H2ONa2SO32NaOHSO2H2OSO2H2SO3(acidic)N2H4O2H2ON2(oxygen consumed)2C4H9NOCO22H2OC4H9NO C4H9COOHHNO3H2(carbon dioxide consumed)2N2H42 NH3N2H2NH3H2ONH4OHDOE-HDBK-1015/2-93Principles of Water TreatmentDISSOLVED GASES, SUSPENDED SOLIDS, AND pH CONTROLRev. 0CH-04Page 19Sodium sulfite reacts rapidly with oxygen and is a very efficient scavenger. However, being asolid and the source of another solid (Na SO ) that is produced during the reaction, sodium24sulfite has the potential of fouling heat transfer surfaces. An additional problem associated withthe use of sodium sulfite is corrosion of secondary system components resulting from itsdecomposition products. At the temperatures present in the steam generators, sodium sulfitecan decompose as follows.(4-13)Sulfur dioxide (SO ) is a gas and is carried over to the remainder of the steam facility. With2water (in the steam or in the feed/condensate system), the SO reacts in the following manner.2(4-14)This acidic condition is corrosive to all components in the secondary system.Because of the problems associated with sodium sulfites, many facilities use volatile chemistrycontrol of the secondary steam system to control dissolved gases in conjunction with airremoval systems. This control utilizes hydrazine (Reaction 4-11) and morpholine (Reaction 4-15) to eliminate oxygen and carbon dioxide, respectively. (4-11)(4-15)As can be seen by Reaction (4-11), no solids are formed; thus, the tendency of fouling heattransfer surfaces is reduced. An additional benefit results from the decomposition of hydrazineby the following reactions.(4-16)(4-17)These reactions result in an alkaline pH condition that decreases corrosion in the steam facility.As can be seen in Reaction (4-15), the consumption of CO takes place. Two benefits result2from this reaction; 1) the inventory of dissolved gases in the steam facility is reduced, and 2)is the reaction contributes to maintaining a higher pH by eliminating carbonic acid (H CO ),23thus reducing corrosion.
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