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RPSEA Project 07122-12 TECHNICAL ASSESSMENT OF PRODUCED WATER TREATMENT TECHNOLOGIES 1st Edition The Sal-ProcTM system has undergone a sustained period of development and improvements including field trials, piloting, and public demonstrations. Sal-ProcTM systems have been employed at various installations with treatment capacities between 217,151 to 2,111,000 gpd (5,170 to 50,250 bpd). The Sal-ProcTM system has been tested on TDS concentrations ranging from 7,500 to 82,000 mg/L [165]. Silica crystallization and removal is not mentioned in any of the literature on the Sal-ProcTM technology, which may indicate that the system is not designed to treat silica-saturated water. Designed to facilitate zero liquid discharge of concentrated saline brines, the Sal-ProcTM process has a theoretical recovery of 100%. However, the final 15% of water removed from a feed solution are not likely to be captured for beneficial use. Infrastructure requirements for Sal- ProcTM systems may be relatively high, and will likely require significant footprint to accommodate chemical reagent storage and product salt storage. The Sal-ProcTM is relatively mobile, and may be constructed to operate out of a cargo trailer. Sal-ProcTM is designed to be highly modular and readily integrated into other unit processes. Energy requirements for the Sal-ProcTM system are unspecified. However, available data indicates that the system has a capital cost ranging from $2.3/gpd to $22.1/gpd ($96/bpd to $928/bpd), and an operations and management cost of roughly $3.9/kgal to $13.9/kgal ($0.16/bbl to $0.58/bbl) [165]. The literature does not provide any indication of serviceable lifetime for the process. This proprietary process requires chemical reagents to produce saleable salts, however the exact nature of these reagents is not reported with the exception of Ca(OH)2 [167]. The process may also require cleaning chemicals, however no reference is made to this affect in the literature. Extensive monitoring and operator oversight may be required to optimize reagent dosing and recovered salt management. Minimal pretreatment is required to remove organic constituents and any micro constituents that may adversely effect the generation of saleable salts from the system. A summary of the technical assessment for the Sal-ProcTM process is shown in Table 49. 131PDF Image | TECHNICAL ASSESSMENT OF PRODUCED WATER TREATMENT TECHNOLOGIES
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