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| LOW PRESSURE ELEMENTS > 1812-HM1-LPE | 2540-HM1-LPE | 8040-HM1-LPE | |||||
| Low Pressure Elements | ||
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| Membrane Element 4040-HM1-LPE | ||
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| Performance | Permeate Flow Salt Rejection-nominal | 2600 gpd (9.8 m3/d) 99.0% |
| Type | Configuration Membrane Polymer Nominal Membrane Area | Spiral wound Composite Polyamide 85 ft 2 |
| Operating Limits & Application Data | Maximum Applied Pressure Maximum Chlorine Concentration Maximum Operating Temperature Feedwater pH Range Maximum Feedwater Turbidity Maximum Feedwater SDI (15 mins) Maximum Feed Flow Minimum Ratio of Concentrate to Permeate Flow for any Element Maximum Pressure Drop for each Element |
600 psig (4.16 MPa) < 0.1 ppm 113 °F (45 °C) 3.0 - 10.0 1.0 NTU 4.0 16 GPM (3.6 m3/h) 5:1 10 psi. |
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| A | inches | (mm) | B | inches | (mm) | |
| 40.00 | (1016) | 3.95 | (100.3) | |||
| C | inches | (mm) | D | weight | lbs. (kg) | |
| 0.75 | (38.1) | 8 | (3.6) |
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| Test Conditions | : | The stated performance is initial (data taken after 30 minutes of operation), based on the following conditions: 1500 PPM NaCl solution,applied pressure- 10.5 kg/ sq.cm2 (150 psi), operating temperature- 77 °F (25 °C) ,15% permeate recovery-15% and pH range 6.5 - 7.0 . |
| Note | : | Minimum permeate flow for individual elements may vary to + or - 15 percent of nominal. All membrane elements are supplied with a brine seal. Elements are vacuum sealed in a polyethylene bag containing a 1.5 % sodium bisulfite solution and 20% propylene glycol solution, and then packaged in a cardboard box. |
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