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Planning BOF repair system in conditions of quasi-periodic operation of units
https://doi.org/10.17073/0368-0797-2024-6-738-743
Abstract
Using the example of the steelmaking production of JSC EVRAZ United West Siberian Metallurgical Plant, the paper considers the task of synchronous calendar planning in the interval of several planned periods of operation of basic oxygen furnace (BOF), BOF shops, production as a whole, as well as ongoing repairs of BOF for steelmaking production (two BOF shops with two and three BOFs). Scheduled stops of the BOF for repair depend on the actual achieved duration of the lining campaign and production schedules of the units and are performed when the current duration of the BOF campaign reaches a given standard value. Thus, the current duration of the BOF campaign is described by a discrete, nonlinear quasi-periodic function that does not have a fixed period, but has some regularity. Technological limitations were formalized, determining the minimum and maximum values of the number of melts per day that each of the workshops can produce with one or two BOFs operating simultaneously. The authors formulated the conditions to avoid performing two “cold” repairs in one shop in one planned period and ensuring daily processing by BOF shops of all cast iron coming from the blast furnace shop. In the proposed mathematical formulation of the problem, it is required to find such schedules of BOF repairs and such calendar plans of their work that satisfy the formulated constraints and optimize the non-linear criterion. The proposed criterion is aimed at ensuring the constant readiness of the shops for implementation of the production program and design productivity. The task is formulated for the conditions of trouble-free operation and stable provision of the shops with liquid cast iron as the main component of the metal charge of BOF smelting.
Keywords
For citations:
Kornet M.Е., Zimin A.V., Burkova I.V., Zimin V.V. Planning BOF repair system in conditions of quasi-periodic operation of units. Izvestiya. Ferrous Metallurgy. 2024;67(6):738-743. https://doi.org/10.17073/0368-0797-2024-6-738-743
Introduction
The basic oxygen furnace (BOF) process is widely regarded as the most effective method for improving economic efficiency and enhancing the quality of metallurgical products [1 – 3].
In Russia, BOF production mirrors the key challenges faced globally, including optimizing the composition of processed charges and reducing losses and resource consumption in the process [4 ‒ 6]. Modern economic conditions demand improvements in production planning, technological advancements, the development of new refractory materials, and innovative BOF lining repair methods. These efforts aim to significantly extend unit campaign durations and reduce refractory consumption [6 ‒ 9]. As a result, planning production metrics, along with the maintenance and repair of equipment and auxiliary systems, remains a critical focus for achieving the highest possible technical and economic performance in BOF shops [10 ‒ 12].
Planning BOF repairs in steelmaking production presents unique challenges, as it requires multifactorial solutions when developing a calendar plan for BOF operations. In the case of other metallurgical units, the BOF repair schedule is a key input for their overall calendar planning [13 ‒ 15]. This distinction stems from the fact that BOFs are taken offline for repairs once the number of melts conducted on a given lining reaches the defined standard campaign duration [16; 17]. The timing of this milestone depends on the unit’s operational calendar and often results in repairs being carried out at irregular intervals under production conditions [18 – 20].
Основные понятия и обозначения
Let O = {OI , OII} represent the structure of the steelmaking production, which includes two BOF shops: OI = {o1 , o2 , o3 } and OII = {o4 , o5 }. The first shop operates three BOFs of the same type, while the second shop operates two. The planning interval for BOF repairs depends on the standard campaign durations of the BOFs, their charge capacities, and the monthly volumes of cast iron supplied for processing. Let (T1 , T2 , ..., Tj , ..., TP ) denote the sequence of months in the BOF repair planning interval \({T_j} = \left( {\Delta {t_{{s_j}}}|{s_j} = {{\overline {1,S} }_j}} \right)\) and Sj represent the number of days in the j-th month. The volumes of cast iron processed per melt cycle by the BOFs in the first and second shops are denoted as g(OI ) and g(OII ) respectively. The cast iron consumption coefficients for producing one ton of steel in the corresponding shops are ρI , ρII and the standard campaign durations of the BOFs are KI and KII . Let \(\left\{ {\left( {s_j^{r_{{i_c}}^n},{\rm{ }}s_{j'}^{r_{{i_c}}^e}} \right)|c = \overline {1,2,...} } \right\},{\rm{ }}i = \overline {1,5} \) represent the planned intervals for BOF repairs, where \(s_j^{r_{{i_c}}^n}\) and \(s_{j'}^{r_{{i_c}}^e}\) are the days when the c-th repair of the i-th BOF begins and ends, respectively. If j = j′, the repair starts and finishes within the same planning period j. If j ≠ j′, the repair begins in period j and ends in period j′, with the repair lasting \(\left( {{S_j} - s_j^{r_{{i_c}}^n}} \right)\) days in period j and \(s_{j'}^{r_{{i_c}}^e}\) days in period j′.
