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首页> 外文期刊>The Journal of Supercritical Fluids >Extraction of tocotrienols from annatto seeds by a pseudo continuously operated SFE process integrated with low-pressure solvent extraction for bixin production
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Extraction of tocotrienols from annatto seeds by a pseudo continuously operated SFE process integrated with low-pressure solvent extraction for bixin production

机译:通过伪连续操作SFE工艺与低压溶剂萃取相结合从安纳托种子中提取生育三烯酚,以生产联苯

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A process to obtain tocotrienols from annatto seeds was studied in a supercritical fluid extraction (SFE) system containing two 1 L extractor vessels with height (H-B) to internal diameter (D-B) ratios of 7.1 (E-1) and 2.7 (E-2). Pseudo continuous operation of the SFE system was validated by producing clove volatile oil at 40 degrees C and 15 MPa. To obtain tocotrienols, the system was operated in pseudo continuous mode at 40 degrees C, 20 MPa and CO2 flow rate of 20.7 g/min. The extraction time, from a technical perspective, was set to 60 min, according to kinetic parameters obtained from an overall extraction curve (OEC) with processing time of 360 min. OECs were initially measured in batch mode (BM) and the kinetic parameters for the constant extraction rate (CER) period were determined to be lengths of the CER period (t(CER)) equal to 43 +/- 11 and 42 +/- 2 min for E-1 and E-2, respectively; mass transfer rates (M-CER) of 0.22 +/- 10.01 g/min for both E-1 and E-2; and total yields (R-CER) of 50 +/- 1 and 49 +/- 1 g of extract/100 g of extractable mass for E-1 and E-2, respectively. No differences were observed between each group of kinetic parameters (t(CER); M-CER; R-CER) obtained in BM. Following the measurement of OECs, the SFE system was operated in pseudo continuous mode for four extraction stages of 60 min each with the extractors organized in parallel. This organization improved the productivity of the process. We also proposed the integration of SFE with low-pressure solvent extraction (LPSE) using water and ethanol as solvents to remove bixin from the defatted annatto seeds. LPSE conditions were: 60 degrees C and solvent mass to feed mass ratio (S/F) of 8 gsolvent/g annatto for ethanol and 50 degrees C and S/F of 8 gsolvent/g annatto for water. LPSE assays were performed in an agitated bed over a 95 min time period. Using partially defatted annatto seeds as the feedstock for LPSE resulted in increased bixin extraction. LPSE with ethanol was found to increase the bixin content in the extract. Thus, the proposed process integration appears to be useful, mainly due to three aspects: (1) the initial removal of the oil layer via supercritical CO2 favors bixin extraction, (2) LPSE is a low-cost methodology for extracting bixin and (3) the cost of raw material in the second step is null. (C) 2014 Elsevier B.V. All rights reserved.
机译:在包含两个1 L高度(HB)与内径(DB)比率为7.1(E-1)和2.7(E-2)的提取容器的超临界流体萃取(SFE)系统中,研究了从胭脂树种子中获得生育三烯酚的方法。 )。通过在40摄氏度和15兆帕下生产丁香挥发油,验证了SFE系统的伪连续运行。为了获得生育三烯酚,该系统在40℃,20MPa和20.7g / min的CO 2流速下以伪连续模式操作。从技术角度出发,根据从总提取曲线(OEC)获得的动力学参数,将提取时间设置为60分钟,处理时间为360分钟。最初以批处理模式(BM)测量OEC,恒定萃取率(CER)周期的动力学参数确定为CER周期的长度(t(CER))等于43 +/- 11和42 +/- E-1和E-2分别为2分钟; E-1和E-2的传质速率(M-CER)为0.22 +/- 10.01 g / min;对于E-1和E-2,总产量(R-CER)分别为50 +/- 1和49 +/- 1 g提取物/ 100 g可提取物质。在BM中获得的每组动力学参数(t(CER); M-CER; R-CER)之间没有观察到差异。在测量OEC之后,SFE系统以伪连续模式运行四个萃取阶段,每个萃取阶段60分钟,萃取器平行组织。该组织提高了过程的生产率。我们还建议将SFE与用水和乙醇作为溶剂的低压溶剂萃取(LPSE)集成,以从脱脂的安纳托种子中除去二恶英。 LPSE条件为:60摄氏度,乙醇的溶剂质量与进料质量比(S / F)为8 gsolvent / g胭脂红,水的50摄氏度和S / F为8 gsolvent / g胭脂红。 LPSE分析在95分钟的时间内在搅拌床中进行。使用部分脱脂的安纳托种子作为LPSE的原料,增加了Bixin的提取。发现含乙醇的LPSE可增加提取物中的联蛋白含量。因此,拟议的工艺整合似乎是有用的,主要是由于三个方面:(1)通过超临界CO2初步去除油层有利于二恶英的提取;(2)LPSE是一种用于提取二恶英的低成本方法;(3) )第二步中的原材料成本为空。 (C)2014 Elsevier B.V.保留所有权利。

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