超临界CO2萃取大蒜精油及油树脂的研究

研究了大蒜精油及油树脂的超临界CO₂提取工艺，探讨了粒度，萃取及分离的温度、压力和时间对各萃取率的影响，建立了萃取温度、压力与各萃取率的数学模型。确定了超临界CO₂同时提取大蒜精油及油树脂的优化工艺条件。     

超临界CO2流体萃取海滨锦葵籽油的工艺条件优化

为了提高海滨锦葵籽的利用价值,开发生物柴油新原料,该文以海滨锦葵籽为原料,利用超临界CO2流体萃取技术提取海滨锦葵籽油。通过单因素试验及正交试验研究了萃取压力、萃取温度、CO2流量和萃取时间等因素对油脂得率的影响,确定了超临界CO2流体萃取技术提取海滨锦葵籽油的最佳工艺条件。结果表明,在试验范围内各影响因素对海滨锦葵籽油得率作用的大小依次为：萃取压力＞萃取温度＞CO2流量＞萃取时间。超临界CO2流体萃取技术提取海滨锦葵籽油的最佳工艺参数为：萃取压力25 MPa,萃取温度45℃,CO2流量21 kg/h,萃取时间为100 min,在该工艺条件下萃取3次,海滨锦葵籽油得率达到19.35%。     

超临界CO2萃取毛竹笋油的工艺及产品成分

为优化超临界CO2萃取毛竹笋油的工艺参数,该研究通过单因素试验和正交试验考察了萃取压力、萃取温度、萃取时间和CO2流量等因素对毛竹笋油得率的影响,并利用气质联用（GC-MS）对毛竹笋油进行成分分析。研究确定超临界CO2萃取毛竹笋油的较佳工艺为：萃取压力25 MPa、萃取温度55℃、萃取时间2.5 h和CO2流量15 L/h,较佳工艺条件下笋油得率为5.74%;GC-MS分析毛竹笋油,共鉴定出17种组分,其中β-谷甾醇、9,12-十八碳二烯酸和9,12,15-十八碳三烯酸的相对含量分别为26.00%、10.50%和9.83%。     

超临界CO2流体萃取杏仁油工艺研究

该研究以单因素试验和正交试验相结合的方法对苦杏仁脂肪油的超临界CO2萃取工艺进行了研究.确定了超临界CO2萃取杏仁油的最佳工艺为:萃取压力35 MPa、萃取温度50 ℃、CO2流量24 L/h、粒径60目、萃取时间2 h.各因素影响杏仁的得率的顺序为:粒径＞时间＞萃取压力＞CO2流量＞萃取温度.最佳工艺验证试验的杏仁油的得率为52.98%.本研究的结果为下一步综合、无毒、高效地开发利用苦杏仁奠定了基础.     

超临界CO_2流体萃取杨梅核仁油的工艺优化

以杨梅核仁为原料,研究超临界CO2流体静、动态结合萃取杨梅核仁油的工艺条件,利用单因素试验与正交试验进行优化,得到最佳萃取方案,即萃取压力35MPa,萃取温度45℃,静态萃取60min后动态萃取50min,CO2流量4L/min,杨梅核仁油的得率最高,达41.7%。     

黑莓籽油的超临界萃取及脂肪酸成分分析

为了获得高品质保健油脂,采用超临界CO2萃取黑莓籽油,以气相色谱-质谱（GC-MS）对黑莓籽油脂肪酸成分进行分析。样品最佳粉碎粒度60目,超临界CO2萃取适宜工艺条件为：萃取压力20 MPa,分离罐压力10 MPa,萃取罐温度45℃,萃取时间30 min,萃取得率为(17.73±0.19)%。GC-MS检测结果显示黑莓籽油中含有丰富的不饱和脂肪酸,尤其是亚油酸、油酸、亚麻酸,质量分数分别为58.04%、11.76%、8.38%,占总脂肪酸的78.18%。研究结果为黑莓籽的综合开发加工利用提供了参考。     

超临界CO2萃取红松种仁油的工艺及其脂肪酸成分分析

为优化超临界COz萃取红松种仁油的工艺，研究了萃取压力、萃取温度和萃取时间对红松种仁油得率的影响，并对试验得到的种仁油进行了气质联用（GC—MS）分析。在单因素试验基础上进行了L9（3^4）正交试验，确定了超临界CO2萃取红松种仁油的最佳的工艺为：萃取压力40MPa，萃取温度50℃，萃取时间3h，最佳工艺条件下红松种仁油得率为45．85％。萃取压力对得率的影响最大，萃取时间次之，萃取温度对得率影响不显著。利用GC—MS鉴定出9个组分，占红松种仁油脂肪酸总量的99．98％，其中亚油酸和α亚麻酸的相对含量分别为41．79％和15．62％。     

