Design and Control of Glycerol-<i>tert</i>-Butyl Alcohol Etherification Process

<div class="floats-full-page floats-full-page-other"><h2>Table 3</h2><div class="floats-full-page-caption">Stream results for the reaction section  (Figure <a href="../fig7/">7</a>).</div><div class="floats-full-page-content"><table class="table-group" id="tab3"><tr><td><table class="table"><tr><td class="thead-hr" colspan="11"><hr /></td></tr><tr class="thead"><td align="left">Stream name</td><td align="center">G0</td><td align="center">TBA1</td><td align="center">TBA0</td><td align="center">GM1</td><td align="center">1</td><td align="center">2</td><td align="center">3a</td><td align="center">3b</td><td align="center">W</td><td align="center">D + T</td></tr><tr><td class="thead-hr" colspan="11"><hr /></td></tr><tr><td align="left">Flow/(kmol/hr)</td><td align="center">2.15</td><td align="center">26.5</td><td align="center">4.37</td><td align="center">6.23</td><td align="center">32.75</td><td align="center">32.8</td><td align="center">26.47</td><td align="center">6.32</td><td align="center">4.35</td><td align="center">2.24</td></tr><tr><td align="left">Flow/(kg/hr)</td><td align="center">198</td><td align="center">1883</td><td align="center">324</td><td align="center">759</td><td align="center">2642</td><td align="center">2642</td><td align="center">1635</td><td align="center">1006.6</td><td align="center">80.8</td><td align="center">445.6</td></tr><tr><td align="left">Temp/(°C)</td><td align="center">20</td><td align="center">79.8</td><td align="center">25</td><td align="center">140.9</td><td align="center">70</td><td align="center">70</td><td align="center">29.3</td><td align="center">177</td><td align="center">25</td><td align="center">139.5</td></tr><tr><td align="left">Pressure/(bar)</td><td align="center">1</td><td align="center">5</td><td align="center">1</td><td align="center">5</td><td align="center">5</td><td align="center">4.95</td><td align="center">1.2</td><td align="center">0.15</td><td align="center">1</td><td align="center">0.1</td></tr><tr><td align="left">Flow/(kmol/hr)</td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td><td align="center"> </td></tr><tr><td align="left"> G</td><td align="center">2.15</td><td align="center">Trace</td><td align="center">0</td><td align="center">2.94</td><td align="center">2.94</td><td align="center">0.8</td><td align="center">Trace</td><td align="center">0.81</td><td align="center">0</td><td align="center">0.01</td></tr><tr><td align="left"> TBA</td><td align="center">0</td><td align="center">24.9</td><td align="center">4.37</td><td align="center">Trace</td><td align="center">24.9</td><td align="center">20.6</td><td align="center">20.6</td><td align="center">0.002</td><td align="center">0.04</td><td align="center">0.003</td></tr><tr><td align="left"> ME</td><td align="center">0</td><td align="center">Trace</td><td align="center">0</td><td align="center">3.27</td><td align="center">3.27</td><td align="center">3.27</td><td align="center">Trace</td><td align="center">3.27</td><td align="center">0</td><td align="center">0.007</td></tr><tr><td align="left"> DE</td><td align="center">0</td><td align="center">Trace</td><td align="center">0</td><td align="center">0.01</td><td align="center">0.01</td><td align="center">2.14</td><td align="center">Trace</td><td align="center">2.14</td><td align="center">0</td><td align="center">2.13</td></tr><tr><td align="left"> TE</td><td align="center">0</td><td align="center">Trace</td><td align="center">0</td><td align="center">Trace</td><td align="center">Trace</td><td align="center">0.002</td><td align="center">Trace</td><td align="center">0.002</td><td align="center">0</td><td align="center">0.0019</td></tr><tr><td align="left"> Water</td><td align="center">0</td><td align="center">1.5</td><td align="center">0</td><td align="center">Trace</td><td align="center">1.5</td><td align="center">5.81</td><td align="center">5.81</td><td align="center">0.005</td><td align="center">4.31</td><td align="center">0.005</td></tr><tr><td align="left"> S</td><td align="center">0</td><td align="center">0.1</td><td align="center">0</td><td align="center">0</td><td align="center">0.1</td><td align="center">0.1</td><td align="center">Trace</td><td align="center">0.1</td><td align="center">Trace</td><td align="center">0.1</td></tr><tr><td align="left"> IB</td><td align="center">0</td><td align="center">0</td><td align="center">0</td><td align="center">0</td><td align="center">Trace</td><td align="center">0.04</td><td align="center">0.04</td><td align="center">Trace</td><td align="center">0</td><td align="center">Trace</td></tr><tr class="table-tr"><td colspan="11"><hr class="tbody-hr" /></td></tr></table></td></tr></table></div></div>

Table 3 | Design and Control of Glycerol-<i>tert</i>-Butyl Alcohol Etherification Process

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Table 3: Design and Control of Glycerol-<i>tert</i>-Butyl Alcohol Etherification Process

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Table 3 | Design and Control of Glycerol-tert-Butyl Alcohol Etherification Process

Table 3

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