| Startup Year | 1993 |
| Process | NF/RO |
| Capacity (MGD) | 12; 8MGD BWRO being added |
| Recovery Rate (%) | 90 |
| Pretreatment | sulfuric acid, anti-scalant, cartridge filtration |
| Post-Treatment | degasification |
| Feed Water Composition | significant hydrogen sulfide |
| Product Water Composition | TDS = 196 mg/L; ph = 8.05 |
| Concentrate Composition | precipitated sulfides |
| Concentrate Disposal | injection well |
| CAPITAL COST ($000) | O & M COSTS ($000) | ||||||||||||||||||||||
| Building | Electric Power | 307 | |||||||||||||||||||||
| Plant Equipment | Steam |
| Wells or feed intake | | O&M Personnel | 575 | Product tanks |
| Parts, Chemicals | 600 | Brine Disposal |
| Replacement Membranes | 5 | Other costs |
| Not specified | | TOTAL | 26,000 | TOTAL | 1487 | | |
*Source: Leitner & Associates, Survey of U. S. Costs and Water Rates for Desalination and Membrane Softening Plants, Water Treatment Technology Program Report No. 24, July 1997: U. S. Bureau of Reclamation Water Treatment Engineering & Research Group