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Page 1: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Optimizing Slime Control Chemical Feed in Tarrant

Regional Water Districts Raw Water PipelinesP. Greg Pope Ph.D., P.E.

Rob Cullwell P.E.

Jason Gehrig P.E. (TRWD)

Page 2: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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3

TRWD Raw Water Supply System

Page 3: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Why feed chloramines?

Bio-Film Control

Zebra Mussel Mitigation

Page 4: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Key Project Goals

• Richland Chambers and Cedar Creek– Improve chloramine feed efficiency– Protect intake conduit/towers– Improvements to existing chemical systems

• Benbrook – Design new chloramine feed system

• Sampling program to monitor chloramine decay• Quantify impacts of biofilm on pipeline friction

factor and power use

Page 5: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Key Project Goals

• Richland Chambers and Cedar Creek– Improve chloramine feed efficiency– Protect intake conduit/towers– Improvements to existing chemical systems

• Benbrook – Design new chloramine feed system

• Sampling program to monitor chloramine decay• Quantify impacts of biofilm on pipeline friction

factor and power use

Page 6: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Bench-Scale Testing

Page 7: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Region 1Monochloramine

Formation

Region 2Monochloramine

Destruction

Region 3Free Chlorine

Residual

Tota

l Chl

orin

e &

Free

Am

mon

iaC

once

ntra

tions

More Chlorine AddedChlorine to Nitrogen (Cl2:N) Mass (Molar) Ratio

0 3 (0.6) 5 (1) 7.6 (1.5)

Breakpoint

Free Ammonia

Total Chlorine

DW

Proper Cl2/N ratio critical for chloramine stability

Page 8: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Higher Cl2/N ratios increased chloramine decay

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

0 20 40 60 80 100

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (hours)

Cedar Creek pH 8.1

Richland Chambers pH 8.1

Benbrook pH 7.9

Notes:1) Water Source: Cedar Creek, Richland Chambers, Benbrook2) Date: 12/15/20143) Cl2:N ratio: 4.5:1 4) Simultaneous addition of chlorine and ammonia

Page 9: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Higher Cl2/N ratio increases chloramine decay

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

0 20 40 60 80 100

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (hours)

Cedar Creek pH 7.6

Richland Chambers pH 8.1

Benbrook pH 7.9

Notes:1) Water Source: Cedar Creek, Richland Chambers, Benbrook2) Date: 12/15/20143) pH:ambient4) Cl2:N ratio: 5.5:1 (solid symbols); 4.5:1 (open symbols) 5) Simultaneous addition of chlorine and ammonia

Page 10: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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High Cl2/N ratio increases DBP formation

0

2

4

6

8

10

12

Cedar Creek Richland Chambers Benbrook

TTHM

Form

ation

(µg/

L)

4.5:1

5.5:1

Notes:1) 48 hour incubation2) pH ambient3) TOC: Cedar Creek = 5.8 mg/L; Richland

Chambers = 4.5 mg/L; Benbrook = 4.7 mg/L

Page 11: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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High Cl2/N ratio increases DBP formation

0

2

4

6

8

10

12

Cedar Creek Richland Chambers Benbrook

HAA5

Form

ation

(µg/

L)

4.5:1

5.5:1

Notes:1) 48 hour incubation2) pH ambient3) TOC: Cedar Creek = 5.8 mg/L; Richland

Chambers = 4.5 mg/L; Benbrook = 4.7 mg/L

Page 12: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Proper pH critical for chloramine stability100

80

60

40

20Tota

l Com

bine

d C

hlor

ine

(%)

pH3 5 6 7 8

Trichloramine

Monochloramine

Dichloramine

Normal Range

9

Page 13: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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pH variability in source waters

5.0

6.0

7.0

8.0

9.0

10.0

11.0

8/11/1987 5/7/1990 1/31/1993 10/28/1995 7/24/1998 4/19/2001 1/14/2004 10/10/2006

pH

Date

RC (0.5m) CC (0.5m)*Note: Data from Jan 1990 to Mar 2008

Page 14: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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pH variability in source waters

