Recovery of poly(3‐hydroxybutyrate‐co‐3‐hydroxyhexanoate) from Ralstonia eutropha cultures with non‐halogenated solvents

Reduced downstream costs, together with high purity recovery of polyhydroxyalkanoate (PHA), will accelerate the commercialization of high quality PHA‐based products. In this work, a process was designed for effective recovery of the copolymer poly(hydroxybutyrate‐co‐hydroxyhexanoate) (P(HB‐co‐HHx)) containing high levels of HHx (>15 mol%) from Ralstonia eutropha biomass using non‐halogenated solvents. Several non‐halogenated solvents (methyl isobutyl ketone, methyl ethyl ketone, and butyl acetate and ethyl acetate) were found to effectively dissolve the polymer. Isoamyl alcohol was found to be not suitable for extraction of polymer. All PHA extractions were performed from both dry and wet cells at volumes ranging from 2 mL to 3 L using a PHA to solvent ratio of 2% (w/v). Ethyl acetate showed both high recovery levels and high product purities (up to 99%) when using dry cells as starting material. Recovery from wet cells, however, eliminates a biomass drying step during the downstream process, potentially saving time and cost. When wet cells were used, methyl isobutyl ketone (MIBK) was shown to be the most favorable solvent for PHA recovery. Purities of up to 99% and total recovery yields of up to 84% from wet cells were reached. During polymer recovery with either MIBK or butyl acetate, fractionation of the extracted PHA occurred, based on the HHx content of the polymer. PHA with higher HHx content (17–30 mol%) remained completely in solution, while polymer with a lower HHx content (11–16 mol%) formed a gel‐like phase. All PHA in solution could be precipitated by addition of threefold volumes of n‐hexane or n‐heptane to unfiltered PHA solutions. Effective recycling of the solvents in this system is predicted due to the large differences in the boiling points between solvent and precipitant. Our findings show that two non‐halogenated solvents are good candidates to replace halogenated solvents like chloroform for recovery of high quality PHA. Biotechnol. Bioeng. 2013; 110: 461–470. © 2012 Wiley Periodicals, Inc.     

Assessment of different sample processing procedures applied to the determination of melatonin in plants

Introduction –  Melatonin, an indoleamine well known in vertebrates and structurally related to other important substances such as tryptophan or indole‐3‐acetic acid, is also present in the plant kingdom although its specific function(s) remain to be established. The emerging field of melatonin studies in plants has progressed very slowly, mainly due to the problems associated with melatonin quantification in plants. Objective –  Two commonly used procedures for plant samples are compared. The analytical characteristics of both procedures are quantitatively presented using different solvents and small amounts of fresh biological material, and the respective recovery rates and quantitative limits are presented. Some improvements are suggested. Methodology –  Two different sample extraction procedures were compared: a direct‐sample extraction (DSE) and a homogenised‐ sample extraction (HSE). Melatonin was then determined in the respective plant samples by HPLC with fluorescence detection. Results –  Using the DSE procedure, more than 94% melatonin was recovered from standard solutions, whereas levels higher than 93% were recovered from the spiked plant samples, with little difference between ethyl acetate and chloroform extractions. In the case of HSE, the recoveries of melatonin were approximately half and never higher than 55%. The ultrasonic treatment proposed in the DSE procedure showed different levels of efficiency (2–20%), depending on the sample. Conclusion –  This study has established that, with the direct sample extraction procedure, higher recovery rates are obtained both in standard solutions and in plant samples. The straightforwardness and reproducibility of the extraction procedure is accompanied by the high sensitivity obtained with fluorescence detection. Copyright © 2008 John Wiley & Sons, Ltd.     

Numerical evaluation of lactoperoxidase inactivation during continuous pulsed electric field processing

A computational fluid dynamics (CFD) model describing the flow, electric field and temperature distribution of a laboratory‐scale pulsed electric field (PEF) treatment chamber with co‐field electrode configuration was developed. The predicted temperature increase was validated by means of integral temperature studies using thermocouples at the outlet of each flow cell for grape juice and salt solutions. Simulations of PEF treatments revealed intensity peaks of the electric field and laminar flow conditions in the treatment chamber causing local temperature hot spots near the chamber walls. Furthermore, thermal inactivation kinetics of lactoperoxidase (LPO) dissolved in simulated milk ultrafiltrate were determined with a glass capillary method at temperatures ranging from 65 to 80°C. Temperature dependence of first order inactivation rate constants was accurately described by the Arrhenius equation yielding an activation energy of 597.1 kJ mol^?1. The thermal impact of different PEF processes on LPO activity was estimated by coupling the derived Arrhenius model with the CFD model and the predicted enzyme inactivation was compared to experimental measurements. Results indicated that LPO inactivation during combined PEF/thermal treatments was largely due to thermal effects, but 5–12% enzyme inactivation may be related to other electro‐chemical effects occurring during PEF treatments. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

