Watertrak - Model 46,000 ppm TDS - Seawater Reverse Osmosis (SWRO) Brochure

 Aquatech International CorporationOne Four Coins DriveCanonsburg, PA 15317 USA724-746-5300 / www.aquatech.comStandard Features• 8” FRP Membrane Housing with 1200 psig (80 bar) Rating• Sea Water TFC Polyamide Low Energy HR Membrane or Equal• Seven RO Elements per Pressure Tube with 400 ft2 Membrane Area• Duplex 2205 Stainless Steel High Pressure Piping• Schedule 80 PVC Low Pressure Piping• High Pressure Multistage Centrifugal Pump in Duplex Material• Hydraulic Turbo Charger Energy Recovery Device• Variable Frequency Drive (VFD) for High Pressure Pump in NEMA One Enclosure• Five Micron Nominal Cartridge Filter in GRP/FRP Housing• Victaulic Cleaning Connections• Digital Instrumentation• Flow Transmitter – Feed & Permeate• Conductivity – Permeate• ORP – Feed• Pressure Indicator – CF Inlet/Outlet, Pump Discharge, RO Feed, Permeate, Concentrate• Pressure Switch – Pump Suction, RO Feed, Permeate & Concentrate• NEMA 4X FRP Local Control Box• Allen Bradley PLC with Panel View 600 HMI• Automatic Valves for Flushing on ShutdownNote: VFD will be provided as lose supply.Seawater Reverse Osmosis (SWRO)46,000 ppm TDS Seawater29-177 gpm (6.6 – 40.2 m3/h)Upgrade Options• Single or Dual Stage Multi-Media Filters Considering Type of Feed Water Intake• pH Analyzer on RO Feed• Clean-in-Place (CIP) System• Chemical Dosing Units• Ultrafiltration• Pressure Exchanger Instead of Turbo Charger• Five Element per Pressure Vessel Design for Cases with Limited Space Available• Containerized Option AvailableDesign Feed Conditions• Recovery – 30% - 35%• Design Temperature - 72°F (22°C)• Design Feed TDS – 46,000 ppm• Feed Water SDI < 5• Feed Water Inlet Pressure – 30 psig (2 bar) . Aquatech WATERTRAK™ SWRO Models 46,000 PPM TDS MODEL AIC-SW-2V-14E AIC-SW-3V-21E AIC-SW-5V-35E AIC-SW-6V-42E AIC-SW-10V-70E AIC-SW-12V-84E Permeate Flow: 158 m3/d 240 m3/d 403 m3/d 500 m3/d 800 m3/d 1000 m3/d 6.6 m3/h (29 gpm) 10 m3/h (44 gpm) 16.8 m3/h (74 gpm) 20.8 m3/h (91.6 gpm) 33.4 m3/h (147 gpm) 41.7 m3/h (183.5 gpm) Feed Flow: 21.5 m3/h (95 gpm) 32.5 m3/h (143 gpm) 54 m3/h (238 gpm) 67 m3/h (295.5 gpm) 108 m3/h (475 gpm) 134.5 m3/h (592 gpm) Concentrate Flow: 14.9 m3/h (66 gpm) 22.5 m3/h (99 gpm) 37.2 m3/h (164 gpm) 46.2 m3/h (203.9 gpm) 74.6 m3/h (328 gpm) 92.8 m3/h (408.5 gpm) Membrane Elements and Vessels Vessel quantity: 2 3 5 6 10 12 No. Elements: 14 (7 per vessel) 21 (7 per vessel) 35 (7 per vessel) 42 (7 per vessel) 70 (7 per vessel) 84 (7 per vessel) High Pressure Feed Pump Model: MSS-20-29 MSS-30-27 MSS-50-28 MSS-70-34 MSS-90-21 MSS-160-11 Manufacturer FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal Motor HP / Type: 60 Hp (44.7 kW) TEFC 75 Hp (55.9 kW) TEFC 125 Hp (93.2 kW) TEFC 150 Hp (112 kW) TEFC 200 Hp (150 kW) TEFC 250 Hp (186 kW) TEFC Design Flow Rate: 21.5 m3/h (95 gpm) 32.5 m3/h (143 gpm) 54 m3/h (238 gpm) 67 m3/h (295.5 gpm) 108 m3/h (475 gpm) 134.5 m3/h (592 gpm) Discharge Pressure: 647 psig (44.6 barg) 610 psig (42.1 barg) 606 psig (41.8 barg) 592 psig (40.8 barg) 579 psig (39.9 barg) 570 psig (39.3 barg) Energy Recovery Device Model: HPBe-30 HPBe-40 HPBe-60 HPBe-80 HPBe-120 HPBe-160 Manufacturer: FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal FEDCO® or equal Pressure Boost: 403 psig (25.1 barg) 440 psig (30.3 barg) 444 psig (30.6 barg) 458 psig (31.6 barg) 471 psig (32.5 barg) 480 psig (33.1 barg) Cartridge Filter Filter Quantity: 1 1 1 1 2 2 Cartridge Quantity Each: 6 10 20 20 20 20 Installation and Utility Requirements Inlet: 2.0” flanged 3.0” flanged 3.0” flanged 4.0” flanged 6.0” flanged 6.0” flanged Permeate: 1.5” flanged 2.0” flanged 2.0” flanged 3.0” flanged 4.0” flanged 4.0” flanged Concentrate: 2.0” flanged 2.0” flanged 3.0” flanged 3.0” flanged 4.0” flanged 4.0” flanged Inlet Water Pressure: 30 psig 30 psig 30 psig 30 psig 30 psig 30 psig Air Pressure: 80 psig, oil free 80 psig, oil free 80 psig, oil free 80 psig, oil free 80 psig, oil free 80 psig, oil free SWMO46000 SWRO 46000 TDS_Part2