Stability of penicillin G in ionic liquid [Bmim]PF6

The extraction of penicillin G by ionic liquid[Bmim]PF_6 has exhibited promising prospect.The stability of penicillin G is crucial for developing a green ionic liquid-based extraction technology.In this work,the stability of penicillin G in[Bmim]PF_6 was systematically investigated.The results showed the stability of penicillin G was significantly influenced by pH and temperature.It tended to be more stable when pH value increased from 1.5 to 4.0 and the temperature gradually decreased.The half-life(t_(1/2))of penicillin G in[Bmim]PF_6 was 17.7 h in the optimal technological condition(pH 2.0 and 10°C),which is enough for the requirement of extraction technology.The reaction of penicillin G in[Bmim]PF_6 followed the first order kinetics in the pH range 2.0–4.0.Three isomers of penicillin G were found through rearrangement at pH 2.0,and their structures were not affected by temperature.     

Effect of Ionic Liquid 1-Butyl-3-Methyl-Imidazolium Dihydrogen Phosphate Pretreatment on Pyrolysis of Lignin

In order to improve the yield of liquid fraction and phenolics content during lignin pyrolysis, an effective method of lignin pyrolysis through the pretreatment of lignin by an acidic ionic liquid 1-butyl-3- methyl-imidazolium dihydrogen phosphate ([Bmim]H₂PO₄) at low temperature is investigated in this study. It is found that [Bmim]H₂PO₄ pretreatment increases the total yield of liquid products of lignin pyrolysis compared to that of original lignin. The [Bmim]H₂PO₄ pretreatment temperature significantly impacts the behaviors of the lignin pyrolysis. In the temperature range of 50 to 150°C, the yield of the overall liquid product obtained by pyrolysis of the sample pretreated at 50°C is the highest. After pretreatment, the [Bmim]H₂PO₄ can be efficiently recovered, but the structure and stability of the [Bmim]H₂PO₄ have been changed. The FTIR analysis shows that the ionic liquid [Bmim]H₂PO₄ pretreatment can break hydrogen bonds, ether linkages and ester bonds in lignin.     

Recycling Chiral Imidazolidin‐4‐one Catalyst for Asymmetric Diels–Alder Reactions: Screening of Various Ionic Liquids

Various imidazolium ionic liquids such as [Bmim]PF₆, [Bmim]SbF₆, [Bmim]OTf and [Bmim]BF₄ were screened for recycling an organic catalyst [(5S)‐5‐benzyl‐2,2,3‐trimethylimidazolidin‐4‐one ( 1 )] for asymmetric Diels–Alder reactions. Good yields and enantioselectivies (up to 85% yield and 93% ee) were obtained from reactions in [Bmim]PF₆ or [Bmim]SbF₆. However, reactions in [Bmim]OTf or [Bmim]BF₄ gave racemic products in low yields. Isolation of the products by simple extraction using diethyl ether allowed recycling of the ionic liquid containing the immobilized catalyst in subsequent reactions without significant decrease of yields and enantioselectivities.     

Partitioning Behavior of Tetracycline in Hydrophilic Ionic Liquids Two-Phase Systems

Ionic liquids-based aqueous two-phase system (ILs-ATPS) offers an alternative approach for the extraction of tetracycline (TC) through their partitioning between two phases. The procedure was composed of 1-butyl-3-methylimidazolium halide ([Bmim]X(X = Cl, Br)) and K₂HPO₄ using a liquid-liquid extraction technique. The influence factors on partition behavior of TC were optimized systematically, including the quality of salts and IL, the amount of TC, pH value, and temperature. The maximum extraction efficiency of TC could reach 99%. The interactions between the ATPS and TC have been examined by isothermal titration calorimetry. Extraction of antibiotics TC using ILs-ATPS could achieve nearly complete extractions in a single-step by way of the proper tailoring of their concentrations in the aqueous media.     

Catalytic conversion of fructose into furans using FeCl3 as catalyst

Conversion of fructose into furan derivates 5-hydroxymethylfurfural (HMF) and 5-ethoxymethylfurfural (EMF) was performed in ethanol-[Bmim]Cl solvent systems, catalyzed by FeCl₃. HMF was obtained in a high yield of 90.8% for 4 h at 100 °C in 1-butyl-3-methylimidazole chloride ([Bmim]Cl). The ratio of [Bmim]Cl to ethanol showed a remarkable effect on the yields of HMF and EMF. The maximum EMF yield of 30.1% was obtained in a mixed solvent of [Bmim]Cl (0.5 g) and ethanol (4.5 g). On the meanwhile, HMF was obtained in a yield of 60.3%.     

