Effects of modifiers on the supercritical CO<Subscript>2</Subscript> extraction of glycyrrhizin from licorice and the morphology of licorice tissue after extraction

Optimal conditions for the supercritical carbon dioxide (scCO₂) extraction of glycyrrhizin from licorice (Glycyrrhiza glabra) were investigated, with an emphasis on the types and levels of modifiers. The morphology of the licorice tissue remaining after the scCO₂ extraction of glycyrrhizin was examined by scanning electron microscopy, coupled with measurements of absolute density. Conventional organic solvent extraction was also carried out for purpose of quantitative comparison. At 50 MPa and 60°C glycyrrhizin could not be extracted with pure scCO₂, while a considerable amount of glycyrrhizin was extracted when water was added to scCO₂ as a modifier. The highest recovery was found to be about 97% when 70% aqueous methanol was added to scCO₂ at a concentration of 15%. The optimal pressure and temperature for the supercritical fluid extraction of glycyrrhizin were observed to be 30 MPa and 60°C, respectively. Under these conditions, the percentage recovery of glycyrrhizin attained a maximum value of 102.67±1.13% within 60 min. Furthermore, in the case of scCO₂ modified with 70% aqueous methanol, the licorice tissue obtained after extraction was found to be severely degraded by excessive swelling, and the absolute density of the licorice residues was observed to be the highest.     

Design of a new cartridge for selective solid phase extraction using molecularly imprinted polymers: Selective extraction of theophylline from human serum samples

This paper describes design of a new cartridge for selective solid phase extraction (SPE) using molecularly imprinted polymers (MIPs). The apparatus which is termed solvent extraction-MISPE (SE-MISPE) cartridge, consisted of a modified conventional micro test tube and has been developed to perform simultaneous forward-extraction of analyte from aqueous sample solution to an organic phase and back-extraction to MIP solid phase. In order to evaluate the performance of the proposed method, extraction of theophylline (THP) from human serum sample was investigated. An appropriate amount of THP-imprinted polymer was placed in the bottom of the micro tube and an organic solvent pipetted onto it and left to swell the polymer completely. A polyethylene frit to secure MIP particles was positioned by two Teflon rings such that it was fixed below the level of the organic layer. Then, aqueous sample solution containing THP was layered over the organic phase and the lid was closed. After completion of extraction, the organic and aqueous phases were removed and the adsorbed analyte was desorbed using a polar organic solvent. In order to reach the highest recovery, the experimental parameters such as the type of organic solvent, pH and ionic strength of aqueous phase, organic to aqueous volume ratio, time of extraction, type and amount of desorbent solvent were optimized. Under the experimental conditions, a plot of HPLC peak areas vs. initial concentrations of THP in the concentration interval of 0.5–30 μg ml⁻¹ showed a good linearity (r = 0.9974). The limit of detection (LOD) and limit of quantification (LOQ) based on three and ten times of the noise of HPLC profile were 0.09 and 0.3 μg ml⁻¹, respectively. The relative standard deviation (RSD) of the proposed method for the extraction and determination of 5 μg THP from 200 μl standard sample solution for 3 replicate measurements was 3.5%. The results showed that by means of the proposed cartridge, THP could significantly separate from the other structurally related compounds such as theobromine (THB) and caffeine (CAF). The added THP could be quantitatively recovered (79–83%) from the serum samples by the proposed procedure, being thus a guarantee of the accuracy of the SE-MISPE procedure. In addition, the loss of capability of the SE-MISPE cartridge was not considerably observed after 10 times loading and elution cycles.     

β-Carotene extraction from Dunaliella salina by supercritical CO2

This paper reports the results of supercritical carbon dioxide (scCO₂) extraction of β-carotene from Dunaliella salina as potential alternative to conventional organic solvent extraction. In pilot-scale scCO₂ experiments, the pressure, temperature, and co-solvent concentration were varied. The supercritical extraction at 500 bar, 70 °C, and 10 wt% ethanol as co-solvent yielded in the highly efficient pigment recovery of over 90%. Techno-economic assessment demonstrated higher energy consumption for the scCO₂ extraction that was compensated by lower solvent costs. Thus, comparable pigment production costs to the reference extraction with n-hexane were estimated for the scCO₂ process. Due to the green solvent properties of scCO₂ and ethanol, this approach is highly promising for extraction of algal biomass in industrial scale.

