FILMTEC flatsheet membranes can be derived from the published flow specification of therespective membrane element and the published value of the active membrane area of thatelement.After the baseline is established, the biocide is then added continuously for at least 1000hours. The normalized permeate flow and salt passage should remain relatively constantduring this time for the chemical to be deem compatible. The upper concentration limit forcompatibility will be the maximum concentration of the chemical in the concentration stream.MembranePreservativesMembrane preservatives are biocide solutions used to prevent biogrowth and change inmembrane performance during extended storage times. Thus, the biocide used must have along lifetime. Surfactants and/or humectants are often present in the solution to keep themembrane wet. Consequently, any of those compounds could affect the membrane negativelyeither in directly or indirectly by interacting with other parts of the element and the formation ofcompounds harmful to the membrane.A compatible membrane preservative should not exhibit any significant decrease in waterpermeability or salt rejection properties of the membrane element during one year storage. Ameans to perform the test is to store five tested elements fully immersed in the storage solutionand test one of them after 2, 4, 6 and 12 months storage. A new element is tested each timeand is returned to the storage solution following the test. The fifth element is included in the testas a spare to use if the test data of any of the other elements is in doubt. Two elements storedin the present storage solution, one percent sodium bisulfite, should be used as controls. Theseare tested at the same time as any one of the other five elements. If the membraneperformance in the preservative solution is maintained, the same test should continue for yearswith element test once or twice yearly to learn about the lifetime of the storage solution.Before wet elements are stored, the elements are initially soaked in the storage solution forabout one hour and then drained and bagged. There should not be any biological growth in thebag or deterioration of the bagged elements performance during the shelf life of the storagesolution. To examine whether another membrane preservative solution can be used for baggedelement storage, elements are tested and then soaked for 1, 2 or 20 hours in the membranepreservative solution. Then the elements are drained and bagged. After 2, 6, 12, 18, 24, 36 and48 months storage, two elements from each soak time are taken out from their bags. Microbialplate counts are taken of the storage solution in the bag, and the elements are tested. Theelement performance is measured both before and after permeate pressure is applied todetermine whether the membrane dries when stored. Permeate pressure is most easily appliedby shutting the permeate port at a feed pressure of at least 150 psi (1,000 kPa) pressure abovethe osmotic pressure of the feed solution. Three soak times, seven test times, and duplicateelements, result in 42 elements per storage solution to test. To save storage space, smallelements are often used. Again, the one percent sodium bisulfite solution is used as a control.Since one-hour soak time is sufficient for the control, only 14 control elements are required.†This section is pulled Form No. 609-00291Page 176 of 180 ® Trademark of The Dow Chemical <strong>Company</strong> ("Dow") or an affiliated company of Dow Form No. 609-00071
9.12 Key Word IndexAbrasion - 150 Burn test - 146 Conductivity meter - 97Acid addition - 27 B-value - 90 Conductivity profile - 140-141Acid cleaner - 126 Continuous process - 75, 76Acridine orange - 59 CAC - 60 Continuous test - 171, 175-177Activated carbon - 59, 62, 64, 65 Calcium - 26-29, 47 Control instruments - 97Adsorption - 65 Calcium carbonate - 27, 28, 32 Copper sulfate - 64Agglomeration - 52 Calcium fluoride - 28, 43 Corrosion - 65, 99, 148Air - 110, 149, 153 Calcium phosphate - 28, 51 Coupler - 106Air break - 98, 112 Calcium sulfate - 40, 42 CRC - 61AISI - 99 Calibration - 138 Crevice corrosion - 99Alarms - 98 Carbon dioxide - 29, 32, 36, 81, 169 Crossflow - 10Al-bronze - 99 Carbonate scaling - 28-29, 32-39, 126, 129, 148Algea - 58 Cartridge filter - 56, 153 DBNPA - 63Alkaline cleaner - 126 Cationic polymers/polyelectrolytes - 28, 52, 150, Dealkalization - 28, 40174Aluminum - 28, 47, 51, 66, 69, 148 Centrifugal pump - 95 Dechlorination - 60Aluminum coagulants - 55, 56 CF - 31, 95 Degasifier - 68Aluminum silicates - 66 CFU - 59 Delamination - 143Ammonium - 55 Check list - 109 Desalination - 9Anoxic - 55, 65, 66, 67 Chemical compatibility - 171-177 Design equations - 90-93Anthracite - 54 Chloramine - 61, 63 Design guidelines - 82-84Antifoulant - 28, 57 Chlorinated biocidal products - 134 Destructive analysis - 144Antiscalant - 28, 33, 56, 58, 66, 154, 173-174 Chlorination - 60 Detergent - 150AOC - 59 Chlorine - 56, 58, 60, 69, 98 Diatomaceous earth - 153Apatite - 51 Chlorine demand - 61 Differential pressure - 54, 57, 58, 123, 146, 152-154Apparent salt passage - 79 Chlorine dioxide - 62, 63, 134 Direct count - 59Application test - 94 Chlorine tolerance - 16, 61, 63 DIRECTOR Service - 142Applications - 11 Clay - 66 Disposal - 136ASTM - 25, 142 Cleaning chemicals - 126, 174-175 Distillation - 9ATP - 60 Cleaning frequency - 82, 139, 174 Dosing pump - 96Automation - 98 Cleaning procedure - 125 Dosing tank - 98Autopsy - 144, 151 Cleaning pump - 125 Double pass - 84, 112A-value - 90 Cleaning solution - 123, 125, 139 Dow sales offices - 181Cleaning system - 124 DOWEX - 28Back-flow - 67, 97 Cleaning tank - 124 Draw-back - 67, 97, 113Backflushable filter - 56 Cleaning test - 142, 144, 175 Dry element - 135, 136Backwash - 54 Clean-in-place (CIP) - 97, 101Bacteria - 58-59 Coagulant - 56, 174 EDXRF - 145, 148Bank filtration - 64 Coagulation-flocculation - 56 Electrodialysis - 10Barium - 28, 29 COD - 69 Element construction - 18Barium sulfate - 42 Colloidal fouling - 52-57, 147 Element outer wrap - 20Barrier layer - 15 Colloidal silica - 47, 56 Element performance - 20, 144Batch process - 75, 84, 97 Combined chlorine - 63 Element removal - 104Beta number - 79 Compaction - 149 Element replacement - 149BFR - 60 Compatibility - 171-177 Element size - 20Biocides - 63, 132, 133, 175-177 Computer program - 90 Element spacer - 81, 106Biofilm - 58, 126, 139, 146 Concentrate recycling/recirculation - 76, 78, 84 Element types - 19, 85Biofiltration - 64 Concentrate valve - 13, 76, 110 Emergency cleaning - 132Biofouling/biological fouling - 21, 58-65, 100, 132, Concentration factor - 31, 95 End cap - 102146, 154Birm - 55 Concentration polarization - 58, 89, 91 Energy consumption - 23Booster pump - 81 Concentration units - 167 Energy recovery - 95Brackish water - 24 Conditioning - 134 Equipment - 102, 107Brine seal - 102, 153-154 Conductance - 164 ESCA - 145Bromide - 61 Conductivity - 81, 112, 116, 165-166 Ethanol - 136Page 177 of 180 ® Trademark of The Dow Chemical <strong>Company</strong> ("Dow") or an affiliated company of Dow Form No. 609-00071
