Fast‐responding thermal‐death‐time tubes for the determination of thermal bacteria inactivation

The knowledge of thermal inactivation kinetics, usually expressed in terms of D‐ and z‐values, is of crucial importance for the design of sanitation and sterilization processes. In this study, we designed a simple, fast‐responding, and mechanically stable aluminum tube for inactivation measurements and compared these experiments with the successive‐sampling method at different temperatures. Up to 65°C, we determined a come‐up time of approximately 15 s for the tubes, which is lower than the corresponding values of other devices, presumably because of lower wall thickness, material properties, and a higher surface to volume ratio. D‐values of Escherichia coli calculated from tube inactivation experiments by first‐order kinetics were 370 s (56°C), 126 s (58°C), 53.2 s (60°C), 33.8 s (62°C), and 3.22 s (65°C), and the corresponding values determined with the successive‐sampling flask method were insignificantly different (417, 138, 48.6, and 29.1 s for 56, 58, 60, and 62°C, respectively). These data as well as those measured for Enterobacter cloacae, Pseudomonas putida, Serratia odorifera, and Yersinia rhodei were in close accordance with literature values.     

Characterizing the release of bioactive N‐glycans from dairy products by a novel endo‐β‐N‐acetylglucosaminidase

Endo‐β‐N‐acetylglucosaminidase isolated from B. infantis ATCC 15697 (EndoBI‐1) is a novel enzyme that cleaves N‐N′‐diacetyl chitobiose moieties found in the N‐glycan core of high mannose, hybrid, and complex N‐glycans. These conjugated N‐glycans are recently shown as a new prebiotic source that stimulates the growth of a key infant gut microbe, Bifidobacterium longum subsp. Infantis. The effects of pH (4.45–8.45), temperature (27.5–77.5°C), reaction time (15–475 min), and enzyme/protein ratio (1:3,000–1:333) were evaluated on the release of N‐glycans from bovine colostrum whey by EndoBI‐1. A central composite design was used, including a two‐level factorial design (2⁴) with four center points and eight axial points. In general, low pH values, longer reaction times, higher enzyme/protein ratio, and temperatures around 52°C resulted in the highest yield. The results demonstrated that bovine colostrum whey, considered to be a by/waste product, can be used as a glycan source with a yield of 20 mg N‐glycan/g total protein under optimal conditions for the ranges investigated. Importantly, these processing conditions are suitable to be incorporated into routine dairy processing activities, opening the door for an entirely new class of products (released bioactive glycans and glycan‐free milk). The new enzyme's activity was also compared with a commercially available enzyme, showing that EndoBI‐1 is more active on native proteins than PNGase F and can be efficiently used during pasteurization, streamlining its integration into existing processing strategies. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1331–1339, 2015     

High‐solids biphasic CO2–H2O pretreatment of lignocellulosic biomass

A high pressure (200 bar) CO₂–H₂O process was developed for pretreating lignocellulosic biomass at high‐solid contents, while minimizing chemical inputs. Hardwood was pretreated at 20 and 40 (wt.%) solids. Switchgrass, corn stover, big bluestem, and mixed perennial grasses (a co‐culture of big bluestem and switchgrass) were pretreated at 40 (wt.%) solids. Operating temperatures ranged from 150 to 250°C, and residence times from 20 s to 60 min. At these conditions a biphasic mixture of an H₂O‐rich liquid (hydrothermal) phase and a CO₂‐rich supercritical phase coexist. Following pretreatment, samples were then enzymatically hydrolyzed. Total yields, defined as the fraction of the theoretical maximum, were determined for glucose, hemicellulose sugars, and two degradation products: furfural and 5‐hydroxymethylfurfural. Response surfaces of yield as a function of temperature and residence time were compared for different moisture contents and biomass species. Pretreatment at 170°C for 60 min gave glucose yields of 77%, 73%, and 68% for 20 and 40 (wt.%) solids mixed hardwood and mixed perennial grasses, respectively. Pretreatment at 160°C for 60 min gave glucan to glucose yields of 81% for switchgrass and 85% for corn stover. Biotechnol. Bioeng. 2010;107: 451–460. © 2010 Wiley Periodicals, Inc.     

