Solubility and Rheological Properties of Live Crude Oils

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Abstract:

Multiphase transportation of the wellhead product in a single pipeline is widely used in oilfields. The oil samples transported in the multiphase pipeline are often live oils saturated by light alkanes. To support the multiphase pipelining more efficiently, in this paper, the solubility and rheology of Chang10 live crude oils are studied at the pressures range from 0 to 2.0 MPa. It was found that the dissolved gas in the live oils is mainly composed of methane (32.70 vol% at 1MPa), ethane (19.43 vol% at 1MPa), propane (21.42 vol% at 1MPa) and C4+ component (22.50 vol% at 1 MPa). The gas-oil ratio, Rs, of the live oils increases rapidly with the increase of saturation pressure. However, the effect of saturation temperature on Rs is very small. The pour point, abnormal point, WAT, viscosity/equilibrium viscosity and yield stress of the live oils decrease obviously with the increase of saturation pressure, meaning that the rheological properties of the live oils improve greatly by gas dissolving. The rheological properties of the live oils are improved mainly by the dilution effect of the dissolved gas.

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Advanced Materials Research (Volumes 524-527)

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1881-1888

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May 2012

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] V.R. Meray, J.-L. Volle, C.J.P. Schranz, et al. Influence of Liht Ends on the Onset Crystallization Temperature of Waxy Crudes Within the Frame of Multiphase Transport, SPE 26549 (1993).

DOI: 10.2118/26549-ms

Google Scholar

[2] K. Karan, J. Ratulowski, P. German. Measurement of Waxy Crude Properties Using Novel Laboratory Techniques, SPE 62945 (2000).

DOI: 10.2118/62945-ms

Google Scholar

[3] T.S. Brown, V.G. Niesen, D.D. Erickson. The Effects of Light Ends and High Pressure on Paraffin Formation, SPE 28505 (1994).

DOI: 10.2118/28505-ms

Google Scholar

[4] E. Uba, K. Ikeji, M. Onyekonwu. Measurement of Wax Appearance Temperature of an Offshore Live Crude, SPE 88963 (2004).

DOI: 10.2118/88963-ms

Google Scholar

[5] G.Z. Ai, Y.M. Li, Q.F. Sun, et al. Determining Wax Precipitation Point of Crude Oil in Flowing Gas/Oil Two Phase Mixture by Using Rotating Wheel Flow Simulator, Oilfield Chemistry 17 (2000) 181-183.

Google Scholar

[6] J.S. Tang, P.X. Zhang. Mass Transfer of Methane into Oil for the Transportation of Gas and Oil Through a Single-Phase Pipeline, SPE 77651 (2002).

DOI: 10.2118/77651-ms

Google Scholar

[7] R. Rai, B. Sarkar, V. Dalal. Multiphase Transpiration of High Waxy Crudes, SPE Advanced Technology Series 4 (1996) 178-184.

DOI: 10.2118/27061-pa

Google Scholar

[8] T.M. Williams, J.J.C. Hsu, H.L. Patterson. System Developed to Predict Waxy Crude's Breakaway Yield Stress, Oil & Gas Journal 94 (1996) 35-39.

Google Scholar

[9] C.X. Li, F. Yang, J. Wu, et al. China Patent: 2011, CN 101776626A.

Google Scholar

[10] F. Yang, C.X. Li, J. Wu, et al. China Patent: 2011, CN 201773053U.

Google Scholar

[11] SY/T 0522-2008, Determination of wax appearance in crude petroleum-Test method by rotational viscometer [S].

Google Scholar