双水相中亮绿的萃取分离及测定

建立聚乙二醇-2000(PEG)-(NH4)2SO4双水相体系萃取光度法测定亮绿(BG)的新方法。测定了PEG相中亮绿吸收光谱和荧光光谱,研究了溶液酸度、盐用量、PEG用量及共存物质对体系测定的影响。结果表明,在溶液酸度pH=6,PEG用量5.0 mL,硫酸铵加入量2.0 g、测定波长630 nm时,PEG相中BG有最大吸光度。线性回归方程Y=0.005 83+0.054 53X,相关系数R=0.999 3,线性范围为0.01～0.17μg/mL。方法具有快速、灵敏、简便的优点,用于天然水中BG测定结果较好。用加入不同类型表面活性剂和光谱方法初步探讨了PEG与BG的相互作用。     

双水相分离提取胃蛋白酶和琼脂糖的初步研究

以聚乙二醇/硫酸钠双水相体系分离提取琼脂糖和胃蛋白酶.结果表明:琼脂糖的回收率高于90%,胃蛋白酶的回收率约为50%,两者最适宜的分离条件为:pH值为3,Na2SO4浓度为0.4 g·mL-1,PEG10000的浓度为0.002 mol·L-1.     

双水相萃取藻蓝蛋白的机理

采用荧光光谱的方法对双水相萃取藻蓝蛋白(PC)的机理进行了研究。不同分子量的聚乙二醇(PEG)对PC均有荧光猝灭作用。PEG与PC相互作用的热力学研究结果表明,PEG1000与PC的结合常数大于PEG2000和PEG4000,两者是熵驱动下的疏水作用力结合。不同的无机盐对PEG1000与PC结合的影响不同,其中Na₂SO₄使PEG1000-PC体系熵增效果最显著。同步荧光光谱的研究表明,PEG1000使PC色氨酸残基微环境的疏水性增强;Na₂SO₄通过促进PEG1000与PC的结合而使色氨酸残基微环境的疏水性进一步增强。单因素扫描实验的结果表明,PEG1000/Na₂SO₄体系双水相萃取纯化藻蓝蛋白(PC)的能力最强,符合PEG1000与PC分子相互作用的热力学规律。     

Liquid-liquid extraction of protease from cold-adapted yeast Rhodotorula mucilaginosa L7 using biocompatible and biodegradable aqueous two-phase systems

This work aimed to optimize the extraction of an extracellular protease produced by the cold-adapted yeast Rhodotorula mucilaginosa L7 using aqueous two-phase systems (ATPS) comprising polyethylene glycol (PEG) and sodium citrate or sodium tartrate. First, the biocompatibility of the phase forming agents was assessed. The results obtained with PEG-2000, PEG-4000, and PEG-6000 demonstrated that even at large PEG concentrations (32 wt%) the protease maintains its activity after 3 h of reaction, whereas an increase in salt concentration provokes a gradual decrease in protease stability. Subsequently, the partitioning of the protease in both types of ATPS was assessed, evaluating the effect of temperature, molecular weight, and concentration of PEG on protease purification, using two 2³-full factorial designs. The best partitioning conditions were obtained in PEG-6000/sodium tartrate-based ATPS, at 30ºC (with a yield of 81.09 ± 0.66% and a purification factor of 2.51 ± 0.03). Thus, considering the biodegradable characteristics of the system, the PEG/sodium tartrate ATPS is a viable and economic low-resolution step in protease purification, with a strong potential for future industrial application.     

Integrated process of extraction and purification of betanin from Opuntia ficus-indica using aqueous two-phase systems based on THF and sodium salts

This research present an integrated process for the extraction and purification of betanin from fruit of Opuntia ficus-indica. The extraction process was evaluated using different solvents (water, acetonitrile, ethanol and tetrahydrofuran), and then integrated into the purification process using aqueous two-phase systems (ATPS). The optimum conditions for extraction was with THF and the purification conditions determined to be 43 wt% of THF and 6 wt% of sodium citrate buffer (pH 5.5) at 25°C. A purification factor of 13.7 ± 0.5 fold, with a partition coefficient of betanin for salt-rich phase and the antioxidant capacity was increased ≈ 65%.     

