimal operating conditions with respect to the leached Pb concentration would be as follows: (1) Plant K1(injection mode operation)--87 tons of scrap iron, 1.4 tons of lime, 0.4 ton of coke, and 0.9 ton of MIFA; (2) Plant K2(injection mode operation)--90 tons of scrap iron, 1.4 tons of lime, 0.7 ton of coke, and 1.1 tons of MIFA; (3) Plant K2(one-time-charge mode operation)--90 tons of scrap iron, 1.4 tons of lime, 0.9 ton of coke, and 0.7 ton of MIFA; (4) Plant K3(injection mode operation)--85 tons of scrap iron, 1.4 tons of lime, 0.7 ton of coke, and 0.9 ton of MIFA; and (5) Plant K3(one-time-charge mode operation)--87 tons of scrap iron, 1.5 tons of lime, 0.4 ton of coke, and 0.7 ton of MIFA. In this study, using MIFA from Plant K2 as an example, it was found that it required 29-35 kg of lime per ton of steel billets produced when MIFA was added. Under a normal operation of EAF steel-making, however, it required 35-45 kg of lime per ton of steel billets produced based on the past experience. In average, when MIFA is added, it needs only 32 kg of lime per ton of steel billets produced as compared to 40 kg of lime for regular steel-making. In other words, it would result in a reduction of 8 kg of lime per ton of steel billets produced by using this novel process. Based on an average monthly production of 20,973 tons of steel billets and a unit cost of 2,200 NT$ per ton of lime, a monthly saving of lime cost would be 369,125 NT$. Namely, about 4.4 million NT$ per year. In addition, it was also found that using this novel process to melt MIFA would not deteriorate the quality of steel billets and bars produced.

O ferro-esponja ou DRI (Direct Reduced Iron) é obtido pelo processo de redução direta onde o minério de ferro é transformado em ferro metálico através de reações químicas envolvendo o estado sólido (minério) e o gasoso (gases redutores). Neste processo o minério de ferro não passa pelo estado líquido como ocorre com o ferro-gusa. Isto confere ao ferro-esponja algumas desvantagens que prejudicam o seu desempenho nas aciarias. Pode-se citar a redução no rendimento metálico e o maior consumo de energia elétrica como principais impactos de sua utilização intensiva. O ferro-esponja apresenta menor quantidade de ferro total (maior quantidade de impurezas) do que o ferro-gusa e também apresenta óxidos de ferro remanescentes em sua estrutura (menor metalização). Para torná-lo mais competitivo, inúmeras melhorias no processo têm sido promovidas para aumento da metalização. No entanto, o limite superior alcançado na prática tem ficado ao redor de 95%. Visando contribuir para melhorar a qualidade do ferro-esponja este trabalho apresenta uma proposta inovadora a partir da técnica de auto-redução. O objetivo é aumentar o grau de metalização do ferro-esponja através de seu aquecimento. Para isso, foram realizadas análises termogravimetrias e aquecimentos em forno mufla; análises químicas por via úmida, difração de raios-x, espectroscopia mössbauer e análise de microssonda de raios-x. As análises estruturais foram realizadas utilizando microscópio eletrônico de varredura para confirmar a efetividade da técnica apresentada. Nesta dissertação pode-se comprovar que, através da técnica de auto-redução, o ferro-esponja alcança metalizações acima de 98% em detrimento da queda do teor de carbono total. Um aumento de 4% na metalização traz um ganho estimado de 5 a 10% no consumo de energia elétrica nos fornos de fusão e um acréscimo proporcional na produção horária das aciarias. / The direct reduced iron is obtained by direct reduction process, where iron ore is transformed in metallic iron via chemical reactions involving solid (ore) and gaseous (reductant gases) states. In this process the iron ore does not pass by liquid state like pig iron. This become to direct reduced iron some disadvantages, which decrease its performance in the steelmaking process. It can be mentioned the reduction of metallic yield and the higher consumption of electric energy as the main impacts of its intensive use. The direct reduced iron presents lower amount of total iron (higher amount of impurities) than pig iron and presents iron oxides remained in its structure (lower metallization). To become more competitive, several improvements in the reduction process have been carried out to increase its metallization. However, the highest level of metallization, which has been reached, is 95%. To improve the direct reduced iron quality, the present work evaluates, in an innovative way, using the technique of self reduction. The objective is increase of metallization of the direct reduced iron through its heating. Thermal, chemical and structural characterization was carried out to check the effectiveness of the investigated technique. The research confirms that the direct reduced iron can reach a metallization higher than 98% with a decrease of total carbon amount using the technique presented in this work. An improvement of 4% in the metallization brings savings of 5 to 10% in the electric energy consumption of the electric arc furnaces and a proportional increase of the production in the steelmaking plants.

