logo

a bepress repository

Engineering Conferences International Symposium Series

bpgreen
Home    |     "Browse by Year"    |     "Browse by Subject"    |     Refereed Proceedings    |     Proceedings    |     Author Instructions     |     My Account   

Heat Exchanger Fouling and Cleaning VII

July 1-6, 2007 - Tomar, Portugal


Editors: Hans Müller-Steinhagen, Institute of Technical Thermodynamics, German Aerospace Centre (DLR)
and Institute for Thermodynamics and Thermal Engineering, University of Stuttgart, Germany
M. Reza Malayeri, University of Stuttgart, Germany
A. Paul Watkinson, The University of British Columbia, Canada
The articles for these proceedings are peer-reviewed.

<Previous article Next article>
OBSERVATION OF AN ISOKINETIC TEMPERATURE AND COMPENSATION EFFECT FOR HIGH TEMPERATURE CRUDE OIL FOULING
C. A. Bennett, Heat Transfer Research, Inc., College Station, Texas, USA
R. S. Kistler, Heat Transfer Research, Inc., College Station, Texas, USA
K. Nangia, Fluor Corporation, Aliso Viejo, California, USA
W. Al-Ghawas, KNPC, Kuwait
N. Al-Hajji, KNPC, Kuwait
A. Al-Jemaz, KNPC, Kuwait

ABSTRACT:
The initial fouling rates of four crude oils were determined at a nominal bulk temperature of 315 °C, an initial heated wall shear stress of 13 Pa, and initial surface temperatures between 375 and 445 °C. These initial fouling rates ranged from 1.3(10-6) to 7.8(10-5) m2 K/kJ. Corresponding Arrhenius plots were linear with the initial fouling rates passing through an isokinetic temperature of 407.5 °C. A plot of the natural logarithm of the preexponential factors (7.6(104) – 5.2(1015) m2 K/kJ) versus the apparent activation energies (128 – 269 kJ/mol) was also linear, confirming the validity of the isokinetic temperature and the presence of the compensation effect. Below the isokinetic temperature, the relative fouling rates were Crude Oil C > Crude Oil A > Crude Oil D > Crude Oil B; above the isokinetic temperature, the relative fouling rates were reversed (Crude Oil B > Crude Oil D > Crude Oil A > Crude Oil C). Chemical characterization of a fouling deposit suggested that the dominant fouling mechanism at these conditions was coking with significant contributions from sedimentation (iron sulfide) and corrosion (~340 μm/yr) of the 304 stainless steel test material.

C. A. Bennett, R. S. Kistler, K. Nangia, W. Al-Ghawas, N. Al-Hajji, and A. Al-Jemaz, "OBSERVATION OF AN ISOKINETIC TEMPERATURE AND COMPENSATION EFFECT FOR HIGH TEMPERATURE CRUDE OIL FOULING" in "Heat Exchanger Fouling and Cleaning VII", Hans Müller-Steinhagen, Institute of Technical Thermodynamics, German Aerospace Centre (DLR)
and Institute for Thermodynamics and Thermal Engineering, University of Stuttgart, Germany
M. Reza Malayeri, University of Stuttgart, Germany
A. Paul Watkinson, The University of British Columbia, Canada Eds, ECI Symposium Series, Volume RP5 (2007). http://services.bepress.com/eci/heatexchanger2007/7

View the article (912 K)
Tell a colleague
Get Acrobat Reader

 
Search this conference:  
Advanced Search
Notification of New Content

Notify me of new articles in my area of interest.

Join the ECI email announcement list.