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Yong Kim, Ph.D.Technical Director
UGSI Chemical Feed, Inc.
Optimizing Polymer Mixing/ActivationImproves Sludge Dewatering: Case Studies
2018 Joint PA-AWWA/PWEA/PMAAWater and Wastewater Technology Summit
State College, PA, November 1 – 2, 2018
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Annual Average Dewatering Cost (2011-2014) = $3.7M
K. Tagney and R. Gupta, Reducing Dewatering Costs through Optimization Program, 2017 WEFTEC.
Dewatering Cost at EMWD - $3.7M/yrPolymer Cost - Average $1.2 M/yr
AR2
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Presentation Overview
1. Science of Polymer Activation• Viscosity as an indicator of polymer solution quality• Effect of dilution water• Two-stage mixing for dry and emulsion polymers• Residence time sufficient for polymer uncoiling/dissolution• Weissenberg effect in dry polymer mixing
2. Case Studies• Water Treatment Plant, PA – emulsion polymer• Wastewater Treatment Plant, CA– dry polymer
3. Aging Issue in Dry Polymer Activation
3
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Three Forms of Polymer Solutions
4
Broken polymer chains byexcessive mixing
Neat polymer
Fisheyes due to poorinitial wetting
Ideal polymer chains bytwo-stage mixing
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Viscosity – Indicator of Polymer Solution Efficiency
0
50
100
150
200
250
4 9 16 22 27
Intrinsic Viscosity of Polymer Solution
Sakaguchi, K.; Nagase, K., Bull. Chem. Soc. Japan, 39, p.88 (1966)
Quantity of friction as measured by the force resisting a flow inwhich parallel layers have at unit speed relative to one another
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Polymer supplier data sheet provides a starting pointfor viscosity – critical factor for polymer efficiency
Solenis, Inc.
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Effect of Dilution Water Quality
Ionic strength (Hardness): multi-valent ion hinders polymer activation- Soft water helps polymer molecules fully-extend faster- Hardness over 400 ppm may need softener
Oxidizer (chlorine): chlorine attacks/breaks polymer chains- Should be less than 3 ppm- Caution in using recycled water for polymer mixing
+ Serious negative impact on aging/maturingTemperature*: higher temperature, better polymer activation
- Water below 40 oF may need water heater- Water over 100 oF may damage polymer chains
Suspended Solids/ Turbidity:- In-line strainer recommended- Caution in using recycled water for polymer mixing
7
*David Oerke, 20% less polymer with warm water, 40% more polymer with 140F sludge, Residuals and Biosolids (2014)
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Effect of Dilution Water Chlorine ContentWhen reclaimed water used for polymer mixing, chlorine < 3 mg/L
0
200
400
600
800
1000
1200
0 1 2 3 4 5 6 7 8 9 10
Visc
osity
Cl2 mg/L
cP
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Polymer Activation (Mixing, Dissolution)
(I) Initial Wetting (Inversion)Sticky layer formedHigh-energy mixing -> No fisheyesMost Critical Stage
(II) DissolutionReptation* or UncoilingLow-energy mixing -> No damage to polymer
Sticky Layer
WaterPolymer (gel)
* de Gennes, P.G., J. Chem. Phys., 55, 572 (1971)
9
time
(I) (II)
Oil
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Two-Stage Mixing (in mix chamber)higher energy mixing low energy mixing
“Discrete” Two-Stage Mixing -discrete means “separation of highand low energy mixing zones”
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One-Stage vs Two-Stage Mixer (Emulsion Polymer)
G-value, mean shear rate (sec-1)
1,700
4,000
1,100
1- stage mixer 2- stage mixer
11
DividingBaffle
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One-Stage Mixing vs. Two-Stage Mixing
Two-stage mixing significant increase of polymer solution efficiency
226
427
310
523
0
100
200
300
400
500
600
Anionic Polymer Cationic Polymer
Viscosity of 0.5% Emulsion Polymer Solution, cP
1-stage mixer 2-stage mixer
37% increase
22% increase
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Vt = Residence time (t) in flocculating basin: Gt-value
Gt-value = mean shear rate x residence time
Contact time (T) in clear well design: CT calcCT calc = residual chlorine concentration x contact time
Residence time (t) in polymer activationSecond stage of polymer activation – “uncoiling” of long chain polymer moleculesrequires more time under low energy mixing than high energy first stage mixing
Residence Time (in mix chamber)Sufficient residence time of low-energy mixing zoneis required for complete polymer dissolution
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Effect of Residence Time on Polymer Activation
Volume of low-energy zone: VLVL,MM = 3* VL,M
M,
0.5
gal
MM
,1.
