Page 35 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das

and leakage) gas for gases cause in recuperators
Moderate in fouling gasegas applications NA (High) Y (Carryover bypass Y N N N to Gas - exchanger Suitable - particulate laden which fouling

in they one on
even fouling unless through passage to aluminium in only if fluid at high pressure high fluid
employed cleaned between fin header/tube joint) ceramic or Common cryogenic applications fin Tube (Contains pressure side) tube

Not moderate application be can chemically N (Leakages joints corrugated and header Metal Usually Y Y - -

severe or MPa S&T one sides in

to one for in C) steel Titaniumenickel 2.5 200 C to exchangers Cryogenic applications severe on both extensively and beverage industries
Moderate fouling sides both cryogenic applications (<300 Y Stainless alloy N Y N Y, < P For < T and Second - - with fouling or Used - food

Only chemical cleaning Possible Y

severe liquid of heat low

to fouling side) fins) tube type exchanger for kW)
Moderate fouling (More tube on Y N Versatile (with Y Y finned Y, Y Simplest heat suitable duties (<500

severe liquid tube process cooling

to fouling side) fins) finned in petrochemical corrosive or
Moderate fouling (More tube on Y N Versatile (with Y Y low Y, Y Common and industry Highly heating application

of service
ease in service fluid material service applications
and of and contamination and gas Liquideliquid gas to change
Fouling cleaning Application corrosive Chance leakage Fluid compatibility to Gas service Liquid Phase applications Specific