O ferro-esponja ou DRI (Direct Reduced Iron) é obtido pelo processo de redução direta onde o minério de ferro é transformado em ferro metálico através de reações químicas envolvendo o estado sólido (minério) e o gasoso (gases redutores). Neste processo o minério de ferro não passa pelo estado líquido como ocorre com o ferro-gusa. Isto confere ao ferro-esponja algumas desvantagens que prejudicam o seu desempenho nas aciarias. Pode-se citar a redução no rendimento metálico e o maior consumo de energia elétrica como principais impactos de sua utilização intensiva. O ferro-esponja apresenta menor quantidade de ferro total (maior quantidade de impurezas) do que o ferro-gusa e também apresenta óxidos de ferro remanescentes em sua estrutura (menor metalização). Para torná-lo mais competitivo, inúmeras melhorias no processo têm sido promovidas para aumento da metalização. No entanto, o limite superior alcançado na prática tem ficado ao redor de 95%. Visando contribuir para melhorar a qualidade do ferro-esponja este trabalho apresenta uma proposta inovadora a partir da técnica de auto-redução. O objetivo é aumentar o grau de metalização do ferro-esponja através de seu aquecimento. Para isso, foram realizadas análises termogravimetrias e aquecimentos em forno mufla; análises químicas por via úmida, difração de raios-x, espectroscopia mössbauer e análise de microssonda de raios-x. As análises estruturais foram realizadas utilizando microscópio eletrônico de varredura para confirmar a efetividade da técnica apresentada. Nesta dissertação pode-se comprovar que, através da técnica de auto-redução, o ferro-esponja alcança metalizações acima de 98% em detrimento da queda do teor de carbono total. Um aumento de 4% na metalização traz um ganho estimado de 5 a 10% no consumo de energia elétrica nos fornos de fusão e um acréscimo proporcional na produção horária das aciarias. / The direct reduced iron is obtained by direct reduction process, where iron ore is transformed in metallic iron via chemical reactions involving solid (ore) and gaseous (reductant gases) states. In this process the iron ore does not pass by liquid state like pig iron. This become to direct reduced iron some disadvantages, which decrease its performance in the steelmaking process. It can be mentioned the reduction of metallic yield and the higher consumption of electric energy as the main impacts of its intensive use. The direct reduced iron presents lower amount of total iron (higher amount of impurities) than pig iron and presents iron oxides remained in its structure (lower metallization). To become more competitive, several improvements in the reduction process have been carried out to increase its metallization. However, the highest level of metallization, which has been reached, is 95%. To improve the direct reduced iron quality, the present work evaluates, in an innovative way, using the technique of self reduction. The objective is increase of metallization of the direct reduced iron through its heating. Thermal, chemical and structural characterization was carried out to check the effectiveness of the investigated technique. The research confirms that the direct reduced iron can reach a metallization higher than 98% with a decrease of total carbon amount using the technique presented in this work. An improvement of 4% in the metallization brings savings of 5 to 10% in the electric energy consumption of the electric arc furnaces and a proportional increase of the production in the steelmaking plants.