An improved method for determination of ethyl carbamate in Korean traditional rice wine

An improved extraction method for ethyl carbamate, a genotoxic and carcinogenic compound found in various fermented foods and beverages, was investigated for its determination in the two most typical Korean traditional rice wines, takju and yakju. When the rice wines were extracted twice with chloroform at 30°C for 60 min, the recovery of ethyl carbamate was less than 16%. When they were saturated with NaCl before extraction, the recovery of ethyl carbamate increased to 24.4% in takju and 67.2% in yakju. Adjustment of pH to 9.0 after NaCl saturation in takju resulted in a dramatic increase of recovery to 81.2%, but not in yakju. When the contents of ethyl carbamate and its precursor, urea, in various Korean traditional rice wines were determined, there was no correlation between the two contents. This is due to the fact that storage time is more important than urea content in the formation of ethyl carbamate in rice wine. In addition, its storage at high temperature resulted in a dramatic increase in ethyl carbamate content according to the prolonged storage time, suggesting that storage time and temperature play a key role in the formation of ethyl carbamate in Korean traditional rice wine. Journal of Industrial Microbiology & Biotechnology (2001) 26, 363–368. Received 10 January 2001/ Accepted in revised form 17 March 2001     

Effect of a Pulsed Electric Field Treatment on Expression Behavior and Juice Quality of Chardonnay Grape

This work discusses the effects of pulsed electric field (PEF) application on low-pressure mechanical expression (the pressure maximum was 1 bar) and characteristics of juice produced from Chardonnay white grape. The experiments were carried out using a texture analyzer equipped with a PEF-treatment compression chamber operated at moderate electric field strength E = 400 V/cm. Two regimes of extraction were compared: expression at constant pressure (0.5 or 1 bar) and expression at progressive pressure increase (from 0 to 1 bar). This last one was chosen for the scale-down modeling of industrial grape pressing process. It was shown that PEF treatment at the electric field E = 400 V/cm and the total time of treatment t _PEF ≈ 0.1 s allowed reaching of a high level of cell disintegration, Z ≈ 0.8. The energy consumption of PEF treatment corresponding to this level of disintegration was rather low and equal to W ≈ 15 kJ/kg. The PEF pretreatment resulted in juice yield increase from 67% to 75% (1 h of pressing at constant pressure of 1.0 bar). PEF treatment accelerated development of grape deformation. Decrease of difference between deformations of untreated and PEF-treated samples at high pressure and long-pressing time was observed. Statistical analysis showed no significant effect of PEF treatment on turbidity and content of polyphenols for the constant pressure regime. However, PEF treatment application resulted in elevation of the content of polyphenols (more than 15%) for the progressive pressure-increase regime.     

Acetic acid removal from corn stover hydrolysate using ethyl acetate and the impact on Saccharomyces cerevisiae bioethanol fermentation

Acetic acid is introduced into cellulose conversion processes as a consequence of composition of lignocellulose feedstocks, causing significant inhibition of adapted, genetically modified and wild‐type S. cerevisiae in bioethanol fermentation. While adaptation or modification of yeast may reduce inhibition, the most effective approach is to remove the acetic acid prior to fermentation. This work addresses liquid–liquid extraction of acetic acid from biomass hydrolysate through a pathway that mitigates acetic acid inhibition while avoiding the negative effects of the extractant, which itself may exhibit inhibition. Candidate solvents were selected using simulation results from Aspen Plus?, based on their ability to extract acetic acid which was confirmed by experimentation. All solvents showed varying degrees of toxicity toward yeast, but the relative volatility of ethyl acetate enabled its use as simple vacuum evaporation could reduce small concentrations of aqueous ethyl acetate to minimally inhibitory levels. The toxicity threshold of ethyl acetate, in the presence of acetic acid, was found to be 10 g L^?1. The fermentation was enhanced by extracting 90% of the acetic acid using ethyl acetate, followed by vacuum evaporation to remove 88% removal of residual ethyl acetate along with 10% of the broth. NRRL Y‐1546 yeast was used to demonstrate a 13% increase in concentration, 14% in ethanol specific production rate, and 11% ethanol yield. This study demonstrated that extraction of acetic acid with ethyl acetate followed by evaporative removal of ethyl acetate from the raffinate phase has potential to significantly enhance ethanol fermentation in a corn stover bioethanol facility. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:929–937, 2016     

