Prediction of Operating Status for Flue-Gas Desulfurization Equipment Based on Deep Fuzzy Inference Model
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摘要: 烟气脱硫处理是聚焦污染防治、实现节能减排的重要举措, 其安全、稳定运行直接影响着经济社会可持续发展与居民生命健康. 然而, 长期运行下的烟气脱硫设备往往不可避免地出现故障且难以预测, 进而导致连锁反应甚至事故. 鉴于此, 本文提出一种基于深度模糊推理模型(DFIM)的烟气脱硫设备运行状态预测方法. 首先, 构建数据驱动的深度模糊信念网络(DFBN), 通过模糊特征学习算法将传感器获取的原始数据映射为抗干扰的模糊语义特征, 并实现模糊特征的预测输出. 其次, 建立推理门控层, 进一步对输出模糊特征进行识别, 并聚焦设备故障模式. 然后, 结合操作经验和运行环境, 对标设备运行状态和故障模式, 给出处置方案. 最后, 以实际烟气脱硫系统循环泵内浆液pH和轴承温度为设备运行状态变量为例, 测试DFIM在烟气脱硫设备运行状态预测中的有效性, 实验结果表明所提出的DFIM在预测精度、稳定性与快速性等方面均优于现有方法, 对设备运维与管理具有重要的指导意义.Abstract: Flue-gas desulfurization treatment is an important measure to focus on pollution prevention and achieve emission reduction. The safe and stable operation of flue-gas desulfurization process directly affects the sustainable development of the economy and society as well as the health of residents. However, under long-term operation, faults inevitably occur in this equipment, which are difficult to be predicted and thus lead to a chain reaction and even accidents. In view of these problems, this paper proposes a deep fuzzy inference model (DFIM) to predict the operating status of flue-gas desulfurization equipment. First, a data-driven deep fuzzy belief network (DFBN) is constructed and trained by fuzzy feature learning, which can map the raw data obtained from the sensor into anti-interference fuzzy semantic features and further give the predicted outputs. Second, an inference gating layer is designed to recognize the output fuzzy features, focusing on the fault modes of flue-gas desulfurization equipment. Third, according to the operational experience and operating status as well as fault modes of the equipment, the optimal disposal plan is then provided. Finally, taking the PH of the slurry in the circulating pump and the temperature of the circulating pump bearing as the variables of the equipment operating status, the effectiveness of DFIM in the prediction of the operating status of flue-gas desulfurization equipment is tested. The experimental results show that the proposed DFIM outperforms the existing methods in terms of prediction accuracy, stability and rapidity, which has important guiding significance for the operation and maintenance as well as management of the operating equipment.
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表 1 离心泵运行状态关联变量
Table 1 Correlation variables of centrifugal pump
标号 单位 相关特征变量 x1 r/min 电机转速 x2 ℃ 入口浆液温度 x3 m3/h 浆液流量 x4 % 出口阀门开度 x5 ℃ 烟气温度 x6 A 泵运行电流 x7 mm/s 泵振动值 x8 kPa 入口压力 y1 - 浆液pH y2 ℃ 轴承温度 表 2 事件定义
Table 2 Event definitions
事件 浆液pH 轴承温度 故障情况 A1 $A_{{\rm{PH}}}(1)$ $A_{{\rm{T}}}(1)$ 酸性腐蚀加速 A2 $A_{{\rm{PH}}}(1)$ $A_{{\rm{T}}}(2)$ 腐蚀 A3 $A_{{\rm{PH}}}(1)$ $A_{{\rm{T}}}(3)$ 严重腐蚀 A4 $A_{{\rm{PH}}}(2)$ $A_{{\rm{T}}}(2)$ 机械负载异常 A5 $A_{{\rm{PH}}}(2)$ $A_{{\rm{T}}}(3)$ 轴承紧急故障 A6 $A_{{\rm{PH}}}(3)$ $A_{{\rm{T}}}(1)$ 结垢初期 A7 $A_{{\rm{PH}}}(3)$ $A_{{\rm{T}}}(2)$ 结垢 A8 $A_{{\rm{PH}}}(3)$ $A_{{\rm{T}}}(3)$ 管路堵塞、过热 A9 $A_{{\rm{PH}}}(2)$ $A_{{\rm{T}}}(1)$ 安全运行 表 3 运维建议
Table 3 Operation and maintenance suggestions
标签 运维建议 ${\rm{Adv}}_1$ 调整浆液配方, 添加石灰石等碱性物质, 将pH值回调至正常范围, 抑制酸性腐蚀. ${\rm{Adv}}_2$ 降低设备负载, 必要时停机避免腐蚀扩散, 检查关键部件的腐蚀深度, 更换受损部件. ${\rm{Adv}}_3$ 检查浆液流量、电机转速是否超出范围, 补充润滑油, 减少摩擦导致的负载增加. ${\rm{Adv}}_4$ 立即停机, 切断电源, 防止轴承过热烧毁; 拆解轴承组件, 检查是否存在滚珠碎裂、保持架断裂等故障, 排查轴承过热原因. ${\rm{Adv}}_5$ 调整浆液成分, 降低pH值至临界结垢点以下, 抑制碳酸钙/硫酸钙结晶, 对喷淋层喷嘴、浆液管道进行低压冲洗. ${\rm{Adv}}_6$ 维持当前运行参数, 定期记录关键指标. 表 4 DFIM与其他模型对设备状态的预测结果对比
Table 4 Comparison results for predicting equipment states of DFIM and other models
参数 模型 MAE R2 浆液PH DFIM 0.12±0.05 0.89±0.07 DFIM(无正则化) 0.16±0.09 0.83±0.09 DBN 0.24±0.05 0.63±0.11 LSTM 0.21±0.08 0.66±0.13 SOFNN 0.18±0.10 0.71±0.15 FNN 0.20±0.09 0.67±0.14 RBFNN 0.23±0.06 0.65±0.12 BPNN 0.26±0.12 0.62±0.19 轴承温度(℃) DFIM 2.28±0.52 0.87±0.12 DFIM(无正则化) 5.38±0.74 0.81±0.14 DBN 7.63±0.61 0.56±0.17 LSTM 7.15±0.76 0.59±0.18 SOFNN 6.87±0.82 0.64±0.21 FNN 6.95±0.79 0.62±0.20 RBFNN 7.49±0.73 0.58±0.16 BPNN 8.34±0.96 0.54±0.24 表 5 DFIM预测结果与触发的运维建议
Table 5 DFIM prediction results and triggered operation and maintenance suggestions
PH 温度(℃) 事件 运维 执行情况 6.1 52.87 A6 ${\rm{Adv}}_5$ 执行冲洗1次 5.7 74.98 A5 ${\rm{Adv}}_4$ 触发2次, 人工确认后停机1次 4.8 48.03 A1 ${\rm{Adv}}_1$ 在PH低于$B_{\mathrm{PH,\;low}}(t)$时执行3次 4.9 72.67 A3 ${\rm{Adv}}_2$ 触发1次, 人工确认后停机0次 5.4 46.6 A9 ${\rm{Adv}}_6$ 多次触发, 作为正常运行建议 5.7 61.89 A4 ${\rm{Adv}}_3$ 在负载异常预警下执行润滑补充2次 -
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