Improved one‐step steam pretreatment of SO2‐Impregnated softwood with time‐dependent temperature profile for ethanol production

In the production of ethanol from lignocellulosic material, pretreatment of the raw material before enzymatic hydrolysis and fermentation is essential to obtain high overall yields of sugar and ethanol. Two‐step steam pretreatment results in higher ethanol yields from softwood than the standard one‐step pretreatment process. However, the difficulty with separation and washing of the material at high pressure between the two pretreatment steps is a major drawback. In this study, a new one‐step pretreatment procedure was investigated, in which the time‐temperature profile was varied during pretreatment. The efficiency of pretreatment was assessed by performing simultaneous saccharification and fermentation on the pretreated slurries. Pretreatment of SO₂‐impregnated softwood performed by varying the temperature (190–226°C), the residence time (5–10 min), and the mode of temperature increase (linear or stepwise), resulted in recovery of about 90% of the mannose and glucose present in the raw material. The highest ethanol yield, 75% of theoretical based on the glucan and mannan content of the raw material, was obtained at pretreatment conditions of 190°C for 12 min. Similar ethanol yields were achieved when running the pretreatment as one‐step (190–200°C), two levels of temperature, at shorter residence time (7 min), which results in lower capital costs for the process. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Structural changes in cartilage and collagen studied by high temperature Raman spectroscopy

Understanding the high temperature behavior of collagen and collagenous tissue is important for surgical procedures and biomaterials processing for the food, pharmaceutical, and cosmetics industries. One primary event for proteins is thermal denaturation that involves unfolding the polypeptide chains while maintaining the primary structure intact. Collagen in the extracellular matrix of cartilage and other connective tissue is a hierarchical material containing bundles of triple‐helical fibers associated with water and proteoglycan components. Thermal analysis of dehydrated collagen indicates irreversible denaturation at high temperature between 135°C and 200°C, with another reversible event at ～60‐80°C for hydrated samples. We report high temperature Raman spectra for freeze‐dried cartilage samples that show an increase in laser‐excited fluorescence interpreted as conformational changes associated with denaturation above 140°C. Spectra for separated collagen and proteoglycan fractions extracted from cartilage indicate the changes are associated with collagen. The Raman data also show appearance of new features indicating peptide bond hydrolysis at high temperature implying that molecular H₂O is retained within the freeze‐dried tissue. This is confirmed by thermogravimetric analysis that show 5‐7 wt% H₂O remaining within freeze‐dried cartilage that is released progressively upon heating up to 200°C. Spectra obtained after exposure to high temperature and re‐hydration following recovery indicate that the capacity of the denatured collagen to re‐absorb water is reduced. Our results are important for revealing the presence of bound H₂O within the collagen component of connective tissue even after freeze‐drying and its role in denaturation that is accompanied by or perhaps preceded by breakdown of the primary polypeptide structure.     

