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Membrane and Desalination Technologies - TCE Moodle Website

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<strong>Membrane</strong> Processes for Reclamation of Municipal Wastewater 451<br />

5.2. Description of Overall Process<br />

An MF/RO pilot plant with the capacity of 20 m 3 /day was used in this study. The overall<br />

pilot plant process <strong>and</strong> pilot operation had been described previously in detail (14). The RO<br />

unit contained six elements of membranes installed in series as single stage configuration.<br />

Operating conditions of the RO unit are shown in Table 10.11. For each RO membrane, the<br />

pilot plant was continuously operated over 2 weeks at Bedok Water Reclamation Plant,<br />

Singapore.<br />

During the study, online TOC of RO permeate was monitored using a model 820 Sievers<br />

portable TOC analyzer <strong>and</strong> online measurements of conductivity were conducted by a model<br />

Ecomet C75.<br />

5.3. Plant Performance<br />

Figure 10.8 shows TOC of RE4040-FL RO permeate as a function of time over 360 h (or<br />

15 days) in Test 1. It should be pointed out that the plant operation had been stabilized over 3<br />

months before the online TOC measurements were conducted (14). It can be seen that the<br />

permeate TOC fluctuated regularly between 36.2 <strong>and</strong> 65.7 ppb. Figure 10.8 also illustrates<br />

that the peak valley of TOC appeared daily. It might be due to high <strong>and</strong> low loading of<br />

influent to the wastewater treatment works, which subsequently produced the secondary<br />

treated effluent with high <strong>and</strong> low TOC, respectively. Also it is well understood that the<br />

pattern of the TOC peak valley is consistent with the daily life of human beings as the raw<br />

sewage is from domestic sources.<br />

Figure 10.9 shows TOC of RE4040-FE RO permeate as a function of time over 340 h (or<br />

14 days). It can be seen that the TOC level dropped significantly over the first 48 h at<br />

operating pressure of 70 psi. After the stabilization of plant operation, the permeate TOC over<br />

26 h at operating pressure of 107 psi in Test 2 was in the range of 30–36 ppb. The low TOC<br />

level of the reclaimed water does not appear to be reported previously for the application of<br />

RO in the reclamation of municipal wastewater. In Test 3 at 70 psi, the permeate TOC over<br />

260 h (or 11 days) fluctuated between 32 <strong>and</strong> 44 ppb, which was lower than that of RE4040-<br />

FL membrane as shown in Fig. 10.8. The RE4040-FE RO permeate with the low TOC level<br />

greatly benefits the special application where the reclaimed water from municipal wastewater<br />

is to supply for the electronics industry to further produce ultrapure water.<br />

Table 10.11<br />

Operating conditions of the RO unit for different membranes (15)<br />

Parameter RE4040-FL RE4040-FE<br />

Test 1 Test 2 Test 3<br />

Flux rate (gallon/ft 2 day) 10 15 10<br />

Feed flow (m 3 /h) 1.7 2.3 1.7<br />

Recovery (%) 50 55 50<br />

Operating pressure (psi) 60 107 70

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