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Table 3 Membrane area calculated based on different flow rates. Under conditions: (feed concentration: 100 g L−1; feed temperature: 25 °C; osmotic solution concentration: 300 g L−1)

From: Development of mass and heat transfer coupled model of hollow fiber membrane for salt recovery from brine via osmotic membrane distillation

Feed flow rate, Qf (L h−1)

Membrane area required (m2)

No. of modules in series (per tray)

No. of trays required in parallel

Volume required on site (m3)

24

190

136

1

0.1

500

2130

136

11

1.1

1000

4300

136

26

2.1

1500

6400

136

34

3.2

2000

8500

136

45

4.3