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用溶剂浸取精制混合二元酸分离出丁二酸。分离工艺条件:浸取温度为88℃,浸取时间为1h,溶剂与二元酸的质量比为6.61。在上述工艺条件下分离得到的丁二酸纯度为99%,丁二酸的收率为61.76%。 相似文献
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二氧化碳在二甲基甲酰胺及其水溶液中溶解度的测定 总被引:1,自引:0,他引:1
采用低压容量法气液平衡测定仪测定了不同温度下CO_2在纯水、纯二甲基甲酰胺(DMF)及其混合溶剂中的溶解度,并计算了Henry常数和Ostwald系数。该装置适用于恒温(室温以上)常压下的气体在纯溶剂和混合溶剂中的气液平衡数据测定。 相似文献
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叶黄素是一种重要的抗氧剂,对视力有很好的保护作用。万寿菊花瓣中的叶黄素含量很高,是叶黄素提取的理想原料。超声波的空化效应可以破坏植物细胞而使溶剂渗透入植物细胞,加速细胞内物质的释放以达到缩短提取时间和提高提取效率的目的。本实验主要考察超声时间,超声功率,提取温度和料液比等因素对叶黄素提取效率的影响。 相似文献
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浸取法制造硬度变化医用聚氯乙烯导管 总被引:1,自引:1,他引:0
通过对浸取法制造硬度变化医用聚氯乙烯(PVC)导管的探索研究,发现溶剂种类、增塑剂含量、浸取时间、试样厚度等都能显著地影响浸取;对邻苯二甲酸二辛酯(DOP)增塑的PVC软管,借助于选择适当的浸取溶剂和浸取工艺,进行部分浸取处理,可有效地改变体系中的DOP含量,从而实现同一导管纵向上的硬度变化。 相似文献
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利用溶剂浸取分离法,研究了不同浸取溶剂种类、液固比、反应温度、反应时间、转速等因素对报废发烟剂中六氯乙烷回收率的影响,并对其固液浸取动力学进行了对比研究。发现以丙酮作为浸取溶剂,液固比在20:1~40:1,转速为450 r?min?1,在298 K条件下浸取发烟剂40 min,六氯乙烷的总浸取率(浸取到液相中的物料量与固体中初始物料总量的比率)可达90%以上,该浸取过程属于属固相产物层内扩散步骤控制类型浸取法能够很好地分离六氯乙烷,是一种分离处理报废发烟剂中的各组分的有效方法。 相似文献
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本文将Prausnitz提出的计算气体在混合溶剂中亨利常数的一般式中q1△项,分解为一个只与混合溶剂有关的参数A_(23)和一个只与气体在纯溶剂中亨利常数有关的常数两部分,为预测气体在混合溶剂中溶解度提供了一种新的方法。参数A_(23)由任一气体在混合溶剂中的溶解度进行估计。利用这一方法,可以从一种气体的溶解度预测其它气体在同一混合溶剂中的溶解度。在较大的温度范围内,预测了各种气体在醇—水混合溶剂中的溶解度,结果明显优于其它方法。 相似文献
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褐藻糖胶的萃取和反萃 总被引:5,自引:1,他引:4
研究了无机盐种类和浓度对N263萃取褐藻糖胶的影响. 结果表明,无机盐浓度是影响褐藻糖胶萃取的最主要因素, 褐藻糖胶的萃取率随盐浓度的增加而迅速降低,在无机盐存在下,增加萃取剂浓度并不能增加对褐藻糖胶的萃取. 用盐水溶液反萃不同条件下萃取的褐藻糖胶,结果表明,反萃率随盐浓度的增加而增加,在相同的氯离子浓度下,钠盐的反萃效率优于钙盐,随有机相中褐藻糖胶浓度的增加, 盐的反萃效率降低. 比较了不同溶剂作为稀释剂对用盐溶液反萃褐藻糖胶的影响,表明CCl4作为稀释剂时盐的反萃效率最低. 相似文献
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A pretreatment process using alcohol for the removal of chlorophyll a, b and β‐carotene from Chlorella vulgaris was developed to improve the yield and selectivity of lutein in the extract obtained by supercritical carbon dioxide extraction. Supercritical carbon dioxide extraction was carried out after pretreatment in the pressure range of 20 to 40 MPa and the temperature range of 40 to 80 °C. Ethanol and methanol were selected as elution solvents, of which ethanol was found most suitable for the elution, or pretreatment, process. The amounts of lutein and other compounds were analyzed by HPLC with the mixture of methanol and THF as the mobile phase. The amount of lutein in the extract increased with pressure, but decreased with extraction temperature. The highest recovery percentage and the selectivity of lutein were around 52.9 ± 0.02 % and 43.1 ± 0.02 %, respectively, obtained from supercritical carbon dioxide extraction with pretreatment and ethanol entrainer at 40 MPa and 40 °C. 相似文献
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Matthias Nomayo 《Advanced Synthesis \u0026amp; Catalysis》2000,342(2):175-178
Sodium dodecylsulfate solutions contaminated with polycyclic aromatic hydrocarbons (PAH), e.g. pyrene, were purified by addition of calcium or barium salt solution and precipitation of the corresponding calcium or barium dodecylsulfate. The precipitates were cleaned up using several organic solvents. Regeneration of sodium dodecylsulfate from the calcium dodecylsulfate precipitate was possible by solving the substance in an ethanol/water mixture (1:1) and precipitation of calcium hydroxide using sodium hydroxide as a precipitating agent. It was shown, that the calcium dodecylsulfate can be used directly as a tenside in a hot water solution or in an ethanol/water mixture. An extraction procedure could be developed, to remove the PAH contaminations quantitatively from the tenside solutions and concentrate them to small quantities by distillation of the organic solvents. It was demonstrated, that closed cycles of reagents in low need of energy are possible. The procedure was tested at a perylene contaminated kaolin sample. 相似文献
