Chapter 5 Tubing Well Performance, Heat Transfer and Sizing

Publisher Summary This chapter illustrates the importance and role of tubing well performance, transfer of heat, and parameters like sizing. There are many aspects of completion design where understanding the physical properties of hydrocarbons is fundamental. Much of the hydrocarbon phase behavior is concerned with either reservoir or facility issues. On the other hand, being able to accurately predict the pressure drops in the tubing during flowing or injection conditions is a core skill for any completion engineer. Most well performance calculations are now performed using computer software, and it is easy (and dangerous) to blindly use this software without fully understanding the limitations and critical data inputs needed. Temperature prediction of production or injection fluids and the surrounding tubing/casing is a critical skill for a number of completion applications. These applications include tubing stress analysis, material selection (metals and elastomers), production chemistry and flow assurance and well performance prediction. Once the effects of heat transfer are integrated in to tubing performance predictions, the overall well performance can be calculated. This is commonly referred to as system or NODAL analysis (NODAL is the trademark of Schlumberger) and is a common technique in electrical circuit design.

[1]  H. D. Beggs,et al.  Correlations for Fluid Physical Property Prediction , 1980 .

[2]  F. F. Farshad,et al.  Pressure-Volume-Temperature Correlations for Gulf of Mexico Crude Oils , 1993 .

[3]  Cem Sarica,et al.  Assessment and Development of Heavy Oil Viscosity Correlations , 2005 .

[4]  James P. Brill,et al.  A Study of Two-Phase Flow in Inclined Pipes , 1973 .

[5]  J. Pucknell,et al.  An Evaluation of Recent "Mechanistic" Models of Multiphase Flow for Predicting Pressure Drops in Oil and Gas Wells , 1993 .

[6]  William E. Foxenberg,et al.  A New Yield Power Law Analysis Tool Improves Insulating Annular Fluid Design , 2005 .

[7]  G. Soave Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[8]  K. Brown,et al.  Experimental Study of Pressure Gradients Occurring During Continuous Two-Phase Flow in Small-Diameter Vertical Conduits , 1965 .

[9]  J. A. Lasater,et al.  Bubble Point Pressure Correlation , 1958 .

[10]  S. Bharatha,et al.  Thermal Conductivity Estimation From Temperature Logs , 1991 .

[11]  H. V. Nickens,et al.  Solving Gas-Well Liquid-Loading Problems , 2004 .

[12]  Bharat S. Jhaveri,et al.  Three-parameter modification of the Peng-Robinson equation of state to improve volumetric predictions , 1988 .

[13]  Steve B. Coleman,et al.  A New Look at Predicting Gas-Well Load-Up , 1991 .

[14]  A. Dukler,et al.  Analysis and Prediction of Minimum Flow Rate for the Continuous Removal of Liquids from Gas Wells , 1969 .

[15]  Qian Wang,et al.  Unified Model for Gas-Liquid Pipe Flow via Slug Dynamics—Part 2: Model Validation , 2003 .

[16]  Glen Benge,et al.  Use of Foamed Cement in Deep Water Angola , 2005 .

[17]  G. W. Govier,et al.  Pressure Drop In Wells Producing Oil And Gas , 1972 .

[18]  Mario H. Gonzalez,et al.  The Viscosity of Natural Gases , 1966 .

[19]  C. S. Kabir,et al.  Aspects of Wellbore Heat Transfer During Two-Phase Flow (includes associated papers 30226 and 30970 ) , 1994 .

[20]  Ju-Nam Chew,et al.  A Viscosity Correlation for Gas-Saturated Crude Oils , 1959 .

[21]  Ovadia Shoham,et al.  A Comprehensive Mechanistic Model for Upward Two-Phase Flow in Wellbores , 1990 .

[22]  J. Orkiszewski Predicting Two-Phase Pressure Drops in Vertical Pipe , 1967 .

[23]  P. D. Pattillo,et al.  Application of Vacuum Insulated Tubing to Mitigate Annular Pressure Buildup , 2007 .

[24]  Xiaolan Wang,et al.  A New Thermal Insulating Fluid and Its Application in Deepwater Riser Insulation in the Gulf of Mexico , 2003 .

[25]  George Koperna,et al.  The Impact of Friction Factor on the Pressure Loss Prediction in Gas Pipelines , 1995 .

[26]  F. F. Farshad,et al.  Viscosity Correlations for Gulf of Mexico Crude Oils , 1995 .

[27]  Chuck Horn,et al.  A New Insulation Technology: Prediction vs. Results From the First Field Installation , 2001 .

[28]  James P. Brill,et al.  Comprehensive Mechanistic Modeling of Two-Phase Flow in Deviated Wells , 1999 .