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

6.0 6.5 7.0 7.5 8.0 8.5 9.0 9.5 10.0 10.5 11.0

Perc

ent n

ot Ex

ceed

ing (

%)

pH

RC (0.5m) CC (0.5m)*Note: Data from Jan 1990 to Mar 2008

Page 15: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Higher pH decreases chloramine decay: Cedar Creek

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

4.5

5.0

0 5 10 15 20 25 30 35 40 45

Tota

l Chl

orin

e, M

onoc

hlor

amin

e Re

sidu

al (m

g/L)

Time (hours)

pH 7.0 Total ChlorinepH 7.0 MonochloraminepH 8.3 Total ChlorinepH 8.3 Monochloramine

Notes:1) Water Source: Cedar Creek2) Date: 8/26/20143) Cl2:N ratio: 4.5:14) Chloramine Dose: 5.0 mg/L5) Simultaneous addition of chlorine and ammonia

Page 16: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Higher pH decreases chloramine decay: Richland Chambers

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

0 5 10 15 20 25 30 35 40 45

Tota

l Chl

orin

e, M

onoc

hlor

amin

e Re

sidu

al (m

g/L)

Time (hours)

pH 7.0 Total ChlorinepH 7.0 MonochloraminepH 8.3 Total ChlorinepH 8.3 Monochloramine

Notes:1) Water Source: Richland Chambers2) Date: 8/26/20143) Cl2:N ratio: 4.5:14) Chloramine Dose: 3.5 mg/L5) Simultaneous addition of chlorine and ammonia

Page 17: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Full-Scale Testing

Page 18: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Pipeline Sampling Locations

Waxahachie Pump Station

Richland-ChambersLake Pump

Station

Cedar CreekLake Pump

Station

Ennis Pump Station

Blackjack Road

Rosewood Ranch

NE 1036

Page 19: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine Decay in the Pipeline: Cedar Creek

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

4.5

5.0

0 5 10 15 20 25

Tota

l Chl

orin

e, M

onoc

hlor

amin

e Re

sidu

al (m

g/L)

Time (hours)

Total Cl2 (hold)

NH2Cl (hold)

Total Cl2 (pipeline)

NH2Cl (pipeline)

Lake Pumpstation

Waxahachie

Rosewood Ranch

Ennis Pumpstation

Blackjack Road

Page 20: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine Decay in the Pipeline: Richland Chambers

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

0 5 10 15 20 25

Tota

l Chl

orin

e, M

onoc

hlor

amin

e Re

sidu

al (m

g/L)

Time (hours)

Total Cl2 (hold)

NH2Cl (hold)

Total Cl2 (pipeline)

NH2Cl (pipeline)

Lake Pumpstation

Waxahachie

NE 1036

Ennis Pumpstation

Blackjack Road

Page 21: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine loss from nitrification

Page 22: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine loss from nitrification

Monitoring Parameters:• Monochloramine• Free ammonia• Nitrite• Nitrate

Page 23: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification parameters measured in the pipeline: Cedar Creek

0.00

0.05

0.10

0.15

0.20

0.25

0.30

0

0.5

1

1.5

2

2.5

3

3.5

4

PS RR Ennis BJ Wax

Cedar Creek

NH3

/Nitr

ite a

s N (m

g/L)

Tota

l Chl

orin

e/M

onoc

hlor

amin

e (m

g/L)

Total Cl (mg/L) Mono Chl (mg/L) NH3 (mg/L) Nitrite (mg/L)

Page 24: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification parameters measured in the pipeline: Richland Chambers

0.00

0.05

0.10

0.15

0.20

0.25

0.30

0

0.5

1

1.5

2

2.5

3

PS NE 1036 Ennis BJ Wax

Richland Chambers

NH3

/Nitr

ite a

s N (m

g/L)