     

Application of organic mono-phase and organic–aqueous two-liquid-phase systems in microalgal conversion of androst-4-en-3,17-dione by Nostoc muscorum

Organic mono-phase and organic–aqueous two-phase systems were applied for 17-carbonyl reduction of androst-4-en-3,17-dione to testosterone by whole cells of the microalga Nostoc muscorum (Nostocaceae). To investigate the correlation between solvent hydrophobicity and biotransformation yield in mono- and biphasic systems, a range of 16 organic solvents with log P_octanol values (logarithm of the solvent partition coefficient in the n-octanol/water system) between ? 1.1 and 8.8 were examined. Organic solvents with log P_octanol values greater than 7, such as hexadecane and tetradecane, provided the best biocompatibility with the bioconversion by algal cells. The data also indicated that the highest yields were obtained using organic–aqueous (1:1, v/v) biphasic systems. The optimum volumetric phase ratio, reaction temperature and substrate concentration were 1:1, 30°C and 0.5 mg mL^?1, respectively. Under the mentioned conditions a fourfold increase in biotransformation yield (from 7.8±2.3 to 33.4±1.8%) was observed.     

Efficient method for the quantitation of urinary leukotriene E4: extraction using an Empore C18 disk cartridge

We describe here an efficient procedure for the precise quantitation of leukotriene E₄ (LTE₄) in a small volume of urine, which was achieved mainly by the use of an Empore extraction disk cartridge. After addition of [³H]LTE₄ to 2 ml of urine, an Empore C₁₈ cartridge was used for initial extraction of the urine, which resulted in the extraction of LTE₄ in a small volume of solvent. The eluate could then be injected onto a high-performance liquid chromatography column without further concentration. After separation by high-performance liquid chromatography, LTE₄ was extracted from the effluent using an Empore C₁₈ cartridge. The concentration of LTE₄ was subsequently quantified by enzyme immunoassay. LTE₄ can be recovered from urine with sufficient efficiency (69.9±4.7%, mean±S.D., n = 101). The coefficient of variation of the assay procedure was less than 10%. When urine was spiked with different amounts of LTE₄, the recovery of LTE₄ added to the urine specimen was less than 120%. The concentration of LTE₄ in urine from normal healthy subjects was 48.0±15.3 pg/mg creatinine (n = 15).     

A sensitive and precise isotopic assay of ATPase activity

A manual ATPase assay which measures the release of ³²P_i from [γ-³²P]ATP is described. Sodium dodecyl sulfate is used to terminate the enzyme reaction and extraction of the phophomolybdate complex into xylene: isobutanol is used to separate ³²P_i from [γ-³²P]ATP for quantitation by scintillation counting. The three-step assay is rapid (75–90 samples/h) and minimizes hydrolysis of ATP due to exposure to acidie conditions. The extraction procedure separates 10⁻¹⁵ to 10⁻⁷ mol of ³²P_i from aqueous solution with an efficiency of 100,7 ± 0.62%. Less than 1% of unhydrolyzed [γ-³²P]ATP is extracted. Extraction efficiency is not affected by protein or salts commonly present in enzyme incubation mixtures. Results obtained with this assay are precise, with an intraassay coefficient of variation of 0.6% and an interassay coefficient of variation of 1.8%. The results are comparable to results obtained with a spectrophotometric assay, with a correlation coefficient of 0,996, though assay performance and sensitivity are greatly improved with the isotopic assay.     

