Heat Transfer of Nanofluid in a Double Pipe Heat Exchanger

<div>Overall heat transfer coefficient of <svg height="9.7821pt" id="M44" style="vertical-align:-3.57194pt" version="1.1" viewbox="-0.0498162 -6.21016 6.91271 9.7821" width="6.91271pt" xmlns="http://www.w3.org/2000/svg" xmlns:xlink="http://www.w3.org/1999/xlink"><g transform="matrix(.0135,0,0,-0.0135,0,0)"><path d="M478 372C478 418 458 448 431 448C409 448 389 431 389 410C389 404 391 400 394 395C398 388 406 371 406 348C406 253 308 122 251 51H249C254 122 249 257 231 336C212 421 189 448 159 448C126 448 75 412 23 327L48 306C83 354 103 371 115 371C125 371 134 360 144 334C185 224 192 64 183 -19C146 -100 116 -202 110 -244L125 -261C154 -259 208 -234 222 -220C222 -194 225 -84 235 -23C247 -3 273 36 308 79C379 165 478 288 478 372Z" id="g113-225"></path><glyph.data ascent="3473" descent="-2876" horiz-adv-x="501" vert-adv-y="501"></glyph.data></g></svg>-Al<sub>2</sub>O<sub>3</sub>/water nanofluid versus Reynolds number for various volume concentrations (<svg height="9.38774pt" id="M45" style="vertical-align:-0.04981995pt" version="1.1" viewbox="-0.0498162 -9.33792 8.76219 9.38774" width="8.76219pt" xmlns="http://www.w3.org/2000/svg" xmlns:xlink="http://www.w3.org/1999/xlink"><g transform="matrix(.0135,0,0,-0.0135,0,0)"><path d="M620 675H597C578 656 570 650 541 650H144C112 650 104 653 94 675H72C59 618 42 552 23 493L53 491C71 534 88 564 105 585C124 608 144 615 238 615H290L197 121C182 40 174 34 88 28L82 0H361L367 28C275 34 266 38 281 121L374 615H441C522 615 543 608 553 583C562 560 566 531 565 493L597 494C603 551 612 629 620 675Z" id="g113-85"></path><glyph.data ascent="3473" descent="-2876" horiz-adv-x="637" vert-adv-y="637"></glyph.data></g></svg> = 35°C, 40°C).</div>

International Scholarly Research Notices

Heat Transfer of Nanofluid in a Double Pipe Heat Exchanger

Figure 3