ro record keeping and maintenance
DESCRIPTION
water treatmentTRANSCRIPT
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RO Recordkeeping and Normalization
Steven Coker
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Topics
RO basic system design
RO operating data recording
Factors influencing RO system
performance
RO operating data normalization
FTNORM an easy method for
conducting normalization
calculations
2
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Performance Monitoring
To track performance of RO system trends
To decide when to clean
To decide when to replace membranes
Useful information in troubleshooting
Required in event of warranty claim
3
Why?
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Performance Monitoring
Record operating data
Manually on log sheet
Automatically in SCADA system
Normalize data to account for variation in feed water
pressure, temperature, concentration and recovery
Graph salt passage, product flow and DP vs. time
4
How?
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Basic RO System Design
5
Pump
Concentrate
Feed
Water Permeate
RO Array
Temperature, C
Conductivity, S/cm
Flow Rate, gpm
Pressure, psig Conductivity, S/cm
Flow Rate, gpm
Pressure, psig
Conductivity, S/cm
Flow Rate, gpm
Pressure, psig
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Factors Influencing RO Performance
Increasing Permeate Salt
Flow Passage
Effective Pressure
Temperature
Recovery
Feed Salt Concentration
6
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Data Normalization
7
Why Normalize?
Fluctuations in operating conditions cause permeate flow
and salt passage to change.
Performance changes due to membrane properties
might go undetected.
Normalization eliminates the effects of fluctuating
operating conditions and allows monitoring of the
membrane properties.
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Example: Raw Data from RO system
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90%
91%
92%
93%
94%
95%
96%
97%
98%
99%
100%
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
Reje
ctio
n (
%)
Tem
pera
ture
(
)
Date
RO operation performance
Temperature Permeate Conductivity
RO membrane properties virtually constant, but the observed performance is changed by the variation of temperature.
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What is Data Normalization?
Normalization is a calculation method to express measured
membrane performance variables in terms of a set of reference
conditions.
This allows the user to determine whether observed changes in
membrane performance (flow and/or rejection) are normal
variation due to a change in operating conditions or may be an
indication of fouling, scaling, or damage to the membrane.
Typical Reference Conditions:
Stabilized start-up performance data
Computer model (ROSA) projected performance at standard
conditions or start-up performance conditions
9
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Homogenous Solution Diffusion Model
10
Fw - solvent flux [gallons per square foot per day, gfd]
A - solvent mass transfer coefficient [gfd/psi]
TCF - temperature correcting factor
DP - transmembrane pressure differential [psi]
Dp - osmotic pressure differential [psi]
Water and Solute Flux
Fw = A * TCF * (DP - Dp)
Fs = B * TCF * (DC) Fs - solute flux [pounds per square foot per day, lbfd]
B - solute mass transfer coefficient [gfd]
DC - transmembrane concentration differential [lb/gal]
The effect of temperature and operating pressure on the membrane performance can be calculated to avoid interfering with the membrane property evalution.
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TCF = exp{ Bm * [1/298.15 - 1/(Tf +273.15)]}
TCF temperature correction factor
Bm membrane TCF coefficient
Tf feed temperature, C
RO Permeate Flow Normalization
NDP = Pf Pfb Pp + p
NDP net driving pressure, psig
Pf feed pressure, psig
Pfb - feed brine differential pressure, psig
Pp - permeate pressure, psig
p - permeate osmotic pressure, psig
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RO Permeate Flow Normalization
12
act
ref
act
refact norm
NDP
NDP
TCF
TCF Q Q
Q - flow rate, gpm
TCF - temperature correction factor
NDP net driving pressure, psig
norm - normalized
act actual measured variable
ref - reference condition
Increasing Permeate
Flow
Effective Pressure
Temperature
Recovery
Feed Salt Conc.
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RO Normalized Salt Rejection
13
)TCF
TCF
Q
Q
c
c
c
c( - 1 100 (%) SR
act
ref
ref
act
act fc,
ref fc,
ref f,
act p,norm
cp - permeate salt concentration
cf - feed salt concentration
cfc - feed-concentrate salt concentration
Q - permeate flow rate
TCF - temperature correction factor
act - actual condition
ref - reference condition
norm - normalized
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When should I clean my RO?
14
0
50
100
150
200
250
300
0 50 100 150 200 250 300
Feed
Pre
ssu
re, p
sig
Days of Operation
Feed Pressure vs. Time
Feed Pressure
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When should I clean my RO?
