impact of divalent cations on fouling potential of bicarbonate-form anion exchange resins

1
PRELIMINARY DATA MOTIVATIONS Increased water demands & diminishing high quality water sources lead to the use of previously underutilized technologies METHODOLOGY CONCLUSIONS The presence of calcium in solution negatively impacts the performance of ion exchange for both bicarbonate-form and chloride-form. The presence of magnesium also impacts performance. Chloride-form ion exchange isn’t impacted as greatly by the presence of divalent cations as bicarbonate-form. Bicarbonate-form anion exchange is greatly impacted by the presence of divalent cations. The presence of magnesium has the most profound and immediate impact. FUTURE WORK Complete additional regeneration cycles and perform regeneration cycles on waters containing no cations, and waters containing Co 2+ . Investigate the biological fouling of bicarbonate- form biological fouling Innovative regeneration by CO 2 (g) sparging and optimization Figure 1: Preliminary results showing resin performance in absence of divalent cations. Synthetic water contained Santa Fe River NOM, nitrate, sulfate, bicarbonate, and chloride. Figure adapted from Rokicki and Boyer 2011 2 . Calcium Magnesium Figure 3: DOC removal by chloride-form ion exchange resins over multiple regeneration cycles in the presence of calcium. Figure 4: DOC removal by bicarbonate-form ion exchange resins over multiple regeneration cycles in the presence of calcium. Species pK sp 1 MgCO 3 5.17 CaCO 3 8.54 CoCO 3 12.84 Species mg/L meq/L Cl - 4.03 0.06895 HCO 3 - 5.79 0.06895 SRNOM 14 0.06895 X 2+ Varies 0.06895 Figure 5: DOC removal by chloride-form ion exchange resins over multiple regeneration cycles in the presence of magnesium. Figure 6: DOC removal by bicarbonate-form ion exchange resins over multiple regeneration cycles in the presence of magnesium. Jar tests are run in triplicate Regeneration occurs at 100x equivalence capacity of resin ACKNOWLEDGEMENTS The author would like to thank Dr. Treavor Boyer for all his support and guidance. I would also like to thank the Boyer research team for all their help and support in and out of the laboratory. References 1 Dean, J.A., 1999. Lange's Handbook of Chemistry, 15th ed. McGraw-Hill.. 2 Rokicki, C.A., Boyer, T.H., 2011. Bicarbonate-form anion exchange: Affinity, regeneration, and stoichiometry. Water Research 45, 1329 -1337. 3 Walker K.M., Boyer, T.H., 2011. Long-term performance of bicarbonate-form anion exchange: Removal of dissolved organic matter and bromide from the St. Johns River, FL, USA.. Water Research 45 (9), 2875-2886. RESULTS Ion exchange (IEX) may be a treatment solution for certain waters with higher levels of natural organic matter (NOM): IEX Resin NOM NOM NOM NOM HCO 3 - HCO 3 - HCO 3 - HCO 3 - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - IEX Resin NOM NOM NOM NOM HCO 3 - HCO 3 - HCO 3 - HCO 3 - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - Cl - However, brine associated with chloride- form resin limits the potential applications of IEX. Bicarbonate-form would generate easier to dispose of regenerant and would prevent increase of salinity of local waters. It is unknown how the presence of bicarbonate within the resin structure will react with divalent cations: Table 2: Synthetic water composition Table 1: Carbonate mineral solubility products. Table adapted from Dean 1999 1 Kinetic study jar tests: Regeneration of resin: IEX Resin HCO 3 - HCO 3 - X 2+ X 2+ H + H + HCO 3 - Brine disposal is a major concern, much like RO concentrate, it often impedes the implementation of this technology. Impact of divalent cations on fouling potential of bicarbonate-form anion exchange resins Christopher A. Rokicki, and Treavor H. Boyer 1 Department of Environmental Engineering Sciences, University of Florida, Gainesville, FL 1 [email protected] ~ (352)846-3351 ~ http://www.ees.ufl.edu/homepp/boyer/ Figure 2: SEM images of chloride- and bicarbonate-form resin after 14 regenerations. Figure adapted from Walker and Boyer 2011 3 . 0.5ml/L IEX resin 1L DI & salt Mix 30min at 150 RPM Stop, allow to settle, decant Add 1L DI to wash, mix 10min Repeat twice 0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100% r0 r1 r2 r3 % DOC removal regeneration# M-Cl M-HCO3 0% 10% 20% 30% 40% 50% 0 50 100 % DOC removal time (min) r0 r1 r2 r3 chloride-form chloride-form 0% 10% 20% 30% 40% 50% 0 50 100 % DOC removal time (min) r0 r1 r2 r3 bicarbonate-form 0% 10% 20% 30% 40% 50% 0 50 100 % DOC removal time (min) r0 r1 r2 r3 bicarbonate-form 0% 10% 20% 30% 40% 50% 0 50 100 % DOC removal time (min) r0 r1 r2 r3 chloride-form

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PRELIMINARY DATA

MOTIVATIONS

Increased water demands & diminishing high quality water sources lead to the use of previously underutilized technologies

METHODOLOGY

CONCLUSIONS

• The presence of calcium in solution negatively

impacts the performance of ion exchange for both

bicarbonate-form and chloride-form. The presence

of magnesium also impacts performance.

