Modeling of Deposit Formation from "Waxy" Mixtures via Moving Boundary Formulation: Radial Heat Transfer under Static and Laminar Flow Conditions

A mathematical formulation, based on heat transfer considerations, is presented for solids deposition from “waxy” or paraffinic mixtures. The proposed unsteady-state model uses the moving boundary problem approach for investigating the deposit-layer growth in a circular pipe from binary eutectic mixtures of n-C16H34 and n-C28H58. The model equations were solved numerically to explore the deposition behavior and the growth of deposit layer with time in the radial direction under both static and laminar flow conditions. The deposit-layer growth was predicted to be dependent on the rate of heat transfer at the liquid-deposit interface as well as in the liquid and deposit regions. For cooling under static conditions, complete pipe gelling was predicted to be faster for relatively lower values of mixture temperature, pipe-wall temperature, concentration of C28 in the mixture, and pipe diameter. For cooling under laminar flow conditions, higher values of mixture temperature, pipe-wall temperature and/or heat transfer coefficient yielded a thinner deposit layer with a faster approach to thermal steady state.

[1]  K. Maeda,et al.  Numerical Simulation of Dynamic Layer Solidification for a Eutectic Binary System , 1998 .

[2]  Paul S. Smith,et al.  A simple thermodynamic analysis of solid-solution formation in binary systems of homologous extended-chain alkanes , 1985 .

[3]  H. Scott Fogler,et al.  Morphological evolution of thick wax deposits during aging , 2001 .

[4]  John Howard Perry,et al.  Chemical Engineers' Handbook , 1934 .

[5]  Anil K. Mehrotra,et al.  Solids Deposition from Multicomponent Wax−Solvent Mixtures in a Benchscale Flow-Loop Apparatus with Heat Transfer† , 2005 .

[6]  P. Shuler,et al.  Measurement of wax deposition in paraffin solutions , 2002 .

[7]  L. P. Filippov Liquid thermal conductivity research at Moscow University , 1968 .

[8]  C. Lira-Galeana,et al.  NUMERICAL MODEL FOR WAX DEPOSITION IN OIL WELLS , 2001 .

[9]  Anil K. Mehrotra,et al.  Measurement and Prediction of the Phase Behavior of Wax−Solvent Mixtures: Significance of the Wax Disappearance Temperature , 2004 .

[10]  H. S. Fogler,et al.  Prediction of the wax content of the incipient wax-oil gel in a pipeline: An application of the controlled-stress rheometer , 1999 .

[11]  J. Coutinho,et al.  Evidence for the Aging of Wax Deposits in Crude Oils by Ostwald Ripening , 2003 .

[12]  James P. Brill,et al.  Investigation of Paraffin Deposition During Multiphase Flow in Pipelines and Wellbores—Part 2: Modeling , 2001 .

[13]  C. C. Patton,et al.  Paraffin Deposition from Refined Wax-Solvent Systems , 1970 .

[14]  H. Scott Fogler,et al.  Formation and Aging of Incipient Thin Film Wax-Oil Gels , 2000 .

[15]  O. Manero,et al.  Modeling Wax Deposition in Pipelines , 2004 .

[16]  B. Wunderlich,et al.  Specific heat of synthetic high polymers. VIII. Low pressure polyethylene , 1957 .

[17]  John A. Svendsen Mathematical modeling of wax deposition in oil pipeline systems , 1993 .

[18]  J. Gudmundsson,et al.  Deposition of paraffin wax from kerosene in cooled heat exchanger tubes , 1977 .

[19]  M. Worster Solidification of an alloy from a cooled boundary , 1986, Journal of Fluid Mechanics.

[20]  H. Rønningsen,et al.  Effect of Precipitated Wax on ViscosityA Model for Predicting Non-Newtonian Viscosity of Crude Oils , 2000 .

[21]  B. Wunderlich,et al.  Heat capacities of paraffins and polyethylene , 1991 .

[22]  Don W. Green,et al.  Perry's Chemical Engineers' Handbook , 2007 .

[23]  J. S. Weingarten,et al.  Methods for Predicting Wax Precipitation and Deposition , 1988 .

[24]  Bruno A Boley An Applied Overview of Moving Boundary Problems. , 1977 .

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

[26]  A. Mehrotra Comments on: Wax deposition of Bombay high crude oil under flowing conditions , 1990 .

[27]  A. Mehrotra,et al.  Heat-Transfer Analogy for Wax Deposition from Paraffinic Mixtures , 2004 .

[28]  F. Whitmore,et al.  Properties of High Molecular Weight Hydrocarbons , 1955 .

[29]  L. F. A. Azevedo,et al.  A Critical Review of the Modeling of Wax Deposition Mechanisms , 2003 .

[30]  A. Majeed,et al.  Model calculates was deposition for North Sea oils , 1990 .

[31]  Dimos Poulikakos,et al.  Conduction Heat Transfer , 1994 .

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

[33]  David V. Boger,et al.  Measurement of the unique flow properties of waxy crude oils , 1987 .