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Evaluation of Potential Impacts of Recycling
Filter Backwash Water on Coagulation Chemistry
A. Gottfried1 and M. Walsh2
1Department of Civil Engineering, McMaster University, Hamilton, ON
2Department of Civil and Resource Engineering, Dalhousie University, Halifax, NS
RATIONALE The recovery and reuse of filter backwash water (FBWW) is viewed as a possible path towards minimizing waste streams and optimizing treatment
performance in a conventional drinking water treatment plant. Recycling FBWW can utilize the existing waste stream to advance residual management practices
and treatment options for water utilities that are required to meet more stringent discharge quality requirements.
INTRODUCTION
FBWW consists of metals, colloidal material, natural organic matter and
microorganisms that concentrate in the filter media during the filtration
process. In Canada, recycling FBWW is not a common practice due to
concerns over potential treatment upsets and impacts to finished water
quality. However, many utilities in the United States recycle FBWW
streams to the head of the plant as a management strategy. The objective
of this research is to examine the changes in coagulation chemistry that can
occur with FBWW recycle by measuring specific water quality parameters.
EXPERIMENTAL DESIGN
Three process designs were evaluated at bench-scale:
Process 1: No recycle → to determine typical treated water quality
Process 2: Recycle of untreated FBWW → impact of raw residuals on water quality
Process 3: Recycle of alum treated FBWW → impact of treated residuals on water quality
Parameters Measured
Bulk Water Quality Metal Analysis Coagulation Behaviour
- TOC/DOC, pH - Manganese - Zeta Potential
- UV-254, Turbidity, Colour - Aluminum
Water Sources:
WTP 1: Windsor, NS: (WTP1) High TOC, conventional FBWW
WTP 2: Hantsport, NS: (WTP2) Low TOC, membrane concentrate
CONCLUSIONS
Preliminary results have demonstrated that there may be potential benefits to recycling FBWW
streams within a drinking water treatment plant in terms of enhanced removal of organic material:
• Bench results showed enhanced removal trends for TOC, DOC, UV-254 & turbidity as the % recycle increased.
• Zeta potentials at constant coagulant dosages showed unique trends for each source water, indicating the
presence of coagulation mechanisms other than charge neutralization for the removal of NOM and turbidity.
• Improved flocculation and sedimentation removal rates observed may be due to the increased number of
bonding sites available due to introduction of FBWW during coagulation.
Further Information
Contact: Dr. Margaret Walsh
E-mail: mwalsh2@dal.ca
Acknowledgements
Natural Sciences and Research Council of Canada
Municipality of Hantsport (Jeff Lawrence & Don Silver)
Municipality of Windsor (Todd Richardson)
RESULTS: Process 2 - WTP 1
Flocculation &
SedimentationRapid Mixing
Dual Media Filtration
Process 2 & 3
FBWW Recycle
Filtrate to Clearwell Backwash Water
Process 3 FBWW Alum Addition
Raw Water
Alum Addition
Raw Water
Solids To Sludge
Thickeners
RESULTS: Process 1 - WTP 2
0
0.02
0.04
0.06
0.08
0.1
0.12
0.14
0 10 20 30 40 50
Alum Dose (mg/L)
UV-254
RW2 UV-254
-25
-20
-15
-10
-5
0
5
10
0 10 20 30 40 50
Alum Dose (mg/L)
ZetaPotential(mV)
RW2 UV-254
-12
-10
-8
-6
-4
-2
0
0 2 4 6 8 10
Recycle %
RW1 Alum Dose = 30mg/L
ZetaPotential(mV)
RW1 Zeta Potential
0.00
0.02
0.04
0.06
0.08
0 2 4 6 8 10
Recycle %
RW1 Alum Dose = 30mg/L
UV-254
2.60
2.65
2.70
2.75
2.80
2.85
2.90
TOC(mg/L))
RW1 UV-254 RW1 TOC

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EM Poster Nov 206

  • 1. Evaluation of Potential Impacts of Recycling Filter Backwash Water on Coagulation Chemistry A. Gottfried1 and M. Walsh2 1Department of Civil Engineering, McMaster University, Hamilton, ON 2Department of Civil and Resource Engineering, Dalhousie University, Halifax, NS RATIONALE The recovery and reuse of filter backwash water (FBWW) is viewed as a possible path towards minimizing waste streams and optimizing treatment performance in a conventional drinking water treatment plant. Recycling FBWW can utilize the existing waste stream to advance residual management practices and treatment options for water utilities that are required to meet more stringent discharge quality requirements. INTRODUCTION FBWW consists of metals, colloidal material, natural organic matter and microorganisms that concentrate in the filter media during the filtration process. In Canada, recycling FBWW is not a common practice due to concerns over potential treatment upsets and impacts to finished water quality. However, many utilities in the United States recycle FBWW streams to the head of the plant as a management strategy. The objective of this research is to examine the changes in coagulation chemistry that can occur with FBWW recycle by measuring specific water quality parameters. EXPERIMENTAL DESIGN Three process designs were evaluated at bench-scale: Process 1: No recycle → to determine typical treated water quality Process 2: Recycle of untreated FBWW → impact of raw residuals on water quality Process 3: Recycle of alum treated FBWW → impact of treated residuals on water quality Parameters Measured Bulk Water Quality Metal Analysis Coagulation Behaviour - TOC/DOC, pH - Manganese - Zeta Potential - UV-254, Turbidity, Colour - Aluminum Water Sources: WTP 1: Windsor, NS: (WTP1) High TOC, conventional FBWW WTP 2: Hantsport, NS: (WTP2) Low TOC, membrane concentrate CONCLUSIONS Preliminary results have demonstrated that there may be potential benefits to recycling FBWW streams within a drinking water treatment plant in terms of enhanced removal of organic material: • Bench results showed enhanced removal trends for TOC, DOC, UV-254 & turbidity as the % recycle increased. • Zeta potentials at constant coagulant dosages showed unique trends for each source water, indicating the presence of coagulation mechanisms other than charge neutralization for the removal of NOM and turbidity. • Improved flocculation and sedimentation removal rates observed may be due to the increased number of bonding sites available due to introduction of FBWW during coagulation. Further Information Contact: Dr. Margaret Walsh E-mail: mwalsh2@dal.ca Acknowledgements Natural Sciences and Research Council of Canada Municipality of Hantsport (Jeff Lawrence & Don Silver) Municipality of Windsor (Todd Richardson) RESULTS: Process 2 - WTP 1 Flocculation & SedimentationRapid Mixing Dual Media Filtration Process 2 & 3 FBWW Recycle Filtrate to Clearwell Backwash Water Process 3 FBWW Alum Addition Raw Water Alum Addition Raw Water Solids To Sludge Thickeners RESULTS: Process 1 - WTP 2 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0 10 20 30 40 50 Alum Dose (mg/L) UV-254 RW2 UV-254 -25 -20 -15 -10 -5 0 5 10 0 10 20 30 40 50 Alum Dose (mg/L) ZetaPotential(mV) RW2 UV-254 -12 -10 -8 -6 -4 -2 0 0 2 4 6 8 10 Recycle % RW1 Alum Dose = 30mg/L ZetaPotential(mV) RW1 Zeta Potential 0.00 0.02 0.04 0.06 0.08 0 2 4 6 8 10 Recycle % RW1 Alum Dose = 30mg/L UV-254 2.60 2.65 2.70 2.75 2.80 2.85 2.90 TOC(mg/L)) RW1 UV-254 RW1 TOC