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< Project Description >
Flow Diagram
Tag 1 2 3 4 5 6 7 8 9 10Flow(m3/hr) 445,50 445,50 445,50 244,80
200,70 75,10 125,60 14,20 111,40 334,10Press(Bar) 0,00 0,00 10,00
0,00 8,80 0,00 7,40 0,00 5,20 0,00TDS(mg/l) 1.566,6 1.617,8 1.617,8
13,7 3.574,6 42,4 5.688,3 142,6 6.394,4 25,7
Tag 11 12 13 14 15 16 17 18 19 20Flow(m3/hr) 334,1 334,1 209,0
125,2 64,3 60,9 10,8 50,1 284,0 284,0Press(Bar) 0,0 7,7 0,0 5,7 0,0
3,7 0,0 0,3 0,0 0,0TDS(mg/l) 25,7 25,7 0,5 67,8 1,5 137,8 4,5 166,4
0,8 0,8
System Configuration
Designated Product Flow 334,12 m3/hr No. of Pressure Vessel
76Membrane Type and Model RE8040-BE No. of Element 456Array
Configuration 3 Array, 42-22-12 , 6 elements/pressure vesselRecover
Ratio 75 % Average Permeate Flux 19,72 lmh
Designated Product Flow 284,00 m3/hr No. of Pressure Vessel
36Membrane Type and Model RE8040-BLN No. of Element 216Array
Configuration 3 Array, 22-10-4 , 6 elements/pressure vesselRecover
Ratio 85 % Average Permeate Flux 35,39 lmh
Project Notedd
CSMPRO v5.0Project Name : dd (PJT ver. 1.0)Projected By dd (dd)
/ ddFile Name: dd.csm3 (31/12/2014) Printed on 31/12/2014
NO GUARANTEE of system performance is expressed or implied.Any
final design should be reviewedby an appropriate application
engineer.These calculations are based on a feed water of acceptable
quality.Toray Chemical Korea Inc.http://www.csmfilter.com
PAGE: 1 OF 6
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< Projection Results >
Projection Details :
Feed flow into RO system 445,49 m3/hr Membrane Age 0,00
year(s)Permeate Flow 334,12 m3/hr Flux decline rate 7,00 %/yearPass
Recovery 75,00 % Salt passage increase 10,00 %/yearFeed TDS 1617,8
mg/L Average permeate flux 19,72 lmhPermeate TDS 25,66 mg/L Feed
Osmotic Pressure 1,22 BarConcentrate TDS 6.394,3 mg/L Concentrate
Osmotic Pressure 4,74 BarSalt rejection 98,41 % Chfem. dose 0,00
mg/LFeed Pressure 9,98 Bar Permeate Blending 0,00 m3/hrTemperature
25,00 C Softener YesFeed water type Sea Water SDI
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< Projection Results >
Projection Details :
Feed flow into RO system 334,12 m3/hr Membrane Age 0,00
year(s)Permeate Flow 284,00 m3/hr Flux decline rate 5,00 %/yearPass
Recovery 85,00 % Salt passage increase 5,00 %/yearFeed TDS 25,66
mg/L Average permeate flux 35,39 lmhPermeate TDS 0,83 mg/L Feed
Osmotic Pressure 0,02 BarConcentrate TDS 166,4 mg/L Concentrate
Osmotic Pressure 0,13 BarSalt rejection 96,77 % Chfem. dose 0,00
mg/LFeed Pressure 7,67 Bar Permeate Blending 0,00 m3/hrTemperature
25,00 C Softener YesFeed water type RO/UF Permeate SDI
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< Water Quality Details >
Unit RawWaterFeedWater
Concentrate Permeate ProductStage1 Stage2 Stage3 Total Stage1
Stage2 Stage3NH4 as Ion 0,8 0,8 1,8 2,8 3,1 0,02 0,01 0,04 0,14
0,02K as Ion 34,0 34,0 75,0 119,3 134,0 0,67 0,36 1,11 3,72 0,67Na
as Ion 420,0 567,1 1.253,4 1.995,1 2.243,1 8,42 4,51 13,91 46,82
8,42Mg as Ion 50,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00Ca as
Ion 46,0 0,1 0,2 0,4 0,4 0,00 0,00 0,00 0,00 0,00Sr as Ion 0,0 0,0
0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00Fe as Ion 0,2 0,2 0,4 0,7 0,8
0,00 0,00 0,00 0,01 0,00Ba as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00
0,00 0,00 0,00HCO3 as Ion 200,0 200,0 440,8 699,7 785,3 4,92 2,64
8,12 27,24 4,92NO3 as Ion 5,9 5,9 13,0 20,6 23,1 0,18 0,10 0,30
1,00 0,18Cl as Ion 733,4 733,4 1.621,0 2.580,2 2.901,0 10,88 5,83
17,99 60,56 10,88F as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00
0,00Boron as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00SO4 as
Ion 75,0 75,0 166,1 265,0 298,3 0,56 0,30 0,92 3,12 0,56SiO2 as Ion
0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00CO2 as Ion 3,6 3,6 3,6
3,6 3,6 3,56 3,56 3,56 3,56 3,56CO3 as Ion 1,3 1,3 2,9 4,6 5,2 0,00
0,00 0,01 0,02 0,00pH - 7,9 7,9 8,2 8,4 8,5 6,35 6,08 6,56 7,08
6,35TDS mg/L 1.566,6 1.617,8 3.574,6 5.688,3 6.394,4 25,66 13,74
