超临界CO2萃取洋葱挥发油工艺研究

本实验采用超临界CO2萃取技术从冻干洋葱粉中萃取挥发油。以洋葱挥发油得率为考察指标,经单因素及正交试验,考察了萃取温度、萃取压力、CO2流量、萃取时间4个因素对超临界CO2流体萃取的影响。结果表明萃取压力20 MPa,萃取温度35℃,CO2流量为14 kg/h的条件下萃取2.5 h为最佳工艺,洋葱挥发油得率达0.53%。     

超临界CO2萃取百合花挥发油的工艺研究

本文介绍了超临界CO2萃取百合花中挥发油的提取分离工艺,重点研究了超临界CO2萃取压力、温度、时间对出油率的影响。正交试验结果表明：影响超临界CO2萃取的主要因素为C3〉A2〉B2（A为萃取压力,B为萃取温度,C为萃取时间）;最佳工艺参数：SC-CO2萃取压力为18MPa,温度为50℃,时间为90min,流量为25L／min,所得百合花挥发油的出油率高达2．92％。     

超临界CO2萃取大豆油与大豆磷脂工艺条件研究

应用超临界CO2萃取技术从大豆中直接提取大豆油和纯度为95.98%的大豆磷脂。探讨了超临界CO2萃取的压力、温度、流量、时间等条件对大豆油和大豆磷脂的影响,确定其最佳萃取条件：萃取压力25MPa,温度50℃,CO2流量30kg/h,萃取时间150min,大豆磷脂夹带剂乙醇的流量为3kg/h,得率分别为15.72%和1.954%。     

超临界CO2提取甘草地上部分总黄酮

采用单因素试验对甘草地上部分(茎叶)的超临界CO2提取工艺进行了研究。实验考察了压力、萃取时间、温度及CO2流量对甘草地上部分总黄酮提取率的影响,以总黄酮提取率和含量为指标,系统的研究了超临界二氧化碳萃取法提取甘草地上部分总黄酮的提取效果。得出的最佳工艺参数为:采用40-60目原料,80%乙醇为夹带剂,萃取时间:1.5 h;萃取压力:30.0 MPa;萃取温度:50℃;CO2流量:10 kg.h-1;分离压力:5.8 MPa;分离温度:40℃。实验结果表明超临界二氧化碳萃取甘草总黄酮的提取率2.09%,含量5.42%,工艺具有提取率高,纯度高的特点,为规模化生产甘草总黄酮的提取提供了研究基础。     

超临界CO_2萃取大豆油与大豆磷脂工艺条件研究

应用超临界CO2 萃取技术从大豆中直接提取大豆油和纯度为 95 98%的大豆磷脂。探讨了超临界CO2 萃取的压力、温度、流量、时间等条件对大豆油和大豆磷脂的影响 ,确定其最佳萃取条件 :萃取压力 2 5MPa ,温度 5 0℃ ,CO2 流量 30kg h ,萃取时间15 0min ,大豆磷脂夹带剂乙醇的流量为 3kg h ,得率分别为 15 72 %和 1 95 4 %。     

超临界CO2萃取鱼腥草的挥发油成分

从萃取的压力、温度、流量和时间等条件探讨超临界CO2萃取对鱼腥草(Houttuynia cordata Thunb.)挥发油萃取率的影响,确定最佳萃取条件为萃取压力20mPa、温度35℃、CO2流量40kg/h和萃取时间80min,鱼腥草挥发油得率为1．76％。而水蒸气蒸馏提取和石油醚提取的得率分别为0．05％和0．08％。超临界CO2法萃取的鱼腥草挥发油收率高,萃取时间短。     

生姜的超临界CO2提取分离工艺的研究

本文研究了超临界CO2流体萃取生姜的工艺,探讨了萃取压力、温度扣时问等因素对生姜萃取率的影响,通过正交实验确定了生姜超临界CO2流体萃取最佳工艺：生姜原料切成薄片,含水率15％以下,萃取条件为压力24Mpa、温度40℃、时间2h。     

超临界CO2萃取薰衣草精油的研究

研究超临界CO2萃取薰衣草精油的工艺,考察萃取压力、温度、时间和CO2流量对薰衣草精油得率的影响,正交设计试验确定工艺条件,各因素对薰衣草精油得率影响程度是萃取时间>压力>CO2温度>流量。薰衣草精油得率为3.26%-4.50%。优化的工艺条件为萃取压力22 MPa、温度45℃、CO2流量20 L/h,萃取时间120 m in。经GC/MS分析结果显示薰衣草精油的主要成分为:顺式氧化芳樟醇2.75%;反式氧化芳樟醇0.75%;桉叶油素0.4%;芳樟醇14.53%;乙酸芳樟脂25.40%;乙酸薰衣草酯7.93%;薰衣草醇2.0%;龙脑1.05%;丁酸己酯1.44%等。     

超临界CO2萃取石香薷挥发油工艺的研究

石香薷（Molsa chinensis）为多年生草本植物,具有重要的药用价值。本文首次探讨了超临界CO2萃取的压力,温度,流量,时间等条件对石薷挥发油收率的影响,确定其最佳萃取条件,萃取压力15MPa,温度45℃,CO2流量25kg/h和90min,得率为3.56%,水蒸气蒸馏提取得率为1.62%,石油醚提取得率为1.87%,结果表明超临界CO2萃取挥发油比后二者质优,收率大大提高,萃取时间短,无溶剂残留。     

