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煤气化装置氧煤比控制策略浅析 被引量:6

Analysis of the Control Strategy of Oxygen/Coal Ratio in Coal Gasifying Plant
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摘要 煤气化是煤、O_2、水或蒸汽在加压条件下进行复杂化学反应,生成以CO和H_2为主的合成气。合成气中,CO和H_2含量是通过控制O_2和煤的进料量比例来实现的。氧煤比控制方案是煤气化装置安全、稳定运行控制方案的核心,氧煤比控制的精确性对碳的转化率、合成气组分、气化炉温度等关键工艺指标有着直接的影响。不同的工艺路线、气化炉炉型、进料方式有不同的氧煤比控制策略。通过对国内部分煤化工装置氧煤比控制方案的研究,阐述了不同装置的控制方案,并对比了优缺点。结果表明,氧煤比控制策略有着不同的适用性,需根据不同的工艺条件进行优化。该分析能为煤气化装置工程技术人员的实际应用提供借鉴。 Coal gasification is a complex chemical reaction of coal,oxygen,water,or steam under pressure conditions,which generates the syngas based on carbon monoxide and hydrogen. The content of carbon monoxide and hydrogen in the syngas is achieved by controlling the proportion of the feed of oxygen and coal. Therefore,oxygen/coal ratio control scheme is the core of long-term safe and stable operation control for coal gasification plant;the accuracy of oxygen/coal ratio control has a direct impact on key process indicators such as carbon conversion,syngas composition and gasifier temperature. Different process routes,different types of gasifier furnace,and different modes of feed have different oxygen/coal ratio control strategy. Through researching on the oxygen/coal ratio control schemes of some domestic mainstream coal gasification plants,the control scheme are introduced and the advantages and disadvantages of different control schemes are expounded and compared. Results show that different oxygen/coal ratio control strategies have different applicability,and need to be optimized according to different process conditions.The analysis can provide reference for the practical application of coal gasification plant engineering technicians.
作者 董清锋 陈菲 DONG Qingfeng;CHEN Fei(Hydrocardon High-Efficiency Utilization Technology Research Center, Shaanxi Yanchang Petroleum (Group) Co., Ltd., Xi' an 710075, China)
出处 《自动化仪表》 CAS 2018年第6期78-80,共3页 Process Automation Instrumentation
关键词 氧煤比 控制策略 气力输送 串级 耦合 限幅器 选择器 Oxygen/Coal ratio Control strategy Pneumatic conveying Cascade Coupling Limiter Selector
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  • 1于海龙,赵翔,周志军,周俊虎,刘建忠,岑可法.煤浆浓度对水煤浆气化影响的数值模拟[J].动力工程,2005,25(2):217-220. 被引量:34
  • 2施仁.自动化仪表与过程控制[M].北京:电子工业出版社,1990:50-62. 被引量:1
  • 3WEN C Y,CHUANG T Z.Entrainment coal gasification modeling[J]. Ind Eng Chem Process Des Dev,1979,18(4):684-695. 被引量:1
  • 4LIU X J,ZHANG W R,PARK T J.Modelling coal gasification in an entrained flow gasifier[J]. Combust Theory and Modelling,2001,5(4):595-608. 被引量:1
  • 5DU M,Hao Y,LIU S.Numerical study on coal gasification in texaco entrained-flow coal gasifier[C]. APPEEC2009,Wuhan,2009. 被引量:1
  • 6周春晖.过程控制手册[M].北京:化学工业出版社,1993. 被引量:2
  • 7吴玉新,张建胜,王明敏,岳光溪,吕俊复.用简化PDF模型对气化炉运行特性的分析[J].中国电机工程学报,2007,27(32):57-62. 被引量:19
  • 8何永德.现代煤化工技术手册[M].化学工业出版社. 被引量:1
  • 9肖玲.化工自动化及仪表《德国SWR(斯维尔)流培计在煤粉气化装置一航天炉中的应用》[M].2010. 被引量:1
  • 10航天石化技术装备工程公司《HT-I.粉煤气工艺及关键设备》[M].2010. 被引量:1

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