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Membrane and Desalination Technologies - TCE Moodle Website

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194 N.K. Shammas <strong>and</strong> L.K. Wang<br />

Fig. 4.8. Schematic of challenge testing facility (Source: ref. (37)).<br />

operators accomplished all repairs to the CBUDSF system with readily available tools. For many<br />

of the repairs to the MF unit, factory-trained technicians were needed.<br />

14. Results of the increased solids loading test indicate that both systems are capable of processing<br />

high solids source water with modified operational protocol (e.g., increased coagulant, chlorine<br />

turnover rate for CBIJDSF <strong>and</strong> increased backwash frequency for MF). The MF unit outperformed<br />

the CBUDSF unit during the tests; however, both units produced filtrate in compliance<br />

with existing regulatory st<strong>and</strong>ards for potable water (e.g., consistent effluent turbidities less<br />

than 0.1 NTU) throughout the test.<br />

15. Both systems performed well as tertiary filtration units <strong>and</strong> in such a way as to confirm that both<br />

units are in compliance with the NYC Watershed Rules <strong>and</strong> Regulations.<br />

Muhammad et al. (40) evaluated various surrogates for Cryptosporidium removal. The<br />

results are useful for future pilot plant challenge testing.

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