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Extraction of metal ions from the aqueous-organic solution containing dimethyl formamide(DMF), dimethyl sulfoxide(DMSO) and acetonitrile(AN) was investigated by using di-2-ethylhexyl-phosphoric acid(D2EHPA) as an extractant. The organic phase was a binary solution of D2EHPA and n-hexane, or D2EHPA and toluene, while the polar phase was a three component solution of metal salt, non-aqueous solvent and water. The extracted metal ions were Cr(III), Fe(III), Al, Cu, Ni, Co(II), Mg and Ag. The extraction behaviors may be explained by the solvation ability of non-aqueous solvents, the decrease in distribution of the extractant and extract into the organic phase, and the interaction between the extractant and non-aqueous solvents due to the dissolution of non-aqueous solvents in the organic phase. 相似文献
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以蔗渣为原料,在高温低酸浓度(H2SO4添加量占蔗渣绝干质量的0.176%)条件下预水解得到富含木糖的预水解糖液,再进一步深度酸解得到糠醛,并以混合有机溶剂实现了糠醛从水相中高效萃取分离。对蔗渣预水解条件、糠醛的有机溶剂萃取条件进行了探索,并采用FT-IR、XRD、SEM、TGA对蔗渣及预水解渣的形貌和结构进行了表征,利用紫外分光光度计对预水解过程中的木糖及深度酸解过程中的糠醛进行了定量检测。结果表明,在160 °C,液固比6:1,浓硫酸/蔗渣绝干质量为0.176%条件下,预水解液中木糖浓度最高(41.72 g/L);该预水解液直接在170 °C条件下深度酸解90 min,溶液中糠醛浓度最高可达15.91 g/L,糠醛摩尔得率最高为59.60%。以v(1,2-二氯乙烷):v(正丁醇) = 9:1的比例混合有机溶剂对水溶液中糠醛进行萃取,萃取相体积比为v(有机相):v(水相) = 2:1,糠醛的萃取率可达93.53%。 相似文献
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离子液体是一种结构可调的绿色溶剂,在催化、分离和电化学等领域具有广泛应用,特别是在有机物萃取分离方面,由于其低挥发性及功能可调,避免了传统有机溶剂可能导致的VOCs二次污染,有望成为绿色高效的新型萃取剂。本文系统地综述了离子液体在萃取分离烃类化合物、有机酸、醇类、酚类以及天然产物中的应用研究进展,详细论述了离子液体萃取分离有机物的萃取机理和影响因素,离子液体与溶质分子之间强的氢键、π-π、范德华力以及静电作用使其具有良好的萃取分离能力,表明离子液体是一类可替代有机溶剂实现高效萃取分离有机化合物的潜在溶剂。针对实际工作应用,还需解决其高黏度、高成本等问题,此外萃取后离子液体的回收仍是其大规模应用而需要亟待解决的难题。 相似文献
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Analysis of the reaction equilibrium and mass transfer in the extraction of penicillin G (Pen G) into an organic phase is an important research area to develop a cost-effective process for its separation from an aqueous fermentation media. In order to evaluate this, equilibrium experiments were first carried out to select the organic phase (composed of the carrier and solvent) that gives good values for the distribution of penicillin G between the aqueous and organic phases. An organic phase of Amberlite LA-2 in any of the solvents (Shellsol TK/butyl acetate/tributyl phosphate) gave high distribution coefficient and the stoichiometry of the reaction has been shown to follow a simple ratio of 2:2. The performance of the organic phases was evaluated in a membrane contactor and very high percentage extraction was achieved. The extraction was performed by contacting a “feed” solution containing penicillin G (flowing in the fiber side) with an “organic phase” of Amberlite LA-2 in one of the solvents (flowing on the shell side) of the contactor. The antibiotic solutes formed complex with the Amberlite LA-2 molecules which were transported across the fiber wall to the shell side and extracted in the organic phase. The extraction in once-through mode was low and the feed/organic solutions need to be recycled to increase the percentage extraction. In the recycle mode operated at flow rates of 3.6–4.4 mL/s, an extraction of 90–98% was achieved. A simple mathematical model and its semi-analytical solution presented here can be used to determine the overall mass transfer coefficient using the experimental values of the distribution coefficient, operating parameters and the dimensions of the membrane module. 相似文献