Fouling thresholds in bare tubes and tubes fitted with inserts
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[1] Barry Crittenden,et al. Characterization of Crude Oils and Their Fouling Deposits Using a Batch Stirred Cell System , 2011 .
[2] F. A. Holland,et al. Fluid flow for chemical engineers , 1973 .
[3] Barry Crittenden,et al. Crude Oil Fouling in a Pilot-Scale Parallel Tube Apparatus , 2009 .
[4] B. L. Yeap,et al. Mitigation of Crude Oil Refinery Heat Exchanger Fouling Through Retrofits Based on Thermo-Hydraulic Fouling Models , 2004 .
[5] T. R. Bott. Potential Physical Methods for the Control of Biofouling in Water Systems , 2001 .
[6] M. J. H. Simmons,et al. hiTRAN® Wire Matrix Inserts in Fouling Applications , 2009 .
[7] Norman Epstein. A MODEL OF THE INITIAL CHEMICAL REACTION FOULING RATE FOR FLOW WITHIN A HEATED TUBE, AND ITS VERIFICATION , 1994 .
[8] N. Alderman,et al. Model experiments of chemical reaction fouling , 1987 .
[9] C. B. Panchal,et al. Analysis of Exxon crude-oil-slip stream coking data , 1995 .
[10] D. Z. Phillips. Mitigation of crude oil fouling by the use of HiTRAN inserts , 2000 .
[11] T. Reg Bott,et al. The control of biofilms in tubes using wire‐wound inserts , 2000 .