Oxidative Desulfurization of Sour Gas Condensate and Optimization of Parameters with Response Surface Methodology

Authors

  • Amin Shafeghat Petroleum Refining Technology Development Division, Research Institute of Petroleum Industry, Tehran, Iran
  • Jafar Tofighi Darian Chemical Engineering Department, Tarbiat Modares University, Tehran, Iran
  • maryam ghaedian Petroleum Refining Technology Development Division, Research Institute of Petroleum Industry, Tehran, Iran
  • mehdi alibolandi Chemical Engineering Department, Tarbiat Modares University, Tehran, Iran
  • Sayed Javid Royaee Petroleum Refining Technology Development Division, Research Institute of Petroleum Industry, Tehran, Iran
Abstract:

Reducing environmental pollution via elimination of sulfur compounds from gas condensate was the aim of this research. Whereby oxidative desulfurization from gas condensate with 3200 ppm initial sulfur was accomplished by hydrogen peroxide (30%wt) as oxidant and formic acid as catalyst. The sulfones after generation in the oxidation step were extracted through a method of liquid-liquid extraction by acetone as a polar solvent. The effects of variables: coefficient of oxidant to sulfur molar ratio (O/S), temperature (T), and coefficient of catalyst to oxidant molar ratio (C/O) were investigated. The experiments were designed with response surface methodology based on central composite design (CCD). The results of experiments demonstrated that none of these variables (O/S, T, and C/O) have any interaction, and among these variables, O/S plays a significant role with the most influence on desulfurization and C/O and T are of the second and third primary of importance, respectively. In addition, 86% desulfurization was obtained in the optimum conditions.

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Journal title

volume 31  issue 1

pages  13- 23

publication date 2020-03-01

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