Research Article

The Research and Mechanism of Extracting Vitamin B6 Using Aqueous Two-Phase Systems

Table 6

Tie-line data for the mixture of polyethylene glycol/isopropyl alcohol + ethanol + salt (Na2CO3/Na2SO4) + water ATPSs at different temperaturesa.

T (K)Total systemTop phaseBottom phaseTLLS
100W1100W2100W1100W2100W1100W2

Polyethylene glycol + ethanol + Na2SO4 + H2O system
308.1519.5311.5727.356.654.0121.3318.33−1.59
14.0014.1823.548.185.7819.359.71−1.59
15.0013.8524.997.575.0620.1111.75−1.59
16.4912.7924.417.815.3419.8013.17−1.59
17.9812.1625.787.254.6920.5215.70−1.59

318.1520.8911.9431.175.792.2723.0721.70−1.67
17.2012.7625.327.904.0420.6415.34−1.67
18.7912.2227.267.153.3621.4617.99−1.67
16.5412.9124.048.424.5320.1014.00−1.67
18.0012.3625.707.753.9020.8016.43−1.67

328.1528.747.3431.835.733.8420.3528.09−1.91
26.258.3930.506.164.2719.8924.81−1.91
17.3412.4426.727.535.8018.4813.03−1.91
22.1110.1728.246.965.1519.0515.09−1.91
18.6311.9527.977.065.2618.9511.89−1.91
15.6013.6028.516.905.0719.12

Isopropyl alcohol + ethanol + Na2SO4 + H2O system
308.1522.8610.0127.536.396.3522.8120.89−1.29
18.9012.4625.217.578.0020.9113.79−1.29
17.3013.5824.687.868.4020.4811.26−1.29
24.588.7927.896.226.1123.1123.37−1.29
19.5612.1225.917.207.4721.4915.30−1.29

Polyethylene glycol + ethanol + Na2CO3 + H2O system
308.1517.6111.0728.055.1710.8114.917.81−1.77
17.8611.1529.154.779.8315.699.22−1.77
18.1111.2030.024.479.0816.3010.37−1.77
18.4511.2831.164.108.1717.0911.81−1.77
18.7710.9630.604.288.6316.6911.65−1.77

aStandard uncertainties u are u (T) = 0.1 K and u () = 10 kPa, and the average uncertainty of u () = 0.01.