Inactivation of Escherichia coli Endotoxin by Soft Hydrothermal Processing

Bacterial endotoxins, also known as lipopolysaccharides, are a fever-producing by-product of gram-negative bacteria commonly known as pyrogens. It is essential to remove endotoxins from parenteral preparations since they have multiple injurious biological activities. Because of their strong heat resistance (e.g., requiring dry-heat sterilization at 250°C for 30 min) and the formation of various supramolecular aggregates, depyrogenation is more difficult than sterilization. We report here that soft hydrothermal processing, which has many advantages in safety and cost efficiency, is sufficient to assure complete depyrogenation by the inactivation of endotoxins. The endotoxin concentration in a sample was measured by using a chromogenic limulus method with an endotoxin-specific limulus reagent. The endotoxin concentration was calculated from a standard curve obtained using a serial dilution of a standard solution. We show that endotoxins were completely inactivated by soft hydrothermal processing at 130°C for 60 min or at 140°C for 30 min in the presence of a high steam saturation ratio or with a flow system. Moreover, it is easy to remove endotoxins from water by soft hydrothermal processing similarly at 130°C for 60 min or at 140°C for 30 min, without any requirement for ultrafiltration, nonselective adsorption with a hydrophobic adsorbent, or an anion exchanger. These findings indicate that soft hydrothermal processing, applied in the presence of a high steam saturation ratio or with a flow system, can inactivate endotoxins and may be useful for the depyrogenation of parenterals, including end products and medical devices that cannot be exposed to the high temperatures of dry heat treatments.Endotoxins are lipopolysaccharides (LPS) that are derived from the cell membranes of gram-negative bacteria and are continuously released into the environment. The release of LPS occurs not only upon cell death but also during growth and division. In the pharmaceutical industry, it is essential to remove endotoxins from parenteral preparations since they have multiple injurious biological activities, including pyrogenicity, lethality, Schwartzman reactivity, adjuvant activity, and macrophage activation (2, 9, 12, 13, 25, 32). Endotoxins are very stable molecules that are capable of resisting extreme temperatures and pH values (3, 16, 17, 29, 30, 34, 38). An endotoxin monomer has a molar mass of 10 to 20 kDa and forms supramolecular aggregates in aqueous solutions (22, 39) due to its amphipathic structure, which makes depyrogenation more difficult than sterilization. Endotoxins are not efficiently inactivated with the regular heat sterilization procedures recommended by the Japanese Pharmacopoeia. These procedures are steam heat treatment at 121°C for 20 min or dry-heat treatment for at least 1 h at 180°C. It is well accepted that only dry-heat treatment is efficient in destroying endotoxins (3, 16, 29, 30) and that endotoxins can be inactivated when exposed to a temperature of 250°C for more than 30 min or 180°C for more than 3 h (14, 36). In the production of parenterals, it is necessary to both depyrogenate the final products and carry out sterilization to avoid bacterial contamination.Several studies have examined dry-heat treatment, which is a very efficient means to degrade endotoxins (6, 20, 21, 26, 41, 42). However, its application is restricted to steel and glass implements that can tolerate high temperatures of >250°C. For sterilization, dry heat treatment tends to be used only with thermostable materials that cannot be sterilized by steam heat treatment (autoclaving). Alternative depyrogenation processes include the application of activated carbon (35), oxidation (15), and acidic or alkaline reagents (27), but steam heat treatment would be an attractive option if it were sufficiently effective. However, the data on the inactivation of endotoxins by steam heat treatment are insufficient and contradictory. It has been reported that endotoxins were not efficiently inactivated by steam heat treatment at 121°C (19, 45). However, Ogawa et al. (31) recently reported that steam heat treatment was efficient in inactivating low concentrations of endotoxin, and that Escherichia coli LPS are unstable in aqueous solutions even at relatively low temperatures such as 70°C (see also reference 40). As mentioned above, these reports have shown that although studies have been carried out on the use of steam heat for depyrogenation, there is little agreement on its efficiency.The U.S. Pharmacopoeia (USP) recommends depyrogenation by dry-heat treatment at temperatures above 220°C for as long as is necessary to achieve a ≥3-log reduction in the activity of endotoxin, if the value is ≥1,000 endotoxin units (EU)/ml (11, 44). Due to the serious risks associated with endotoxins, the U.S. Food and Drug Administration (FDA) has set guidelines for medical devices and parenterals. The protocol to test for endotoxin contamination of medical devices recommends immersion of the device in endotoxin-free water for at least 1 h at room temperature, followed by testing of this extract/eluate for endotoxin. Current FDA limits are such that eluates from medical devices may not exceed 0.5 EU/ml, or 0.06 EU/ml if the device comes into contact with cerebrospinal fluid (43). The term EU describes the biological activity of endotoxins. For example, 100 pg of the standard endotoxin EC-5, 200 pg of EC-2, and 120 pg of endotoxin from E. coli O111:B4 all have an activity of 1 EU (17, 23).Steam heat treatment is comparatively easy to apply and control. If steam heat treatment could reliably inactivate endotoxins, it could be applied with sterilization, reducing labor, time, and expenditure. However, to our knowledge, few studies have addressed steam heat inactivation to determine the chemical and physical reactions that occur during the hydrothermal process, nor have any studies examined the relationship between the steam saturation ratio and the inactivation of endotoxins. Moreover, to date no study has been conducted on steam heat activation of endotoxins with reference to the chemical and physical parameters of the hydrothermal process.We have developed a groundbreaking method to thermoinactivate endotoxins by means of a soft hydrothermal process, in which the steam saturation ratio can be controlled. The steam saturation ratio is calculated as follows: steam saturation ratio (%) = [steam density (kg/m³)/saturated steam density (kg/m³)] × 100.The soft hydrothermal process lies in the part of the liquid phase of water with a high steam saturation ratio that is characterized by a higher ionic product (k_w) than that of ordinary water. The ionic product is a key parameter in promoting ionic reactions and can be related to hydrolysis. The ionic product of water is 1.0 × 10⁻¹⁴ (mol/liter)² at room temperature and increases with increasing temperature and pressure. A high ionic product favors the solubility of highly polar and ionic compounds, creating the possibility of accelerating the hydrolysis reaction process of organic compounds. Thus, water can play the role of both an acidic and an alkaline catalyst in the hydrothermal process (Fig. ​(Fig.1)1) (1, 37, 46). However, the soft hydrothermal process lies in the high-density water molecular area of the steam-gas biphasic field (Fig. ​(Fig.1)1) and is characterized by a lower dielectric constant (ɛ) than that of ordinary water. This process opens the possibility of promoting the affinity of water for nonpolar or low-polarity compounds, such as lipophilic organic compounds (46). We previously reported that most of the predominant aromatic hydrocarbons were removed from softwood bedding that had been treated by soft hydrothermal processing (24, 28).Open in a separate windowFIG. 1.Reaction field in the pressure-temperature relationship of water. The curve represents the saturated vapor pressure curve. The fields show where the pressure-temperature relationships are conducive to a variety of hydrothermal processing conditions, in which water has a large impact as a reaction medium. Because high-density water has a large dielectric constant and ionic product, it is an effective reaction medium for advancing ionic reactions, whereas water (in the form of steam) on the lower-pressure side of the saturated vapor pressure curve shows a good ability to form materials by covalent bonding. Small changes in the density of water can result in changes in the chemical affinity, which has the potential to advance a range of ionic and radical reactions.The purpose of the present study was to evaluate the thermoinactivation of endotoxins by the soft hydrothermal process, by controlling the steam saturation ratio, temperature, and time of treatment. There have been reports that endotoxins were thermoinactivated by steam heat treatment at 121°C in the presence of a nonionic surfactant and at over 135°C in its absence (4, 5, 10), but the minimum temperature for the inactivation of endotoxin remained unknown. This report provides the answer to this question.     