O objetivo desse trabalho foi o de obter-se fios de cobre em três composições químicas distintas da liga Cu-Mg a partir de cobre eletrolítico e de magnésio. Foram avaliadas as etapas envolvidas, começando com a fusão de botões em forno a arco na composição do eutético Cu-Mg, diluição destes botões em forno resistivo, vazamento em lingoteira de cobre, seguido de tratamento térmico de homogeneização em forno resistivo a 910 ºC por 2 h. Os tarugos foram posteriormente trabalhados mecanicamente por forjamento rotativo seguido de um passe final de acabamento por trefilação, para obtenção do fio. As análises químicas realizadas nos lingotes indicaram que a rota de preparação dos fios mostrou-se adequada aos estudos em escala de laboratório, suficiente para a confecção de fios com área de seção transversal de 4 mm2 por 10 m de comprimento, para cada composição de liga. Os fios foram caracterizados mecanicamente por ensaio de tração e de dureza após tratamento térmico de recristalização a 510 ºC por 1 h. Os fios também tiveram as condutividades elétricas medidas na condição recristalizada e os resultados foram comparados com dados experimentais da literatura. Os materiais obtidos mostraram-se adequados à utilização como fio condutor de energia elétrica. Os limites de escoamento e de resistência a tração tiveram seus valores melhorados com o aumento do teor de magnésio na liga, 11 % e 24 %, respectivamente, enquanto houve queda nos valores de condutividade elétrica para cerca de 60 % IACS (International Annealed Copper Standard). / The aim of this work was to obtain copper wires in three different chemical compositions starting from electrolytic copper and magnesium. The mains steps were evaluated, starting from the melting of small eutectic cooper-magnesium specimens in an electric arc furnace, followed by further dilution of this buttons in a resistive furnace and casting it in a copper mould. The as cast billets were homogenized in a resistive furnace at 910 ºC for 2 h. The billets were mechanically cold worked by swaging and a final drawing step to attain a round shape and a reasonable surface quality. The cast ingots chemical analysis indicated that the processing route showed to be adequate, in laboratory scale, to obtain wires with cross sectional area of 4 mm2 and 10 m in length. The wires in both conditions as cold worked and after a recovering heat treatment at 510 ºC for 1 h, were mechanically characterized by tensile testing and hardness. The wires had also the electric conductivity assessed in the recovered heat-treated state and the results were compared to the literature data. The obtained material showed to be adequate to be used as electric conductor. The yield strain and ultimate tensile strength were improved with the increasing amount of Mg in the alloy, 11 % and 24 %, respectively, while the electric conductivity decreased to 60 % IACS (International Annealed Copper Standard).

O ferro-esponja ou DRI (Direct Reduced Iron) é obtido pelo processo de redução direta onde o minério de ferro é transformado em ferro metálico através de reações químicas envolvendo o estado sólido (minério) e o gasoso (gases redutores). Neste processo o minério de ferro não passa pelo estado líquido como ocorre com o ferro-gusa. Isto confere ao ferro-esponja algumas desvantagens que prejudicam o seu desempenho nas aciarias. Pode-se citar a redução no rendimento metálico e o maior consumo de energia elétrica como principais impactos de sua utilização intensiva. O ferro-esponja apresenta menor quantidade de ferro total (maior quantidade de impurezas) do que o ferro-gusa e também apresenta óxidos de ferro remanescentes em sua estrutura (menor metalização). Para torná-lo mais competitivo, inúmeras melhorias no processo têm sido promovidas para aumento da metalização. No entanto, o limite superior alcançado na prática tem ficado ao redor de 95%. Visando contribuir para melhorar a qualidade do ferro-esponja este trabalho apresenta uma proposta inovadora a partir da técnica de auto-redução. O objetivo é aumentar o grau de metalização do ferro-esponja através de seu aquecimento. Para isso, foram realizadas análises termogravimetrias e aquecimentos em forno mufla; análises químicas por via úmida, difração de raios-x, espectroscopia mössbauer e análise de microssonda de raios-x. As análises estruturais foram realizadas utilizando microscópio eletrônico