离子液体[Bmim]BF_4合成反应后的纯化工艺

考察了离子液体[Bmim]BF4(四氟硼酸1-丁基-3-甲基咪唑)合成反应后纯化步骤中CH2Cl2用量、H2O用量及不同萃取水洗方式等因素对[Bmim]BF4得率的影响,得到了纯化时合理的CH2Cl2用量及H2O用量,质量比为:CH2Cl2:H2O:[Bmim]BF4粗品=7:3:10,其中H2O采用多次加入方式进行萃取水洗效果较好、离子液体的得率较高,纯化后[Bmim]BF4得率约为93.15%。     

离子液体/盐双水相萃取分离锁阳中熊果酸

利用1-丁基-3-甲基咪唑氯([Bmim]Cl)和磷酸氢二钾(KH2PO4)双水相体系萃取分离锁阳中熊果酸,首先对[Bmim]Cl质量分数、KH2PO4质量分数、熊果酸粗提取液质量分数、NaCl质量分数、pH进行单因素研究,确定双水相体系组成为质量分数25%[Bmim]Cl-21%KH2PO4。然后,利用Box-Benhnken Design实验,对黄酮粗提取液质量分数、pH、NaCl质量分数进行了优化,结果表明:粗提液质量分数8.5%、NaCl质量分数1%、pH=4.7,熊果酸萃取率可达97.85%,与预测值98.3%接近。说明该优化工艺具有可行性。     

Liquid phase catalytic dehydration of glycerol to acrolein over Brønsted acidic ionic liquid catalysts

Liquid phase dehydration of glycerol to acrolein catalyzed by Brønsted acidic ionic liquids (BAILs) using semi-batch reaction technique was investigated. For the BAILs catalysts, the acrolein yields were in an order of [Bmim]H₂PO₄ > [Bmim]HSO₄ > [BPy]HSO₄ > [PSPy]HSO₄ > [N₂₂₂₄]HSO₄ > [PSPy]H₂PO₄ > [BPy]H₂PO₄ > [N₂₂₂₄]H₂PO₄. When [Bmim]H₂PO₄ and [Bmim]HSO₄ were used as the catalysts at 270 °C with the molar ratio of catalyst to glycerol of 1:100, the acrolein yields were 57.4% and 50.8%, respectively, at complete conversion of glycerol. The BAILs with [Bmim] cation and moderate acidity favored the formation of acrolein in liquid phase glycerol dehydration.     

Study of phase behavior and Congo red dye partitioning in aqueous two-phase systems composed of hydrophilic alcohols (1-propanol/ 1-butanol) and sodium salts

ABSTRACT

The partitioning of the Congo red dye in ATPSs formed by alcohols (1-butanol, 1-propanol)/sodium salts was considered. Binodal and the LLE data were experimentally determined at 298.15 K. The salting-out abilities of the salts follow the order Na₃C₆H₅O₇ > NaH₂PO₄ > C₂H₃ O₂Na. The phase-forming abilities of the alcohols follow the order: 1-butanol > 1-propanol. The four-parameter equation was applied to correlate the binodal curves data. Therefore, The Bancroft and Othmer-Tobias equations were used to prove the reliability of the corresponding LLE data. ATPS composed of 6.5% of 1-butanol and 20% of Na₃C₆H₅O₇ had the highest values of extraction by the yield of 98.54%.     

Study on removal of Fe3+ from sodium dihydrogen phosphate by emulsification solvent extraction