False codling moth Thaumatotibia leucotreta (Lepidoptera,Tortricidae) larvae are chill‐susceptible

Abstract This study reports on the low temperature tolerance and cold hardiness of larvae of false codling moth, Thaumatotibia leucotreta. We found that larvae have mean critical thermal minima (lower limits of activity) of 6.7°C which was influenced by feeding status. The effects of low temperature exposure and duration of exposure on larval survival were assessed and showed that the temperature at which 50% of the population survives is ?11.5 ± 0.3°C after 2 h exposure. The supercooling point (SCP, i.e., freezing temperature) was investigated using a range of cooling rates and under different conditions (feeding and hydration status) and using inoculative freezing treatments (in contact with water or orange juice). The SCP decreased significantly from ?15.6°C to ?17.4°C after larvae were fasted for 24 h. Twenty‐four hour treatments at either high or low relative humidity (95.9% or 2.4%) also significantly decreased SCP to ?17.2°C and ?18.2°C respectively. Inoculative freezing (by water contact) raised SCP from ?15.6°C to ?6.8°C which could have important implications for post‐harvest sterilization. Cooling rates did not affect SCP which suggests that there is limited phenotypic plasticity of SCP during the larval life‐stage, at least over the short time‐scales investigated here. In conclusion, larvae of T. leucotreta are chill‐susceptible and die upon freezing. These results are important in understanding this pest's response to temperature variation, understanding pest risk status and improving post‐harvest sterilization efficacy.     

Thermoinactivation of cellobiohydrolase I from Trichoderma reesei QM 9414

Irreversible thermoinactivation of cellobiohydrolase I from Trichoderma reesei has been analyzed at 70°C and pH 4.8. The time course of thermal inactivation and the dependence of the inactivation rates on protein concentration suggested that aggregation followed by precipitation was the main process leading to irreversible thermoinactivation. The enzyme activity was very resistant to 4 M urea which stabilized the enzyme against thermal inactivation. Deamidation of Asn/Gln residues and hydrolysis of peptide bonds were responsible for the loss of enzyme activity at long times of exposure at 70°C.     