de varredura para confirmar a efetividade da técnica apresentada. Nesta dissertação pode-se comprovar que, através da técnica de auto-redução, o ferro-esponja alcança metalizações acima de 98% em detrimento da queda do teor de carbono total. Um aumento de 4% na metalização traz um ganho estimado de 5 a 10% no consumo de energia elétrica nos fornos de fusão e um acréscimo proporcional na produção horária das aciarias. / The direct reduced iron is obtained by direct reduction process, where iron ore is transformed in metallic iron via chemical reactions involving solid (ore) and gaseous (reductant gases) states. In this process the iron ore does not pass by liquid state like pig iron. This become to direct reduced iron some disadvantages, which decrease its performance in the steelmaking process. It can be mentioned the reduction of metallic yield and the higher consumption of electric energy as the main impacts of its intensive use. The direct reduced iron presents lower amount of total iron (higher amount of impurities) than pig iron and presents iron oxides remained in its structure (lower metallization). To become more competitive, several improvements in the reduction process have been carried out to increase its metallization. However, the highest level of metallization, which has been reached, is 95%. To improve the direct reduced iron quality, the present work evaluates, in an innovative way, using the technique of self reduction. The objective is increase of metallization of the direct reduced iron through its heating. Thermal, chemical and structural characterization was carried out to check the effectiveness of the investigated technique. The research confirms that the direct reduced iron can reach a metallization higher than 98% with a decrease of total carbon amount using the technique presented in this work. An improvement of 4% in the metallization brings savings of 5 to 10% in the electric energy consumption of the electric arc furnaces and a proportional increase of the production in the steelmaking plants.

Direct Reduced Iron (DRI) is used as an alternative feedstock in electric arc furnaces, making up 50% or more of the total iron charge. DRI produced with coal based reductants (for example in rotary kilns) make up roughly 25% of DRI produced in the world. It was found that SL/RN DRI samples from a kiln cooler had high nitrogen contents (50-250ppm, depending on particle size), higher than DRI from gas-based reduction. The higher nitrogen content of SL/RN DRI would increase the levels of nitrogen of liquid steel produced in the EAFs. The problem is exacerbated by the fact that the SL/RN DRI contains virtually no carbon (which would aid in preventing nitrogen pickup). The proposed mechanism of nitrogen pick-up by the SL/RN DRI is one where nitrogen present within the atmosphere of the rotary cooler (where hot DRI, discharged at 1000°C from the rotary kiln, is cooled to approximately 100 °C in ca. two hours) penetrates the solids bed and nitrides DRI particles. Possible rate-determining steps for nitriding in the cooler have been evaluated. Nitriding of DRI particles is predicted to be rapid: the most plausible location for rapid nitrogen pickup is the first 5 meters of the rotary cooler, where the high temperature, nitrogen-rich gas atmosphere and rapid solids bed mixing are conducive to nitriding; solid-state and pore diffusion of nitrogen into DRI particles are predicted to be rapid too. The most plausible rate determining step for nitriding of DRI particles is that of nitrogen dissociation on the DRI surface, which can be further retarded by the presence of sulphur. A strong correlation was found between the amount of “melt-in” carbon in the liquid steel and the final tap nitrogen content, with 0.3% C resulting in nitrogen levels as low as 50 ppm (80 ppm or less is desired on the plant in question) at tap, even with DRI material that is high in nitrogen and contains virtually no carbon. Proposals to increase the melt-in carbon are included. / Dissertation (MEng)--University of Pretoria, 2013. / gm2014 / Materials Science and Metallurgical Engineering / unrestricted