• Chloride-form ion exchange isn’t impacted as

greatly by the presence of divalent cations as

bicarbonate-form.

• Bicarbonate-form anion exchange is greatly

impacted by the presence of divalent cations. The

presence of magnesium has the most profound and

immediate impact.

FUTURE WORK

• Complete additional regeneration cycles and

perform regeneration cycles on waters containing

no cations, and waters containing Co2+.

• Investigate the biological fouling of bicarbonate-

form biological fouling

• Innovative regeneration by CO2(g) sparging and

optimization

Figure 1: Preliminary results showing resin performance in

absence of divalent cations. Synthetic water contained Santa

Fe River NOM, nitrate, sulfate, bicarbonate, and chloride.

Figure adapted from Rokicki and Boyer 20112.

Calcium

Magnesium

Figure 3: DOC removal by chloride-form ion exchange resins over

multiple regeneration cycles in the presence of calcium. Figure 4: DOC removal by bicarbonate-form ion exchange resins over

multiple regeneration cycles in the presence of calcium.

Species pKsp1

MgCO3 5.17

CaCO3 8.54

CoCO3 12.84

Species mg/L meq/L

Cl- 4.03 0.06895

HCO3- 5.79 0.06895

SRNOM 14 0.06895

X2+ Varies 0.06895

Figure 5: DOC removal by chloride-form ion exchange resins over

multiple regeneration cycles in the presence of magnesium.

Figure 6: DOC removal by bicarbonate-form ion exchange resins over

multiple regeneration cycles in the presence of magnesium.

• Jar tests are run in

triplicate

• Regeneration occurs

at 100x equivalence

capacity of resin

ACKNOWLEDGEMENTS

The author would like to thank Dr. Treavor Boyer for all

his support and guidance. I would also like to thank

the Boyer research team for all their help and support

in and out of the laboratory.

References 1Dean, J.A., 1999. Lange's Handbook of Chemistry, 15th ed.

McGraw-Hill.. 2Rokicki, C.A., Boyer, T.H., 2011. Bicarbonate-form anion

exchange: Affinity, regeneration, and stoichiometry.

Water Research 45, 1329 -1337. 3Walker K.M., Boyer, T.H., 2011. Long-term performance of

bicarbonate-form anion exchange: Removal of dissolved

organic matter and bromide from the St. Johns River,

FL, USA.. Water Research 45 (9), 2875-2886.

RESULTS

• Ion exchange (IEX) may be a treatment

solution for certain waters with higher

levels of natural organic matter (NOM):

IEX ResinNOM

NOM

NOM

NOM

HCO3-

HCO3-

HCO3-

HCO3-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

IEX Resin

NOM

NOMNOM

NOM

HCO3-

HCO3-

HCO3-HCO3

-

Cl-

Cl-Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

Cl-

• However, brine associated with chloride-

form resin limits the potential applications

of IEX. Bicarbonate-form would generate

easier to dispose of regenerant and would

prevent increase of salinity of local waters.

• It is unknown how the presence of

bicarbonate within the resin structure will

react with divalent cations:

Table 2: Synthetic water

composition

Table 1: Carbonate mineral

solubility products. Table adapted

from Dean 19991

Kinetic study jar tests:

Regeneration of resin:

IEX Resin

HCO3-

HCO3-

X2+

X2+

H+

H+HCO3-

Brine disposal is a major concern,

much like RO concentrate, it often

impedes the implementation of this

technology.

Impact of divalent cations on fouling potential of

bicarbonate-form anion exchange resins Christopher A. Rokicki, and Treavor H. Boyer1

Department of Environmental Engineering Sciences, University of Florida, Gainesville, FL [email protected] ~ (352)846-3351 ~ http://www.ees.ufl.edu/homepp/boyer/

Figure 2: SEM images of chloride- and bicarbonate-form

resin after 14 regenerations. Figure adapted from Walker

and Boyer 20113.

0.5ml/LIEX resin

1L DI& salt

Mix 30min at 150 RPM

Stop, allow to settle, decant

Add 1L DI to wash, mix 10min

Repeat twice

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

r0 r1 r2 r3

% D

OC

re

mo

va

l

regeneration#

M-Cl

M-HCO3

0%

10%

20%

30%

40%

50%

0 50 100

% D

OC

rem

oval

time (min)

r0

r1

r2

r3

chloride-form chloride-form

0%

10%

20%

30%

40%

50%

0 50 100

% D

OC

rem

oval

time (min)

r0

r1

r2

r3

bicarbonate-form

0%

10%

20%

30%

40%

50%

0 50 100

% D

OC

rem

oval

time (min)

r0

r1

r2

r3

bicarbonate-form

0%

10%

20%

30%

40%

50%

0 50 100

% D

OC

rem

oval

time (min)

r0

r1

r2

r3

chloride-form