Wet-process phosphoric acid (WPA) is gradually paid attention to in recent years. However, there are some undesirable impurities (Fe³⁺, Al³⁺, Mg²⁺) in WPA, which will degrade the quality of sodium dihydrogen phosphate (NaH₂PO₄) products. To get the superior grade NaH₂PO₄, the WPA should be purified. Enhancing the pH of the solution, often to 4, can remove most of the metal ions, but there is still some Fe³⁺ which has great effect on the NaH₂PO₄ crystal products, seem to be irregular long strips. Therefore, before the neutralized NaH₂PO₄ solution is concentrated, the Fe³⁺ must be removed.The emulsification extraction of Fe³⁺ from sodium dihydrogen phosphate (NaH₂PO₄) solution by di(2-ethylhexyl)phosphoric acid (D2EHPA) is investigated. The good extraction efficiency of Fe³⁺ with D2EHPA from NaH₂PO₄ solution by emulsification extraction is verified. Meanwhile, to study the advantages of the emulsification extraction process, the major influencing factors, such as the D2EHPA volume fraction, the phase volume ratio, the initial pH of NaH₂PO₄ solution, the stirring time and agitation speed on the extraction efficiencies of Fe³⁺, are studied, and the optimal process conditions are obtained. The results of extraction experiments from practical NaH₂PO₄ solution show that superior grade NaH₂PO₄ can be obtained by three stages of extraction under appropriate condition.     

Effect of small amount of water on the dynamics properties and microstructures of ionic liquids

A series of systems of 1‐butyl‐3‐methylimidazolium acetate ([Bmim][Ac]), 1‐butyl‐3‐methylimidazolium tetrafluoroborate ([Bmim][BF₄]), and 1‐butyl‐3‐methylimidazolium bis(trifluoromethylsulfonyl)imide ([Bmim][Tf₂N]) with a small amount of water were simulated. Viscosities of systems were obtained by nonequilibrium molecule dynamics simulation and the results show that the viscosities change in different ways: for [Bmim][BF₄] and [Bmim][Tf₂N], viscosities decrease rapidly in the first stage, and then decrease slowly with the increase of water content. But for [Bmim][Ac], the viscosities increase first and then decrease. The unique phenomenon of [Bmim][Ac] can be attributed to the formation of chain‐like structure of anion???water???anion???. Hydrogen bond (HB) interaction between ion pairs is weakened, but the number of HB between water and anions increases with increase of water content. Besides, the microstructures of water in ionic liquids‐water systems were compared and found that the distribution of water is more concentrated in [Bmim][Tf₂N]‐H₂O system, while it is isotropy in [Bmim][Ac]‐H₂O system. © 2016 American Institute of Chemical Engineers AIChE J, 63: 2248–2256, 2017     

Separation and Purification of Aloe Anthraquinones Using PEG/Salt Aqueous Two-Phase System

The anthraquinones were extracted from Curacao aloe leaves. Aqueous two-phase system (ATPS) of polyethylene glycol (PEG)/salt, coupled with spectrophotometry and high performance liquid chromatography (HPLC) were employed for the first time as an attractive alternative for the downstream processing of aloe anthraquinones, mainly for the removal of the impurities without additional steps. The influence factors such as molecular mass and concentration of PEG, type, and concentration of neutral salt, temperature, and pH on the phase partition behavior of ATPS had been studied. Under the optimal condition, the highest extraction yield 90.54% was obtained in PEG phase using PEG-6000/(NH₄)₂SO₄ system to a mass ratio of 2:1 at 40°C, pH 3.0 with 0.6 g sodium chloride added. The reverse extraction of anthraquinones from the PEG phase was achieved with a recovery of 70.15% by adjusting the pH. Meanwhile, the PEG could be recycled. The major components in aloe anthraquinones of aloe-emodin and chrysophanol were analyzed by HPLC before and after ATPS extraction process. Compared with conventional purification methods, this technique can be completed in one operation; besides it is low-cost and environmentally friendly.     

Enrichment of Aromatic Compounds Using Ionic Liquid and Ionic Liquid-Based Aqueous Biphasic Systems

Both hydrophibic [C₈mim][PF₆] and [C₄mim]Cl/(K₂CO₃, K₂HPO₄ or K₃PO₄) aqueous biphasic system (ABS) were employed for the enrichment of aromatic compounds including nitrobenzene, 4-nitrophenol, phenol and aniline from aqueous solutions. In [C₈mim][PF₆] enrichment system, the distribution ratio (D) of nitrobenzene and aniline increase with the increasing of pH values of aqueous phase from 2 to 8, but there is no obvious change for 4-nitrophenol and phenol. And the D values of the aromatic compounds decrease with the phase ratio change from 1/5 to 1/30 (IL phase volume/aqueous phase volume). In [C₄mim]Cl/(K₂CO₃, K₂HPO₄ or K₃PO₄), the distribution ratio increase with the increasing of the salts concentrations. The distribution ratio order in [C₈mim][PF₆] and [C₄mim]Cl/kosmotropic salt ABS is nitrobenzene > phenol > aniline > 4-nitrophenol. It is expected that these results are promising for the removal of the aromatic compounds from water, especially for sample enrichment in analytical science.     

