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260t/h焦煤混烧CFB锅炉燃烧控制策略优化
引用本文:贺悦科,田晓兰,邹包产,赫尔东.260t/h焦煤混烧CFB锅炉燃烧控制策略优化[J].发电设备,2014(1):23-26.
作者姓名:贺悦科  田晓兰  邹包产  赫尔东
作者单位:[1]华北电力科学研究院(西安)有限公司,西安710065 [2]长岭炼化岳阳机电技术有限公司,岳阳414012 [3]北京京丰燃气发电有限责任公司,北京100074
摘    要:结合一台260t/h CFB锅炉燃用石油焦的实践经验,介绍了锅炉设备及系统工艺流程;并针对锅炉控制系统的控制目标和难点,提出了增加主蒸汽压力设定值微分、汽包压力微分、能量需求基准函数等锅炉主控的前馈修改方案;并对一次风、二次风,以及床温控制等系统的控制方案进行了完善和优化。结果表明:负荷扰动5MW时蒸汽压力动态偏差最大0.55MPa,床温变化小于25K,满足标准要求。

关 键 词:CFB锅炉  焦煤混烧  前馈  能量需求  床温  一次风

Optimization on Combustion Control Strategy for a 260 t/h Coking Coal Co-firing CFB Boiler
He Yueke,Tian Xiaolan,Zou Baochan,He Erdong.Optimization on Combustion Control Strategy for a 260 t/h Coking Coal Co-firing CFB Boiler[J].Power Equipment,2014(1):23-26.
Authors:He Yueke  Tian Xiaolan  Zou Baochan  He Erdong
Affiliation:1. North China Electric Power Research Institute (Xi'an) Co., Ltd., Xi'an 710065, China; 2. Changling Petrochemical Yueyang Mechanical and Electrical Technology Co., Ltd., Yueyang 414012, China; 3. Beijing Jingfeng Gas-fired Power Generation Co., Ltd., Beijing 100074, China)
Abstract:A boiler system and its process flow were introduced in combination with the practical experience of burning petroleum coke in a 260 t/h CFB boiler. Aiming at the control objectives and difficulty of the boiler control system, a boiler master feedforward modification scheme was put forward, such as adding main steam pressure set value differential, drum pressure differential, and energy demand baseline function, etc. Moreover, control schemes for primary air, secondary air and bed temperature control systems were improved and optimized. Results show that the maximum dynamic deviation of steam pressure is only 0.55 MPa and the change of bed temperature is less than 25 K, under the load disturbance of 5 MW, which meets the requirements of relevant standards.
Keywords:CFB boiler  coking coal co-firing  feedforward  energy demand  bed temperature  primaryair
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