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Table 10.6.2. - Brxkish water reverse osmosis membranes by producer, MAX PRESSURE OPERATING p” CLEANING ‘ACTURER ,mion System. MDDELI MAX DROP, MAX MAXMAX .----------- kPa ELEMENT SD, NTU *C MIN MAX MIN MAX CONC. VESSEL VESSEL ,kgI CD404DF CDS04OF CE404DF CE8D40F ND404OF ND804OF SE404OF SE8040F SG404OF SGBMOF SH4G4OF SHBO40F 89 OS40 89 OS80 SW304040 Bw308040 402, LP 422, “Pi 4221 SD 423, HR 4231 SD 4821 LP 4826 LP 8021 LP 8021 MP 8221 till 8221 SD 8231 HR 8231 SD 2DO0 2896 882, LP zoo0 1551 3.0 8.0 1.0 3.0 8.0 1.0 3.0 8.0 1.0 3.0 8.0 1.0 2.0 11.5 LOW 2.0 11.5 LOW 2.0 11.5 LOW 2.0 11.5 LOW 2.0 11.5 0.1 2.0 11.5 0.1 2.0 11.5 0.1 2.0 11.5 0.1 2.3 11.9 0.0 2.3 11.9 0.0 1.0 12.0 0.1 1.0 (2.0 0.1 B ----.- TESTlNG CDNDITION --- mg/L % TEMP. N.CI kP, RECDVERY -2 p” 10 25 3103 10 25 4137 10 25 3103 10 25 4137 10 25 4137 10 25 4137 10 25 4137 10 25 4137 10 25 7.8 4137 10 25 7.8 4137 to 25 7.8 4137 10 25 7.8 2758 75 25 2758 75 25 4137 15 25 8.0 4137 15 25 8.0 4137 10 25 5.7 4137 10 25 5.7 4137 10 25 5.7 4137 18 25 5.7 4137 18 25 5.7 2413 10 25 7.5 2089 10 25 7.5 2413 to 25 5.7 4137 59 10 25 5.7 4137 103 10 25 5.7 4137 103 10 25 5.7 4137 to3 16 25 5.7 4137 103 16 25 5.7 4137 69 10 25 7.5 ,551 89 pii t.mX I MAX SHIPPED CONT. DX.ELEMENTS REC., WEIGHT too0 2758 lDD0 2758 IDDO 2758 loo0 2758 too0 2758 too0 2758 low 2758 lM)o 2758 too0 1379 IDo0 ,379 too0 ,034 too0 1034 ,500 2758 1500 2758 2000 1551 2000 1544 2cmO 2896 2000 2898 2000 2891) 2Om 2898 2000 2898 2Ow 1551 2D30 1551 2OaO 1551 2000 2896 2wO 28W 2om 28w) 2000 2890 5 5 5 5 5 5 5 5 5 5 5 5 3 4 5 5 t 35 5.0 8.5 1 35 5.0 8.5 t 35 5.0 6.5 1 5.0 8.5 t 50 4.0 11.0 1 50 4.0 11.0 1 50 4.0 11.0 1 50 4.0 11.0 t 50 4.0 tt.0 1 50 4.0 11.0 1 50 4.0 11.0 1 50 4.0 11.0 4.0 (1.0 40 4.0 11.0 1 45 2.0 11.0 1 45 2.0 11.0 1 45 5.0 10.0 1 40 t 40 3.0 7.0 1 40 4.0 0.0 1 40 3.0 7.0 t 45 4.0 11.0 t 45 4.0 11.0 1 45 5.0 10.0 1 45 5.0 10.0 1 40 4.0 6.0 t 40 3.0 7.0 t 40 4.0 6.0 t 3.0 7.0 1 45 4.0 11.0 053 15 053 15 s53 15 11 53 5 8 53 11) 8 53 18 (I 53 5 e 53 1s 0 18 0 53 5 0 53 ,.3 (I 53 to 1 50 59 2 50 113 I3 50 4.5 11.0 0.0 1.0 3.0 8.0 1.0 3.0 7.0 1.0 3.0 8.0 1.0 2.5 11.0 0.0 2.5 11.0 0.0 4.5 11.0 0.0 4.5 11.0 0.0 3.0 7.0 1.0 3.0 8.0 1.0 3.0 7.0 1.0 2.5 8.0 1.0 2.5 11.0 0.0 e 53 5 5 (I 53 5 4 55 7 55 7 ii 53 5 3 40 5 s 53 18 0 53 1s 0 53 18 0 53 1s 4 55 20 4 55 28 0 53 (8PDF Image | DESALTING AND WATER TREATMENT MEMBRANE
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