Safety‐Reinforced Poly(Propylene Carbonate)‐Based All‐Solid‐State Polymer Electrolyte for Ambient‐Temperature Solid Polymer Lithium Batteries

An integrated preparation of safety‐reinforced poly(propylene carbonate)‐based all‐solid polymer electrolyte is shown to be applicable to ambient‐temperature solid polymer lithium batteries. In contrast to pristine poly(ethylene oxide) solid polymer electrolyte, this solid polymer electrolyte exhibits higher ionic conductivity, wider electrochemical window, better mechanical strength, and superior rate performance at 20 °C. Moreover, lithium iron phosphate/lithium cell using such solid polymer electrolyte can charge and discharge even at 120 °C. It is also noted that the solid‐state soft‐package lithium cells assembled with this solid polymer electrolyte can still power a red light‐emitting diode lamp without suffering from internal short‐circuit failures even after cutting off one part of the battery. Considering the aspects mentioned above, the solid polymer electrolyte is eligible for practical lithium battery applications with improved reliability and safety. Just as important, a new perspective that the degree of amorphous state of polymer is also as critical as its low glass transition temperature for the exploration of room temperature solid polymer electrolyte is illustrated. In all, this study opens up a kind of new avenue that could be a milestone to the development of high‐voltage and ambient‐temperature all‐solid‐state polymer electrolytes.     

OPTIMIZATION OF PROCESSING OF PEANUT BEVERAGE1

Peanut beverages were prepared and homogenized at 2000, 4000, and 6000 psi and processed at 100°C for 10, 15, and 20 min and at 121°C for 5, 10, and 15 min. Sensory analysis, gas chromatographic (GC) analysis, and viscosity measurements were performed on the products. Sulfur aromatic was found sufficient to discriminate between samples processed at 100°C whereas sulfur aromatic, cooked peanut flavor, and bitterness provided the most efficient combination for discriminating between samples processed at 121°C. Processing time had a more significant effect on the sensory attributes of products. Optimum conditions for processing were found to be at homogenization pressure > 3100 psi and process time > 16 min at a processing temperature of 100°C. No sensory characteristic of the peanut beverage correlated with the instrumental analyses done.     

Kinetic study of the thermal denaturation of a hyperthermostable extracellular α-amylase from Pyrococcus furiosus

Hyperthermophilic enzymes are of industrial importance and interest, especially due to their denaturation kinetics at commercial sterilisation temperatures inside safety indicating time–temperature integrators (TTIs). The thermal stability and irreversible thermal inactivation of native extracellular Pyrococcus furiosus α-amylase were investigated using differential scanning calorimetry, circular dichroism and Fourier transform infrared spectroscopy. Denaturation of the amylase was irreversible above a T_m of approximately 106 °C and could be described by a one-step irreversible model. The activation energy at 121 °C was found to be 316 kJ/mol. Using CD and FT-IR spectroscopy it was shown that folding and stability greatly increase with temperature. Under an isothermal holding temperature of 121 °C, the structure of the PFA changes during denaturation from an α-helical structure, through a β-sheet structure to an aggregated protein. Such data reinforces the use of P. furiosus α-amylase as a labile species in TTIs.     

Production of 8,11‐dihydroxy and 8‐hydroxy unsaturated fatty acids from unsaturated fatty acids by recombinant Escherichia coli expressing 8,11‐linoleate diol synthase from Penicillium chrysogenum