Ultrasound-assisted extraction of flaxseed oil using immobilized enzymes

An aqueous enzymatic process assisted by ultrasound extraction (AEP-UE) was applied to the extraction of oil from flaxseed (Linum usitatissimum L.). The highest oil recovery of 68.1% was obtained when ground flaxseed was incubated with 130 U/g of cellulase, pectinase, and hemicellulase for 12 h, at 45 °C and pH 5.0. The IC₅₀ values of oil obtained by AEP-UE and organic solvent extraction (OSE), as measured by DPPH scavenging activity essay, were 2.27 mg/mL and 3.31 mg/mL. The AEP-UE-derived oil had a 1.5% higher content of unsaturated fatty acids than the OSE-derived oil. AEP-UE is therefore a promising environmentally friendly method for large-scale preparation of flaxseed oil.     

Butanol recovery from aqueous solution into ionic liquids by liquid–liquid extraction

Biobutanol has currently attracted considerable attention as an alternative biofuel to the petroleum-derived fuel due to several advantages including high energy content, low water absorption and easy application to the existing gasoline infrastructure. However, its production has still faced many obstacles to overcome including lack of energy-efficient butanol separation process from fermentation broth. To solve this issue, the extraction behavior of butanol from aqueous media into a variety of imidazolium-based ionic liquids (ILs) was investigated by liquid–liquid extraction. To understand the effect of ILs properties, the solvent characteristics of ILs such as mutual solubility of feed solvent (water) and extraction solvent (IL), distribution coefficient of butanol between water and IL, selectivity, and extraction efficiency were correlated with hydrophobicity and polarity of ILs. The butanol distribution between ILs and water strongly depends on the hydrophobicity of anions of ILs followed by the hydrophobicity of cations of ILs. On the other hand, butanol extraction efficiency and selectivity depend on the polarity of ILs. Considering extraction efficiency and selectivity, [Tf₂N]-based ILs among the tested ILs showed to be the best extract solvent for the recovery of butanol from aqueous media. Among the studied ILs, [Omim][Tf₂N] showed the highest butanol distribution coefficient (1.939), selectivity (132) and extraction efficiency (74%) at 323.15 K, respectively.     

Reactive extraction of penicillin G in a pilot plant Karr-column

Summary Penicillin G was extracted from a model medium with a secondary amine (Amberlite LA-2) as carrier in n-butylacetate as solvent in a 7.6 m high pilot plant Karr-column at different stroke frequencies, throughput of the phases, concentrations of Penicillin G and carrier and ratios of the throughputs of the aqueous and organic phases. Up to penicillin concentrations of 30 gl^–1, throughputs of the aqueous phase of 100 lh^–1 and throughput ratios of the aqueous phase-to-organic phase of 3, very high degrees of extraction (99%) can be achieved with a penicillin loss below 1%.Symbols a specific interfacial area with regard to the volume of the continuous phase - C partition coefficient - cA, cA, i concentration of carrier (sec. amine) in the bulk at the interface - cAHP, cAHP, i concentration of complex in the bulk at the interface - cH proton concentration - cHP_a, cHP_a,i concentration of free acid in the bulk of the aqueous phase at the interface - cHP_o, cHP_{o, i} concentration of free acid in the bulk of the organic phase, at the interface - cP, cP, i concentration of acid anions in the bulk of the aqueous phase, at the interface - d₃₂ Sauter droplet diameter - E degree of extraction - f stroke frequency - KG reaction equilibrium constant - K_phys distribution coefficient - N number of stages in cascade - t mean residence time of the aqueous phase - _aq throughput of the aqueous phase - _o throughput of the organic phase - Z dimensionless longitudinal coordinate of the column with regard to its active length (4 m) - holdup of the organic phase     

Repeated batch and continuous syntheses of N-(benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester with immobilized thermolysin