双水相萃取法分离纯化黄酮类化合物的研究进展

综述双水相体系的组成、特点和双水相萃取法分离纯化黄酮类化合物的研究进展。双水相萃取是一项利用不复杂的设备,并在温和条件下进行简单的操作就可获得较高收率和有效成分的新型分离技术,该技术在黄酮类化合物的分离分析中取得了较好的效果,有望成为一种新型的黄酮类化合物的分离纯化方法。     

Solid–liquid extraction of terbium from phosphoric acid solutions using solvent‐impregnated resin containing TOPS 99

BACKGROUND: In this work, the solid‐liquid extraction of terbium from phosphoric acid solutions using solvent‐impregnated resin containing TOPS 99, an equivalent of di‐2‐ethylhexyl phosphoric acid, has been investigated. The parameters studied include equilibration time, acid concentration, amount of resin, metal concentration, kinetics, temperature, loading, elution, regeneration and recycling. RESULTS: FT‐IR results confirm the physical interaction of the extractant with the resin. The extraction of terbium with TOPS 99 impregnated Amberlite XAD 4 resin was acid dependent and transfer of metal follows a cation exchange mechanism. The loading capacity of TOPS 99‐impregnated resin for terbium was calculated to be 23.8 mg g^?1 resin. Controlling mechanism of the adsorption was found to be a chemical reaction following pseudo‐second‐order kinetics. The endothermic nature of extraction was confirmed by temperature studies. Among the various eluants studied, H₂SO₄ was the best. Regeneration and recycling of the resin indicated the resin can be used for continuous cycles. CONCLUSIONS: Terbium was successfully extracted from phosphoric acid using TOPS 99 extractant impregnated into Amberlite XAD4 with a maximum loading of 23.8 mg g^?1 resin and fully recovered with 1 mol L^?1sulfuric acid. The resin was subjected to seven cycles of extraction and elution without any loss of performance. Further studies showed that terbium could be separated from lutetium. Copyright © 2010 Society of Chemical Industry     

Enhancing the recovery and concentration of polyphenols from camu-camu (Myrciaria dubia H.B.K. McVaugh) by aqueous two-phase flotation and scale-up process

In this study, polyphenols obtained from camu-camu pulp residue were recovered and concentrated from aqueous two-phase flotation (ATPF) by evaluating different operating conditions, such as solvent type, pH, ammonium sulfate concentration, flotation time, air flow, and volumetric ratio. Under optimal conditions, the polyethylene glycol 400/ammonium sulfate ATPF system showed an efficiency of 81.02% and a concentration coefficient two times higher than traditional aqueous two-phase extraction. Experiments were also carried out on a semi-pilot scale, using an apparatus with a 2.5-L working volume. The results showed that the semi-pilot system was comparable to the smaller scale system.     

Optimizing the extraction of cobalt ions under response surface methodology and without organic solutions

In this study, response surface methodology was used to evaluate the extraction of cobalt ions using an aqueous two-phase system (ATPS). This method is environmentally benign and low-risk because water has replaced the poisonous and dangerous organic solvents in this extraction procedure. For the first time, a central composite design was employed to examine the effect of various factors on the extraction of cobalt ions. The findings of the experimental design revealed that the concentration and volume of cobalt ions had a considerable impact on the extraction percentage in the ATPS system. In contrast, the concentration of ammonium sulphate and pH had only a minor effect. The value of the correlation coefficient (R² = 0.9565) clearly shows the agreement between the mathematical model and the experimental results. The maximum extraction percentage was attained in optimum conditions (50% polyethylene glycol concentration, 3.75 M salt concentration, 0.5 ml cobalt volume, and pH 4).     