Hydroxy unsaturated fatty acids can be used as antimicrobial surfactants. 8,11‐Linoleate diol synthase (8,11‐LDS) catalyzes the conversion of unsaturated fatty acid to 8‐hydroperoxy unsaturated fatty acid, and it is subsequently isomerized to 8,11‐dihydroxy unsaturated fatty acid by the enzyme. The optimal reaction conditions of recombinant Escherichia coli expressing Penicillium chrysogenum 8,11‐LDS for the production of 8,11‐dihydroxy‐9,12(Z,Z)‐octadecadienoic acid (8,11‐DiHODE), 8,11‐dihydroxy‐9,12,15(Z,Z,Z)‐octadecatrienoic acid (8,11‐DiHOTrE), 8‐hydroxy‐9(Z)‐hexadecenoic acid (8‐HHME), and 8‐hydroxy‐9(Z)‐octadecenoic acid (8‐HOME) were pH 7.0, 25°C, 10 g/L linoleic acid, and 20 g/L cells; pH 6.0, 25°C, 6 g/L α‐linolenic acid, and 60 g/L cells; pH 7.0, 25°C, 8 g/L palmitoleic acid, and 25 g/L cells; and pH 8.5, 30°C, 6 g/L oleic acid, and 25 g/L cells, respectively. Under these optimized conditions, the recombinant cells produced 6.0 g/L 8,11‐DiHODE for 60 min, with a conversion of 60% (w/w) and a productivity of 6.0 g/L/h; 4.3 g/L 8,11‐DiHOTrE for 60 min, with a conversion of 72% (w/w) and a productivity of 4.3 g/L/h; 4.3 g/L 8‐HHME acid for 60 min, with a conversion of 54% (w/w) and a productivity of 4.3 g/L/h; and 0.9 g/L 8‐HOME for 30 min, with a conversion of 15% (w/w) and a productivity of 1.8 g/L/h. To best of our knowledge, this is the first report on the biotechnological production of 8,11‐DiHODE, 8,11‐DiHOTrE, 8‐HHME, and 8‐HOME. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:390–396, 2017     

Isolation and Partial Characterization of Antifungal Metabolites Produced by <Emphasis Type="Italic">Bacillus</Emphasis> sp. IBA 33

Antifungal proteins produced by Bacillus sp. IBA 33 were purified by ammonium sulfate precipitation and DEAE-Sephacel column chromatography. The two purified proteins inhibited the growth of Geotrichum candidum, the sour rot disease agent in lemon. The proteins were stable at 20 (3 months), 40, 60 and 100°C (30 min) and remained active after sterilization at 121°C for 15 min. Their hydrophobic nature was proved and when were developed with ninhydrin they did not show any free amino groups. The infrared spectrum showed vibrational modes corresponding to peptide, ester or ketone links and saturated CH links corresponding to long chain fatty acids. UV scan spectroscopy showed tyrosine and or tryptophan amino acids in their composition. The remarkable thermo-resistance of proteins may be a good feature to be used in the development of a new biocontrol method of Geotrichum candidum.     

Detecting cellulase penetration into corn stover cell walls by immuno‐electron microscopy

In general, pretreatments are designed to enhance the accessibility of cellulose to enzymes, allowing for more efficient conversion. In this study, we have detected the penetration of major cellulases present in a commercial enzyme preparation (Spezyme CP) into corn stem cell walls following mild‐, moderate‐ and high‐severity dilute sulfuric acid pretreatments. The Trichoderma reesei enzymes, Cel7A (CBH I) and Cel7B (EG I), as well as the cell wall matrix components xylan and lignin were visualized within digested corn stover cell walls by immuno transmission electron microscopy (TEM) using enzyme‐ and polymer‐specific antibodies. Low severity dilute‐acid pretreatment (20 min at 100°C) enabled <1% of the thickness of secondary cell walls to be penetrated by enzyme, moderate severity pretreatment at (20 min at 120°C) allowed the enzymes to penetrate ～20% of the cell wall, and the high severity (20 min pretreatment at 150°C) allowed 100% penetration of even the thickest cell walls. These data allow direct visualization of the dramatic effect dilute‐acid pretreatment has on altering the condensed ultrastructure of biomass cell walls. Loosening of plant cell wall structure due to pretreatment and the subsequently improved access by cellulases has been hypothesized by the biomass conversion community for over two decades, and for the first time, this study provides direct visual evidence to verify this hypothesis. Further, the high‐resolution enzyme penetration studies presented here provide insight into the mechanisms of cell wall deconstruction by cellulolytic enzymes. Biotechnol. Bioeng. 2009;103: 480–489. © 2009 Wiley Periodicals, Inc.     

