Effect of Crude Oil and Nitrogen Gas Flow Rates on the Time Taken for Flow Initiation of Waxy Crude Oil

Transportation of waxy crude oil in a production pipeline often encountered flow assurance issues, such as wax deposition. In a case where pipeline shutdown is needed, wax deposit is likely to form within the pipelines, which leads to operational complexity during the restart phase. Commonly, crude oil restarts to flow after a significantly high restart pressure is pumped longer than is necessary. This is due to the physical hindrance caused by the solid wax, which requires additional pressure to disintegrate it before achieving a steady crude oil flow. This study aims to investigate the effect of crude oil and nitrogen gas flow rates on the time taken for crude oil flow initiation using a flow loop rig, which is connected to a nitrogen gas injection system. The nitrogen gas was injected into the test section pipeline at predetermined flow rates within specified periods. After 45 min of static cooling, the crude oil gear pump is switched on to build sufficient pressure to initiate the waxy crude oil flow in the pipeline. Additionally, a statistical analysis by the response surface methodology was also performed by Minitab® 19 software. Results show that the maximum reduction in flow initiation is 73.7% at 5 L/min of crude oil and 1 L/min of nitrogen gas. This study reveals that the presence of nitrogen gas improved the pipeline restart phase by minimizing both restart pressure and time taken for flow initiation.

[1]  A. Pantaleo,et al.  Mitigation and Remediation Technologies of Waxy Crude Oils’ Deposition within Transportation Pipelines: A Review , 2022, Polymers.

[2]  Palaniselvam Kuppusamy,et al.  Box–Behnken Response Surface Methodology Design for Amaranth dye degradation using Gold Nanoparticles , 2022, Optik.

[3]  H. A. Umar,et al.  Parametric optimisation through the use of Box-Behnken design in the Co-gasification of oil palm trunk and frond for syngas production , 2022, Fuel.

[4]  A. Dargahi,et al.  Enhanced electrocatalytic degradation of bisphenol A by graphite/β-PbO2 anode in a three-dimensional electrochemical reactor , 2021 .

[5]  Behbood Abedi,et al.  Startup flow of gelled waxy crude oils in pipelines: The role of volume shrinkage , 2020 .

[6]  N. Rahman,et al.  Effective removal of acetaminophen from aqueous solution using Ca (II)-doped chitosan/β-cyclodextrin composite , 2020 .

[7]  S. Sulaiman,et al.  Experimental investigation of compressibility of waxy crude oil subjected to static cooling , 2019, Journal of Petroleum Science and Engineering.

[8]  Pavel Valeryevich Roschin,et al.  Investigations of temperature and dilution effect on rheological properties of waxy crude oil , 2019, Journal of Petroleum Exploration and Production Technology.

[9]  S. Chakraborty,et al.  Application of response surface methodology (RSM) for optimization of leaching parameters for ash reduction from low-grade coal , 2018, International Journal of Mining Science and Technology.

[10]  N. Hasan,et al.  Review of the Factors that Influence the Condition of Wax Deposition in Subsea Pipelines , 2018 .

[11]  M. Theyab Wax deposition process: mechanisms, affecting factors and mitigation methods , 2018 .

[12]  S. Sulaiman,et al.  Flow start-up and transportation of waxy crude oil in pipelines-A review , 2018 .

[13]  S. Sulaiman,et al.  Injection of non-reacting gas into production pipelines to ease restart pumping of waxy crude oil , 2017 .

[14]  R. Mohsin,et al.  Effect of emulsified water on the wax appearance temperature of water-in-waxy-crude-oil emulsions , 2016 .

[15]  Wanwisa Rukthong,et al.  Integration of computational fluid dynamics simulation and statistical factorial experimental design of thick-wall crude oil pipeline with heat loss , 2015, Adv. Eng. Softw..

[16]  H. S. Fogler,et al.  Wax Deposition: Experimental Characterizations, Theoretical Modeling, and Field Practices , 2015 .

[17]  P. T. Bhaskoro,et al.  Yield stress measurement of gelled waxy crude oil: Gap size requirement , 2015 .

[18]  S. Sulaiman,et al.  Gas void formation in statically cooled waxy crude oil , 2014 .

[19]  Qiyu Huang,et al.  Effect of operating conditions on wax deposition in a laboratory flow loop characterized with DSC technique , 2014, Journal of Thermal Analysis and Calorimetry.

[20]  Y. Joliff,et al.  Numerical modelling of pipe internal stresses induced during the coating process – Influence of pipe geometric characteristics on stress state , 2013 .

[21]  Bin Jiang,et al.  The Research of Mooring System of FPSO and its Application , 2013 .

[22]  S. Correra,et al.  Waxy Oil Pipeline Transportation through Cold Flow Technology: Rheological and Pressure Drop Analyses , 2013 .

[23]  Ali Reza Soleimani Nazar,et al.  An experimental design approach for investigating the effects of operating factors on the wax deposition in pipelines , 2013 .

[24]  Jinjun Zhang,et al.  Effect of Carbon Number Distribution of Wax on the Yield Stress of Waxy Oil Gels , 2013 .

[25]  M. Deo,et al.  The propagation of pressure in a gelled waxy oil pipeline as studied by particle imaging velocimetry , 2012 .

[26]  M.K.S. Sastry,et al.  Wax formation in oil pipelines: A critical review , 2011 .

[27]  M. Deo,et al.  Yield behavior of gelled waxy oil in water-in-oil emulsion at temperatures below ice formation , 2011 .

[28]  Ekeh Modesty Kelechukwu,et al.  Influencing factors governing paraffin wax deposition during crude production , 2010 .

[29]  M. Deo,et al.  Yield Behavior of Gelled Waxy Oil: Effect of Stress Application in Creep Ranges , 2009 .

[30]  A. Mehrotra,et al.  Deposition from Wax−Solvent Mixtures under Turbulent Flow: Effects of Shear Rate and Time on Deposit Properties† , 2009 .

[31]  S. Patil,et al.  Measurement of Wax Appearance Temperature under Simulated Pipeline (Dynamic) Conditions , 2008 .

[32]  Ian A. Frigaard,et al.  Compressible displacement of waxy crude oils in long pipeline startup flows , 2007 .

[33]  Julian Y. Zuo,et al.  An improved thermodynamic model for wax precipitation from petroleum fluids , 2001 .

[34]  J. P. Brill,et al.  Wax deposition in single phase flow , 1999 .

[35]  T. Lundstedt,et al.  Experimental design and optimization , 1998 .

[36]  I. M. El-Gamal,et al.  Nitrogen-based copolymers as wax dispersants for paraffinic gas oils , 1998 .

[37]  David V. Boger,et al.  The Yielding of Waxy Crude Oils , 1998 .

[38]  R. Brereton,et al.  Experimental design. III. Quantification , 1996 .

[39]  C. U. Ikoku,et al.  Criteria for the design of waxy crude oil pipelines: maximum pump (horsepower) pressure requirement , 1995 .

[40]  M. Sanjay,et al.  Paraffin problems in crude oil production and transportation: A review , 1995 .

[41]  T. K. Perkins,et al.  STARTING BEHAVIOR OF GATHERING LINES AND PIPELINES WHEN FILLED WITH GELLED PRUDHOE BAY OIL , 1971 .