chemicals investigation programme 2 - aquaenviro

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Chemicals Investigation Programme 2 DynaSand Oxy for combined Phosphorus and Ammonia removal: experiences from Anglian Water Adam Brookes 1 , Paul Barter 2 1 Anglian Water 2 Hydro International The Big Phosphorus Conference, Manchester, 4 th and 5 th July 2017

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Page 1: Chemicals Investigation Programme 2 - AquaEnviro

Chemicals Investigation Programme 2

DynaSand Oxy for combined Phosphorus and Ammonia removal: experiences from Anglian Water

Adam Brookes1, Paul Barter2

1 Anglian Water2 Hydro International

The Big Phosphorus Conference, Manchester, 4th and 5th July 2017

Page 2: Chemicals Investigation Programme 2 - AquaEnviro

National Collaborative Project

Page 3: Chemicals Investigation Programme 2 - AquaEnviro

DynaSand Oxy for combined Phosphorus and

Ammonia removal

Content:

• Process description and history

• Trial site and results

• Conclusions

Page 4: Chemicals Investigation Programme 2 - AquaEnviro

Process Background

• Used in Anglian Water since late 1990s for

P removal, such as Stalham WRC in Norfolk Broads

• Not used for both ammonia and phosphorus

removal to very low concentrations so included in

the trial, phosphorus removal is priority

Page 5: Chemicals Investigation Programme 2 - AquaEnviro

Dynasand Oxy filter - continuous sand filtration system

1. Inlet distributor

2. Filtrate outlet

3. Media with entrapped

solids

4. Airlift pump

5. Media washer

6. Washer labyrinth

7. Washwater outlet

8. Media bed

Page 6: Chemicals Investigation Programme 2 - AquaEnviro

Site PE site Upfront

Process

No.

filters

Trial max flow

Watton WRC 13,900

Trickling filter

with ferric dosing

in PSTs

6 80 L/s (30.7 L/s DWF)

CIP2 Low P Programme – DynaSand Oxy trial site

Page 7: Chemicals Investigation Programme 2 - AquaEnviro

Anglian Water – Dyna Sand Oxy trial site

Page 8: Chemicals Investigation Programme 2 - AquaEnviro

Watton WRC

Page 9: Chemicals Investigation Programme 2 - AquaEnviro

Results of DynaSand Oxy trial – Summary of influent

Company Average

(mg/l)

Min

(mg/l)

Max

(mg/l)

Total P 1 0.7 1.7

SRP 0.5 0.17 0.9

Ammonia* post Jun ‘16

2.41.7

0.70.7

7.93

Page 10: Chemicals Investigation Programme 2 - AquaEnviro

Results of DynaSand Oxy trial – Summary of effluent

Company Average

(mg/l)

Min

(mg/l)

Max

(mg/l)

95 %ile

(mg/l)

Total P 0.29 0.13 0.7 0.65

SRP 0.17 0.04 0.43 0.42

Ammonia* post Jun ‘16

0.870.39

0.230.23

5.420.96

2.660.83

Page 11: Chemicals Investigation Programme 2 - AquaEnviro

Phosphorus

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Ammonia

Page 13: Chemicals Investigation Programme 2 - AquaEnviro

Conclusions

• Total phosphorus concentration of 0.3 mg/L and Ammonia < 1 mg/L

were achieved providing stable operation upstream and no increased

loading (e.g. from sludge liquors)

• Optimisation carried out when site receiving relatively low phosphorus

load

• Nitrification was not inhibited at low SRP concentration during the trial

• Extended operation at low temperatures not encountered

• Thanks to @one alliance delivery team and operations team

Page 14: Chemicals Investigation Programme 2 - AquaEnviro

Any Questions?Questions?