摘要
等压开式制冷工艺是一种较新的天然气凝液回收工艺技术,与目前广泛采用的直接换热工艺相比,该工艺所需设备数量少,投资和运行费用低。以长庆油田典型伴生气为例,对该工艺进行了模拟研究,分析并优化了影响该工艺C_3^+回收率以及能耗的主要工艺参数。计算结果表明:(1)C_3^+回收率随原料气预冷温度的降低而增加,当原料气预冷温度低于-30℃后,C_3^+回收率随温度变化的增幅变缓;(2)混合冷剂节流压力对C_3^+回收率以及脱乙烷塔塔底重沸器热负荷的影响不显著,但节流压力降低会增加混合冷剂压缩机的能耗;(3)混合冷剂冷却温度越低,C_3^+回收率越高。最优操作条件为:原料气预冷温度-30℃,混合冷剂节流压力500kPa,混合冷剂冷却温度-30℃。此时,C_3^+回收率可达96.1%。
Isobaric open refrigeration process is a new NGL-recovery technology . Compared with the traditional direct heat exchange process, this new process requires less equipment, and has lowercapital and operating costs. In this study, associated gas from Changqing Oiltield is taken as anexample. The process is simulated, and the process parameters affecting C^ recovery and energyconsumption are investigated and optimized. The results indicate that：①Cf recovery increases as the feed gas temperature decreases, however when the feed gas temperature is below -30℃ , C3＋ recovery increases slowly;②refrigerant throttle pressure has lktle influence on ethanizer reboiler duty, but a lower refrigerant throttle pressure means a larger mixed refrigerantcompressor duty required;③ C3＋ recovery increases with the decrease of refrigerant coolingtemperature. The optimum operating conditions are as follows： feed gas temperature is -30℃ , refrigerant throttle pressure is 500 kPa, refrigerant cooling temperature s -30℃. Under these conditions, the C2＋ recovery can reach 96. 1%.
出处
《石油与天然气化工》
CAS
北大核心
2017年第3期46-50,共5页
Chemical engineering of oil & gas
关键词
天然气
凝液回收
开式
制冷混合冷剂
natural gas llquid recovery, open refrigeration, m ixed refrigerant
