河北联合大学学报(自然科学版)
河北聯閤大學學報(自然科學版)
하북연합대학학보(자연과학판)
Journal of Hebei United university natural sclence edition
2014年
3期
35-40
,共6页
转炉%优化配料%静态控制模型%终点预报
轉爐%優化配料%靜態控製模型%終點預報
전로%우화배료%정태공제모형%종점예보
Converter%proportioning optimizaiton%static control model%end-point pridiction
在分析转炉炉料结构优化及 BP 预报模型特点的基础上,针对某厂50 t 转炉生产条件,构建了由优化配料、静态预测、过程控制、脱氧合金化和成本计算等模块构成转炉冶炼静态控制系统。以机理模型为基础、采用增量模型校正的优化配料模块,用以精确计算入炉料结构;以 BP 神经网络为基础构建了静态预测模块,对转炉冶炼终点碳和温度进行预测;以操作经验为基础构建了过程控制模块,动态给出冶炼过程控制的枪位曲线、加料时机和加入量;基于终点预测和全氧计算模型构建了脱氧及合金化模块,进而对转炉冶炼成本进行计算,构建了成本计算模块。通过本系统的开发,建立了全过程指导的炉料结构优化与冶炼静态控制,为现场生产提供了指导。
在分析轉爐爐料結構優化及 BP 預報模型特點的基礎上,針對某廠50 t 轉爐生產條件,構建瞭由優化配料、靜態預測、過程控製、脫氧閤金化和成本計算等模塊構成轉爐冶煉靜態控製繫統。以機理模型為基礎、採用增量模型校正的優化配料模塊,用以精確計算入爐料結構;以 BP 神經網絡為基礎構建瞭靜態預測模塊,對轉爐冶煉終點碳和溫度進行預測;以操作經驗為基礎構建瞭過程控製模塊,動態給齣冶煉過程控製的鎗位麯線、加料時機和加入量;基于終點預測和全氧計算模型構建瞭脫氧及閤金化模塊,進而對轉爐冶煉成本進行計算,構建瞭成本計算模塊。通過本繫統的開髮,建立瞭全過程指導的爐料結構優化與冶煉靜態控製,為現場生產提供瞭指導。
재분석전로로료결구우화급 BP 예보모형특점적기출상,침대모엄50 t 전로생산조건,구건료유우화배료、정태예측、과정공제、탈양합금화화성본계산등모괴구성전로야련정태공제계통。이궤리모형위기출、채용증량모형교정적우화배료모괴,용이정학계산입로료결구;이 BP 신경망락위기출구건료정태예측모괴,대전로야련종점탄화온도진행예측;이조작경험위기출구건료과정공제모괴,동태급출야련과정공제적창위곡선、가료시궤화가입량;기우종점예측화전양계산모형구건료탈양급합금화모괴,진이대전로야련성본진행계산,구건료성본계산모괴。통과본계통적개발,건립료전과정지도적로료결구우화여야련정태공제,위현장생산제공료지도。
Based on the analysis about the proportioning optimization and prodiction model applied with BP neural network,a static control system for converter has been established for 50t converter used in a plant,which comprised with some modules as the proportioning optimization,the static pridiction,process control,deoxidation and alloying, and cost calculation. The porportioning optimization module has been established on mechanical modle,and used to calculate the burden sturcture for converter. The static pridiction model has been set up on BP neural network to pridicting the endpoint carbon content in liquid steel and its temperature. The process control model has been con-structed with operating experiences to provide lance level curve,the charging time and the feeding quantities. The deoxidation and alloying model has been set up on endpoint pridiction and total oxygen content module to provide the quantities of deoxidant and alloys. The cost calculation model has been established on process control and static pridcition. The static control system could provide real-time and direct guidance for operater through the proportion optimization and static control model.