Tota

l Chl

orin

e/M

onoc

hlor

amin

e (m

g/L)

Total Cl (mg/L) Mono Chl (mg/L) NH3 (mg/L) Nitrite (mg/L)

Page 25: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Additional Pipeline Sampling Locations

Waxahachie Pump Station

Richland-ChambersLake Pump

Station

Cedar CreekLake Pump

Station

Mansfield

Kennedale Balancing Reservoir

Arlington Outlet

Midlothian

Page 26: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Additional pipeline sampling: Cedar Creek

0.00

0.10

0.20

0.30

0.40

0.50

0.60

0.70

0.80

0.90

0

0.5

1

1.5

2

2.5

3

3.5

Pump Station

Waxahachie Midlothian Mansfield @ Church

KBR Arlington Outlet

NH3

/Nitr

ite/N

itrat

e as

N (m

g/L)

Tota

l Chl

orin

e/M

onoc

hlor

amin

e (m

g/L)

Total Chlorine Monochloramine Free Ammonia Nitrite Nitrate

Page 27: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Additional pipeline sampling: Richland Chambers

0.00

0.10

0.20

0.30

0.40

0.50

0.60

0

0.5

1

1.5

2

2.5

3

Pump Station

Waxahachie Midlothian Mansfield @ Church

KBR Arlington Outlet

NH3

/Nitr

ite/N

itrat

e as

N (m

g/L)

Tota

l Chl

orin

e/M

onoc

hlor

amin

e (m

g/L)

Total Chlorine Monochloramine Free Ammonia Nitrite Nitrate

Page 28: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine Decay in the Pipeline: Richland Chambers – August 2015

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

0 10 20 30 40 50

Tota

l Chl

orin

e Re

sidu

al (m

g/L)

Time (hours)

8/15 (hold)

8/15 (pipeline)Lake Pumpstation

Waxahachie

Ennis Pumpstation

Rosewood Ranch

Page 29: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Chloramine Decay in the Pipeline: Richland Chambers – August 2015

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

0 10 20 30 40 50

Tota

l Chl

orin

e Re

sidu

al (m

g/L)

Time (hours)

8/15 (hold)

8/15 (pipeline)

9/11 (pipeline)

9/15 (pipeline)

Lake Pumpstation

Waxahachie

Ennis Pumpstation

Rosewood Ranch

Page 30: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Test for Presence of Nitrifying Bacteria

0.2 micron filter

Pipeline water sample

Page 31: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification evaluation in the Cedar Creek pipeline: Blackjack Road

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.0

0.5

1.0

1.5

2.0

2.5

3.0

0 1 2 3 4 5 6 7 8 9

Nitr

ite/F

ree A

mm

onia

(mg/

L as N

)

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (days)

NH2Cl (mg/L)

NH3 (mg/L)

Nitrite (mg/L)

Notes:1) Dashed lines represent filtered sample (0.2 µm filter)

Page 32: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification evaluation in the Cedar Creek pipeline: Blackjack Road

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.0

0.5

1.0

1.5

2.0

2.5

3.0

0 1 2 3 4 5 6 7 8 9

Nitr

ite/F

ree A

mm

onia

(mg/

L as N

)

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (days)

Monochloramine (mg/L)Monochloramine (mg/L)NH3 (mg/L)Nitrite (mg/L)NH3 (mg/L)Nitrite (mg/L)

Notes:1) Dashed lines represent filtered sample (0.2 µm filter)

Page 33: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification evaluation in the Richland Chambers pipeline: Blackjack Road

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

1.8

0 1 2 3 4 5 6 7 8 9

Nitr

ite/F

ree A

mm

onia

(mg/

L as N

)

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (days)

NH2Cl (mg/L) NH3 (mg/L)

Nitrite (mg/L)