Fungal Transformation of the Tricyclic Antidepressant Amoxapine: Identification of N-Carbomethoxy Compounds Formed as Artifacts by Phosgene in Chloroform used for the Extraction of Metabolites

The biotransformation of the antidepressant drug amoxapine by Cunninghamella elegans formed three metabolites, 7-hydroxyamoxapine, N-formyl-7-hydroxyamoxapine, and N-formylamoxapine; two other compounds were only present when chloroform was used in the extraction process. All five of the compounds were separated by reversed-phase HPLC, then analyzed by ¹H NMR and mass spectrometry, and by ¹³C NMR when sample quantities permitted. The artifacts were identified as N-carbomethoxy-7-hydroxyamoxapine and N-carbomethoxyamoxapine. Phosgene is a decomposition product of chloroform that can form carbomethoxy compounds at the secondary nitrogen of a piperazine ring in an alcoholic solution. Since N-carbomethoxy compounds were not observed when ethyl acetate was used for extraction of the culture medium, they were considered artifacts and not metabolites. These findings suggest that chloroform should be tested for the formation of phosgene before using it to extract any compound with a piperazine ring or any other amine-containing structure.     

Formation of ethyl acetate by Kluyveromyces marxianus on whey: Influence of aeration and inhibition of yeast growth by ethyl acetate

The ability of the yeast Kluyveromyces marxianus to convert lactose into ethyl acetate offers good opportunities for the economical reuse of whey. The formation of ethyl acetate as a bulk product depends on aerobic conditions. Aeration of the bioreactor results in discharge of the volatile ester with the exhaust gas that allows its process‐integrated recovery. The influence of aeration (varied from 10 to 50 L/h) was investigated during batch cultivation of K. marxianus DSM 5422 in 0.6 L whey‐borne medium using a stirred reactor. With lower aeration rates, the ester accumulated in the bioreactor and reached higher concentrations in the culture medium and the off gas. A high ester concentration in the gas phase is considered beneficial for ester recovery from the gas, while a high ester concentration in the medium inhibited yeast growth and slowed down the process. To further investigate this effect, the inhibition of growth by ethyl acetate was studied in a sealed cultivation system. Here, increasing ester concentrations caused a nearly linear decrease of the growth rate with complete inhibition at concentrations greater than 17 g/L ethyl acetate. Both the cultivation process and the growth rate depending on ethyl acetate were described by mathematical models. The simulated processes agreed well with the measured data.     

Purification of Xylitol from Fermented Hemicellulosic Hydrolyzate Using Liquid–Liquid Extraction and Precipitation Techniques

Xylitol was produced by Candida guilliermondii by fermentation of sugarcane bagasse hemicellulosic hydrolysate. Undesirable impurities were extracted from the broth using either ethyl acetate, chloroform or dichloromethane. The best results on clarification of the broth without xylitol loss were obtained with ethyl acetate. When ethanol, acetone or tetrahydrofuran were used for precipitation of impurities, only tetrahydrofuran clarified the fermented broth, but a high xylitol loss (~30%) was observed.     

Co-Utilization of Canola Oil and Glucose on the Production of a Surfactant by <Emphasis Type="Italic">Candida lipolytica</Emphasis>

Candida lipolytica synthesized a surfactant in a cultivation medium supplemented with canola oil and glucose as carbon sources. Measurements of biosurfactant production and surface tension indicated that the biosurfactant was produced at 48 h of fermentation. The surface-active species is constituted by the protein–lipid–polysaccharide complex in nature. The cell-free broth was particularly influenced by the addition of salt, the pH and temperature depending on the emulsified substrate (hexadecane or a vegetable oil). After comparison between ethyl acetate and mixtures of chloroform and methanol as solvent systems for surfactant recovery, it was found that ethyl acetate was able to extract crude surfactant material with high product recovery (8.0 g/L). The isolated biosurfactant decreased the surface tension to values of 30 mN/m at the critical micelle concentration. Emulsification properties of the biosurfactant produced were compared to those of commercial emulsifiers and other microbial surfactants.     

Determination of benzimidazole residues using liquid chromatography and tandem mass spectrometry

The determination of residues of benzimidazole using liquid chromatography and tandem mass spectrometry (LC–MS–MS) with ion spray ionization is described. Swine muscle tissue was spiked with a mixture of fifteen benzimidazoles, including metabolites of fenbendazole and albendazole. As clean-up procedure, an ethyl acetate extraction followed by solid-phase extraction on styrol-divinyl-benzene cartridge was used. The evaluation was performed by selecting the characteristic product ions for the benzimidazoles and using multiple reaction mode. 2-n-Butylmercaptobenzimidazole was used as internal standard. Blank muscle samples were fortified in the concentration range of 1–22 μg/kg. The limits of detection were below 6 μg/kg and the limits of quantification for most benzimidazoles were below 10 μg/kg. The matrix effect was checked using spiked muscle tissues of cattle and sheep as well as liver of cattle. Practical application will be shown by incurred egg material from laying hens treated with flubendazole. The recovery of the clean-up was mostly above 50% in muscle tissue and 70% in egg yolk.     