It is important to note that the reduction in scrap metal supply under current market conditions has made scrap metal prices comparable to the cost of cast iron production. As a result, the cast iron consumption coefficients ρI and ρII are no longer considered constants and are now given as interval-based estimates:
\[\begin{array}{c}{\rho _I} \in \left( {\rho _I^{\min }{\rm{, }}\rho _I^{\max }} \right);\\{\rho _{II}} \in \left( {\rho _I^{\min }{\rm{, }}\rho _I^{\max }} \right).\end{array}\] | (1) |
Advancements in BOF production technology – such as the introduction of secondary steelmaking, real-time monitoring of BOF lining conditions, and periodic “hot” repairs between scheduled overhauls involving lining replacement – have significantly extended BOF campaign durations, which now often exceed 6000 melts. At the same time, the total number of “cold” BOF repairs has decreased. Additionally, different suppliers of specialized materials for “hot” repairs offer varying guarantees on BOF campaign durations, leading to the widespread use of the term “guaranteed BOF durability.” In modern practice, campaign duration is typically determined by the refractory supplier under a specific contractual agreement:
\[\begin{array}{c}{\rm{ }}{K_I} = \left( {K_1^{\min },{\rm{ }}K_1^{\max }} \right);\\{K_{II}} = \left( {K_{1I}^{\min },{\rm{ }}K_{1I}^{\max }} \right).\end{array}\] | (2) |
The understanding of “cold” repairs has also evolved. Previously, this term referred exclusively to the time required to replace the BOF lining. Today, such repairs are generally combined with maintenance of auxiliary equipment and other metallurgical units. As a result, BOF stop for repairs may exceed the duration of the current planned production period.
Unless otherwise specified, the evaluations of the parameters introduced will be treated as point estimates rather than interval estimates.
Let us denote the number of melts produced daily by BOF i in shops OI and OII as \({m_{ij}}\left( {\Delta {t_{{s_j}}}} \right),{\rm{ }}{m_{Ij}}\left( {\Delta {t_{{s_j}}}} \right),{\rm{ }}{m_{IIj}}\left( {\Delta {t_{{s_j}}}} \right)\). It is evident that
\[\begin{array}{c}\sum\limits_{i = 1}^3 {{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right) = {\rm{ }}} {m_{Ij}}\left( {\Delta {t_{{s_j}}}} \right);\\\sum\limits_{i = 4}^5 {{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right) = } {\rm{ }}{m_{IIj}}\left( {\Delta {t_{{s_j}}}} \right).\end{array}\] | (3) |
The calendar plan for the operation of the i-th BOF in the j-th month is defined as the sequence
\[{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right)|s = {\overrightarrow {1,S} _j}.\] | (4) |
The joint operation of BOFs in the shops is governed by technological constraints that define the range of daily melts in each shop, depending on whether one or two BOFs are operating simultaneously:
\[\underline {m_I^1} \le {m_{ij}}\left( {\Delta {t_{{s_j}}}} \right) \le \overrightarrow {m_I^1} ,{\rm{ }}i{\rm{ = }}\overline {{\rm{ }}1,3} ,{\rm{ }}j{\rm{ = }}\overrightarrow {1,P} ;\] | (5) |
\[\underline {m_{II}^1} \le {m_{ij}}\left( {\Delta {t_{{s_j}}}} \right) \le \overrightarrow {m_{II}^1} ,{\rm{ }}i{\rm{ = }}\overline {{\rm{ }}4,5} ,{\rm{ }}j{\rm{ = }}\overrightarrow {1,P} ;\] | (6) |
\[\begin{array}{c}2\underline {m_I^1} \le \left( {{m_{ij}}(\Delta {t_s}) + {m_{i'j}}(\Delta {t_s})} \right) \le \overline {2m_I^1} ;{\rm{ }}\\i \ne i'{\rm{, }}i,{\rm{ }}i' = \overline {1,3} ,{\rm{ }}j = \overrightarrow {1,P} ;\end{array}\] | (7) |
\[2\underline {m_{II}^1} \le \left( {{m_{4j}}(\Delta {t_s}) + {m_{5j}}(\Delta {t_s})} \right) \le \overline {2m_{II}^1} ,{\rm{ }}j = \overrightarrow {1,P} ,\] | (8) |
where \(\underline {m_I^1} ,{\rm{ }}\overrightarrow {m_I^1} ,{\rm{ }}\underline {m_{II}^1} ,{\rm{ }}\overrightarrow {m_{II}^1} ,{\rm{ 2}}\underline {m_I^1} ,{\rm{ }}\overrightarrow {2m_I^1} ,{\rm{ 2}}\underline {m_{II}^1} ,{\rm{ }}\overrightarrow {2m_{II}^1} \) are the minimum and maximum numbers of melts produced in the first and second shops, respectively, when operating a single BOF, as well as the minimum and maximum numbers of melts produced when two BOFs are in operation.