Notes:1) Dashed lines represent filtered sample (0.2 µm filter)

Page 34: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification evaluation in the Richland Chambers pipeline: Blackjack Road

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

1.8

0 1 2 3 4 5 6 7 8 9

Nitr

ite/F

ree A

mm

onia

(mg/

L as N

)

Mon

ochl

oram

ine

(mg/

L as C

l 2)

Time from sample collection (days)

Monochloramine (mg/L)Monochloramine (mg/L)NH3 (mg/L)Nitrite (mg/L)NH3 (mg/L)Nitrite (mg/L)

Notes:1) Dashed lines represent filtered sample (0.2 µm filter)

Page 35: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification Control

Page 36: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification Control

Nitrification Control → Inactivation > Growth

Page 37: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification Control

Nitrification Control → Inactivation > GrowthOperational Controls• Chloramine Concentration

• Free ammonia concentration

• Residence time (reaction time)

Page 38: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Nitrification Control

Nitrification Control → Inactivation > GrowthOperational Controls• Chloramine Concentration

• Free ammonia concentration

• Residence time (reaction time)

• Free Chlorination of Pipeline

Page 39: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Conclusions

• Optimum chloramine formation conditions lead to – Reduced decay– Reduced DBP formation

• Significant nitrification occurring in the pipeline– Increased chloramine loss

• Demonstrated simple test for the presence of nitrifying bacteria

Page 40: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Next Steps…..

Page 41: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Contact Information

P. Greg Pope, Ph.D., P.E.Carollo [email protected]

Page 42: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Extra Slides

Page 43: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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TTHM Formation

0

5

10

15

20

25

30

35

40

45

50

0 5 10 15 20 25 30 35

TTHM

(µg/

L)

Time (minutes)

Cedar Creek

Richland Chambers

Benbrook

Notes:1) Samples collected 9/4/20142) pH: Cedar Creek - 7.5

Richland Chambers - 7.8Benbrook - 8.1

Page 44: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Historical LSI – Raw Water

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

-2.0 -1.5 -1.0 -0.5 0.0 0.5 1.0 1.5 2.0 2.5 3.0

Perc

ent n

ot Ex

ceed

ing (

%)

LSI

Cedar Creek Reservoir Richland Chambers Reservoir Benbrook Reservoir

Notes: 1) Data from Jan 1990 to Mar 2008 (depth

ranges from 3-6m)2) Data obtained from Appendix A of Water

Quality Analysis Technical Memorandum (RPS Espey)

Page 45: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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Caustic currently fed to Cedar Creek for Corrosion control

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

-1.500 -1.000 -0.500 0.000 0.500 1.000 1.500

Perc

ent n

ot Ex

ceed

ing (

%)

LSI

Cedar Creek Intake Cedar Creek Treated

Page 46: TWCA Annual Convention: Optimizing Slime Control Chemical Feed in TRWD Raw Water Pipelines, Greg Pope

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DBP formation testing

0

2

4

6

8

10

12

14

16

18

20

Waxahachie (10 hours)

Lake Pump Station Hold (22 hours)

Bench (22 hours)

Waxahachie (13 hours)

Lake Pump Station Hold (22 hours)

Bench (22 hours)

TTHM

(µg/

L); H

AA5

(µg/

L); N

DMA

(ng/

L)TTHM

HAA5

NDMA

Total Chlorine Demand

Notes:1) Samples collected 9/4/20142) Bench testing - Chlorine and ammonia added

simultaneously at a 4.5:1 Cl2:N ratio3) NDMA detection limit = 2 ng/L

Richland Chambers Cedar Creek

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High Cl2/N ratio increases DBP formation

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Cedar Creek Richland Chambers Benbrook

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Notes:1) 48 hour incubation2) pH ambient3) TOC: Cedar Creek = 5.8 mg/L; Richland

Chambers = 4.5 mg/L; Benbrook = 4.7 mg/L