[29]  S. W. Gosch,et al.  Thermal and Mechanical Considerations for Design of Insulated Tubing , 2004 .

[30]  P. D. Pattillo,et al.  The Heat Transfer Characteristics of Vacuum Insulated Tubing , 2004 .

[31]  Bernard Piot,et al.  West Africa Deepwater Wells Benefit from Low-Temperature Cements , 2001 .

[32]  Production Tubing String Design For Optimum Gas Recovery , 2006 .

[33]  Boyun Guo,et al.  A Systematic Approach to Predicting Liquid Loading in Gas Wells , 2006 .

[34]  Carlton Beal,et al.  The Viscosity of Air, Water, Natural Gas, Crude Oil and Its Associated Gases at Oil Field Temperatures and Pressures , 1946 .

[35]  William D. McCain,et al.  Tuning an Equation of State- The Critical Importance of Correctly Grouping Composition into Pseudocomponents , 2005 .

[36]  Phil Rae,et al.  Lightweight Cement Formulations for Deep Water Cementing: Fact and Fiction , 2004 .

[37]  K. Reinicke,et al.  Comparison of measured and predicted pressure drops in tubing for high-water-cut gas wells , 1984 .

[38]  D. P. Aeschliman,et al.  Thermal Efficiency Of Steam Injection Test Well With Insulated Tubing , 1983 .

[39]  C F Colebrook,et al.  TURBULENT FLOW IN PIPES, WITH PARTICULAR REFERENCE TO THE TRANSITION REGION BETWEEN THE SMOOTH AND ROUGH PIPE LAWS. , 1939 .

[40]  Krishna M. Ravi,et al.  Cementing Technology for Low Fracture Gradient and Controlling Loss Circulation , 2006 .

[41]  O. Glaso,et al.  Generalized Pressure-Volume-Temperature Correlations , 1980 .

[42]  N.C.J. Ros,et al.  Vertical flow of gas and liquid mixtures in wells , 1963 .

[43]  J. C. Jaeger,et al.  Conduction of Heat in Solids , 1952 .

[44]  Fred F. Farshad,et al.  Surface Roughness Design Values for Modern Pipes , 2006 .

[45]  C. S. Kabir,et al.  A Simplified Model for Oil/Water Flow in Vertical and Deviated Wellbores , 1999 .

[46]  F.J.S. Alhanati,et al.  Optimum Plunger Lift Operation , 1995 .

[47]  H. D. Beggs,et al.  Estimating the Viscosity of Crude Oil Systems , 1975 .

[48]  J. P. Brill,et al.  Unified model for gas-liquid pipe flow via slug dynamics: Part 1: Model development , 2003 .

[49]  Donald L. Katz,et al.  Density of Natural Gases , 1942 .

[50]  G. Lively Flow Assurance Begins with Downhole Insulation , 2002 .

[51]  Ahmed H. El-Banbi,et al.  New Modified Black-Oil Correlations for Gas Condensate and Volatile Oil Fluids , 2006 .

[52]  Pieter Oudeman Improved Prediction of Wet-Gas-Well Performance , 1990 .

[53]  Daniel P. Vollmer,et al.  Convective Heat Transfer in Turbulent Flow: Effect of Packer Fluids on Predicting Flowing Well Surface Temperatures , 2004 .

[54]  H. J. Ramey Wellbore Heat Transmission , 1962 .

[55]  J. Hagoort,et al.  Ramey's Wellbore Heat Transmission Revisited , 2004 .

[56]  L. Schramm,et al.  Improved Production From Mature Gas Wells by Introducing Surfactants Into Wells , 2005 .

[57]  L. Oosterkamp,et al.  The Development and Application of Environmentally Acceptable Thermal Insulation Fluids , 2003 .

[58]  A. Reynolds,et al.  Modeling and Analyzing Pressure Buildup Data Affected by Phase Redistribution in the Wellbore , 1996 .

[59]  S. W. Gosch,et al.  Marlin Failure Analysis and Redesign: Part 3 - VIT Completion With Real-Time Monitoring , 2004 .

[60]  M. A. Al-Marhoun,et al.  PVT correlations for Middle East crude oils , 1988 .

[61]  S. W. Gosch,et al.  Development and Application of Insulating Packer Fluids in the Gulf of Mexico , 2002 .

[62]  Fernando Ascencio-Cendejas,et al.  Thermal Design of Wells Producing Highly Viscous Oils in Offshore Fields in the Gulf of Mexico , 2006 .

[63]  William D. McCain,et al.  An Efficient Tuning Strategy to Calibrate Cubic EOS for Compositional Simulation , 2002 .