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Separation performance of supercritical carbon dioxideudextraction column for crude palm oil processing:udobservation using process simulatorud

机译:超临界二氧化碳的分离性能 ud粗棕榈油加工用萃取塔: ud使用过程模拟器进行观察 ud

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摘要

Separation behaviour of crude palm oil (CPO), which contains principally triglycerides, fatty acids and valuable minor components such as alpha-tocopherol and beta-carotene, with supercritical carbon dioxide was observed using process simulator Aspen® Plus. Solubility of palm oil components in supercritical CO2 extraction column was calculated by Redlich-Kwong –Aspen equation of state. Process flow diagram for the CPO processing by supercritical CO2 extraction column was successfully constructed to evaluate the separation performance. The effects of reflux ratio,stage number of extraction column and solvent-to-feed (S/F) flow rote ratio on the extract and raffinate product purities as well as the recovery of palm oil TG were studied at 373K and 20-30Mpa.ud
机译:使用过程仿真器Aspen®Plus,观察到粗棕榈油(CPO)的分离行为,该棕榈油主要包含甘油三酸酯,脂肪酸和宝贵的微量成分(如α-生育酚和β-胡萝卜素)与超临界二氧化碳。超临界CO2萃取塔中棕榈油成分的溶解度通过Redlich-Kwong –Aspen状态方程计算。成功构建了超临界CO2萃取塔处理CPO的工艺流程图,以评估分离性能。研究了在373K和20-30Mpa下回流比,萃取塔级数和溶剂-进料(S / F)流动速率对萃取液和残液产物纯度以及棕榈油TG回收率的影响。 ud

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