Summary N-(Benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester was synthesized from N-(benzyloxycarbonyl)-l-phenylalanine and l-phenylalanine methyl ester in an aqueous solution (aqueous phasic reaction), in an aqueous/organic biphasic system (biphasic reaction), and in an organic solvent (organic phasic reaction) with immobilized thermolysin. In the aqueous phasic reaction with thermolysin immobilized on Amberlite XAD-7, the whole product was trapped inside the support; extraction with ethyl acetate was needed to recover the product, and the equilibrium yield was low (about 65%). With the biphasic and organic phasic reactions with ethyl acetate as an organic solvent, the yield was around 95%. Because of the high yield and feasibility of operation, repeated batch and continuous reactions were done in the biphasic and organic phasic systems, respectively. The half-lives of the activity for the immobilized enzyme used in the biphasic system at 40°C by repeated batch operation and in a plug flow reactor fed with substrate dissolved in ethyl acetate at 40°C and 30°C were estimated to be about 200 h (67 batches), 420 h, and 1100 h, respectively.     

New reactive extraction systems for separation of bio-succinic acid

Biotechnologically produced succinic acid has the potential to displace maleic acid and its uses and to become an important feedstock for the chemical industry. In addition to optimized production strains and fermentation processes, an efficient separation of succinic acid from the aqueous fermentation broth is indispensable to compete with the current petrochemical production processes. In this context, high molecular weight amines are known to be effective extractants for organic acids. For this reason, as a first step of isolation and purification, the reactive extraction of succinic acid was studied by mixing aqueous succinic acid solutions with 448 different amine–solvent mixtures as extraction agents (mixer-settler studies). The extraction agents consist either of one amine and one solvent (208 reactive extraction systems) or two amines and two solvents (240 reactive extraction systems). Maximum extraction yields of succinic acid from an aqueous solution with 423 mM succinic acid at pH 2.0 were obtained with more than 95% yield with trihexylamine solved in 1-octanol or with dihexylamine and diisooctylamine solved in 1-octanol and 1-hexanol. Applying these optimized reactive extraction systems with Escherichia coli fermentation broth resulted in extraction yields of 78–85% due to the increased ionic strength of the fermentation supernatant and the co-extraction of other organic acids (e.g., lactic acid and acetic acid), which represent typical fermentation byproducts.     

Reactive extraction of cephalosporin antibiotics in hollow fiber membrane

Non-dispersive reactive extraction of cephalosporin antibiotics has been studied using hollow fiber membrane modules. Extraction as well as stripping has been studied using a pH swing procedure. Cephalosporin was extracted from an aqueous solution of cephalosporin having a pH above the pK_a2 value to an organic phase containing Aliquat-336 as the extractant and n-heptane as the diluent. The solute was stripped from the loaded organic phase to another aqueous phase of pH maintained well below the pK_a2 value of the cephalosporin. The extraction cum stripping relies on pH dependance of the distribution coefficient of cephalosporin in aqueous phase. Reasonably high solute recovery and mass transfer rate have been achieved in the hollow fiber module. Mass transfer performance of a single module has been evaluated and experimentally observed low value of height of transfer unit (HTU) indicates good prospect of hollow fiber membrane for the extraction duty.     

Enantioselectivity of Epoxide Formation from Halohydrins by Means of Flavobacterium Rigense

The formation of epoxides from several halohydrins was achieved using resting cells from Flavobacterium rigense. The reaction showed a high substrate specificity for halohydrins with a terminal halogen atom but only low enantioselectivity (12–58% e.e.). The epoxides always had the (S)-configuration. Substrates which in the halogen atom was replaced by another leaving group (-O-SO₂CH₃, -O-Tos, -N₃) were not accepted. An attempt to improve the enantioselectivity by using a two phase system consisting of an aqueous and an organic solvent phase was not successful.     

