首页> 外国专利> TITANIUM BEARING MATERIAL FLOW CONTROL IN THE MANUFACTURE OF TITANIUM TETRACHLORIDE WITH SILICA CONTENT MONITORING OF THE TITANIUM PRODUCT USING FEEDBACK AND FEED FORWARD RESPONSES

TITANIUM BEARING MATERIAL FLOW CONTROL IN THE MANUFACTURE OF TITANIUM TETRACHLORIDE WITH SILICA CONTENT MONITORING OF THE TITANIUM PRODUCT USING FEEDBACK AND FEED FORWARD RESPONSES

机译:利用反馈和前馈反应控制四氯化钛中钛材料的流失并通过硅含量监测钛产品

摘要

This disclosure relates to a process for controlling chlorination reactions in manufacturing titanium tetrachloride in a fluidized bed reactor, followed by processing to form a titanium product comprising an amount of silica, the process comprising: (a) feeding carbonaceous material, titanium bearing material comprising an amount of silica, and chlorine to the fluidized bed reactor to form a gaseous stream, and condensing the gaseous stream to form titanium tetrachloride, a non-condensed gas stream and a condensable product stream; (b) processing the titanium tetrachloride to form a titanium product comprising an amount of silica; (c) analyzing the titanium product comprising an amount of silica to determine the analyzed concentration of silica; (d) identifying a set point concentration of silica; (e) calculating the difference between the analyzed concentration of silica and the set point concentration of silica; (f) measuring the titanium tetrachloride flow to a processing reactor that releases chlorine; (g) measuring the flow of fresh chlorine added to the fluidized bed; (h) measuring the flow of the titanium bearing material added to the fluidized bed reactor and establishing a historic average flow of the titanium bearing material added to the fluidized bed reactor; (i) calculating the chlorine released from the titanium tetrachloride that is processed using the titanium tetrachloride flow data from step (f); (j) calculating the total chlorine flow to the fluidized bed reactor by adding the chlorine flow in step (g) to the chlorine flow calculated in step (i) and establishing a historic average chlorine flow; (k) calculating a unit titanium bearing material consumption per unit chlorine; (l) calculating an estimated current consumption rate of titanium bearing material based on the total chlorine flow from step (j) times the unit titanium bearing material consumption per unit chlorine from step (k); (l) calculating an estimated current consumption rate of titanium bearing material based on the total chlorine flow from step (j) times the unit titanium bearing material consumption per unit chlorine from step (k); and (m) generating a signal based on difference generated in step (e) that provides a feedback response and combining this to the estimated current consumption rate of titanium bearing material from step (l) to provide a feed forward response to control the flow of the titanium bearing material into the fluidized bed reactor.
机译:本公开涉及一种在流化床反应器中制造四氯化钛时控制氯化反应的方法,随后进行处理以形成包含一定量二氧化硅的钛产品,该方法包括:(a)进料含碳材料,含钛材料,以及向流化床反应器中加入一定量的二氧化硅和氯气以形成气态物流,并冷凝该气态物流以形成四氯化钛,非冷凝气流和可冷凝产物物流; (b)处理四氯化钛以形成包含一定量二氧化硅的钛产品; (c)分析包含一定量二氧化硅的钛产品以确定所分析的二氧化硅浓度; (d)确定二氧化硅的设定浓度; (e)计算分析的二氧化硅浓度与二氧化硅设定浓度之间的差; (f)测量流向释放氯气的处理反应器的四氯化钛的流量; (g)测量添加到流化床中的新鲜氯的流量; (h)测量添加到流化床反应器中的含钛材料的流量,并确定添加到流化床反应器中的含钛材料的历史平均流量; (i)使用步骤(f)中的四氯化钛流量数据计算从四氯化钛释放的氯; (j)通过将步骤(g)中的氯流与步骤(i)中计算出的氯流相加并确定历史平均氯流,来计算流向流化床反应器的总氯流; (k)计算每单位氯的单位含钛材料消耗量; (l)根据步骤(j)中的总氯流量乘以步骤(k)中每单位氯的单位含钛材料消耗量,计算出含钛材料的估计电流消耗率; (l)根据步骤(j)中的总氯流量乘以步骤(k)中每单位氯的单位含钛材料消耗量,计算出含钛材料的估计电流消耗率; (m)基于在步骤(e)中产生的差异产生信号,该信号提供反馈响应,并将其与步骤(l)中的含钛材料的估计电流消耗率相结合,以提供前馈响应以控制流体的流动。将含钛材料放入流化床反应器中。

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