化工学报 ›› 2010, Vol. 61 ›› Issue (9): 2401-2408.

• 分离工程 • 上一篇    下一篇

油水乳液体系水合分离塔的模拟计算

马庆兰,陈光进   

  1. 中国石油大学流体高压相态及物性研究实验室
  • 出版日期:2010-09-05 发布日期:2010-09-05

Simulation of hydrate separation tower for water-in-oil emulsion system

MA Qinglan,CHEN Guangjin   

  • Online:2010-09-05 Published:2010-09-05

摘要:

在水合物法辅助分离乙烯裂解气流程中,水合物分离塔是非常关键的单元操作设备。气体混合物在塔内的分离过程与气体吸收塔类似,但因涉及气-液-液-固4相,所以计算更加复杂。将速率法和平衡级法相结合,提出了油水微乳体系吸收-水合分离塔的模拟计算方法。模拟计算了一典型乙烯裂解气在水合分离塔内的分离状况。为了确定适宜的操作条件,分别考核计算了操作温度和气液比对分离效果及能量消耗的影响。所得结果对水合分离塔的设计、操作条件的确定以及乙烯裂解气分离流程的制定有很重要的意义。计算结果还表明,通过水合物技术在0℃左右可实现氢气、甲烷和C2以上组分的有效分离,因此可以节约大量制冷功耗。

关键词:

水合物, 油水乳液, 吸收-水合, 分离塔

Abstract:

The hydrate separation tower is the most important unit operation equipment in the process of separating pyrolysis gas with the aid of hydrate technique for recovering ethylene.The water-in-oil emulsion could enhance the hydrate formation rate and improve the flow behavior of hydrate slurry.In this work,the simulation algorithm of absorption-hydration separation tower for the water-in-oil emulsion system was developed,which was involved with the vapor-liquid-liquid-hydrate four phase equilibria.The operation conditions,separation efficiency and energy consumption of the hydrate separation tower were studied under the different gas-liquid ratio conditions by combining the equilibrium and non-equilibrium stage approach.The calculation results indicated that the lower gas-liquid ratio could improve the separation efficiency,but may bring about the high energy consumption.The results also showed that hydrogen and methane could be separated effectively from C2 plus-components at around 0℃ through hydrate technique.The calculation results are of significance for the design of hydrate separation equipment,the determination of operation conditions and the planning of separation process for the ethylene pyrolysis gas.

Key words:

水合物, 油水乳液, 吸收-水合, 分离塔