Experimental Investigation of Heat and Mass Transfer in Tubular Membrane Distillation Module for Desalination

<table>Water flux versus <svg height="14.7625" id="M53" style="vertical-align:-3.29303pt" version="1.1" viewbox="0 0 34.075001 14.7625" width="34.075001" xmlns="http://www.w3.org/2000/svg">
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<g transform="translate(72,-60.19)">
<text transform="matrix(1,0,0,-1,-71.95,63.52)">
<tspan style="font-size: 12.50px; " x="0" y="0">Δ</tspan>
<tspan style="font-size: 12.50px; " x="9.0271664" y="0">𝑃</tspan>
</text>
<text transform="matrix(1,0,0,-1,-55.5,60.4)">
<tspan style="font-size: 8.75px; " x="0" y="0">v</tspan>
<tspan style="font-size: 8.75px; " x="3.8858881" y="0">m</tspan>
</text>
</g>
</g>
</svg> at different feed temperatures, feed flow rate 120 L/h; permeate temperature 23°C.</table>

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fig5

Figure 5

Figure 5: Experimental Investigation of Heat and Mass Transfer in Tubular Membrane Distillation Module for Desalination 