- Page 1: Persulfate Persistence and Treatabi
- Page 6 and 7: temporal profiles from these push-p
- Page 8 and 9: also increased for SO which is a by
- Page 10 and 11: Andrews played the role of this pan
- Page 13 and 14: Table of Contents List of Figures
- Page 15: 2− 5.3.2 Mass loading: SO , Na +
- Page 18 and 19: Figure 4.2. Concentration profiles
- Page 21: List of Tables Table 2.1. Selective
- Page 24 and 25: compounds. In the absence of site r
- Page 26 and 27: alkanes, fuel-related contaminants
- Page 28 and 29: term contamination sources and rele
- Page 30 and 31: persulfate interacts with the aquif
- Page 33 and 34: Chapter 2 1 Persistence of Persulfa
- Page 35 and 36: In the presence of aquifer material
- Page 37 and 38: materials
- Page 39 and 40: flow column experiments is that the
- Page 41 and 42: Data from the control reactors indi
- Page 43 and 44: Since the buffering capacity of car
- Page 45 and 46: with 23 (2.6) where kcat is the min
- Page 47 and 48: catalyzed reaction in the systems f
- Page 49 and 50: COD test results illustrated loss o
- Page 51 and 52: g/mL vs. 3.9±0.4 g/mL). This will
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flow mode of column operation was u
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Pilot-scale data are representative
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Ionic Strength (M) 0.5 0.4 0.3 0.2
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C/C o 0 0 10 20 30 40 50 Figure 2.6
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39 Table 2.1. Selective chemical pr
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activation trials, lower stability
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solvents) (Anipsitakis and Dionysio
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catalyst drainage from the aqueous
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2− − − 2− −• −• S2
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lined plastic cap and manually shak
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3.4. RESULTS AND DISCUSSION 3.4.1.
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eaction with Fe(II) (Figure 3.1). C
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At a molar ratio of 10 for the 1 g/
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that persulfate degradation was inf
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persulfate treatability studies to
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C TOS /C o C TOS /C o C TOS /C o 10
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pH pH pH 14 12 10 8 6 4 2 0 14 12 1
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Table 3.2. Summary of activated per
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Chapter 4 Persulfate Oxidation of G
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minimize disturbance to above groun
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emediation of gasoline contaminated
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materials, ~29 g of the selected so
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Residual oxidant analysis was perfo
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The overall mass action law for oxi
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−• SO 4 and OH ● ). The kobs
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chelating agent (citric acid) and t
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indicates that at an extremely high
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extension, both the F1 fraction and
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natural activation and unactivated
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C/C o C/C o C/C o 1.2 1 0.8 0.6 0.4
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Table 4.1. Summary of experimental
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Chapter 5 In Situ Gasoline Source Z
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effectiveness in the treatment of t
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from 2.25 to 4.5 m. The injection w
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controller and connected to the tan
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To capture changes in the mass load
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Inorganic analysis consisted of per
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converted to SO . The estimate for
- Page 131 and 132:
inorganic species were flushed from
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observed for all MGCs. The mass loa
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end of the idealized injection slug
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monitoring fence-line was primarily
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Figure 5.2. Image of the persulfate
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Persulfate (mg/L) 2- SO4 (mg/L) Na
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M (g/day) ● M/M o ● ● 30 20 1
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Cumulative Mass (g) Cumulative Mass
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Chapter 6 Closure 6.1. CONCLUSIONS
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persulfate kinetic behavior. It hig
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persulfate implying that substantia
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conditions than bench-scale studies
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References CHAPTER 1 Appelo, C.A.J.
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Lundegard, P.D., Johnson, P.C., 200
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CHAPTER 2 Balazs, G.B., Cooper, J.F
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Langmuir, D., 1997. Aqueous Environ
- Page 163 and 164:
Kolthoff, I.M., Medalia, A.I., Raae
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CHAPTER 4 Agency for Toxic Substanc
- Page 167 and 168:
Lundegard, P.D., Johnson, P.C., 200
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CHAPTER 5 Agency for Toxic Substanc
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Sudicky, E.A., 1986. A natural grad