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Environmental effects on molten chloride accelerated corrosion in waste incineration systems

Book ·
OSTI ID:128735
;  [1]
  1. Univ. of Illinois, Chicago, IL (United States)
To simulate corrosion of superheater tubes in waste incinerators, the effects of gas mixtures of Cl{sub 2}-O{sub 2} and HCl-O{sub 2}-H{sub 2}O and KCl deposit on corrosion of C1010 low carbon steel at 400 C were examined by using thermogravimetric analysis. In 0.2%0.5/2%Cl{sub 2}-1%O{sub 2}-bal. Ar, accelerated corrosion occurred, and followed by mass decrease. In 0.2%Cl{sub 2}-1%O{sub 2}-bal. Ar, the top layer of scale was Fe{sub 3}O{sub 4}, which had a different morphology from that produced in environments without KCl, and beneath the Fe{sub 3}O{sub 4} layer more K and Cl was detected. Accelerated corrosion would be hot corrosion by molten eutectic salt of KCl and FeCl{sub 2}, by chlorination of iron. Fe{sub 3}O{sub 4} would be precipitated from the molten salt because of higher oxygen potential at the gas/scale interface than the metal/scale interface. Volatilization of chloride would be the reason for the mass decrease. In 0.2%HCl-1%O{sub 2}-2%H{sub 2}O-bal. Ar, accelerated corrosion did not occur. However, by eliminating O{sub 2} from the gas system, accelerated corrosion was seen. The main corrosion product was Fe{sub 3}O{sub 4}. The accelerated corrosion could also be explained by hot corrosion by KCl-FeCl{sub 2} molten eutectic salt. It did not occur in 0.2%HCl-1%O{sub 2}-2%H{sub 2}O-bal. Ar probably because the chlorine potential was too small to produce enough FeCl{sub 2}.
OSTI ID:
128735
Report Number(s):
CONF-950304--
Country of Publication:
United States
Language:
English