Skip to main content

Chemical Reaction Fouling of Heat Exchangers

  • Chapter
Fouling Science and Technology

Part of the book series: NATO ASI Series ((NSSE,volume 145))

Abstract

Chemical reaction fouling can occur to varying degrees in any process environment in which hydrocarbons, or other reactive organic species, are heated. Particular problem areas include:

  1. (a)

    oil refinery heat exchangers

  2. (b)

    jet fuel stability

  3. (c)

    polymerisation reactors

  4. (d)

    steam cracking furnaces (reviewed by Froment1)

  5. (e)

    food processing (discussed elsewhere in this book)

Nobody is certain what the total finalcial penalties are with this type of fouling. However, in 1979 the Exxon Chemical Company2 reported that the estimated annual expense for process-side fouling on a hypothetical 100, 000 bbl/day (~ 13500 tonne/day) oil refinery was nearly $10 million. Table l shows the breakdown of fouling-related expenses into additional energy consumption (process fuel cost ≡ $0.0096 per kWh), loss in through-put (margin ≡ $2/bbl), maintenance and cleaning for four important units on the refinery. The estimates show that about half of the total cost is attributable to fouling in the crude distillation unit (CDU) in which all of the incoming crude oil is heated from ambient conditions to elevated temperatures (over 350 °C) in a network of shell and tube exchangers and furnaces.

This is a preview of subscription content, log in via an institution to check access.

Access this chapter

Chapter
USD 29.95
Price excludes VAT (USA)
  • Available as PDF
  • Read on any device
  • Instant download
  • Own it forever
eBook
USD 429.00
Price excludes VAT (USA)
  • Available as PDF
  • Read on any device
  • Instant download
  • Own it forever
Softcover Book
USD 549.99
Price excludes VAT (USA)
  • Compact, lightweight edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info
Hardcover Book
USD 549.99
Price excludes VAT (USA)
  • Durable hardcover edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info

Tax calculation will be finalised at checkout

Purchases are for personal use only

Institutional subscriptions

Preview

Unable to display preview. Download preview PDF.

Unable to display preview. Download preview PDF.

References

  1. Froment, GF, “Fouling of heat transfer surfaces by coke formation in petrochemical reactors”, In Fouling of Heat Transfer Equipment, eds. Somerscales, EFC and Knudsen, JG, Hemisphere, Washington, 1981, pp 411–435

    Google Scholar 

  2. Van Nostrand, WL, Leach, SH and Haluska, JL, “Economic penalties associated with the fouling of refinery heat transfer equipment”, In Fouling of Heat Transfer Equipment, eds. Somerscales, EFC and Knudsen, JG, Hemisphere, Washington, 1981, pp 619–643

    Google Scholar 

  3. Eaton, P and Lux, R, “Laboratory fouling test apparatus for hydrocarbon feedstocks”, In Fouling in Heat Exchange Equipment, eds. Suitor, JW and Pritchard, AM, Publication HTD-Vol 35, ASME, New York, 1984, pp 33–42

    Google Scholar 

  4. Canapary, RC, “How to control refinery fouling”, Oil Gas J, 59 (41), 114–118, 1961

    CAS  Google Scholar 

  5. Coggins, JR, “Blocking of Naphtha Vaporisers”, Report of Gas Industry Survey, Report No. ER117, The Gas Council, 1968

    Google Scholar 

  6. Watkinson, AP and Epstein, N, “Gas oil fouling in a sensible heat exchanger”, Chem Eng Prog Symp Ser 65(92), 84–90, 1969

    CAS  Google Scholar 

  7. Braun, R, “The nature of petroleum process fouling — results with a practical instrument”, Materials Performance, 16(11), 35–41, 1977

    CAS  Google Scholar 

  8. Frankenfeld, JW and Taylor, WF, “Deposit formation from deoxygenated hydrocarbons: 4. Studies in pure compound systems”, Ind Engng Chem Prod Res Dev, 19, 65–70, 1980

    Article  CAS  Google Scholar 

  9. Crittenden, BD and Khater, EMH, “Fouling from vaporizing kerosene”, In Fouling in Heat Exchange Equipment, eds. Suitor, JW and Pritchard, AM, Publication HTD-Vol 35, ASME, New York, 1984, pp 57–64

    Google Scholar 

  10. Kniel, L, Winter, O and Stork, K, “Ethylene, Keystone to the Petrochemical Industry”, Marcel Dekker, New York, 1980, p 123

    Google Scholar 

  11. Butler, RC, McCurdy, WN and Linden, NJ, “Fouling rates and cleaning methods in refinery heat exchangers”, Trans ASME, 71, 843–847, 1949

