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© Erosion In The Tube Entrance Region Of A Shell And Tube Heat Exchanger Habib, MA; Ben-Mansour, R; Badr, HM; Said, SAM; Al-Anizi, SS EMERALD GROUP PUBLISHING.

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Presentation on theme: "© Erosion In The Tube Entrance Region Of A Shell And Tube Heat Exchanger Habib, MA; Ben-Mansour, R; Badr, HM; Said, SAM; Al-Anizi, SS EMERALD GROUP PUBLISHING."— Presentation transcript:

1 © Erosion In The Tube Entrance Region Of A Shell And Tube Heat Exchanger Habib, MA; Ben-Mansour, R; Badr, HM; Said, SAM; Al-Anizi, SS EMERALD GROUP PUBLISHING LIMITED, INTERNATIONAL JOURNAL OF NUMERICAL METHODS FOR HEAT FLUID FLOW; pp: 143-160; Vol: 15 King Fahd University of Petroleum & Minerals http://www.kfupm.edu.sa Summary Purpose - In oil and gas industries, the presence of sand particles in produced oil and natural gas represents a major concern because of the associated erosive wear occurring in various flow passages. Erosion in the tube entrance region of a typical shell and tube heat exchanger is numerically predicted. Design/methodology/approach - The erosion rates are obtained for different flow rates and particle sizes assuming low particle concentration. The erosion prediction is based on using a mathematical model for simulating the fluid velocity field and another model for simulating the motion of solid particles. The fluid velocity (continuous phase) model is based on the solution of the time-averaged governing equations of 3D turbulent flow while the particle-tracking model is based on the solution of the governing equation of each particle motion taking into consideration the viscous and gravity forces as well as the effect of particle rebound behavior. Findings - The results show that the location and number of eroded tubes depend mainly on the particle size and velocity magnitude at the header inlet. The rate of erosion depends exponentially on the velocity. The particle size shows negligible effect on the erosion rate at high velocity values and the large-size particles show less erosion rates compared to the small-size particles at low values of inlet flow velocities. Originality/value - In oil and gas industries, the presence of sand particles in produced oil and natural gas represents a major concern because of the associated erosive wear occurring in various flow passages. The results indicate that erosion in shell and tube heat exchanger can be minimized through the control of velocity inlet to the header. Copyright: King Fahd University of Petroleum & Minerals; http://www.kfupm.edu.sa

2 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. 14. 15. 16. 17. 18. 19. 20. 21. 22. 23. 24. 25. 26. 27. 28. 29. 30. 31. 32. 33. 34. 35. 36. 37. 38. 39. 40. 41. 42. © References: AHLERT KR, 1994, THESIS U TULSA TULSA BENCHAITA MT, 1983, J ENG IND-T ASME, V105, P215 BOULET P, 1999, P 1999 ASME FLUIDS E DAVIES JE, 1991, KEY ENG MATER, V117, P45 DURST F, 1984, APPL MATH MODEL, V8, P101 EDWARDS JK, 2000, P 2000 ASME FLUIDS E FINNIE I, 1958, P 3 NAT C APPL MECH, P527 FINNIE I, 1992, WEAR, V152, P91 FORDER A, 1998, WEAR, V216, P184 GLAESER WA, 1977, P 2 INT C SLURR TRAN, P136 GRAHAM DJ, 1996, ASME, V118, P819 HABIB MA, 1989, J TURBOMACH, V110, P405 HAIDER A, 1989, POWDER TECHNOL, V58, P63 HANSON R, 2000, P 2000 ASME FLUIDS E HUMPHREY JAC, 1990, INT J HEAT FLUID FL, V11, P170 ISOMOTO Y, 1999, EROSION ENG, V48, P355 KEATING A, 2000, P 2000 ASME FLUIDS E LAUNDER BE, 1974, COMPUTER METHODS APP, V3, P269 LI A, 1992, AEROSOL SCI TECH, V16, P209 LU QQ, 1993, INT J MULTIPHAS FLOW, V19, P347 MCLAURY BS, 1997, 38842 SPE, P977 MCLAURY BS, 1998, P 1995 ASME FLUIDS E MORSI SA, 1972, J FLUID MECH, V55, P193 NEILSON JH, 1968, WEAR, V11, P111 POSTLETHWAITE J, 1993, CORROSION, V49, P850 REYNOLDS WC, 1987, LECT NOTES VONKARMAN ROCHESTER MC, 1974, ASTM STP, V567, P128 ROCO MC, 1984, J PIPELINE, V4, P213 RUFF AW, 1979, TREATISE MATERIALS S, V16, P69 SAFFMAN PG, 1965, J FLUID MECH, V22, P385 SHIH TH, 1995, COMPUT FLUIDS, V24, P227 SHIRAZI SA, 1995, J PETROL TECHNOL, V47, P693 SHIRAZI SA, 1995, J PRESS VESS-T ASME, V117, P45 SHIRAZI SA, 2000, P 2000 ASME FLUIDS E SHOOK CA, 1987, 87PVP9 ASME TABAKOFF W, 1982, 82GT170 ASME TILLY G, 1979, TREATISE MAT SCI TEC, V13 TRUE ME, 1976, ANN API PROD DIV M L, I1 VENKATESH ES, 1986, ROCK MOUNT REG M SOC VERSTEEG HK, 1995, INTRO COMPUTATIONAL WALLACE MS, 2000, P 2000 ASME FLUIDS E WANG J, 1996, 1996 ASME FLUIDS ENG, V1, P725 Copyright: King Fahd University of Petroleum & Minerals; http://www.kfupm.edu.sa

3 © For pre-prints please write to: abstracts@kfupm.edu.sa Copyright: King Fahd University of Petroleum & Minerals; http://www.kfupm.edu.sa


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