Antibacterial and antifungal activities of andrachne cordifolia muell

The crude methanolic extract of Andrachne cordifolia Muell. (Euphorbiaceae) and its various fractions in different solvent systems (chloroform, ethyl acetate and n- butanol) were screened for antibacterial and antifungal activities. Crude extract and subsequent fractions demonstrated moderate to excellent antibacterial activities against the tested pathogens. Highest antibacterial activity was displayed by both chloroform and ethyl acetate fractions (100%) followed by the crude extract (68%) against Salmonella typhi. Similarly, crude extract and its subsequent fractions showed mild to excellent activities in antifungal bioassay with maximum (76%) antifungal activity against Microsporum canis by the chloroform fraction followed by the crude extract (65%).     

Effect of Pulsed Electric Field Treatments on Permeabilization and Extraction of Pigments from Chlorella vulgaris

The effect of pulsed electric field (PEF) treatments of different intensities on the electroporation of the cytoplasmatic membrane of Chlorella vulgaris, and on the extraction of carotenoids and chlorophylls were investigated. Staining the cells with propidium iodide before and after the PEF treatment revealed the existence of reversible and irreversible electroporation. Application of PEF treatments in the range of 20–25 kV cm^?1 caused most of the population of C. vulgaris to be irreversibly electroporated even at short treatment times (5 pulses of 3 µs). However, at lower electric field strengths (10 kV cm^?1), cells that were reversibly electroporated were observed even after 50 pulses of 3 µs. The electroporation of C. vulgaris cells by PEF higher than 15 kV cm^?1 and duration is higher than 15 µs increased significantly the extraction yield of intracellular components of C. vulgaris. The application of a 20 kV cm^?1 for 75 μs increased the extraction yield just after the PEF treatment of the carotenoids, and chlorophylls a and b 0.5, 0.7, and 0.8 times, respectively. However, further increments in electric field strength and treatment time did not cause significant increments in the extraction yield. The extraction of carotenoids from PEF-treated C. vulgaris cells after 1 h of the application of the treatment significantly increased the extraction yield in comparison to the yield obtained from the cells extracted just after the PEF treatment. After PEF treatment at 20 kV cm^?1 for 75 µs, extraction yield for carotenoids, and chlorophylls a and b increased 1.2, 1.6, and 2.1 times, respectively. A high correlation was observed between irreversible electroporation and percentage of yield increase when the extraction was conducted after 1 h of the application of PEF treatment (R: 0.93), but not when the extraction was conducted just after PEF treatment (R: 0.67).     

Enzyme inhibition and radical scavenging activities of aerial parts of Paeonia emodi Wall. (Paeoniaceae)

The ethanolic extract derived from aerial parts of an indigenous medicinal plant Paeonia emodi was screened for enzyme inhibition activities against Urease (jack bean and Bacillus pasteurii) and α-Chymotrypsin. The extract was also investigated for its radical scavenging activity using DPPH assay. The crude extract was found to possess significant enzyme inhibition activities against jack bean (74%) and Bacillus pasteurii (80%) urease and a moderate activity (54%) against α-Chymotrypsin. The extract also displayed excellent (83%) radical scavenging activity. On the basis of these results, the crude extract was subsequently fractionated into n-hexane, chloroform, ethyl acetate, n-butanol and water fractions and tested independently for the aforesaid activities. Significant inhibitory activity against urease enzyme was observed for the ethyl acetate, n-butanol and water fractions while the n-hexane and chloroform fractions were devoid of any such activity. In the α-Chymotrypsin enzyme inhibition studies the activity was concentrated into the ethyl acetate fraction. All the fractions displayed potent radical scavenging activity. The crude extract and fractions thereof were also subjected to total phenolic content determination. A correlation between radical scavenging capacities of extracts and total phenolic content was observed in the majority of cases.     

Enzyme inhibition activities of teucrium royleanum

The crude methanolic extract and chloroform, ethyl acetate and n-butanol fractions of Teucrium royleanum were examined as inhibitors of actylcholinesterase, butyrylcholinesterase, lipoxygenase and urease. A significant enzyme inhibition activity (52–83%) was shown by the crude methanolic extract and its fractions against acetylcholinesterase, while low to outstanding enzyme inhibitory activity was shown (19–93%) against butyrylcholinesterase. The crude methanolic extract and its various fractions demonstrated low activity against lipoxygenase and inactive against urease.     

