Figures & data
Table 1. Fatty acid compositions of palm oil and result of crystallization (%)
Figure 2. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 1
![Figure 2. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 1](/cms/asset/2542c8e6-eb4a-416e-bb28-96fe2a0a2bfd/ljfp_a_1632345_f0002_b.gif)
Figure 3. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 2
![Figure 3. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 2](/cms/asset/646e66b4-5feb-436b-960e-6fc59aeeba9f/ljfp_a_1632345_f0003_b.gif)
Table 2. Fatty acid compositions of palm stearin (%)
Figure 4. Influence of Reaction Time, Temperature and Amount of Sodium Methoxide on Sn-2 PA Content in the First Step of Method 3
![Figure 4. Influence of Reaction Time, Temperature and Amount of Sodium Methoxide on Sn-2 PA Content in the First Step of Method 3](/cms/asset/cc463434-fa00-4b35-a4fd-f09b5a0a157e/ljfp_a_1632345_f0004_b.gif)
Figure 5. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 3
![Figure 5. Influence of Reaction Time, Temperature, Molar Ratio and Amount of Lipase on OPO Content of Method 3](/cms/asset/7c3e31e6-f957-43a0-a085-6eefdffb09a9/ljfp_a_1632345_f0005_b.gif)
Table 3. The OPO content in final product after purification of the three methods (%, P < .05)
Table 4. The raw material dosage of OPO and the purified yield
Table 5. Fatty acid composition and distribution of the three-final product after purification step under the optimized conditions (%)
Table 6. The PA content located at sn-2 position in OPO (%, P < .05)
Table 7. The sn-2 PA content of PPP and palm stearin enriched in PA (%, P < .05)