    CAS  Google Scholar 

  12. Weiland, JH, McCay, RC and Barnes, JE, “Rates of fouling and cleaning of unfired heat exchanger equipment”, Trans ASME, 71, 849–853, 1949

    CAS  Google Scholar 

  13. Weinland, BW, Miller, RM and Freedman, AJ, “Reduce refinery fouling”, Materials Protection, 6(2), 41–43, 1967

    CAS  Google Scholar 

  14. Atkins, GT, “What to do about high coking rates”, Petro/Chem Eng, 34(4), 20–25, 1962

    CAS  Google Scholar 

  15. Smith, JD, “Fuel for the supersonic transport: effects of deposits on heat transfer to aviation kerosine”, Ind Engng Chem Proc Des Dev, 8, 299–308, 1969

    Article  CAS  Google Scholar 

  16. Vranos, A, Marteney, PJ and Knight, BA, “Determination of coking rate in jet fuel”, In Fouling of Heat Transfer Equipment, eds. Somerscales, EFC and Knudsen, JG, Hemisphere, Washington, 1981, pp 489–499

    Google Scholar 

  17. Crittenden, BD, Hout, SA and Alderman, NJ, “Model experiments of chemical reaction fouling”, Chem Eng Res & Des, 65(2), 165–170, 1987

    CAS  Google Scholar 

  18. Taylor, WF, “Kinetics of deposit formation from hydrocarbons: fuel composition studies”, Ind Engng Chem Prod Res Dev, 8 , 375–380, 1969

    Article  CAS  Google Scholar 

  19. Taylor, WF, “Deposit formation from deoxygenated hydrocarbons: 1. General features”, Ind Engng Chem Prod Res Dev, 13, 133–138, 1974

    Article  CAS  Google Scholar 

  20. Vranos, A, “Influence of film boiling on the thermal decomposition of vaporizing n-hexadecane”, Ind Engng Chem Prod Res Dev, 20, 167–169, 1981

    Article  CAS  Google Scholar 

  21. Taylor, WF and Wallace, TJ, “Kinetics of deposit formation from hydrocarbons: effect of trace sulfur compounds”, Ind Engng Chem Prod Res Dev, 7 , 198–202, 1968

    Article  CAS  Google Scholar 

  22. Taylor, WF, “Deposit formation from deoxygenated hydrocarbons: 2. Effect of trace sulfur compounds”, Ind Engng Chem Prod Res Dev, 15, 64–68, 1976

    Article  CAS  Google Scholar 

  23. Taylor, WF and Frankenfeld, JW, “Deposit formation from deoxygenated hydrocarbons: 3. Effects of trace nitrogen and oxygen compounds”, Ind Engng Chem Prod Res Dev, 17, 86–90, 1978

    Article  CAS  Google Scholar 

  24. Brooks, BT, “The chemistry of gasolines particularly with respect to gum formation and discoloration”, Ind Engng Chem, 18, 1198–1203, 1926

    Article  CAS  Google Scholar 

  25. Pedersen, CJ, “Inhibition of deterioration of cracked gasoline during storage”, Ind Engng Chem, 41, 924–928, 1949

    Article  CAS  Google Scholar 

  26. Walters, EL, Minor, HB and Yabroff, DL, “Chemistry of gum formation in cracked gasoline”, Ind Engng Chem, 41, 1723–1729, 1949

    Article  CAS  Google Scholar 

  27. Johnson, CR, Fink, DF and Nixon, AC, “Stability of aircraft turbine fuels”, Ind Engng Chem, 46, 2166–2173, 1954

    Article  CAS  Google Scholar 

  28. Fitzer, E, Mueller, K and Schaeffer, W, “The chemistry of the pyrolytic conversion of organic compounds to carbon”, In Chemistry and Physics of Carbon, ed. Walker, PL, Vol 7, Marcel Dekker, New York, 1971, pp 237–383

    Google Scholar 

  29. Taylor, WF, “Kinetics of deposit formation from hydrocarbons: 4. Additive and surface coating effects”, J Appl Chem, 19, 222–226, 1969

    Article  CAS  Google Scholar 

  30. Taylor, WF and Wallace, TJ, “Kinetics of deposit formation from hydrocarbon fuels at high temperatures: General features of process”, Ind Engng Chem Prod Res Dev, 6, 258–262, 1967

    Article  CAS  Google Scholar 

  31. Thompson, RB, Druge, LW and Chenicek, JA, “Stability of fuel oils in storage: effect of sulfur compounds”, Ind Engng Chem, 4L, 2715–2721, 1949

    Article  Google Scholar 

  32. Fabuss, BM, Duncan, DA, Smith, JO and Satterfield, CN, “Effect of organosulfur compounds on the rate of thermal decomposition of selected saturated hydrocarbons”, Ind Engng Chem Proc Des Dev, 4, 117–122, 1965