Operating three BOFs in the first shop is technologically challenging to implement.
We define the function kij (sj ), which represents the number of melts produced by the i-th BOF by the end of day sj in the j-th period. The number of melts is limited by the campaign durations of the BOFs
\[{k_{ij}}\left( {{s_j}} \right) \le \left\{ {\begin{array}{*{20}{c}}{{K_I},{\rm{ }}i{\rm{ = }}\overline {1,3} ;}\\{{K_{II}},{\rm{ }}i{\rm{ = }}\overline {4,5} .}\end{array}} \right.\] | (9) |
The set of possible start times \(s_j^{r_{{i_c}}^n}\) for BOF repairs is determined by the following relationships
\[\begin{array}{c}\left\{ {s_j^{r_{{i_c}}^n}|{k_{ij}}\left( {{s_j}} \right) \ge {K_I}} \right\},{\rm{ }}i = \overline {1,3} ;\\\left\{ {s_j^{r_{{i_c}}^n}|{k_{ij}}\left( {{s_j}} \right) \ge {K_{II}}} \right\},{\rm{ }}i = \overline {4,5} .\end{array}\] | (10) |
The completion time \(s_{j'}^{r_{{i_c}}^e}\) for repairs is determined by their specified duration \({r_{{i_c}}},{\rm{ }}c = \overline {1,2,...} \)
In steelmaking production, the design and repair management system ensures that no two “cold” repairs are carried out in the same shop during a single planned period. Additionally, the first shop is designed to maintain the continuous operation of two BOFs, while the third is either under repair or held in reserve. As a result, during each planned period Tj one of the following four operating modes is implemented in each shop:
1. No repairs are performed on either of the two operational BOFs
\[\left( {s_j^{r_{{i_c}}^n},s_j^{r_{{i_c}}^e}} \right) \not\subset {T_j}.\] | (11) |
2. One of the operational BOFs is undergoing repairs
\[\left( {s_j^{r_{{i_c}}^n},s_j^{r_{{i_c}}^e}} \right) \subset {T_j}.\] | (12) |
3. Repairs on one of the operational BOFs, started in a previous period, are completed
\[{T_{j - 1}}\left( {s_{j - 1}^{r_{{i_c}}^n},s_j^{r_{{i_c}}^e}} \right) \cap {T_j} = \overline {1,s_j^{r_{{i_c}}^e}} .\] | (13) |
4. Repairs on one of the operational BOFs are initiated and will be completed in a subsequent period
\[{T_{j + 1}}\left( {s_j^{r_{{i_c}}^n},s_{j + 1}^{r_{{i_c}}^e}} \right) \cap {T_j} = \overline {s_{j + 1}^{r_{{i_c}}^n},{S_j}} .\] | (14) |
Let \(k_{ij}^n\) represent the number of melts produced by the i-th BOF at the beginning of the j-th planning period. Based on expression (4), the number of melts \(k_{ij}^e\), produced by the i-th BOF by the end of the j-th planning period, for each operating mode, is described by the following functions
\[k_{ij}^e = k_{ij}^n + \sum\limits_{l = 1}^{{S_j}} {{m_i}\left( {\Delta {t_{{s_j}}}} \right)} ;\] | (15) |
\[k_{ij}^e = k_{ij}^n + \sum\limits_{l = 1}^{s_j^{r_{{i_c}}^n}} {{m_i}\left( {\Delta {t_{{s_j}}}} \right)} + \sum\limits_{l = s_j^{r_{{i_c}}^e} + 1}^{{S_j}} {{m_i}\left( {\Delta {t_{{s_j}}}} \right)} ;\] | (16) |
\[k_{ij}^e = k_{ij}^n + \sum\limits_{l = s_j^{r_{{i_c}}^e} + 1}^{{S_j}} {{m_i}\left( {\Delta {t_{{s_j}}}} \right)} ;\] | (17) |
\[k_{ij}^e = k_{ij}^n + \sum\limits_{l = 1}^{s_j^{r_{{i_c}}^n}} {{m_i}\left( {\Delta {t_{{s_j}}}} \right)} .\] | (18) |
The function kij (sj ), which represents the number of melts produced by the i-th BOF by the end of day sj exhibits quasi-periodic behavior (irregular periodicity). It has a “sawtooth” shape, with a maximum value of KI for BOFs in the first shop and KII for BOFs in the second shop. The length of the “sawtooth base” depends on the number of melts produced daily by the BOF until the function reaches its maximum value, at which point it resets to zero. The spacing between the “teeth” of the saw corresponds to the BOF repair duration, during which the function also equals zero.