Rapid screening of solvents and carrier compounds for lactic acid recovery by emulsion liquid extraction and toxicity on Lactobacillus casei (ATCC 11443)

This paper describes a rapid method to identify the best solvent and carrier compound combinations with the highest extraction capability and the lowest microbial toxicity characteristics for product recovery from microbial fermentation. The extraction system has an aqueous phase, and an emulsion phase, which was a blend of sodium carbonate and organic phase [91% (v/v) organic solvent, 5% (v/v or wt/v) carrier compound, and 4% (v/v) surfactant Span 80]. Alamine 336, or tri-n-octylamine in n-heptane; Alamine 336, Alamine 304, or tributyl phosphate in hexane; and Alamine 304 or tributyl phosphate in iso-octane; Alamine 304 or Amberlite in xylene demonstrated high lactic acid extraction. For determination of bacterial toxicity of selected solvent and carrier compounds, Lactobacillus casei subsp. rhamnosus (ATCC 11443) was grown in LAF medium containing one of the selected organic solvent, carrier compound, and Span 80 in 250 ml flask at 37 °C and 125 rpm. Samples were collected regularly during 48 hour incubation, and measured for changes in cell density by absorbance at 620 nm, cell count using a fluorescent dye with flow cytometry, and lactic acid, and glucose concentrations by HPLC. Hexadecane:tributyl phosphate, n-dodecane:tri-n-octylamine, and kerosene:tri-n-octylphosphine oxide demonstrated the least microbial toxicity among the tested blends with excess solvent media. Whereas, hexanes:Alamine 304 and xylenes:Alamine 304 were nontoxic in solvent saturated media.This revised version was published online in October 2005 with corrections to the Cover Date.     

Recovery of penicillin G from fermentation broth with reactive extraction in a mixer-settler

Summary In a laboratory countercurrent mixer-settler, penicillin was recovered from its fermentation broth by extraction with Amberlite LA-2 in n-butylacetate at pH 5.0 and reextracted from the ion-pair complex containing a solvent phase with a buffer at 7.2–7.5 with an overall degree of extraction above 90 %.Symbols A amine - AHP complex - c concentration - C partition coefficent - E degree of extraction - HP penicillin acid - K_G equilibrium constant - P, P^– penicillin acid anion Indices aq aqueous phase - org organic phase - A amine - AHP complex - G overall - HP free acid - P penicillin     

Chemical Inactivation of Lipase in Organic Solvent: A Lipase from Pseudomonas aeruginosa TE3285 is More Like a Typical Serine Enzyme in an Organic Solvent than in Aqueous Media

A microbial lipase from Pseudomonas aeruginosa TE3285 was treated in anhydrous diisopropyl ether with three kinds of serine-reactive reagents, ethyl p-nitrophenyl methylphosphonate (ENMP), diisopropyl fluorophosphate (DFP), and phenylmethylsulfonyl fluoride (PMSF) to lose its catalytic activity for both transesterification in an organic solvent and ester hydrolysis in aqueous system. In contrast with the facile inactivation in an organic solvent, no or very slow inactivation was observed in an aqueous solution. The lipase was shown to behave more like a typical serine enzyme in an organic solvent than in aqueous solution with regard to the chemical inactivation by serine-reactive reagents. The unique behavior of the lipase in an organic solvent may be associated with inferfacial activation of the lipase, which is one of the most distinct characteristics of the lipase family, and the activiation of lipase could be induced by a hydrophobic interaction with an organic solvent.     

Ultrafast molecular dynamics of biofuel extraction for microalgae and bacteria milking: blocking membrane folding pathways to damaged lipid-bilayer conformations with nanomicelles

Cell milking is a 100% renewable green energy for CO₂ by extraction of biofuels inside the cytosol of photosynthetic micro-organisms as microalgae and bacteria. The cells are exposed to a hydrophobic solvent forming holes and cracks through their membranes from which the biofuels can leak out. In protein folding, the goal would be to find pathways to the unique functional protein conformer. However, in the lipid-bilayer interaction with the solvent for milking, the objective is to block the pathways for damaged membrane conformations of low free energy with undesired nanostructures, using the solvent properties, as shown with an ab initio structural bioinformatic model. Statistical thermodynamics is used to compute the free energy (including entropy) from the molecular dynamics trajectory of the biomolecular system with many conformational changes. This model can be extended to the general problem of biomolecules folding as for proteins and nucleic acids. Using an adaptation of the Einstein diffusion law, the conformational change dynamics of the lipid bilayer depends on the two diffusion coefficients of the solvent: D₁ before the irreversible folding transition time and the much smaller D₂ thereafter. In contrast to the n-hexane and n-heptane hydrocarbons of smaller size, the residual D₂?=?4.7?×?10^?7?cm²/s of the n-decane solvent, with the highest partition coefficient among the three extractors, is the only to present a D₂ value that is significantly below the critical threshold of 10^?6?cm²/s. Therefore, the membrane would resist to long hydrocarbons and the exposed cells would remain viable for milking.     

