...
首页> 外文期刊>The Journal of Supercritical Fluids >Supercritical CO2 extraction and transesterification of the residual oil from industrial palm kernel cake with supercritical methanol
【24h】

Supercritical CO2 extraction and transesterification of the residual oil from industrial palm kernel cake with supercritical methanol

机译:超临界甲醇的工业棕榈仁蛋糕残留油的超临界CO2提取和酯交换

获取原文
获取原文并翻译 | 示例
           

摘要

The oil extracts from palm kernel cake were obtained with supercritical CO2 at temperatures of (40-80) degrees C and pressures of (150-350) bar. The highest extraction yield on dry basis was (7.82 +/- 0.28)%, obtained at 350 bar/80 degrees C; however, the oil fraction employed in the transesterification process was that obtained at 150 bar/40 degrees C. The transesterification reaction was performed under the following operating conditions: methanol/oil molar ratios of 24:1 and 42:1, temperatures of (250-350) degrees C, and reaction times of (5-25) min. A statistical analysis and mathematical modeling for the optimal yield of SFE were also performed. The fatty acid with the highest concentration was lauric acid (60.24 +/- 0.62) % and the transesterification conditions affording the highest conversion of methyl esters (99.81 +/- 0.10) % were a methanol/oil molar ratio of 42:1, 350 degrees C, and 5 min.
机译:在(40-80)℃的温度和(150-350)棒的压力温度下,获得来自棕榈仁蛋糕的油提取物。 干基的最高提取产率为(7.82 +/- 0.28)%,在350巴/ 80℃下获得; 然而,在酯交换过程中使用的油馏分在150巴/ 40℃下获得。在以下操作条件下进行酯交换反应:甲醇/油摩尔比为24:1和42:1,温度(250 -350)℃,反应时间(5-25)分钟。 还进行了统计分析和用于SFE最佳产量的数学建模。 具有最高浓度的脂肪酸是月桂酸(60.24 +/- 0.62)%,并且甲酯最高转化的酯交换条件是甲醇/油摩尔比为42:1,350 D度C和5分钟。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号