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Petroleum Science and Technology Volume 36, 2018 - Issue 19
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Original Articles

Modeling crude oil gasification

Yisheng Hua State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southwest Petroleum University, Chengdu, China; Correspondence[email protected]
,
Songhai Qina State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southwest Petroleum University, Chengdu, China;
,
Xu Wangb Institute of Petroleum Engineering, Heriot-Watt University, Edinburgh, UK;
&
Longhao Caic Drilling & Production Technology Research Institute of Liaohe Oilfield, PetroChina, Panjin, China
Pages 1568-1572 | Received 07 Jun 2018, Accepted 15 Jun 2018, Published online: 04 Oct 2018
 
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Abstract

The characteristics of CO2-gasification of crude oil under steady-state condition were studied using a simulator. The model was developed using the minimization Gibbs free energy minimization. The effects of reactor temperature and CO2/crude oil ratio on gas composition and lower heating value (LHV) of the produced syngas were investigated. As a result, the maximum LHV was obtained at a CO2/crude oil ratio of 0.1 and gasification temperature of 800 °C.

Acknowledgments

The authors would like to thank Emate (www.emate.ac.cn) for their excellent language service. The authors are thankful to IAMSET for their research improving and revising suggestions from many scholars. Supported by the National Natural Science Foundation of China (Grant No. 41702286); Supported by Scientific Research starting project of SWPU (No. 2017QHZ002); Supported by Open Fund of State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation in Southwest Petroleum University (No. PLN201724).

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