0 ga
l
370
1795
397
1936
0
500
1000
1500
2000
2500
Cationic Anionic
Effect of Residence Time of Mix Chamber(0.5% polymer solution viscosity, cP)
M MM
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Existing Polymer SystemSiemens M1200-D10AA (2011)
New Polymer SystemUGSI MM1200-D10AA (2016)
16-mgd Water Plant, PA with two BFP (2-M)
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• Side-by-Side Trial from Feb to May 2016• Polymer savings 30% - 35%• Sludge throughput increased by 10%
Test Results of Two Mixing Chambers
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
2/9/16 2/16/16 2/23/16 3/1/16 3/8/16 3/15/16 3/22/16 3/29/16 4/5/16 4/12/16 4/19/16 4/26/16 5/3/16 5/10/16 5/17/16
Poly
mer
Usa
ge, l
b/to
n
Test Date
Effect of Residence Time of Low-shear Zone
M2400
MM2400
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High Energy atMOIW
Transition to low energy“quiescent zone”
AdequateResidence time
Fully activatedpolymer solution at
desired concentration
Polymer science dictates the most effective way of activatingpolymers- Your activation equipment should follow:
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First StageHigh Energy Mixing
(3,450 rpm, < 0.5 sec)
Second StageLow Energy Mixing
(60 rpm, 20 min)
DD4 Disperser Mix and Hold Tanks
PolyBlend® Dry Polymer SystemTwo-Stage Mixing
Polymer SolutionStorage/Holding
(no mixing)
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First-Stage of Dry Polymer Mixing:High Energy Initial Wetting
Very High-Energy Mixing for Short Time
G = 15,000 sec-1
3,450 rpm for < 0.5 sec
Disperses Individual Polymer Particles
* No Fisheye Formation
* Shorter Mixing Time in Next Stage
Water inSolution Out
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Why Initial High-Energy Mixing is So Critical?
Polymer dissolution time, ts ~ (diameter)2 Tanaka (1979)*
d
10*d
Assume ts 1 min
ts 100 min
Initial high-energy mixing No fisheye formation Significantly short mixing time
* Tanaka, T., Fillmore, D.J., J. Chem. Phys., 70 (3), 1214 (1979)
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Mixing Tank for Dissolution of Dry Polymer
Patented Hollow-Wing Impeller
No Weissenberg Effect
Large Impeller, 70% of tank diameter
Uniform Mixing Energy
Low RPM, 60 rpm
Low-intensity Mixing
Minimize Damage to Polymer Chain
Shorter Mixing Time – Due to high energy DD4
20 - 30 min for Cationic Polymer
30 - 40 min for Anionic Polymer
Minimize Damage to Polymer Chain
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Weissenberg Effect in Polymer Mixing
Water(Newtonian)
Polymer Solution(Non-Newtonian, Pseudoplastic)
extremely low mixing
very high mixing
extremely low mixing
* Polymer solution exceeding “critical concentration” climbs up mixing shaft* Extremely non-uniform mixing* Critical factor for “conventional” polymer mix tankmax 0.2% limit for HMW polymer
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Notice polymer solution is “climbing” up the mixer shaft(30 min after mixing (Nalco TX13182): 0.25%, 0.50%)
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Polymer Mixing Tank With No Weissenberg Effect
Impeller / tank diameter > 0.7 Cationic Polymer Solution @ 0.75%
Eye of impeller
Hollow-wing impeller
PVC sleeve aroundmixer shaftseparates mixershaft from polymersolution
PVC sleeve preventsWeissenburg effect at highconcentration, up to 1.0%
Why high conc. solution?* Smaller tank size* Longer shelf life solution
Rotating shaft
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• Solano County, CA, 40 miles North San Francisco• Design capacity: 24 MGD tertiary treatment/ UV• Population served: 135,000• Polymer use for dewatering (screw press) and thickening
(GBT)
Problems with existing polymer system• Struggled to make proper polymer solution• Polymer performance inconsistent• Frequent maintenance issues
FKC screw press runs at average 70 gpm of sludge(2% solids content)
Case Study: Dry Polymer Mixing SystemFairfield-Suisun Sewer District, CA
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Pilot Testing with Two Polymer Mix Equipment
26
Existing Polymer System• Initial wetting: air blower –> wetting head• Mixing: two (2) 4,600 gal mix/age tanks• 1 hour mixing and 4 - 8 hour aging time
UGSI PolyBlend Dry Polymer Demo System• Initial wetting: high-energy mechanical mixing• Mixing: two (2) 360 gal mix tanks• 20 minute mixing, 10+ minute transfer time
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Newly Installed Dry Polymer System
Hollow wing impellerExisting impeller
Old: Two 4,600 gal mixing/aging tanks* 60 min mixing, 2-4 hour aging
New: Two 1,000 gal mixing tanks* 30 min mixing, 15 min holding
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FSSD Installed New PolyBlend®DP2000Performance Data in 2016
38.3 38.435.2 34.5
19.6
0
500
1000
1500
2000
2500
3000
0
5
10
15
20
25
30
35
40
45
2012 2013 2014 2015 2016
FSSD saved 42% on Screw Press Polymer in 2016despite an increase in solids throughput by 18%
Slud
ge P
roce
ssed
, DT/
year
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AGING “accelerated maturing” by initial high-energy wetting
Very High-Intensity Mixing for Short Time
G = 15,000 sec-1 @ 3,450 rpmResidence time < 0.5 sec
Disperses Individual Polymer Particles
* No Fisheye Formation
* Complete dissolution in 20 - 30 min mixing
* Aging – reduced or eliminated
Water in
Solution Out
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How Much Aging is Required for Dry Polymer?
0 20 40 60 80 100 120
Visc
osity
(cP)
Mix Time (min)
stoppedmixing
stoppedmixing
stoppedmixing
1.00%
1.00%
0.86%
aging
aging
aging
Minimum aging required for well-designed equipment
Rao, M, Influents (WEA Ontario, Canada), Vol. 8, 42 (2013)
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Aging – heavily depends on Polymer, Mixing, Water
Aging may help:* Very high molecular-weight, low charge (nonionic) polymers, or
* Low energy mixing at initial wetting stage
Aging does not help:* Medium high molecular-weight, high charge polymers, or
* Very high energy mixing at initial wetting stage
Aging may hurt:* Reclaimed water for polymer mixing, or
* Low concentration of polymer solution
Aging must be reconsidered when reclaimed water is used
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Thank YouAny Questions?