The oscillations of kij (sj ) follow a regular pattern but lack a fixed period.
Using the sequences
\[\left( {g_j^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right),\]
\[\left( {g_{Ij}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right),\]
\[\left( {g_{IIj}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right)\]
we can describe the daily inflow of liquid iron from blast furnace production to the steelmaking facilities as a whole, as well as to the first and second shops during the j-th period. It is evident that \(g_{Ij}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right) + g_{IIj}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right) = {g^{{\rm{in}}}}\left( {\Delta {t_{{s_j}}}} \right),{\rm{ }}{s_j} = \overline {1,{S_j}} .\) Let
\[\sum\limits_{{s_0} = 1}^{{S_j}} {g_j^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)} = G_{{T_j}}^{{\rm{in}}},\]
where \(G_{{T_j}}^{{\rm{in}}}\) is the monthly volume of cast iron requiring processing. Similarly, we define the values \(G_{I{T_j}}^{{\rm{in}}}\) and \(G_{II{T_j}}^{{\rm{in}}}\), \(G_{I{T_j}}^{{\rm{in}}} + G_{II{T_j}}^{{\rm{in}}} = G_{{T_j}}^{{\rm{in}}}.\) To calculate the number of melts required to process the incoming cast iron on day sj described by the sequence \(\left( {g_{Ij}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right),\) we use плавок, the following recursive procedure:
\[\begin{array}{c}m_{Ij}^{{\rm{in}}}(\Delta {t_1}) = \left[ {\frac{{g_{Ij}^{{\rm{in}}}(\Delta {t_1})}}{{g({O_I})}}} \right];\\m_{Ij}^{{\rm{in}}}(\Delta {t_2}) = \left[ {\frac{{g_{Ij}^{{\rm{in}}}(\Delta {t_2}) + g_{Ij}^{{\rm{in}}}(\Delta {t_1})}}{{g({O_I})}} - } \right.\left. {\frac{{m_{Ij}^{{\rm{in}}}(\Delta {t_1})g({O_I}){\rho _I}}}{{g({O_I})}}} \right]\end{array}\] | (19) |
continuing until sj = Sj .
This results in a sequence \(\left( {m_{Ij}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right),\) that describes the daily number of melts the first shop must produce. A similar sequence can be calculated \(\left( {m_{IIj}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overline {1,{S_j}} } \right),\) for the second shop. Let us represent the monthly volumes of cast iron requiring processing in the \({M_{I{T_j}}} = \sum\limits_{{s_j} = 1}^{{S_j}} {m_I^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)} \) and \({M_{II{T_j}}} = \sum\limits_{{s_j} = 1}^{{S_j}} {m_{II}^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right)} \) first and second shops, respectively, expressed as the number of melts. It is evident that \({M_{I{T_j}}}g({O_I}) + {M_{II{T_j}}}g({O_{II}}) = G_{{T_j}}^{{\rm{in}}}.\)
The current campaign durations of the BOFs are significantly higher than the monthly production volume of their respective shops:
\[{M_{I{T_j}}} \ll {K_I},{\rm{ }}{M_{II{T_j}}} \ll {K_{II}}.\] | (20) |
Now, let us define a condition to prevent two “cold” repairs from being carried out in the same shop during a single planning period. We will start with the second shop, which operates two BOFs. Due to the quasi-periodic nature of the functions k4j (sj ) and k5j (sj ), and because the campaign durations KII of the BOFs are identical, the maximum possible difference between the values k4j (sj ) and k5j (sj ) of these functions is KII /2:
\[\left| {{k_{4j}}\left( {{s_j}} \right) - {k_{5j}}\left( {{s_j}} \right)} \right| \le {K_{II}}/2.\] | (21) |
Therefore, the best way to stagger the repairs of the fourth and fifth BOFs is to maintain the approximate equality
\[\left| {{k_{4j}}\left( {{s_j}} \right) - {k_{5j}}\left( {{s_j}} \right)} \right| \approx {K_{II}}/2.\] | (22) |
Equation (20) also indicates that if one BOF is taken offline for repair, the remaining BOF has enough capacity to handle the entire production plan for the current planning period.