影响大蒜精油提取得率的工艺参数研究

研究了大蒜精油提取条件，包括反应温度、反应pH值、反应时间和蒸馏时间对大蒜精油提取得率的影响，初步确定了采用鲜蒜提取风味物质的最适工艺条件。     

超临界CO2静态膨胀-动态循环萃取灵芝孢子油

为了直接从未破壁的灵芝孢子中萃取油脂,在超临界CO2动态循环萃取之前引入静态膨胀工艺,考察了各膨胀因素对灵芝孢子油萃取率的影响。试验结果表明,膨胀压力越高,膨胀时间越短,静态萃取时间越长,越有利于灵芝孢子油的萃取,而膨胀温度过高或过低均不利于灵芝孢子油的萃取。超临界CO2静态膨胀-动态循环萃取灵芝孢子油的优化工艺为:膨胀压力30MPa,膨胀时间30s,膨胀温度70℃,静态萃取时间20min,在此条件下灵芝孢子油的萃取率达94.3%。     

乙醇溶剂与超临界CO_2相结合提取高纯度卵黄磷脂的研究

采用乙醇溶剂首先提取蛋黄粉中的卵黄油 ,然后用超临界 CO2 萃取方法脱除卵黄油中的中性脂肪 ,获得高纯度的卵黄磷脂。考察了工艺参数对提取效果的影响。试验表明 :在乙醇溶剂提取卵黄油阶段 ,乙醇浓度是影响卵黄油提取率的最主要因素 ,温度是影响卵黄磷脂提取率的最主要因素 ;在超临界 CO2 萃取阶段 ,磷脂的溶解度随萃取温度的升高而降低 ,中性脂质在 5 5℃时溶解度最大。采用此工艺 ,卵黄磷脂得率为 17.6 6 % ,纯度 94.41% ,且不含胆固醇。     

超高压提取丹参素的研究

该文研究常温下超高压提取丹参素的最优工艺.采用超高压常温提取,正交试验对丹参素超高压提取工艺优化,高效液相色谱法测定丹参素的含量,并与传统的热回流提取法进行比较.结果显示优选的最优工艺为:提取压力300 MPa,溶剂乙醇浓度80%,溶液pH 13,浸泡时间16 h,在此条件下丹参素得率为0.465%.超高压提取不仅得率高、时间短、耗能低,而且提取产物易于分离、纯化,同时超高压提取可以维持在低温下进行,特别适宜于受热不稳定化合物的提取,该技术适合中药有效成分的快速提取.     

Optimization of extraction conditions for active components in Hypericum perforatum using response surface methodology

Optimal conditions for extraction of Hypericum perforatum were determined using response surface methodology. A 3 x 4 x 4 full factorial design representing three extraction temperatures, four extraction times, and four solvent concentrations was executed. The overall extraction efficiency was defined by comparing either the total extractable material weight or the individual component peak area to the peak area of luteolin as internal standard. Of the tested variables, the extraction temperature most significantly affected extraction efficiency. Higher temperatures gave better extraction efficiencies, but high temperature also caused decomposition of hypericin. Within the test range, responses for most variables had local maxima. Optimum ranges of time and concentration for individual variables were overlaid. Considering all variables, optimum ranges for extraction time and extraction solvent concentration (percent ethanol in acetone) were 5.0-6.7 h and 44-74% at 23 degrees C, 5.4-6.9 h and 45-72% at 40 degrees C, and 5.3-5.9 h and 44-69% ethanol in acetone at 55 degrees C, respectively.     

CO2超临界萃取技术提取被孢霉菌丝体油脂的研究

采用被孢霉菌丝体作为实验材料，比较系统地研究了在超临界状态下，预处理条件（水分含量、粉碎方法、粉碎度）、萃取条件（萃取温度与压力）、分离条件（分离温度与压力）对油脂萃取率的影响；分析了操作条件对油脂质量特别是γ－亚麻酸（ＧＬＡ）的影响；确定了最佳工艺路线，为批量生产提供了依据。     

Supercritical fluid extraction of limonoid glucosides from grapefruit molasses

Limonoid glucosides (primarily limonin 17-beta-D-glucopyranoside, LG) were extracted from grapefruit molasses by supercritical fluid extraction using a supercritical carbon dioxide-ethanol (SC CO(2)-ethanol) system. Extraction conditions to maximize the yield of LG were determined by varying pressure, temperature, ethanol concentration, and extraction time. The highest yield of LG at 0.61 mg/g molasses was obtained at a pressure 48.3 MPa, a temperature of 50 degrees C, 10% ethanol (X(Eth) = 0.1), and 40 min of extraction time at a flow rate of 5.0 L/min. The results demonstrated that SC CO(2) extraction of limonoid glucosides from grapefruit molasses has practical significance for commercial production.     