15
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
0
50
100
150
200
250
300
0 50 100 150 200 250 300
Te
mp
era
ture
, C
Feed
Pre
ssu
re, p
sig
Days of Operation
Feed Pressure vs. Time
Feed Pressure Feed Temp (C)
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16
100
150
200
250
300
350
400
0 50 100 150 200 250 300
Flo
w (
gp
m)
Operating Time (days)
Normalized Permeate Flow
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FTNorm for RO Operation Data Normalization
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FTNORM Data Normalization Program
Based on ASTM D 4516
Written as Excel spreadsheet
Data normalized to start-up conditions
Designed for manual data entry but can be incorporated into
SCADA system
Automatic graphing includes:
Normalized permeate flow
Pressure drop
Normalized salt rejection
Graphs of other variables can be easily added
18
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FTNORM - 1 Stage Data Entry Section
19
Reverse Osmosis Plant
Operating Data Normalization
Plant Identification: Train 1 C
Start-Up Date: 5/1/14 0:00 Feed Conductivity / Feed TDS: 1.43446
Date
Permeate
Flow
Concentrate
Flow
Feed
Pressure
Concentrate
Pressure
Permeate
Pressure
Calculated
Feed TDS
Feed
Conductivity
Calculated
Perm TDS
Permeate
Conductivity
Feed
Temp (C)
1/5/14 14:00 297.4 379.1 55.1 54.12 3.7 35205 50500 582 1178 25.4
2/5/14 13:00 298.2 378.7 55.0 53.96 3.4 35414 50800 573 1161 25.5
3/5/14 22:00 296.6 378.3 55.0 54.00 3.5 35275 50600 564 1142 25.5
4/5/14 22:00 295.7 378.4 54.9 53.86 3.3 35344 50700 559 1133 25.3
5/5/14 13:00 297.7 378.6 55.1 54.12 3.6 35275 50600 557 1129 25.5
7/5/14 22:00 296.7 377.3 55.1 54.12 3.7 35344 50700 629 1270 25.3
8/5/14 22:00 297.4 378.6 55.1 54.16 4.3 34926 50100 643 1297 25.3
9/5/14 21:00 296.5 377.3 54.8 53.86 3.9 34787 49900 606 1224 25.3
10/5/14 21:00 297.0 377.7 54.7 53.71 4.0 34717 49800 593 1200 25.6
11/5/14 17:00 300.8 386.7 54.2 53.19 3.4 34577 49600 573 1161 25.7
12/5/14 21:00 296.4 376.9 54.7 53.75 3.9 34647 49700 575 1163 25.6
13/5/14 14:00 298.5 378.9 55.4 54.36 4.3 34577 49600 578 1170 25.9
14/5/14 13:00 296.4 377.3 54.9 53.86 4.1 34787 49900 578 1169 25.9
15/5/14 22:00 297.6 378.1 54.8 53.82 3.6 34717 49800 559 1133 25.4
16/5/14 18:00 297.4 378.8 55.0 54.06 4.0 34647 49700 556 1127 25.4
17/5/14 21:00 296.9 376.6 55.0 53.96 3.8 34856 50000 552 1118 25.3
18/5/14 16:00 296.2 376.4 54.7 53.71 3.7 34787 49900 552 1119 25.6
19/5/14 16:00 297.2 378.1 54.9 53.88 3.7 34856 50000 548 1110 25.6
22/5/14 21:00 297.0 376.3 55.0 54.02 3.9 35414 50800 605 1222 25.3
23/5/14 19:00 296.1 377.9 54.9 53.92 4.0 35205 50500 585 1183 25.3
24/5/14 13:00 296.4 380.0 55.1 53.96 4.0 35275 50600 575 1163 25.5
25/5/14 14:00 297.3 378.2 54.8 53.77 3.7 35344 50700 569 1152 25.5
26/5/14 16:00 297.6 378.5 55.2 54.22 4.0 35344 50700 561 1136 25.5
27/5/14 19:00 295.4 378.2 54.9 53.90 4.1 35275 50600 561 1137 25.3
28/5/14 17:00 297.1 378.6 55.3 54.26 3.9 35414 50800 555 1124 25.4
29/5/14 21:00 297.7 378.5 54.7 53.65 3.5 35344 50700 551 1117 25.3
30/5/14 13:00 297.3 378.6 54.9 53.92 3.9 35344 50700 551 1117 25.5
31/5/14 17:00 296.9 378.7 54.8 53.82 3.8 35344 50700 547 1109 25.4
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FTNORM - 1 Stage Calculation Section
20
Reverse Osmosis Plant
Operating Data Normalization
Plant Identification: Train 1 C
Feed
Flow
Days of
Operation
Recovery
(%)
Differential
Pressure
Temperature
Correction
Factor
Calculated
Feed/Brine
Avg Conc
Feed/Brine
Osmotic
Pressure
Permeate
Osmotic
Pressure
Net Driving
Pressure
Normalized
Permeate
Flow
Normalized
Permeate
Salt Passage
Normalized
Permeate
Salt
Rejection
677 1 44% 0.99 1.012 46378 38.6 0.5 12.9 297 1.7% 98.3%