Fabrication of cellulose membrane with “imprinted morphology” and low crystallinity from spherulitic [Bmim]Cl

In the present study, regenerated cellulose membrane with “imprinted morphology” and low crystallinity was fabricated from the crystal cellulose/[Bmim]Cl solution. Spherulites of 1‐butyl‐3‐methilimidazolium chloride ([Bmim]Cl) and cellulose/[Bmim]Cl solution were observed using polarized optical microscopy under certain condition. The fabricated cellulose membranes presented some particular characteristics compared with the membrane prepared from traditional cellulose/[Bmim]Cl solution. All the fabricated membranes were characterized by optical microscope, Wide‐angle X‐ray diffraction (WAXD), thermo‐gravimetric analysis, and mechanical testing. The images showed that the resulting membranes prepared from crystal cellulose/[Bmim]Cl solution were “imprinted” with patterns which originated from the crystalline structure of [Bmim]Cl. The results of WAXD showed that the obtained cellulose membrane exhibited low diffraction peaks and crystallinity of approximately 24.57%. Furthermore, the low crystallinity led to the low mechanical property (27.5 MPa), thermal stability (315.4 °C), and high moisture regain (9.5%). © 2016 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2016 , 133, 43798.     

Partitioning of lysozyme in aqueous two-phase systems containing ethylene oxide-propylene oxide copolymer and potassium phosphates

Lysozyme partitioning in EO₅₀PO₅₀/potassium phosphate aqueous two-phase systems (ATPS) was studied. In the work, the influence of EO₅₀PO₅₀, potassium phosphate and sodium chloride concentration in the ATPS on lysozyme partition coefficient and separation yield was examined. In addition, the influence of the pH of potassium phosphate solution was also investigated. A Box–Behnken design was defined, and response surface models for the partition coefficient K and percentage yield of the enzyme in the top phase Y were calculated. Among the examined factors, the NaCl concentration had the highest influence on lysozyme separation parameters. This influence can be explained mainly by the hydrophobic interactions between the protein and the phase-forming components. A maximum partition coefficient K_L1, yield Y_L1 and Y_L2 were predicted for EO₅₀PO₅₀, potassium phosphate and NaCl concentrations of 17.40, 22.67% and 0.85 mol/l, respectively, and for pH 9.0. A good agreement was obtained between the experimental and the predicted results.     

Deep Desulfurization of Gasoline Fuel using FeCl3-Containing Lewis-Acidic Ionic Liquids

The FeCl₃-containing Lewis-acidic ionic liquids (ILs) [C₆mim]Cl/FeCl₃(1:1.5), [C₆mim]Cl/FeCl₃(1:2), [C₈mim]Cl/FeCl₃(1:1.5), and [C₈mim]Cl/FeCl₃(1:2) were used as extractants for desulfurization of model fuel and gasoline fuel, respectively. The results demonstrate that these ILs are effective for the removal of sulfur compounds from model fuel under different mass ratio of IL to model fuel (1:1, 1:3, 1:5, 1:10) at 25°C. The extractive performance of ILs increased as the molar ratio of FeCl₃ to [C_nmim]Cl(n = 6, 8) varied from 1:1 to 1:2. The selectivity of sulfur compounds by extraction process followed the order of dibenzothiophene (DBT)>benzothiophene (BT) > 4,6-dimethyldibenzothiophene (4,6-DMDBT). The sulfur removal of gasoline fuel containing sulfur content of 440.3 ppmw could be up to 85.8%; that is to say that the sulfur content of gasoline fuel varied from 440.3 ppmw to 62.4 ppmw after one extraction stage. Moreover, the [C₆mim]Cl/FeCl₃(1:2) can be recycled for at least 4 times with a little decrease in the desulfurization activity.     