Thermotolerance of IVM‐derived bovine oocytes and embryos after short‐term heat shock

A series of experiments were designed to study the effect of elevated temperatures on developmental competence of bovine oocytes and embryos produced in vitro. In experiment 1, the effect of heat shock (HS) by a mild elevated temperature (40.5°C) for 0, 30, or 60 min on the viability of in vitro matured (IVM) oocytes was tested following in vitro fertilization (IVF) and culture. No significant difference was observed between the control (39°C) and the heat‐treated groups in cleavage, blastocyst formation, or hatching (P > 0.05). In experiment 2, when the HS temperature was increased to 41.5°C, neither the cleavage rate nor blastocyst development was affected by treatment. However, the rate of blastocyst hatching appeared lower in the HS groups (13% in control group vs. 3.9% and 5.6% in 30 min and 60 min, respectively; P < 0.05). When IVM oocytes were treated at 43°C prior to IVF (experiment 3), no difference was detected in blastocyst and expanded blastocyst development following heat treatment for 0, 15, or 30 min, but heat treatment of oocytes for 45 or 60 min significantly reduced blastocyst and expanded blastocyst formation (P < 0.05). In experiment 4, the thermotolerance of day 3 and day 4 bovine IVF embryos were compared. When embryos were pre‐treated with a mild elevated temperature (40.5°C) for 1 hr, and then with a higher temperature (43°C) for 1 hr, no improvement in thermotolerance of the embryos was observed as compared to those treated at 43°C alone. However, a higher thermotolerance was observed in day 4 than day 3 embryos. In conclusion, treatment at 43°C, but not 40.5°C or 41.5°C significantly reduced oocyte developmental competence. An increase in thermotolerance was observed from day 3 to day 4 of in vitro embryonic development, which corresponds to the maternal to zygotic transition of gene expression in bovine embryos. Mol. Reprod. Dev. 53:336–340, 1999. © 1999 Wiley‐Liss, Inc.     

Application of microwave‐assisted extraction coupled with high‐speed counter‐current chromatography for separation and purification of Dehydrocavidine from Corydalis saxicola Bunting

Introduction – Dehydrocavidine is a major component of Corydalis saxicola Bunting with sedative, analgesic, anticonvulsive and antibacterial activities. Conventional methods have disadvantages in extracting, separating and purifying dehydrocavidine from C. saxicola. Hence, an efficient method should be established. Objective – To develop a suitable preparative method in order to isolate dehydrocavidine from a complex C. saxicola extract by preparative HSCCC. Methodology – The methanol extract of C. saxicola was prepared by optimised microwave‐assisted extraction (MAE). The analytical HSCCC was used for the exploration of suitable solvent systems and the preparative HSCCC was used for larger scale separation and purification. Dehydrocavidine was analysed by high‐performance liquid chromatography (HPLC) and further identified by ESI‐MS and 1H NMR. Results – The optimised MAE experimental conditions were as follows: extraction temperature, 60°C; ratio of liquid to solid, 20; extraction time, 15 min; and microwave power, 700 W. In less than 4 h, 42.1 mg of dehydrocavidine (98.9% purity) was obtained from 900 mg crude extract in a one‐step separation, using a two‐phase solvent system composed of chloroform–methanol–0.3 m hydrochloric acid (4 : 0.5 : 2, v/v/v). Conclusion – Microwave‐assisted extraction coupled with high‐speed counter‐current chromatography is a powerful tool for extraction, separation and purification of dehydrocavidine from C. saxicola. Copyright © 2009 John Wiley & Sons, Ltd.     

Structure,activity, and stability of metagenome‐derived glycoside hydrolase family 9 endoglucanase with an N‐terminal Ig‐like domain

A metagenome‐derived glycoside hydrolase family 9 enzyme with an N‐terminal immunoglobulin‐like (Ig‐like) domain, leaf‐branch compost (LC)‐CelG, was characterized and its crystal structure was determined. LC‐CelG did not hydrolyze p‐nitrophenyl cellobioside but hydrolyzed CM‐cellulose, indicating that it is endoglucanase. LC‐CelG exhibited the highest activity at 70°C and >80% of the maximal activity at a broad pH range of 5–9. Its denaturation temperature was 81.4°C, indicating that LC‐CelG is a thermostable enzyme. The structure of LC‐CelG resembles those of CelD from Clostridium thermocellum (CtCelD), Cel9A from Alicyclobacillus acidocaldarius (AaCel9A), and cellobiohydrolase CbhA from C. thermocellum (CtCbhA), which show relatively low (29–31%) amino acid sequence identities to LC‐CelG. Three acidic active site residues are conserved as Asp194, Asp197, and Glu558 in LC‐CelG. Ten of the thirteen residues that form the substrate binding pocket of AaCel9A are conserved in LC‐CelG. Removal of the Ig‐like domain reduced the activity and stability of LC‐CelG by 100‐fold and 6.3°C, respectively. Removal of the Gln40‐ and Asp99‐mediated interactions between the Ig‐like and catalytic domains destabilized LC‐CelG by 5.0°C without significantly affecting its activity. These results suggest that the Ig‐like domain contributes to the stabilization of LC‐CelG mainly due to the Gln40‐ and Asp99‐mediated interactions. Because the LC‐CelG derivative lacking the Ig‐like domain accumulated in Escherichia coli cells mostly in an insoluble form and this derivative accumulated in a soluble form exhibited very weak activity, the Ig‐like domain may be required to make the conformation of the active site functional and prevent aggregation of the catalytic domain.     