For the first shop, which operates three BOFs, the design provides for the continuous operation of two BOFs, while the third is either under repair or held in reserve. The reserved BOF is brought online whenever one of the operating BOFs is taken offline for repair. Under this scheme, with two BOFs operating continuously, the condition for staggering their repairs, similar to that of the second shop, can be written as
\[\left| {{k_{ij}}\left( {{s_j}} \right) - {k_{i'j}}\left( {{s_j}} \right)} \right| \approx {K_I}/2,{\rm{ }}i,{\rm{ }}i' \in \{ 1,{\rm{ }}2,{\rm{ }}3\} ,\] | (23) |
where i, i′ \( \in \) {1, 2, 3} are the BOFs operating in the first shop on day sj .
Task formulation for planning BOF repairs and operations across planned periods (T1 , T2 , ..., Tj , ..., TP )
The objective is to determine sequences
\[\left( {{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right)|{s_j} = \overrightarrow {1,{S_j}} } \right),{\rm{ }}i = \overline {1,5} ,{\rm{ }}j = \overrightarrow {1,P} \] | (24) |
and BOF repair schedules
\[\left( {s_j^{r_{{i_c}}^n},s_j^{r_{{i_c}}^e}} \right) \subset \bigcup\limits_{j = 1}^P {{T_j}} ,{\rm{ }}i = \overrightarrow {1,5} ,{\rm{ }}c = \overline {1,2,...} ,\] | (25) |
that satisfy equations (5) – (8), the constraint
\[g({O_I})\sum\limits_{i = 1}^3 {{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right) + g({O_{II}})\sum\limits_{i = 4}^5 {{m_{ij}}\left( {\Delta {t_{{s_j}}}} \right)} } = g_j^{{\rm{in}}}\left( {\Delta {t_{{s_j}}}} \right),\] | (26) |
and conditions (11) – (14) for performing repairs under specific operational modes, while minimizing criterion
\[\begin{array}{c}Q = \sum\limits_{j = 1}^P {\left\{ {\left( {\left| {k_{ij}^e - k_{i'j}^e} \right| - 0,5{K_1}} \right) + } \right.} \\ + \left. {\left( {\left| {k_{4j}^e - k_{5j}^e} \right| - 0,5{K_{II}}} \right)} \right\} \to \min ,\end{array}\] | (27) |
where i, i′ \( \in \) {1, 2, 3} denote the indices of the BOFs operating in the first shop on day Sj , and the values \(k_{ij}^e\) are determined in accordance with rules (15) – (18).
The criterion is designed to ensure conditions that enable the shops to achieve their design production capacities during each planning period.
Conclusions
Using the steelmaking production at JSC EVRAZ United West Siberian Metallurgical Plant as an example, the problem of synchronous calendar planning is examined. This planning covers multiple periods, including the operation of BOFs, BOF shops, and the production process as a whole, as well as ongoing BOF repairs. Scheduled BOF stops for repairs depend on the actual duration of the lining campaign achieved and the production schedules of the units. Repairs are carried out when the current campaign duration of a BOF reaches the specified standard value.
References
1. Grigorovich K.V. Metallurgy of the XXI century: Current state and directions of development. In: Proceedings of the XIV Int. Congress of Steelmakers. Moscow, Elektrostal, October 17-21, 2016. Moscow: Metallurgical Plant “Elektrostal’”; 2016:56–65. (In Russ.).
2. Guzela D., Oliveira J., Staudinger G., Muller J. The latest model of the oxygen converter as a result of half a century of technology development. In: Proceedings of the IX Congress of Steelmakers. Moscow: Chermetinformatsiya; 2014:153–163. (In Russ.).
3. Petrushka R., Manley S. Improvement in oxygen lance life. In: Steelmaking Conference Proceedings. 2000:245–250.
4. Tabata Y., Marsh R.C., Kelly P., etc. Impovement of ВОР steel refining blowing control using wide angle lance nozzles. In: Steelmaking Conference Proceedings. 1998:451–457.
