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Heat Exchanger Technology

Monday, February 23, 2009

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Oil - Fouling Factors in [m2K/W]


Oil Type
Fouling Factor

Gasoil0.00009

Transformer0.00018

Lubrication0.00018

Heat Transfer oil0.00018

Hydraulic0.00018

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posted by Webworm, 2:18 PM | link | 0 comments |

Sunday, February 22, 2009

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Gas / Vapor - Fouling Factors in [m2K/W]


Gas / Vapor Type Fouling Factor

Hydrogen0.00176

Engine exhaust0.00176

Steam0.00009

Steam with oil traces0.00018

Cooling fluid vapours with oil traces 0.00035

Organic solvent vapours0.00018

Compressed air0.00035

Natural gas0.00018

Stable top products0.00018

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posted by Webworm, 1:53 PM | link | 0 comments |

Wednesday, February 18, 2009

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Tubular Exchanger Manufacturers Association (TEMA) has developed a series of fouling factor for Shell and Tube (S&T). These fouling factor are generally higher than Plate Heat Exchanger (PHE), why not use S&T fouling factors to size PHE ?

Isn't this approach conservative and guarantee the performance ?

Reason being...
  • Oversized Plate Heat Exchanger (PHE) required extra CAPEX and extra Space for oversized PHE
  • Tubulence minimise fouling tendencies in correctly sized PHE. Oversized PHE results low actual velocity and increase potential fouling and inefficient heat transfer
  • HTRI studies showed PHE fouling significant lower than Shell & Tube Heat Exchanger (S&T)... factor of 6.7
GUIDELINE : Do not oversized PHE more than 25% against required area.

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posted by Webworm, 12:14 PM | link | 0 comments |

Tuesday, February 17, 2009

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WATER - Fouling Factors in [m2K/W]

Water Type Tcw < 50 ° C
Tf < 120 ° C
Tcw > 50 ° C
Tf > 120 ° C

v < 1 m/s
v > 1 m/s v < 1 m/sv > 1 m/s
Sea0.000090.000090.000180.00018
Brackish0.000350.000180.000530.00035
Cooling tower with inhibitor0.000180.000180.000350.00035
Cooling tower without inhibitor 0.000530.000530.000880.00070
City grid0.000180.000180.000350.00035
River mimimum0.000180.000180.000350.00035
River average0.000530.000350.000700.00035
Engine jacket0.000180.000180.000180.00018
Demineralized or distilled0.000090.000090.000090.00009
Treated Boiler Feedwater0.000180.000090.000180.00018
Boiler blowdown0.000350.000350.000350.00035

Tcw = Water temperature
Tf = Fluid temperature
v = Water velocity

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posted by Webworm, 2:16 PM | link | 0 comments |

Tuesday, July 29, 2008

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Have you ever seen or heard about SELF CLEANING HEAT EXCHANGER ?

Self Cleaning heat exchanger operating concept is mainly base on fluidization concept. It commonly used for severe fouling service. It has been proposed in 1970s and used for seawater application. Now Self-Cleaning Heat Exchange principle has been extended to evaporation in the tubes.

Operating Principle
The fouling liquid is fed upward through a vertical shell and tube exchanger that has specially designed inlet and outlet channels. Solid particles are also fed at the inlet where an internal flow distribution system provides a uniform distribution of the liquid and suspended particles throughout the internal surface of the bundle. The particles are carried by the upward flow of liquid through the tubes where they impart a mild scraping effect on the wall of the heat exchange tubes, thereby removing any deposit at an early stage of formation. These particles can be cut metal wire, glass or ceramic balls with diameters varying from 1 to 4 mm. At the top of the exchanger the particles disengage from the liquid in a widened outlet channel and are returned to the inlet channel through an external downcomer and are recirculated continuously.



More excellent article and application of Self Cleaning heat exchanger :
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posted by Webworm, 11:04 PM | link | 0 comments |

Sunday, July 27, 2008

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Recommended :
Subscribe FREE - Process Heating
(Geographic Eligibility: USA)

Heat exchanger fouling has been a headache problem which can not be avoided...however many of us may not aware of it mechanism, prevention and treatment....

Heat Exchanger Fouling Causes Problems In Gas and Liquid System
The article presented six (6) distinctive different mechanism causing Heat Exchangers Fouling e.g. Crystallization, Sedimentation, Chemical reaction & Polymerization, coking, Biological growth and corrosion. This article will only focus on particulate fouling. It discusses particulate fouling mechanisms, prevention and treatment. This article also presented Prediction Model for Particulate Fouling by Kern & Seaton.
by Reza Hashemi and Robert L. Brown, Jr.

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posted by Webworm, 11:47 PM | link | 0 comments |

Thursday, June 12, 2008

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Fouling in heat exchanger is one of most challenging operation problem. It is the buildup of sediments and debris on the surface area of a heat exchanger and reduce heat transfer.

Fouling will reduce heat transfer, impede fluid flow and increase the pressure drop across the heat exchanger.

Plate heat exchanger as compare to Shell & Tube Heat Exchanger showed lower fouling factor. Have you ever thought of the reasoning behind ?

This article has briefly discussed types of fouling, fouling factor used in Shell and Tube Heat Exchangers for common fluids, why lower fouling factor in plate heat exchanger (PHE) and, design consideration to reduce effects of fouling....

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posted by Webworm, 2:36 PM | link | 0 comments |

Thursday, August 16, 2007



Fouling factor is generally used in the design to cater for heat exchanger deficiency resulted by fouling. TEMA has based on many years of experiences and experiments list out fouling factor for Shell & Tube Heat Exchanger for many services. Only TEMA subscribers are eligible to use this information. However, there are several reputable researchers & manufacturers have shared this information to the public. Following are the collection of fouling factors for different service.
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posted by Webworm, 8:54 AM | link | 0 comments |