Controlled inactivation of Trichophyton rubrum using shaped electrical pulse bursts: Parametric analysis

The dermatophytes infect the skin by adherence to the epidermis followed by germination, growth, and penetration of the fungal hyphae within the cells. The aim of this study was to investigate the efficacy of the pulsed electric fields (PEF) of controlled inactivation of Trichophyton rubrum (ATCC 28188). In this work, we have used bursts of the square wave PEF pulses of different intensity (10–30 kV/cm) to induce the irreversible inactivation in vitro. The electric field pulses of 50 µs and 100 µs have been generated in bursts of 5, 10, and 20 pulses with repetition frequency of 1 Hz. The dynamics of the inactivation using different treatment parameters were studied and the inactivation map for the T. rubrum has been defined. Further, the combined effect of PEF with the antifungal agents itraconazole, terbinafine, and naftifine HCl was investigated. It has been demonstrated that the combined effect results in the full inactivation of T. rubrum colony. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1056–1060, 2016     

Lipid sovent systems are not equivalent for analysis of lipid classes in the microeukaryotic green alga,Chlorella

A comparison of three lipid solvent system indicated that they are not equivalent for the analysis of lipid classes in the green alga, Chlorella. Soxhlet extraction (methylene chloride/methanol, 3 h refulx) recovers more neutral lipid than the other methods but is equivalent to the room-temperature Bligh and Dyer (chloroform/methanol/water) extraction modified with phosphate buffer in glycolipid and polar lipid recovery. The Soxhlet method, however, gave a significantly lower recovery of many polyunsaturated fatty acids. The hexane/isopropanol method is selective for algal neutral lipids with poor recovery of membrane lipids (glyco- and polar lipids). Although this selectivity may have some useful applications, for biochemical studies of lipid synthesis in Chlorella, the modified Bligh and Dyer provides the most quantitative and reproducible recovery of all Chlorella lipid classes while minimizing artifacts due to the extraction procedure.     

Enzyme inhibition activities of the extracts from rhizomes of Gloriosa superba Linn (Colchicaceae)

An alcoholic extract obtained from the rhizomes of Gloriosa superba Linn (Colchicaceae) was screened for enzyme inhibition activities. The crude extract and its subsequent fractions including chloroform, ethyl acetate, n-butanol and aqueous were screened against lipoxygenase, actylcholinesterase, butyrylcholinesterase and urease. An outstanding inhibition on lipoxygenase was observed. The highest enzyme inhibition potency was expressed by the chloroform fraction (90%) among the tested fractions on lipoxygenase. Overall 67– 90% inhibition was found for lipoxygenase, 46-69% for acetylcholinesterase and 10–33% for butyrylcholinesterase, while urease was not inhibited.     

Optimization of protein extraction from Chlorella Vulgaris via novel sugaring‐out assisted liquid biphasic electric flotation system

Microalgae biomass has been consumed as animal feed, fish feed and in human diet due to its high nutritional value. In this experiment, microalgae specie of Chlorella Vulgaris FSP‐E was utilized for protein extraction via simple sugaring‐out assisted liquid biphasic electric flotation system. The external electric force provided to the two‐phase system assists in disruption of rigid microalgae cell wall and releases the contents of microalgae cell. This experiment manipulates various parameters to optimize the set‐up. The liquid biphasic electric flotation set‐up is compared with a control liquid biphasic flotation experiment without the electric field supply. The optimized separation efficiency of the liquid biphasic electric flotation system was 73.999 ± 0.739% and protein recovery of 69.665 ± 0.862% compared with liquid biphasic flotation, the separation efficiency was 61.584 ± 0.360% and protein recovery was 48.779 ± 0.480%. The separation efficiency and protein recovery for 5 × time scaled‐up system was observed at 52.871 ± 1.236% and 73.294 ± 0.701%. The integration of simultaneous cell‐disruption and protein extraction ensures high yield of protein from microalgae. This integrated method for protein extraction from microalgae demonstrated its potential and further research can lead this technology to commercialization.     

Novel urease inhibitors from Daphne oleoids

Phytochemical investigations on the chloroform and ethyl acetate soluble fractions of the roots of the Daphne oleoids led to the isolation of the coumarin glycosides 1–6. Compound 5 with IC₅₀ values 22.05 and 26.30 μM repectively, was found to be the most active of these compounds when screened against Bacillus pasteurii and jack bean urease enzymes in a concentration-dependent fashion.