Development of novel adsorbent materials for recovery and enrichment of uranium from aqueous media

A new polymeric adsorbent bearing both hydrophilic groups providing swelling in water and amidoxime groups for chelating with uranyl ions (UO₂²⁺), has been developed and its adsorptive ability for recovering uranium from aqueous media has been investigated. The polymers obtained by irradiating the solution of polyethylene glycol (PEG) in acrylonitrile (AN) are defined as interpenetrating polymer networks (IPNs) and the adsorbent has been obtained by applying the amidoximation reaction to the IPNs with a conversion ratio of ∼ 60%. Kinetics of the conversion reaction of the cyano (CN) group to the amidoxime (HONCNH₂) group has been studied by reacting with hydroxylamine (NH₂OH) solution at a molar ratio of NH₂OH/CN = 1.25 in aqueous media at three different temperatures, 30, 40, and 50°C, for 3–4 days. The degree of amidoximation ratio was determined by UO₂²⁺ ion adsorption and FTIR spectrometry and the UO₂²⁺ ion adsorption values were found by both UV and gamma spectrometry and also by gravimetry. It was found that the polymeric adsorbent has a very high adsorption ability for uranium and quite a good stability in aqueous media. © 1997 John Wiley & Sons, Inc. J Appl Polym Sci 66: 2475–2480, 1997     

The optimization of aqueous two‐phase extraction of lysozyme from crude hen egg white using response surface methodology

BACKGROUND: Aqueous two‐phase extraction is a versatile method for separating biological particles and macromolecules. In the present wok, the feasibility of using PEG 4000/potassium citrate aqueous two‐phase system (ATPS) for recovering and purifying lysozyme was investigated. Response surface methodology was used to determine an optimized ATPS for purification of lysozyme from crude hen egg white. RESULTS: Mathematical models concerning the purification of lysozyme from chicken egg white in polyethylene glycol 4000 (PEG 4000)/potassium citrate ATPS are established using response surface methodology. Screening experiments using fractional factorial designs show that the pH of the system significantly affects the recovery and purification of lysozyme. An optimized ATPS was proved to be at pH 5.5 and 30 °C and contained 18% (w/w) PEG, 16% (w/w) potassium citrate, 3.75% (w/w) potassium chloride (KCl). Under those conditions, the specific activity, purification factor and activity yield for lysozyme were 31100 U mg^?1, 21.11 and 103%, respectively. CONCLUSION: The PEG 4000/potassium citrate ATPS has the potential to be applied to establish bioprocesses for the primary recovery and partial purification of lysozyme. © 2012 Society of Chemical Industry     

用乙醇-水从双液相棉粕中提取棉子糖的研究

用双液相萃取工艺处理后的棉籽粕为原料,乙醇-水溶液为溶剂进行了棉子糖的提取试验,并考察了影响浸出率的因素。在单因素实验的基础上,通过正交实验得出优化后的提取工艺条件为:乙醇体积分数为70%,提取温度60℃,提取时间150 m in,物料溶剂比1∶14(即每克物料需14 mL溶剂)。在此工艺条件下,棉子糖的浸出率为92.5%。     

Influence of pre-soaking conditions on ultrasonic extraction of Spirulina platensis proteins and its recovery using aqueous biphasic system

Ultrasonic aqueous extraction of proteins from dry Spirulina platensis at acidic (ACSU), alkali (ALSU), and neutral (NSU) conditions and its recovery using aqueous biphasic system (ABS) was studied. S. platensis was soaked in the solvent for 12 h prior to extraction. Neutral condition showed a higher protein release of 18.6 mg/ml at optimum conditions (solid–liquid ratio 1:20, 80% ultrasound amplitude, 100% ultrasound duty cycle, and 4ºC). The Box–Behnken design (BBD) suggested optimum conditions for ABS (PEG 6000, pH 8, and 5% NaCl) and gave 84.1% recovery. Although microscopic observations indicated structural changes, sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) and Fourier-transform infrared spectroscopy (FTIR) analyses confirmed that the proteins are intact.     

Optimization of a solvent extraction route for the recovery of Mo from petroleum refinery spent catalyst using Cyphos IL 102

