Mamey sapote (Pouteria sapota) seeds oil has potential as human consumption oil due to its high content of oleic acid. In order to design a solid-liquid extraction sustainable process, (hexane)-(oil)-(Pouteria sapota seeds) extractive system was modeled for different extraction modes applying novel mathematical relations. One equilibrium stage solid-liquid extractions (SLE) and dynamic SLE with continuous solvent flow through a particles fixed bed were experimentally performed in order to estimate the extractive system thermodynamic properties. The results for thermodynamic distribution constant, specific retained solution and oil diffusivity in underflow (seeds-extract mixture) were 0.24 g/g, 1.58 g/g and 8.68 $\times$ 10⁻¹¹ m²/s (at 30 °C) respectively. These properties, applied in the mathematical models of counter-current equilibrium multistage and dynamic SLE processes, reproduced experimental behavior with 4.53–16.7 average difference %.

Mamey sapote ( Pouteria sapota ) 种子油由于油酸含量高，具有作为人类食用油的潜力。为了设计可持续的固液萃取工艺，应用新颖的数学关系针对不同的萃取模式对（己烷）-（油）-（ Pouteria sapota种子）萃取系统进行了建模。通过实验进行了一级固液萃取 (SLE) 和连续溶剂流过颗粒固定床的动态 SLE，以评估萃取系统的热力学性质。底流（种子提取物混合物）中的热力学分布常数、特定保留溶液和油扩散系数的结果分别为 0.24 g/g、1.58 g/g 和 8.68$\times$分别为10 ^-11  m ² /s（30℃时）。这些特性应用于逆流平衡多级和动态 SLE 过程的数学模型，以 4.53–16.7 的平均差异 % 再现了实验行为。