Identification and characterization of a novel salt‐tolerant esterase from a Tibetan glacier metagenomic library

A salt‐tolerant esterase, designated H9Est, was identified from a metagenomic library of the Karuola glacier. H9Est gene comprised 1071 bp and encoded a polypeptide of 357 amino acids with a molecular mass of 40 kDa. Sequence analysis revealed that H9Est belonged to the family IV of bacterial lypolitic enzyme. H9Est was overexpressed in Escherichia coli and the purified enzyme showed hydrolytic activity towards p‐nitrophenyl esters with carbon chain from 2 to 8. The optimal esterase activity was at 40°C and pH 8.0 and the enzyme retained its activity towards some miscible organic solvents such as polyethylene glycol. A three‐dimensional model of H9Est revealed that S200, D294, and H324 formed the H9Est catalytic triad. Circular Dichroism spectra and molecular dynamic simulation indicated that the esterase had a wide denaturation temperature range and flexible loops that would be beneficial for H9Est performance at low temperatures while retaining heat‐resistant features. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:890–899, 2015     

Molecular basis of the structural stability of hemochromatosis factor E: A combined molecular dynamic simulation and GdmCl‐induced denaturation study

Hemochromatosis factor E (HFE) is a member of class I MHC family and plays a significant role in the iron homeostasis. Denaturation of HFE induced by guanidinium chloride (GdmCl) was measured by monitoring changes in [θ]₂₂₂ (mean residue ellipticity at 222 nm), intrinsic fluorescence emission intensity at 346 nm (F₃₄₆) and the difference absorption coefficient at 287 nm (Δε₂₈₇) at pH 8.0 and 25°C. Coincidence of denaturation curves of these optical properties suggests that GdmCl‐induced denaturation (native (N) state ? denatured (D) state) is a two‐state process. The GdmCl‐induced denaturation was found reversible in the entire concentration range of the denaturant. All denaturation curves were analyzed for , Gibbs free energy change associated with the denaturation equilibrium (N state ? D state) in the absence of GdmCl, which is a measure of HFE stability. We further performed molecular dynamics simulation for 40 ns to see the effect of GdmCl on the structural stability of HFE. A well defined correlation was established between in vitro and in silico studies. © 2015 Wiley Periodicals, Inc. Biopolymers 105: 133–142, 2016.     

Efficient racemization of N‐phenylacetyl‐D‐glufosinate for L‐glufosinate production

Most amino acids contain chiral centres and exist as both D‐enantiomer and L‐enantiomer. The optically pure enantiomer is often more valuable than the racemate. Enzymatic resolution provides an effective strategy to obtain optically pure amino acids but often results in large amounts of unwanted isomer. In this study, optically pure L‐glufosinate (L‐PPT) was obtained by coupling amidase‐mediated hydrolysis of N‐phenylacetyl‐D,L‐glufosinate with racemization of N‐phenylacetyl‐D‐glufosinate (NPDG), which exclusively exhibits effective herbicidal properties compared with its D‐enantiomer. To improve the yield of L‐PPT, the racemization reaction conditions were optimized, and through single‐factor experiments, the optimal reaction temperature, reaction time, and mole ratio of phenylacetic acid to NPDG were determined to be 150°C, 30 minutes, and 1.5, respectively. The response surface methodology was applied to further optimize the racemization conditions, and the final yield of L‐PPT reached 96.13% with optimum reaction temperature of 154°C, reaction time of 23 minutes, and phenylacetic acid/NPDG mole ratio of 1.7, respectively. Moreover, adding a small amount of acetic anhydride further raised the yield of L‐PPT to 97.02%.