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超声对超临界CO_2萃取传质的影响 总被引:2,自引:0,他引:2
自行设计了超声强化超临界CO2萃取装置,并以人参为原料,研究了超声的功率密度、频率和超声的辐照方式对超临界CO2萃取人参皂甙传质的影响。萃取压力、萃取温度、萃取时间和CO2流量分别为25 MPa、45℃、4 h和2.5 L/h。实验结果表明,当功率密度、超声频率和辐照方式分别为100 W/L、20 kHz和3 s/6 s时,人参皂甙的萃取率是不使用超声时的1.51倍;皂甙的萃取率随超声功率的增大而升高;低频超声较高频超声更有利于萃取;超声辐照时间对皂甙的萃取率影响较小;在高压下超声对超临界CO2萃取传质强化作用更明显;在适当的低温下更有利于超声强化超临界CO2萃取。 相似文献
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根据质量衡算微分模型和运用Fick第一定律,建立了超声强化亚临界水萃取(USWE)和亚临界水萃取(SWE)原花青素的动力学模型,并通过对比这2个模型说明了超声对亚临界水萃取的强化作用。结果表明,Y=5.3974×(1-e~(-0.001 4t))和Y=5.2019×(1-e~(-0.001 2t))分别是USWE和SWE原花青素的动力学模型,并且这2个动力学模型都能很好地模拟萃取的过程;对比这2个模型方程的参数可知,超声能够加快葡萄籽内部原花青素的扩散及促进其解吸,因此能够对SWE起到强化作用。 相似文献
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蛇床子油为绿黄色或绿棕色挥发性油,具有蛇床子特有气味。为发掘及提升蛇床子油的品质,本研究采用亚临界法探讨水萃取蛇床子油的工艺条件及保润性能。采用单因素试验及中心试验研究萃取压力、温度、时间、液固比对蛇床子油得率的影响,从而确定了最佳萃取工艺条件。研究结果显示,最优工艺条件为亚临界萃取压力8.50 MPa、萃取温度144.84℃、液固比(mL/g)为35.89∶1、萃取时间7.96 min,最高得率为40.974 mg/g。结果表明通过亚临界水萃取得到的蛇床子油可用于卷烟保润。 相似文献
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《硅酸盐学报》2016,(11)
针对水热反应处置固体废弃物的亚临界水热环境,综述了水介质和碱作用的研究进展。水介质是水热反应中不可或缺的介质环境和反应载体,在亚临界水热处置固体废弃物体系中,水介质的离子积随温度的升高、压力的增加而急剧增大;水介质压强与填充度的关系不显著;水介质密度随压力变化不明显,主要由温度控制;水介质与产物的相关关系,符合水热反应"生长基元"模型。碱的引入,不但可以提高固体废弃物在水热溶液中的溶解度,且提高了其溶解度温度系数;不同阳离子及碱浓度均会对反应进程和反应产物产生重要影响。亚临界水热反应中水介质和碱的作用是固体废弃物水热反应的基础,对提高固体废弃物水热资源化的效果及进程具有重要作用。 相似文献
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超声强化超临界流体萃取机理的研究 总被引:7,自引:0,他引:7
从实验和理论上对超声强化超临界流体萃取的机理进行了研究。采用自行设计的内插式超声强化超临界流体萃取装置,运用数码显微成像系统和透射电镜观察了有、无超声作用下超临界流体萃取中空化测试材料和海藻细胞微观结构的前后变化,分析了超声对超临界流体萃取海藻中二十碳五烯酸(EPA)和二十二碳六烯酸(DHA)的传质和萃取率的影响,并根据声化学原理对超临界流体中附加超声场时能否产生空化现象进行了探讨。实验结果发现超声对超临界二氧化碳流体中的空化材料和海藻细胞壁不产生破坏作用,不会产生声空化效应,但提高了海藻中EPA和DHA的萃取传质效果。其实验结果与理论推导相一致。结果表明:超声强化超临界流体萃取的机理不是源于超声空化,而是超声在微环境内产生的机械波动效应和热效应。 相似文献
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文章选用二氧化碳作为超临界溶剂,采用超临界溶液快速膨胀技术制备超细氟比洛芬药物粒子,在较宽的温度压力范围内测定了氟比洛芬在超临界二氧化碳中的溶解度,考察了各种操作参数对药物粒子粒径的影响,研究了药物粒子粒径随各种操作参数的变化规律。结果表明:在实验考察的范围内,氟比洛芬的溶解度较小,在10-5~10-7之间(摩尔分率),溶解度随着温度和压力的升高而增大。同时实验结果表明:粒径随预膨胀压力的升高而减小;一定范围内随接收距离的增大而增大;在萃取温度较低的情况下,粒子粒径基本随着萃取温度的升高而减小;随着萃取温度的升高,在相对较高预膨胀温度下,粒径随着萃取温度升高而增大。 相似文献
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我厂3号回转窑(Φ4m×60m)生产线在1996年年底由SP窑(产量912t/d)改为NSP窑(产量1320t/d),预分解系统为四级旋风预热器带离线式分解炉 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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The miscibility of various amorphous polybutadienes with mixed microstructures of 1,4 addition units (cis, 1,4 and trans 1,4) and 1,2 addition units have been investigated. The studies here involved optical transparency, differential scanning calorimetry, and small angle light scattering. It was found that a 90 percent (cis) 1, 4 addition polybutadiene was immiscible with high (91 percent) 1,2 addition polybutadiene. Reduction of the 1,2 content to 71 percent induced an upper critical solution temperature (UCST) with the cis 1,4 polymer. Polybutadienes with 50 percent and 10 percent 1,2 contents were miscible above the crystalline melting temperature of the cis 1,4 polybutadiene. Immiscibility of the 91 percent 1,2 addition polymer was also found with a 10 percent 1,2 polybutadiene. The latter polymer also exhibits an UCST with the 71 percent 1,2 polymer. The results are used to interpret the characteristics of blends of polybutadienes of varying microstructure. 相似文献
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以F类粉煤灰为例,详细介绍了测定粉煤灰中烧失量的步骤、计算数学模型、影响测量不确定度的因素以及各项测量不确定度分量评定,人员、设备、材料、方法、环境都是影响测量不确定的因素。 相似文献
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The objective of the study was to explore the effect of the degree of deacetylation (DD) of the chitosan used on the degradation rate and rate constant during ultrasonic degradation. Chitin was extracted from red shrimp process waste. Four different DD chitosans were prepared from chitin by alkali deacetylation. Those chitosans were degraded by ultrasonic radiation to different molecular weights. Changes of the molecular weight were determined by light scattering, and data of molecular weight changes were used to calculate the degradation rate and rate constant. The results were as follows: The molecular weight of chitosans decreased with an increasing ultrasonication time. The curves of the molecular weight versus the ultrasonication time were broken at 1‐h treatment. The degradation rate and rate constant of sonolysis decreased with an increasing ultrasonication time. This may be because the chances of being attacked by the cavitation energy increased with an increasing molecular weight species and may be because smaller molecular weight species have shorter relaxation times and, thus, can alleviate the sonication stress easier. However, the degradation rate and rate constant of sonolysis increased with an increasing DD of the chitosan used. This may be because the flexibilitier molecules of higher DD chitosans are more susceptible to the shear force of elongation flow generated by the cavitation field or due to the bond energy difference of acetamido and β‐1,4‐glucoside linkage or hydrogen bonds. Breakage of the β‐1,4‐glucoside linkage will result in lower molecular weight and an increasing reaction rate and rate constant. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 90: 3526–3531, 2003 相似文献