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Frank Qiao and Michael Wang
Cost-effective Data Mining from SCADA system to Replace Flow Monitoring Predicting H2S Corrosion “Hotspot” in Large Sewer Collection System Frank Qiao and Michael Wang March 27, 2018
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Outline Process of H2S Formation First Lesson Case Study
Observation and Conclusion
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Process of H2S Formation
Sulfate Sulfide (l) Sulfide (g) Sulfuric Acid Pipe Crown Liquid Bio/Chemical Physical Bacteria reduction oxidation
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First Lesson Constructed in 1986 to a build out capacity of 8 MGD
~ 17,000 LF 30" Force Main ~ 13,000 LF 24" Force Main
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Profile
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Permanent Dry Area in Transition Zone Most Risky
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24 inch DIP
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Polybond Liner Failure
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Recent Study 14 mile FM
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Typical H2S Gas (ppm)
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Higher pH limits H2S-L Formation
H2S-G (ppm)
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H2S-G to H2S-L Ratio Varies by Location
Location Matters a lot More pumping More FM discharge More downstream More H2S formation
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H2S-G to H2S-L Ratio
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Physics plays a big role
Henry’s Law Equilibrium needs lots of energy
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Henry’s Law Constant
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Carbon Can H2S In (ppm)
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14 Mile Long Force Main
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FM TRANSITION GRAVITY AV2 AV3 AV8 AV9 AV10 AV4 AV7 AV11 AV5 AV6 AV12
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More Extreme Cases
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Conclusion H2S formation is very high in transition zone
H2S-L to H2S-G plays an important role in H2S formation High pressure, long detention time and more turbulence from pumping/hydraulic jump leads to higher H2S-G to H2S-L ratio Bi-oxide may not be a good treatment strategy pH adjustment and H2S treatment strategy (H2O2/Fe) may be more effective
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