Sandvik produces about 230 000 tonnes of steel annually by melting in an electric arc furnace, where more than 90% of this steel is casted via continuous casting. When the strands are cast, these strands will be cuts to specific lengths with 2 cm thick cuts by using gas and iron powder. This generates approximately 750 tonnes of steel chips (cutting residues) each year, with a composition from the entire annual production of steel that falls as a residual. The purpose of the work was to review a possible reuse of the cutting residues as a raw material in the electric arc furnace. The problem with the cutting residue is the large reactive surface area, which could cause the material to burn in the electric arc furnace during operation. Since there are a high gas flow in the electric arc furnace during operation, the cutting residue that has a small particle size can also disappear from the furnace with the gas flow to the particle filters. By briquetting the cutting residue, these problems could be minimized and a reuse of the cutting slag as raw material could thus be possible. Therefore the cutting residue was transported to a company that sieved, dried and briquetted the cutting residue.  37 tonnes of cutting residue briquettes have been reused into 18 charges under normal operations with 2 tonnes of cutting residue briquettes in each charge (one charge with only 1 tonne of cutting slag). In order to measure how efficient, the reuse of the cutting residue was, a reference was needed. The reference was based on how the yield of steel for the elements, molybdenum, nickel, copper, cobalt and chromium in the electric arc furnace behaves in daily operation. This yield was used as a basis for calculating the yield when reusing the cutting residue. The results showed that nickel and molybdenum had a consistently good yield. The results for the cobalt and copper was not as clear, but the yields were generally good. In the case of chromium the results are naturally varied, as chromium reacts with the slag during the process. However, the predominant conclusion of the work was that it is possible to reuse the cutting residue as a raw material in the electric arc furnace with an acceptable yield by briquetting it. Analysis of the slag was also done to see any deviations from daily operations. The results showed that the slag was not affected when the cutting residue was reused as raw material in the electric arc furnace. / Varje år producerar Sandvik ungefär 230 000 ton stål genom nedsmältning av stålskrot i ljusbågsugnen där mer än 90 % av stålet gjuts via stränggjutning. När strängarna gjuts kapas de till specifika längder med ett 2 cm tjockt snitt med hjälp av syrgas och järnpulver. Detta resulterar i en restprodukt (skärslagg) om ca 750 ton per år, med sammansättningen från den årliga produktionen av stål. Syftet med arbetet var att se över en möjlig återanvändning av skärslaggen som råvara i ljusbågsugnen. Problematiken med skärslaggen är den stora reaktiva ytan vilket kan medföra att materialet börjar brinna i ljusbågsugnen under drift. Skärslaggen har en liten partikelstorlek och kan således följa med till gas- och partikelfilter då det är ett högt gasflöde i ljusbågsugnen under drift. Genom att brikettera skärslaggen kan dessa problem minimeras och en återföring av skärslaggen som råvara kan således vara möjlig. Skärslaggen transporterades till ett företag som siktade, torkade och briketterade skärslaggen. 37 ton skärslaggsbriketter har återförts i 18 försökscharger under normal drift med 2 ton skärslaggsbriketter i varje charge (en charge med enbart 1 ton skärslagg). För att mäta hur effektivt återföringen av skärslaggen var behövdes en referensnivå. Referensnivån baserades på hur utbytet till stål för elementen, molybden, nickel, koppar, kobolt och krom i ljusbågsugnen förhåller sig vid daglig drift. Detta utbyte användes som bas för att beräkna utbytet vid återföringen av skärslaggen. Av resultaten framgår det att nickel och molybden visade genomgående goda utbyten. Utfallet för elementen kobolt och koppar var inte lika tydliga men utbytena var till övervägande del goda. Beträffande krom var resultaten av naturliga skäl varierande, då krom reagerar med slaggen under processens gång. Den övervägande slutsatsen av arbetet var emellertid att det går att återföra skärslagg som råvara i ljusbågsugnen med godtagbara utbyten genom att brikettera den. Analysering av ljusbågsugnsslaggen gjordes också för att se eventuella avvikelser ifrån den dagliga driften. Resultaten visade att slaggen inte påverkas när skärslaggen återförs som råvara i ljusbågsugnen.

No description available.