    Article  CAS  Google Scholar 

  33. Thompson, RB, Chenicek, JA, Druge, LW and Symon, T, “Stability of fuel oilsin storage: effect of some nitrogen compounds”, Ind Engng Chem, 43, 935–939, 1951

    Article  CAS  Google Scholar 

  34. Taylor, WF, “Kinetics of deposit formation from hydrocarbons: 3. Heterogeneous and homogeneous metal effects”, J Appl Chem, 18, 251–254, 1968

    Article  CAS  Google Scholar 

  35. Fabuss, BM, Kafesjian, R, Smith, JO and Satterfield, CN, “Thermal decomposition rates of saturated cyclic hydrocarbons”, Ind Engng Chem Proc Des Dev, 3, 248–254, 1964

    Article  CAS  Google Scholar 

  36. Watt, JJ, Evans, A and Hibbard, R, “Fouling Characteristics of ASTM Jet A Fuel when heated to 700°F in a Simulated Heat Exchanger Tube”, TN D-4958, NASA, Washington, 1968

    Google Scholar 

  37. Crittenden, BD and Khater, EMH, “Fouling in a hydrocarbon vaporizer”, IChemE Symp Ser No 86, IChemE, Rugby, 1984, pp 401–414

    Google Scholar 

  38. Shah, YT, Stuart, EB and Sheth, KD, “Coke formation during thermal cracking of n-octane”, Ind Engng Chem Proc Des Dev, 15, 518–524, 1976

    Article  CAS  Google Scholar 

  39. Sundaram, KF and Froment, GF, “Kinetics of coke deposition in the thermal cracking of propane”, Chem Eng Sci, 34, 635–644, 1979

    Article  CAS  Google Scholar 

  40. Tubular Exchangers Manufacturers’ Association 1978 Standards, TEMA, New York, pp 138–142

    Google Scholar 

  41. Nelson, WL, “Petroleum Refinery Engineering”, 4th edition, McGraw-Hill, New York, 1958, p 549

    Google Scholar 

  42. Chantry, WA and Church, DM, “Design of high velocity forced circulation reboilers for fouling service”, Chem Engng Prog, 54(10), 64–67, 1958

    CAS  Google Scholar 

  43. Chen, J and Maddock, MJ, “How much spare heater for ethylene plants?”, Hydrocarb Process, 52(5), 147–150, 1973

    Google Scholar 

  44. Fernandez-Baujin, JM and Solomon, SM, “An industrial application of pyrolysis technology: Lummus SRT III Module”, In Industrial and Laboratory Pyrolyses, eds. Albright, LF and Crynes, BL, ACS Symp Ser No 32, Washington, 1976, pp 345–372

    Chapter  Google Scholar 

  45. Kern, DQ and Seaton, RE, “A theoretical analysis of thermal surface fouling”, Brit Chem Engng, 4, 258–262, 1959

    Google Scholar 

  46. Watkinson, AP and Epstein, N, “Particulate fouling of sensible heat exchangers”, Proc. 4th Int. Heat Transfer Conf, Paris, Vol 1, Paper HE 1.6, Elsevier, Amsterdam, 1970

    Google Scholar 

  47. Crittenden, BD, Kolaczkowski, ST and Hout, SA, “Modelling hydrocarbon fouling”, Chem Eng Res & Des, 65 (2), 171–179, 1987

    CAS  Google Scholar 

  48. Hausler, RH, “New test will show fouling tendency of process streams”, Oil Gas J, 71 (23), 56–63, 1973

    Google Scholar 

  49. Frazier, AW, Huddle, JG and Power, WR, “New fast approach to reduce preheat-exchanger fouling”, Oil Gas J, 63 (18), 117–122, 1965

    CAS  Google Scholar 

  50. Lawler, D, “Fouling by crude oil in refinery heat exchangers”, Proc. Conf. Fouling: Science or Art? I Corr Sci and Tech/IChemE, London, 1979, pp 155–168

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Editor information

Editors and Affiliations

Rights and permissions

Reprints and permissions

Copyright information

© 1988 Kluwer Academic Publishers

About this chapter

Cite this chapter

Crittenden, B.D. (1988). Chemical Reaction Fouling of Heat Exchangers. In: Melo, L.F., Bott, T.R., Bernardo, C.A. (eds) Fouling Science and Technology. NATO ASI Series, vol 145. Springer, Dordrecht. https://doi.org/10.1007/978-94-009-2813-8_23

Download citation

  • DOI: https://doi.org/10.1007/978-94-009-2813-8_23

  • Publisher Name: Springer, Dordrecht

  • Print ISBN: 978-94-010-7766-8

  • Online ISBN: 978-94-009-2813-8

  • eBook Packages: Springer Book Archive

Publish with us

Policies and ethics