Lipase-catalyzed reaction in the packed-bed reactor with continuous extraction column to overcome a product inhibition

The resolution of rac-α-methyl-β-propiothiolactone (rac-MPTL) was performed in a packed-bed reactor (PBR) using Pseudomonas cepacia lipase (PCL) in organic media to produce enantiopure (R)-MPTL. By comparing enzyme stability of three enzyme forms, i.e. commercial PCL powder, Celite-immobilized PCL, and cross-linked enzyme crystals of PCL (CLECs-PCL), Celite-immobilized PCL was chosen for the construction of PBR because of its comparable stability to that of CLEC and easy handling. Owing to the severe product inhibition by 3-mercapto-α-methylpropionic acid (MMPA), the batch reaction system was inappropriate for the hydrolysis with PCL at high concentration of rac-MPTL. To overcome these problems, PBR with a continuous extraction column was used. The product inhibition was successfully overcome by incorporating an aqueous extraction unit. However, the yield of (R)-MPTL (enantiomeric excess, ee>99%) was only about 20% based upon the initial concentration of rac-MPTL, due to the concomitant partitioning of rac-MPTL to the aqueous phase in the extraction column as well as the subsequent auto-hydrolysis of rac-MPTL to rac-MMPA during extraction. To reduce the undesired partitioning of rac-MPTL to aqueous phase, various salts were screened to modulate the partitioning coefficient of the reaction components. Using 1 M ammonium sulfate solution as the aqueous phase of the extraction column, the yield of (R)-MPTL (ee>99%) was enhanced to 40%.     

Reactive extraction of penicillin G in a pilot plant Karr-column II. Fermentation broths

Summary Penicillin G was extracted from mycelfree fermentation broths by means of the carrier (Amberlite LA-2) in n-butylacetate at pH 5 in a 7.6 m high pilot plant Karr-column with degrees of extraction E=98–99% and penicillin enrichments up to 3. The reextraction was carried out with phosphate buffer at pH-values above 7.5 with degree of extractions E=86–88% and penicillin enrichments up to 3. The penicillin and carrier losses were negligible. The influence of the process variables on the extraction degree was investigated. The penicillin extraction of the model medium and the fermentation broths were compared. Recommendations are given for the optimal penicillin recovery with reactive extraction.Symbols a specific interfacial area with regard to the volume of the continuous phase - cA concentration of carrier - cAHP,O concentration of complex in feed - cP,cP,O concentration of penicillin acid anion in theaqueous phase, in the feed - d ₃₂ Sauter droplet diameter - E degree of extraction - f stroke frequency - V _aq throughput of the aqueous phase - V ₀ throughput of the organic phase - Z dimensionsless longitudinal coordinate of the column with regard to its active length (4m) - holdup of the organic phase     

Studies on equilibrium of anthranilic acid in aqueous solutions and in two-phase systems: Aromatic solvent–water

The acid–base equilibria of anthranilic acid have been characterized in terms of macro- and microdissociation constants (dissociation constants K_a1, K_a2 and tautomeric constant K_z). On the basis of spectrophotometric investigations the values of the distribution ratio D of anthranilic acid in the two-phase systems: aromatic solvent (benzene, ethylbenzene, toluene, chlorobenzene, bromobenzene)–aqueous solution were obtained. Employing the results of potentiometric titration in the two-phase systems: aromatic solvent–aqueous solution the distribution constant K_D and dimerization constant K_dim values were calculated. The influence of organic solvent polarity and pH of the aqueous phase on the contents of the particular forms of the acid in the two-phase systems were analyzed.