SSAB i Oxelösund ska bygga en ljusbågsugn för konvertering av verksamheten från huvudsakligen malmbaserad produktion till skrotbaserad produktion. I samband med byggandet av ljusbågsugnen kommer en ny 130 kV linje byggas och från denna linje kommer ett nytt 30 kV nät byggas för att mata ljusbågsugnen och två stycken skänkugnar. En av dessa skänkugnar är idag (2019) i drift med 10 kV men ska konverteras till 30 kV medan den andra är en ny elektriskt sett identisk ugn. Anslutningen av dessa tre ugnar till det avskilda 30 kV nätet är till för att begränsa spridning av övertoner och flimmer till övriga laster. Ugnarna ska sedan anslutas till ett gemensamt elektriskt filter, för 30 kV nätet. Ljusbågsugnen och skänkugnarna ska vara i drift första kvartalet 2024, på grund av att det är några år in i framtiden är kortslutningsimpedanser osäkra. För att uppfylla termisk- och korttidsströmsdimensionering för kabeln mellan huvudställverk (OT40) och skänkugnsställverk (SU2) fodras enledarkabel med 300 mm2 aluminiumledare och PEX-isolering. Denna dimensionering förutsätter att förläggning sker i triangelformation, temperaturen är högst 35 °C och kabeln förläggs på sådant sätt att den inte påverkas av andra kablar. Maximal kortslutningsström som kabeln klarar av under den maximala bortkopplingstiden är 32,5 kA. Kortslutnings- och spänningsfallsberäkningar är utförda iprogrammet GNU Octave. Högsta och lägsta kortslutningström i respektive ställverk är beräknad. Överströmsskydden ställs in så att selektiv bortkoppling erhålls, med maximal bortkopplingstid 0,9 sekunder. En blockeringslogik används för att försäkra anläggning enmot oselektiv utlösning. Logiken innebär, enligt SSAB:s praxis, att skyddet närmast felstället ska blockera överordnat skydds kortslutningsströmsteg (>> I). Jordfelsskydd dimensioneras efter en nollpunktsresistor om 10 A. Jordfelsskydden är riktade och friges av nollpunktsspänningsskydd för att säkerställa att okynnesutlösning av jordfelsskydden inte uppstår i samband med omkopplingar eller fel i nätet. Frigivningen fungerar upp till en maximal snedavstämning om cirka 21 A. / SSAB in Oxelösund will build an electric arc furnace to transform business from a mainly ore-based production, with blast furnaces, to a scrap based production. Together with the construction of the electric arc furnace, a new 130 kV overhead line and a 30 kV substation will be built. The 30 kV substation will feed one electric arc furnace and two ladle furnaces. One of these ladle furnaces is currently (2019) being fed with 10 kV, but is going to be converted to 30 kV, while the other one is a new electrically identical furnace. The connection of these three furnaces to the 30 kV grid is done in order to limit the distribution of harmonic distortions and flicker to the other loads. The furnaces on the 30 kV grid will be connected to a common electrical filter. The electric arc furnace and the ladle furnaces will be operational and produce steel in the first quarter of 2024. Since the installation will be performed some years ahead the short circuit impedance is not known. The cable between the main substation (OT40) and the ladle furnace substation (SU2) was being selected according to thermals and short time currents which determined the cable to consist of a single core cable with 300 mm2 aluminium conductor isolated by XLPE-isolation. This is provided that the cable is mountedin a triangle formation along a path with temperatures at maximum 35 C and is placed in such a way that the cable is not influenced thermally by other cables. Short circuit and voltage drop calculations are made in the program GNU Octave. The highest three phase and the lowest two phase short circuit current is calculated in every substation. The overcurrent protection is set to a maximum disconnection time of 0.9 seconds. A blocking logic is being used to further ensure a selectivity in the facility. The logic means, according to SSAB praxis, that the protection closest to the fault blocks the upstream short circuit protection ( I). The earth fault protection is designed around using a neutral grounding resistor of 10 A. The earth fault protection is directional and is being released by the neutral displacement protection to asure no unwanted tripping of the earth fault protection by change-over switching or faults in the grid. The release of the protection works with detuning up to about 21 A.