JOURNAL OF SHANDONG UNIVERSITY (ENGINEERING SCIENCE) ›› 2012, Vol. 42 ›› Issue (3): 57-62.

• Articles • Previous Articles     Next Articles

A static simulation model of overall process for the NGL recovery unit

PAN Duo-tao1,  HUANG Ming-zhong1, ZHANG Xue-jun2, YUAN De-cheng1   

  1. 1. Chemical Control Technology Key Laboratory of Liaoning Province, Shenyang University of
    Chemical Technology, Shenyang 110142, China;
    2. PetroChina Liaohe Petroleum Oil and Gas Gathering Co., Ltd, Panjin 124010, China
  • Received:2011-09-13 Online:2012-06-20 Published:2011-09-13

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Abstract:

 A static simulation model of overall process for a light hydrocarbon recovery plant were  developed, which could  not only improve the yield, save energy and reduce loss,  but could also ensure safety in production.The distillation units were modeled based on CAPE-OPEN technology, the parameters of the process were analyzed by simulation and emendated according to the actual data. The correlative process parameters which could  meet the requirement of improving the ethane yield were simulated and evaluated by sensitivity analysis. The process parameters of the demethanizer were optimized. The results showed that the simulation data were in good agreement with the plant data, and the optimum process parameters could  be applied to guide the actual industrial production.

Key words:  natural gas, light hydrocarbon recovery, distillation column, simulation, modeling, industrial application

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