Extraction of Puerarin using Ionic Liquid Based Aqueous Two-Phase Systems

Various ionic liquid-based aqueous two-phase systems (IL-ATPS) were evaluated to extract puerarin. The results indicated that the nature of ILs, the salting-out ability of salt, and the acidity and basicity of the salt-rich solution had important influence on the extraction efficiency. Various factors were optimized systematically, that is, the amount of IL, salt, puerarin, and short-chain alcohol. Under the optimal experimental conditions (the amount of K₂HPO₄ 0.30–0.42 g/mL, [Bmim]Br 0.30–0.36 g/mL and 1.0 mL puerarin stock solution), the extraction efficiency of puerarin was over 99% by a single-step extraction, which indicated that the evaluated IL-ATPS was a prospective extraction medium. Finally, the IL-ATPS was successfully used to extract puerarin from Radix Puerariae Lobatae extracts.     

Flame‐retardant finishing of cotton fabrics using polyamino carboxylic acids and sodium hypophosphite

The purpose of this research was to use polyamino carboxylic acids (PACAs) and their combination with sodium hypophosphite (NaH₂PO₂) as a flame‐retardant finishing system for cotton fabrics. Flammability of cotton fabric was evaluated by 45° flammability test, differential scanning calorimetry and measuring the char yield. The combination of polyamino carboxylic acids and sodium hypophosphite as a phosphorus‐containing catalyst reduces the flammability of cotton. The pyrolysis properties and the results of char yield of the finished cotton show that with increasing amount of catalyst, the flame retardancy increases. Fastness against multiple laundering, whiteness and tensile strength of the cotton finished with PACAs/NaH₂PO₂ to multiple standard laundering have been studied, too. The flame retardancy effect has an acceptable washing fastness. Whiteness and tensile strength of the finished cotton do not change significantly. Copyright © 2012 John Wiley & Sons, Ltd.     

Partitioning behaviour of cephalexin and 7‐aminodeacetoxicephalosporanic acid in PEG/ammonium sulfate aqueous two‐phase systems

In order to develop an aqueous two‐phase system (ATPS) for cephalexin synthesis with extractive bioconversion, the partitioning behaviour of cephalexin and 7‐aminodeacetoxicephalosporanic acid (7‐ADCA) in poly(ethylene glycol) (PEG)/salt ATPS were examined. Parameters such as PEG size, salt type and tie line length were investigated to find a primary extraction system. In PEG400/ammonium sulfate and PEG400/magnesium sulfate systems, the partition coefficient of cephalexin (K_C) was larger than 1 while that of 7‐ADCA (K_A) deviated about 1.5. Addition of neutral salts, surfactants and water‐miscible solvents were also investigated in the primary ATPS in order to improve the separation efficiency. K_C greatly increased when neutral salts and surfactants were added to the PEG400/ammonium sulfate primary systems whereas K_A was only slightly higher than that of the additive‐free ATPS. In an improved ATPS for extractive bioconversion, consisting of PEG400 (20% w/w), ammonium sulfate (17.5% w/w), methanol (5% w/w) and NaCl (3% w/w), a K_C value of up to 15.2 was achieved; K_A was 1.8; K_P (partition coefficient of phenylglycine methyl ester) was 1.2 and the recovery yield of cephalexin was 94.2%. The results obtained from the extractive bioconversion of cephalexin in the improved ATPS showed that it is feasible to perform such an enzymatic process in an ATPS and the system offers the potential as a model for enzymatic synthesis of some water soluble products. © 2001 Society of Chemical Industry     

Rheological properties of cotton pulp cellulose dissolved in 1‐butyl‐3‐methylimidazolium chloride solutions

Rheological properties of cotton pulp dissolved in 1‐butyl‐3‐methylimidazolium chloride ([Bmim]Cl) solutions were characterized using an advanced rheometer. The complex viscosity, dynamic modulus, and shear viscosity at different temperature were studied. In the steady shear measurements, all the solutions show a shear‐thinning behavior at high shear rates. The complex viscosity as a function of frequency was fitted by extended Carreau–Yasuda model. In all cotton pulp/[Bmim]Cl solutions, the complex dynamic viscosity (η*) and steady shear viscosity (η_a) followed the Cox–Merz rule only at lower frequency. The effects of tested temperature on viscosity and viscoelastic behavior of the solutions were also investigated. The value of activation energy for the dissolution of cotton pulp in ionic liquids was 65.28 kJ/mol at the concentration of 10 wt% and was comparable with the ones for the dissolution of cellulose in NMMO. POLYM. ENG. SCI., 2011. © 2011 Society of Plastics Engineers