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基于粒子群算法的轉爐用氧節能優化調度

Optimal scheduling of converter oxygen based on particle swarm optimization

  • 摘要: 針對鋼鐵空分企業氧氣放散率高、綜合能耗高的問題,建立了以減小轉爐用氧總量波動和降低系統能耗為目標的轉爐用氧調度模型。綜合考慮了吹煉區間時長不變、各吹煉區間起始時刻滿足工藝要求、鋼水溫度大于1250 °C、轉爐用氧調度前后變動最小等約束,以基于整數空間的粒子群(Particle swarm optimization, PSO)算法進行求解。同時,以國內某大型鋼鐵企業空分廠為案例,采用Pipeline Studio軟件建立該廠區氧氣管網輸配系統模型,對轉爐用氧調度的節能優化效果進行了驗證。結果表明,本文提出的轉爐用氧節能優化調度在研究時間段盡可能安排單臺轉爐生產,有效降低多臺轉爐吹氧重疊時間,在生產時間內錯峰用氧,減小轉爐用氧總量波動,緩解氧氣供求不平衡的矛盾。在120 min研究時長內,調度前后系統氧氣放散量由1242.1 m3降低至0,相應的空分系統的電耗節約了1192.42 kW·h,氧壓機的壓縮能耗增大了41 kW·h,氧氣管網輸配系統節約總能耗為1151.42 kW·h。綜合計算來看,轉爐用氧調度應用到全年,預計減少氧氣放散總量5.44×106 m3,節約氧氣管網輸配系統總能耗5.22×106 kW·h。

     

    Abstract: The air separation plants of iron and steel enterprises are characterized by a high oxygen-emission rate and high comprehensive energy consumption. To solve this problem, a converter oxygen scheduling model was established based on particle swarm optimization (PSO) with the goal of reducing the fluctuation of the total oxygen consumption and saving system energy consumption in the converter. With the full consideration of constraints, such as the constant duration of blowing intervals, compliant starting time of each blowing interval, molten steel temperature above 1250 °C, and minimal variation before and after converter scheduling, PSO based on integer space was used to solve the hypothesis. With the air separation plant of a large domestic iron and steel enterprise as a case study, Pipeline Studio software was used to establish the oxygen transmission and distribution model, and the energy-saving performance of the converter oxygen scheduling was verified. The results show that the optimal scheduling of converter oxygen based on PSO can arrange oxygen for a single converter as much as possible during the study period; moreover, the optimal scheduling can effectively reduce the overlapping time of oxygen blowing in multiple converters, reduce the fluctuation of the total oxygen amount, and alleviate the contradiction between oxygen supply and demand. The oxygen emission of the pipeline transmission and distribution system before and after the dispatch is reduced from 1242.1 m3 to 0 within the 120 min simulation period; the corresponding air separation system oxygen production energy consumption saves 1192.42 kW·h; the compression energy consumption of the oxygen compressor increases by 41 kW·h; and the total energy saving of the system is 1151.42 kW·h. Based on comprehensive calculations, optimal scheduling of converter oxygen based on PSO is applied throughout the year. The oxygen transmission and distribution pipeline system is expected to reduce the total amount of oxygen emission by 5.44×106 m3 and save the total energy consumption by 5.22×106 kW·h.

     

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