5. Brun L. Overcapacity in steel: China’s Role in a Global Problem. Center on Globalization, Governance & Competitiveness, Duke University; 2016:54. https://doi.org/10.13140/RG.2.2.11923.48161
6. Mutumi Ohji. Recent trends and future in steelmaking technology in Japan. ISIJ International. 1996;36:S2–S5. https://doi.org/10.2355/isijinternational.36.Suppl_S2
7. Springorum D. The management of research and technology in the German steel industry with respect to the European Union. ISIJ Intemational. 1998;38(9):935–942. https://doi.org/10.2355/isijinternational.38.935
8. Macanley D. Engineering developments lead to greater economy. Steel Times International. 1996;(5):12–14.
9. Rymarchyk N. Post combustion lances in Basic Oxygen Furnace (BOF) operations. In: Steelmaking Conference Proceedings. 1998:445–449.
10. Messina C.J. Slag splashing in the BOF – world wide status, practices and results. Iron and Steel Engineer. 1996;(5):17–19.
11. Protopopov E.V., Temlyantsev M.V. Improving the Technology of Increasing the Durability of Oxygen Converter Lining. Novosibirsk: SB RAS; 2023:324. (In Russ.).
12. Shoukhin’ T., Yan’ven’ Yu. Reuse and restoration of used refractories. Ogneupory i tekhnicheskaya keramika. 2007; (5):29–34.
13. Lasdon Leon S. Optimization Theory for Large Systems. New York: Macmillan; 1970:523.
14. Russell R.O., Donaghy N., Meyer E.C., Goodson К.М. Everlasting BOF linings at LTV Steel? In: Proceedings of the 1st European Oxygen Steelmaking Congress, Düsseldorf/Neuss, June 21–23, 1993. Verlag Stahleisen GmbH; 1993:220–225.
15. Prokhorov I.M., Zimin A.V., Burkova I.V., Zimin V.V. Formulation and decomposition of the task of calendar planning of repairs and operation of steelmaking converters. Sistemy upravleniya i informatsionnye tekhnologii. 2024;(2(96)): 38–40. (In Russ.).
16. Prokhorov I.M., Zimin A.V., Burkova I.V., Zimin V.V. On the procedure for solving the problem of scheduling repairs of converters of a steelmaking workshop with two units. Sistemy upravleniya i informatsionnye tekhnologii. 2024;(2(96)): 64–67. (In Russ.).
17. Zimin V.V. Building coordinated schedules for production units of the steel-rolled complex: Extended Abstract of Cand. Sci. Diss. Moscow: MISiS; 1979:21.
18. Lohmer J., Lasch R. Production planning and scheduling in multi-factory production networks: A systematic literature review. International Journal of Production Research. 2021;59(7):2028–2054. https://doi.org/10.1080/00207543.2020.1797207
19. Moghaddam M., Moosavi E. A view on recent developments for production scheduling optimization. In: Proceedings of the 26th Int. Mining Congress and Exhibition of Turkey (IMCET 2019). 2019:166–173.
20. Li Y., Goga K., Tadei R., Terzo O. Production scheduling in industry 4.0. In: Complex, Intelligent and Software Intensive Systems, Advances in Intelligent Systems and Computing. Barolli L., Poniszewska-Maranda A., Enokido T. eds. 2020;1194.
About the Authors
M. Е. KornetRussian Federation
Maria E. Kornet, Senior Lecturer of the Chair of Engineering Cybernetics
4 Leninskii Ave., Moscow 119049, Russian Federation
A. V. Zimin
Russian Federation
Aleksei V. Zimin, Dr. Sci. (Eng.), Assist. Prof., Head of the Chair of Automation and Information Systems
42 Kirova Str., Novokuznetsk, Kemerovo Region – Kuzbass 654007, Russian Federation
I. V. Burkova
Russian Federation
Irina V. Burkova, Dr. Sci. (Eng.), Assist. Prof., Leading Researcher
65 Profsoyuznaya Str., Moscow 117997, Russian Federation
V. V. Zimin
Russian Federation
Valerii V. Zimin, Dr. Sci. (Eng.), Prof. of the Chair of Automation and Information Systems
42 Kirova Str., Novokuznetsk, Kemerovo Region – Kuzbass 654007, Russian Federation
Review
For citations:
Kornet M.Е., Zimin A.V., Burkova I.V., Zimin V.V. Planning BOF repair system in conditions of quasi-periodic operation of units. Izvestiya. Ferrous Metallurgy. 2024;67(6):738-743. https://doi.org/10.17073/0368-0797-2024-6-738-743