677 2 44% 1.03 1.015 46688 38.8 0.5 12.7 301 1.6% 98.4%
675 3 44% 0.99 1.015 46464 38.6 0.4 12.8 298 1.6% 98.4%
674 4 44% 1.01 1.009 46525 38.7 0.4 12.8 297 1.6% 98.4%
676 5 44% 1.01 1.015 46491 38.7 0.4 12.8 297 1.6% 98.4%
674 7 44% 0.99 1.009 46583 38.7 0.5 12.7 302 1.8% 98.2%
676 8 44% 0.97 1.009 46022 38.2 0.5 12.6 304 1.8% 98.2%
674 9 44% 0.91 1.009 45842 38.1 0.5 12.9 297 1.7% 98.3%
675 10 44% 1.02 1.018 45756 38.0 0.5 12.6 300 1.7% 98.3%
688 11 44% 1.03 1.021 45474 37.8 0.5 13.0 295 1.7% 98.3%
673 12 44% 0.98 1.018 45665 38.0 0.5 12.8 295 1.6% 98.4%
677 13 44% 1.03 1.027 45589 37.9 0.5 13.1 288 1.7% 98.3%
674 14 44% 1.01 1.027 45839 38.1 0.5 12.6 299 1.6% 98.4%
676 15 44% 1.01 1.012 45765 38.0 0.4 13.1 292 1.6% 98.4%
676 16 44% 0.97 1.012 45650 37.9 0.4 13.1 292 1.6% 98.4%
674 17 44% 1.01 1.009 45963 38.2 0.4 12.9 296 1.6% 98.4%
673 18 44% 1.02 1.018 45855 38.1 0.4 12.9 294 1.6% 98.4%
675 19 44% 1.01 1.018 45936 38.2 0.4 12.9 294 1.6% 98.4%
673 22 44% 0.99 1.009 46709 38.8 0.5 12.2 313 1.6% 98.4%
674 23 44% 1.01 1.009 46366 38.5 0.5 12.3 309 1.6% 98.4%
676 24 44% 1.11 1.015 46416 38.6 0.5 12.4 307 1.6% 98.4%
676 25 44% 1.02 1.015 46580 38.7 0.5 12.3 311 1.5% 98.5%
676 26 44% 0.99 1.015 46582 38.7 0.4 12.5 306 1.5% 98.5%
674 27 44% 0.97 1.009 46429 38.6 0.4 12.2 313 1.5% 98.5%
676 28 44% 1.03 1.012 46656 38.8 0.4 12.5 306 1.5% 98.5%
676 29 44% 1.02 1.009 46585 38.7 0.4 12.4 311 1.5% 98.5%
676 30 44% 1.01 1.015 46570 38.7 0.4 12.2 313 1.5% 98.5%
676 31 44% 0.99 1.012 46555 38.7 0.4 12.2 312 1.5% 98.5%
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FTNORM 1 Stage
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0
100
200
300
400
500
0 5 10 15 20 25 30 35
Perm
eate
Flo
w (
m3/h
r)
Operating Time (days)
Normalized Permeate Flow
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FTNORM 1 Stage
22
95.0%
96.0%
97.0%
98.0%
99.0%
100.0%
0.0%
1.0%
2.0%
3.0%
4.0%
5.0%
0 5 10 15 20 25 30 35
Salt
Reje
cti
on
(%
)
Salt
Pas
sa
ge (
%)
Operating Time (days)
Normalized Salt Passage and Salt Rejection
Salt Passage Salt Rejection
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FTNORM 1 Stage
23
0.0
0.5
1.0
1.5
2.0
2.5
3.0
0 5 10 15 20 25 30 35
Pre
ssu
re (
bar)
Operating Time (days)
Differential Pressure
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FTNORM available from the web:
Go to: www.dowwaterandprocess.com
Click on Answer Center and enter FTNORM in search field
Click on FTNORM System Data Normalization Download
Download and save FTNORM spreadsheet appropriate for your system
Follow instructions for setup and entering data into FTNORM
One-stage system:
US Units (gpm psig)
Metric Units (m3/hr bar)
Metric Units (m3/hr kg/cm2)
Two-stage system:
US Units (gpm psig)
Metric Units (m3/hr bar)
Metric Units (m3/hr kg/cm2)
Additional FTNORM features available from DWPS TS&D:
Three-stage systems
Permeate backpressure
Boost pumps
Energy recovery devices
Data entry macro
Normalized DP
Specific flux
http://www.dowwaterandprocess.com/
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Conclusions
Track the performance of RO trains in order to identify
problems early.
RO systems react to variation in feed water
characteristics and operating conditions.
RO data normalization allows the RO operator to
distinguish between normal variation in performance and
potential problems.
Use normalization software such as FTNORM to easily
trend the important performance variables and review
the data frequently.
25
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Questions?
26
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Thank You!
Steven D. Coker [email protected]
http://www.dowwaterandprocess.com/