42,41 142,63 25,66SDI - 0,0 - - - - - - - - -TOC mg/L 0,0 - - - - -
- - - -COD mg/L 0,0 - - - - - - - - -BOD mg/L 0,0 - - - - - - - -
-Hardness as CaCO3 320,00 0,25 0,55 0,88 0,99 0,00 0,00 0,00 0,01
0,00
CSMPRO v5.0Project Name : dd (PJT ver. 1.0)Projected By dd (dd)
/ ddFile Name: dd.csm3 (31/12/2014) Printed on 31/12/2014
NO GUARANTEE of system performance is expressed or implied.Any
final design should be reviewedby an appropriate application
engineer.These calculations are based on a feed water of acceptable
quality.Toray Chemical Korea Inc.http://www.csmfilter.com
PAGE: 4 OF 6
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< Water Quality Details >
Unit RawWaterFeedWater
Concentrate Permeate ProductStage1 Stage2 Stage3 Total Stage1
Stage2 Stage3NH4 as Ion 0,0 0,0 0,1 0,1 0,2 0,00 0,00 0,00 0,01
0,00K as Ion 0,7 0,7 1,8 3,6 4,3 0,03 0,01 0,04 0,14 0,03Na as Ion
8,4 8,4 22,3 45,3 54,8 0,24 0,13 0,42 1,31 0,24Mg as Ion 0,0 0,0
0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00Ca as Ion 0,0 0,0 0,0 0,0 0,0
0,00 0,00 0,00 0,00 0,00Sr as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00
0,00 0,00 0,00Fe as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00
0,00Ba as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00HCO3 as
Ion 4,9 4,9 12,9 26,1 31,5 0,23 0,12 0,40 1,24 0,23NO3 as Ion 0,2
0,2 0,5 1,0 1,1 0,01 0,01 0,02 0,06 0,01Cl as Ion 10,9 10,9 28,8
58,6 70,8 0,31 0,16 0,54 1,70 0,31F as Ion 0,0 0,0 0,0 0,0 0,0 0,00
0,00 0,00 0,00 0,00Boron as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00
0,00 0,00SO4 as Ion 0,6 0,6 1,5 3,0 3,7 0,01 0,00 0,01 0,04
0,01SiO2 as Ion 0,0 0,0 0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00CO2 as
Ion 3,6 3,6 3,6 3,6 3,6 3,56 3,56 3,56 3,56 3,56CO3 as Ion 0,0 0,0
0,0 0,0 0,0 0,00 0,00 0,00 0,00 0,00pH - 6,4 6,4 6,8 7,1 7,1 5,02
4,75 5,27 5,75 5,02TDS mg/L 25,7 25,7 67,8 137,8 166,4 0,83 0,45
1,45 4,49 0,83SDI - 0,0 - - - - - - - - -TOC mg/L 0,0 - - - - - - -
- -COD mg/L 0,0 - - - - - - - - -BOD mg/L 0,0 - - - - - - - -
-Hardness as CaCO3 0,00 0,00 0,00 0,01 0,01 0,00 0,00 0,00 0,00
0,00
CSMPRO v5.0Project Name : dd (PJT ver. 1.0)Projected By dd (dd)
/ ddFile Name: dd.csm3 (31/12/2014) Printed on 31/12/2014
NO GUARANTEE of system performance is expressed or implied.Any
final design should be reviewedby an appropriate application
engineer.These calculations are based on a feed water of acceptable
quality.Toray Chemical Korea Inc.http://www.csmfilter.com
PAGE: 5 OF 6
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< Additional Information >
Scale Calculation
PASS 1 PASS 2Raw Water Feed Water Concentrate Raw Water Feed
Water Concentrate
pH 7,897 7,900 8,449 6,347 6,347 7,140LSI 0,278 -2,366 -0,839
-6,607 -6,607 -5,019Stiff & Davis Index -0,094 -2,744 -1,196
-7,194 -7,194 -5,524Ionic Strength (molal) 0,030 0,026 0,104 0,000
0,000 0,003TDS (mg/L) 1.566,620 1.617,800 6.394,347 25,658 25,658
166,426HCO3 (mg/L) 200,000 200,000 785,270 4,915 4,915 31,481CO3
(mg/L) 1,302 1,302 5,195 0,004 0,004 0,027CO2 (mg/L) 3,556 3,556
3,556 3,556 3,556 3,556CaSO4 (%Saturation) 0,664 0,002 0,010 0,000
0,000 0,000BaSO4 (%Saturation) 0,000 0,000 0,000 0,000 0,000
0,000SrSO4 (%Saturation) 0,000 0,000 0,000 0,000 0,000 0,000CaF2
(%Saturation) 0,000 0,000 0,000 0,000 0,000 0,000SiO2 (%Saturation)
0,000 0,000 0,000 0,000 0,000 0,000
< Scale recommendation >No recommendation.
CHEMICAL CONSUMPTION :No Chemical.
COST ANALYSIS :
1st Pass 2nd Pass TotalCapital Specific Cost ($/m3) 0 0
0Operating Specific Cost ($/m3) 0 0 0Total Specific Cost ($/m3) 0 0
0
ERRORS & WARNINGS :
recommendations and Errors :No Error.
No recommendation.
CSMPRO v5.0Project Name : dd (PJT ver. 1.0)Projected By dd (dd)
/ ddFile Name: dd.csm3 (31/12/2014) Printed on 31/12/2014
NO GUARANTEE of system performance is expressed or implied.Any
final design should be reviewedby an appropriate application
engineer.These calculations are based on a feed water of acceptable
quality.Toray Chemical Korea Inc.http://www.csmfilter.com
PAGE: 6 OF 6