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DowWater SolutionsFILMTEC Reverse O
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2.6 Biological Fouling Prevention .
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1. Basics of Reverse Osmosis and Na
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Nanofiltration (NF)Nanofiltration r
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How to Use Reverse Osmosis and Nano
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1.4 Membrane DescriptionThe FILMTEC
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Membrane systems are typically desi
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1.8 Element CharacteristicsFILMTEC
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2. Water Chemistry and Pretreatment
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SeawaterSeawater with TDS of 35,000
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Table 2.5 Water analysis for RO/NFS
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Table 2.7 Solubility products of sp
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In this process, only Ca 2+ , Ba 2+
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For the concentration ranges presen
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The conditions for CaCO 3 scale con
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Figure 2.3 Langelier saturation ind
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These computations have been descri
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Figure 2.5 “K” versus ionic str
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Figure 2.6 Ksp for CaSO 4 versus io
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2.4.6 Calcium Fluoride Scale Preven
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Figure 2.8 K sp for SrSO 4 versus i
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2.4.7 Silica Scale PreventionDissol
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Table 2.10 Solubility of SiO 2 vers
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2.4.8 Calcium Phosphate Scale Preve
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Table 2.9 Various fouling indicesIn
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Frequent shutdowns and start-ups sh
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If the differential pressure across
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1. Intake (surface) or well, before
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or combined residual chlorine (CRC)
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2.6.5 DBNPADBNPA (2,2, dibromo-3-ni
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2.6.11 Use of Fouling Resistant Mem
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2.11 Treatment of Feedwater Contain
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2.13 Summary of Pretreatment Option
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26. Handbook of Industrial Membrane
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Table 3.1 System design information
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3.2 Batch vs. Continuous ProcessAn
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3.4 Single-Stage SystemIn a single-
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The apparent salt passage of the sy
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Instead of having a separate high-p
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3.9.1 Membrane System Design Guidel
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In Table 3.6, the small commercial
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Table 3.8 Number of stages of a sea
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3.11 System Performance Projection3
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3.11.2 Design Equations and Paramet
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Table 3.10 Design equations for pro
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3.11.3 Comparing Actual Performance
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The high-pressure concentrate is fe
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If the product water from an RO sys
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Besides the above recommendations,
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4. Loading of Pressure VesselsThis
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The process of shimming is performe
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4.5.2 Summary of Large Element Inte
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5. System Operation5.1 Introduction
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5.2.3 Start-Up SequenceProper start
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5.2.4 Membrane Start-Up Performance
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5.5.3 SeawaterIn principle, the ope
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Table 5.1 Reverse osmosis operating
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A. Normalized Permeate FlowQS=ΔPsP
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For the operating conditions we hav
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4. During recirculation of cleaning
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2. The cleaning pump should be size
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