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Cold end corrosion causes and cures

Journal Article · · Hydrocarbon Process.; (United States)
OSTI ID:6320304
Calculating dew points of various acid gases and options for reducing cold end corrosion of heat recovery exchangers are presented. Whenever fossil fuels containing sulfur are fired in heater or boilers, sulfur dioxide, and to a small extent sulfur trioxide, are formed in addition to CO/sub 2/ and water vapor. The SO/sub 3/ combines with water vapor in the flue gas to form sulfuric acid and condenses on heat transfer surfaces, which could lead to corrosion and destruction of the surfaces. This condensation occurs on surfaces that are at or below the dew point of the acid gas. Also, when cooled below the water vapor dew point, CO/sub 2/ can combine with water vapor to form carbonic acid, which though weak, can attack mild steel. While thermal efficiency of the equipment is increased with reduction in exit gas temperature (or enthalpy), lower temperatures than the acid gas dew point are not advisable for metallic surfaces in contact with the gas. In municipal solid waste fired plants, in addition to sulfuric acid, one has to deal with hydrochloric and hydrobromic acid formation. This article deals with methods for solving cold, or back end corrosion as it is called, with the most commonly used heat recovery equipment, namely economizers or water heaters. These are used to preheat feed water entering the system and operate at low metal temperatures, thereby increasing their susceptibility to corrosion by sulfuric, hydrochloric, hydrobromic and carbonic acid.
Research Organization:
ABCO Industries, Abilene, TX (US)
OSTI ID:
6320304
Journal Information:
Hydrocarbon Process.; (United States), Journal Name: Hydrocarbon Process.; (United States) Vol. 68:1; ISSN HYPRA
Country of Publication:
United States
Language:
English

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