In this study, trihexyl(tetradecyl)phosphonium bromide (Cyphos IL 102) diluted in toluene has been explored for the first time as an organic phase for the extraction, separation, and recovery of Mo(VI) from hydrochloric acid medium. The study focuses on the recovery of metals from spent catalyst, a hazardous solid waste. The metal recovered in the form of metal oxide has further applications in various fields. The widespread use of solvent extraction for metal recovery can be assigned to its economic feasibility and the built-in concentration step thereby providing an appropriate commercial technology for the beneficiation of low-grade sources of metals and recovery of substances from complex matrices. The influence of fundamental extraction variables on Mo(VI) extraction and loading and recycling capacity of the extractant has also been evaluated. Binary separations of Mo(VI) from other associated metal ions have been achieved with high separation factors. Optimized conditions have been employed for the extraction and recovery of Mo(VI) from petroleum refinery spent catalyst leach liquor containing Mo-1141.18 ppm, Al-2158.42 ppm, Ni-270.39 ppm, and Co-61.82 ppm. Quantitative and selective extraction (98.4%) of Mo from spent petroleum refinery catalyst was achieved in two stages at A:O = 3:2 using 2.0 × 10^?2 mol/L Cyphos IL 102. Almost 99% Mo was stripped with 1.0 mol/L (NH₄)₂CO₃ in two stages at O:A = 1:1. MoO₃, obtained from the stripped solution by thermal decomposition was characterized by XRD, FESEM, and EDX techniques. Economical and environmental aspect of present work is supported by high loading capacity and reusability of extractant.     

蒲公英总黄酮在聚乙二醇-硫酸铵双水相体系中的分配与提取

蒲公英中内含的黄酮类物质具有较高药用价值,用双水相萃取法提取植物中有效成分是新型提取高附加值生物质的有效方法。本文考察了PEG/(NH4)2SO4双水相体系萃取分离蒲公英总黄酮时聚乙二醇相对分子质量、PEG质量分数、(NH4)2SO4质量分数、温度、pH值5个因素对分配行为的影响,并通过正交实验优化了工艺条件。结果表明最佳双水相提取工艺条件为：(NH4)2SO4质量分数18%,PEG1000质量分数23%,pH值5.34,提取温度25℃,NaCl盐的存在与否对萃取影响很小,蒲公英中总黄酮的提取率可达5.47%。因此,使用双水相法提取蒲公英总黄酮是该类提取技术中一种更加绿色环保和高效的方法。     

Recovery of value‐added globular proteins from tannery wastewaters using PEG – salt aqueous two‐phase systems

Leather processing involves discharge of high‐value soluble globular proteins in the wastewater. The recovery of value‐added products from the wastewaters is gaining more importance in the context of recovery of wealth from waste. The recovery of these globular proteins from tannery wastewater was selected as a practical model system to study the implementation of polyethylene glycol (PEG)‐sulfate aqueous two‐phase systems (ATPS). The partition coefficient of bovine serum albumin is comparable to that of soluble proteins from tannery wastewaters. The influence of concentration of polymer, salt, pH and temperature on the partitioning of soluble proteins from tannery wastewaters has been studied. The PEG6000 + sodium sulfate + water system provide better partitioning of these soluble proteins as compared to PEG6000 + ammonium sulfate system. The maximum protein recovery yield for PEG6000 + sodium sulfate + water system at 20 °C is 92.75%. The influence of temperature indicates the recovery of proteins from tannery wastewater to be better at lower temperature. The findings of these studies raise the potential application of ATPS processes for protein recovery from complex biological systems. Copyright © 2006 Society of Chemical Industry     

Separation and recovery of vanadium from leached solution of spent residuehydrodesulfurization (RHDS) catalyst using solvent extraction

Leached solution, generated by oxalic acid washing of spent residue hydrodesulfurization (RHDS) catalyst, was used for separation and recovery of vanadium. First of all, solvent extraction, using mixture of 20% (v/v) Alamine-336 and 5% (v/v) tri-butyl phosphate (TBP) as a phase modifier, was conducted to extract molybdenum completely at pH 0.50. Then molybdenum-free solution was used for vanadium extraction at pH 1.25 with 20% Alamine-336 and 5% TBP. Stripping of vanadium from loaded organic solution was performed with 1.5 M H₂SO₄ at O/A phase ratio of 5:1 where more than 99% of vanadium was stripped in two stages. The stripped vanadium solution was further processed by precipitating with ammonium hydroxide to recover ammonium-meta-vanadate which was calcined to obtain vanadium pentoxide. Finally a conceptual process was established for recovery of high purity vanadium pentoxide from oxalic acid leached solution of spent residue hydrodesulfurization (RHDS) catalyst.