Determination of wax content in crude oil

ABSTRACT Wax deposition is one of the chronic problems in the petroleum industry. The various crude oils present in the world contain wax contents of up to 32.5%. Paraffin waxes consist of straight chain saturated hydrocarbons with carbons atoms ranging from C18 to C36. Paraffin wax consists mostly with normal paraffin content (80–90%), while, the rest consists of branched paraffins (iso-paraffins) and cycloparaffins. The sources of higher molecular weight waxes in oils have not yet been proven and are under exploration. Waxes may precipitate as the temperature decreases and a solid phase may arise due to their low solubility. For instance, paraffinic waxes can precipitate out when temperature decreases during oil production, transportation through pipelines, and oil storage. The process of solvent dewaxing is used to remove wax from either distillate or residual feedstocks at any stage in the refining process. The solvents used, methyl-ethyl ketone and toluene, can then be separated from dewaxed oil filtrate stream by membrane process and recycled back to be used again in solvent dewaxing process.

[1]  K. Bhatt,et al.  Wax Content of Crude Oil: A Function of Kinematic Viscosity and Pour Point , 2015 .

[2]  Adel M. Elsharkawy,et al.  Wax deposition from Middle East crudes , 2000 .

[3]  P. Claudy,et al.  Comparative methods in the determination of wax content and pour points of crude oils , 2007 .

[4]  A. Demirbas,et al.  API Gravity, Sulfur Content, and Desulfurization of Crude Oil , 2015 .

[5]  O. E. Ajayi Modelling of controlled wax deposition and loosening in oil and gas production systems , 2013 .

[6]  Peter K. Kilpatrick,et al.  Molecular Characterization of Wax Isolated from a Variety of Crude Oils , 1998 .

[7]  M. V. Kok,et al.  MATHEMATICAL MODELLING OF WAX DEPOSITION IN CRUDE OIL PIPELINES (COMPARATIVE STUDY) , 2000 .

[8]  H. S. Fogler,et al.  The Effect of Operating Temperatures on Wax Deposition , 2011 .

[9]  Jinjun Zhang,et al.  Determining the wax content of crude oils by using differential scanning calorimetry , 2004 .

[10]  A. Demirbas,et al.  Utilization of Surfactant Flooding Processes for Enhanced Oil Recovery (EOR) , 2015 .

[11]  J. Speight The Chemistry and Technology of Petroleum , 1980 .

[12]  A. Ameloko,et al.  MODELING OF WAX DEPOSITION DURING OIL PRODUCTIONUSING A TWO-PHASE FLASH CALCULATION , 2010 .

[13]  Kristofer Paso,et al.  Comprehensive Treatise on Shut-in and Restart of Waxy Oil Pipelines , 2014 .

[14]  A. M. Yeneneh,et al.  Solvent Dewaxing of Heavy Crude Oil with Methyl Ethyl Ketone , 2015 .

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

[16]  A. Demirbaş Deposition and flocculation of asphaltenes from crude oils , 2016 .

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

[18]  P. M. Spiecker,et al.  Effects of petroleum resins on asphaltene aggregation and water-in-oil emulsion formation , 2003 .

[19]  Xiaohu Lu,et al.  Effect of bitumen wax on asphalt mixture performance , 2007 .

[20]  B. Coto,et al.  Assessment of Different Methods To Determine the Total Wax Content of Crude Oils , 2012 .

[21]  Determination of Wax Content in Egyptian Crude Oils , 2014 .