超临界二氧化碳萃取鸢尾油的工艺条件研究

本文采用L9（3^4）正交实验考察了二氧化碳超临界萃取中萃取压力、萃取温度和萃取时间对鸢尾精油提取率的影响。结果表明各影响因子的影响顺序为：压力〉时间〉温度;当原料的颗粒度为60-80目、CO2流量为20．0m^3/h时,用超临界二氧化碳萃取鸢尾精油的最佳工艺条件为：萃取压力26．0MPa,萃取温度55．0℃,萃取完成时间为2．5h,此条件下鸢尾香根中鸢尾油的萃取率高达12．71％,得到的精油中鸢尾酮的含量为39．95％,与索氏法和微波提取法相比,超临界萃取具有提取率高和产品质量好的优点。     

Recent extraction techniques for natural products: microwave-assisted extraction and pressurised solvent extraction

In the last 10 years there has been an increased interest in using techniques involving microwave-assisted extraction and pressurised solvent extraction in analytical laboratories. This review gives a brief overview of both methods, and reports on their application to the extraction of natural products. The influence of parameters such as the nature of the solvent and volume, temperature, time and particle size of the matrix is discussed. Through numerous examples, it is demonstrated that both techniques allow reduced solvent consumption and shorter extraction times, while the extraction yields of the analytes are equivalent to or even higher than those obtained with conventional methods.     

连续逆流提取机及其在绞股蓝皂苷提取工艺中的应用

简述了中草药连续逆流提取机的基本结构和工作原理.以水为溶媒、绞股蓝为原料,进行绞股蓝有效成分的提取试验.以绞股蓝水溶出物和总皂苷为目标物,考察提取温度、液料比和提取时间等因素对提取得率的影响,并通过L9(33)正交实验设计,对提取工艺进行优选.采用中草药连续逆流提取机提取绞股蓝有效成分的最佳工艺条件:提取溶剂温度80 ℃,料液比1:35(g/mL),提取时间50 min;所得提取物得率为33.95%,总皂苷得率为8.9%.     

Forward and backward extraction rates of amino acid in reversed micellar extraction

The mass transfer characterization in reversed micellar extraction of amino acid phenylalanine (Phe) is presented. The mass transfer rates in forward extraction of Phe from aqueous KCl solutions (pH 1.4 – 2.3) to AOT/isooctane reversed micellar solutions and in backward extraction from the reversed micellar organic phase to KHCO₃/KOH buffer solutions (pH 9.0 – 11.0) were investigated using a stirred cell with a flat liquid–liquid interface. Both the forward and the backward extraction rates are controlled by the interfacial rate processes, i.e., the solubilization and the release processes. The solubilizing rate constants for the forward extraction of Phe increase with decreasing pH and initial Phe concentration and with increasing initial AOT concentration. On the other hand, the releasing rate constants for the backward extraction decrease with increasing initial AOT concentration and with decreasing ionic strength, but are little influenced by pH. The backward extraction rates are fairly slow compared to the forward extraction rates, and are accelerated by the addition of 2-methyl-2-propanol, similar to the extraction of protein lysozyme.     

Coextraction during reactive extraction of phenylalanine using Aliquat 336: modeling extraction equilibrium

Reactive liquid-liquid extraction can be used to recover hydrophilic fermentation products that would not otherwise partition into nonpolar solvents through an ion-exchange reaction at the two-phase interface. However, the ion-exchange reagent may not be specific to the solute of interest and other compounds present may also be extracted. In this study, the effect on solute extraction of other compounds present in the extraction medium was investigated for phenylalanine extraction using Aliquat 336. The extent of extraction at equilibrium was modeled using the equilibrium constants for the reactions present in the process. The interaction of different species within a multicomponent medium was examined using the model and experimental results. It was found that the extent of extraction and coextraction is controlled by the thermodynamics of each extraction reaction and, due to the formation of a common product, the interaction between each of the reactions. The main competition to reactive extraction will come from hydrophobic anionic compounds that will be present in fermentation broth.     

Effect of salts on the extraction characteristics of succinic acid by predispersed solvent extraction

Predispersed solvent extraction (PDSE) of succinic acid with Tri-n-octylamine (TOA) dissolved in 1-octanol from aqueous solutions of 50 g/L succinic acid was examined. It was found that the equilibrium data in PDSE was equal to that in conventional solvent extraction in spite of the lack of mechanical mixing in PDSE. The influence of salts on succinic acid extraction and the stability of colloidal liquid aphrons (CLAs) were also investigated. Results indicated that in the presence of sodium chloride, less succinic acid was extracted by CLAs and the stability of CLAs decreased. However, the stability of CLAs was sufficient to make PDSE practically applicable to real fermentation broth, considering the concentration range of salts in the fermentation process for succinic acid.     

超声波辅助抽提法在孔雀石绿分子印迹固相萃取中的应用

采用沉淀聚合法制备孔雀石绿分子印迹聚合物(MG-MIPs),以洗脱效率及吸附量为指标,考察超声波辅助抽提法对MIPs中MG洗脱效果及吸附性能的影响,通过扫描电镜观察MIPs的表面形态,并对其吸附性能进行研究。结果表明:模板分子MG在超声30 min、超声10次、料液比m(MG-MIPs)∶V(甲醇-乙酸溶液)为1∶10(g/m L)、温度为25℃、超声功率为270 W的条件下,洗脱效果最好,MIPs在固相萃取柱中的吸附效率较高,达到198μg/g。