Pressurized fluids for extraction of cedarwood oil from Juniperus virginianna

The extraction of cedarwood oil (CWO) using liquid carbon dioxide (LC-CO(2)) was investigated and compared to supercritical fluid extraction, including the effects of extraction pressure and length of extraction. The chemical composition of the extracts was monitored over the course of the extraction as well. The cumulative yields of CWO from cedarwood chips using 80 L of carbon dioxide varied very little treatment to treatment, with all temperature/pressure combinations yielding between 3.55 and 3.88% CWO, and the cumulative yields were statistically equivalent. The rate of extraction was highest under the supercritical extraction conditions (i.e., 100 degrees C and 6000 psi). Under the liquid CO(2) conditions (i.e., 25 degrees C), the extraction rates did not vary significantly with extraction pressure. However, there were differences in the chemical composition of the collected CWO. Extractions at 100 degrees C gave a much lower ratio of cedrol/cedrene than extractions at 25 degrees C. The highest ratio of cedrol/cedrene was obtained using 25 degrees C and 1500 psi. The use of subcritical water was also investigated for the extraction of CWO as well. Although some CWO was extracted using this method, the temperature/pressure combinations that gave the highest weight percentage yields also gave oils with an off odor while those combinations that gave a higher quality oil had very low yields. It appears that the high temperatures and acidic conditions cause a dehydration of the tertiary alcohol, cedrol, to its hydrocarbon analogue, cedrene, during CO(2) or pressurized water extractions of cedarwood.     

Supercritical carbon dioxide extraction of turmeric (Curcuma longa)

Turmeric oil was extracted from turmeric (Curcuma longa) with supercritical carbon dioxide in a semicontinuous-flow extractor. Extraction rate was measured as a function of pressure, temperature, flow rate, and particle size. The extraction rate increased with an increase in CO(2) flow rate and with a reduction of particle size. The effect of pressure and temperature on turmeric extraction suggested the use of higher pressure and lower temperature at which solvent density is greater and thus the solubility of the oil in the solvent is greater in the range of 313-333 K and 20-40 MPa. The major components ( approximately 60%) of the extracted oil were identified as turmerone and ar-turmerone by GC-MS.     

Supercritical carbon dioxide extraction of oil and squalene from amaranthus grain

Supercritical carbon dioxide (SC CO(2)) was used for the extraction of oil and squalene from Amaranthus grain. Very small amounts of oil could be extracted by SC CO(2) from undisrupted grains, although SC CO(2) possesses higher diffusivity. Grinding increased the extraction rate and oil yield, and smaller particle size gave higher extraction rate. The oil yield and initial extraction rate increased linearly with the increasing SC CO(2) flow rate from 1 to 2 L/min. Increasing the flow rate of SC CO(2) above 2 L/min resulted in only a slight increase of oil yield and extraction rate. In the pressure range of 150-250 bar, extraction decreased with increasing temperature at a constant pressure, whereas at a pressure of 300 bar, the extraction yield increased with increasing temperature. Possible reasons for this are discussed. Effects of temperature and pressure on squalene yield were different from those on oil yield. A good oil yield (4.77 g of oil/100 g of grain) was obtained at 40 degrees C and 250 bar. The highest squalene yield (0.31 g of squalene/100 g of grain) and concentration (15.3% in extract) were obtained at 50 degrees C and 200 bar, although the oil yield under this condition was low (2.07 g of oil/100 g of grain). The moisture content within 0-10% had little influence on yields of oil and squalene at 40 degrees C and 250 bar. Finally, the oil yield and the squalene concentration in the extracts by SC CO(2) were compared to those by solvent extraction.     

Experimental study on the removal of dioxins and coplanar polychlorinated biphenyls (PCBS) from fish oil

Recently, it has been found that fish oils contain a high proportion of contaminants, namely, polychlorinated dibenzo-p-dioxins (PCDDs), polychlorinated dibenzofurans (PCDFs), and coplanar polychlorinated biphenyls (cPCBs). In this study, the removal of contaminants from fish oil by supercritical CO2 extraction (SCE) and by using adsorbents (0.13 wt % of oil) was investigated. Dioxins and cPCBs were extracted from fish oil by SCE at a temperature of 60 degrees C and a pressure of 28 MPa, and the removal efficiencies for PCDDs and PCDFs were in the range of 15-90% and those for cPCBs were in the range of 70-90%. However, 40% of the oil was extracted simultaneously with contaminants. On the adsorbent treatment, activated carbon showed high efficiency, and the removal efficiencies were >90% for PCDDs and PCDFs, but below 30% for cPCBs. A combination of both of these methods is more effective, and almost 100% of the total toxicity equivalence quantity value could be reduced.