Bioconversion of phospholipids by immobilized phospholipase A2

Phospholipase A₂ selectively hydrolyses the ester linkage at the sn-2 position of phospholipids forming lysocompounds. This bioconversion has importance in biotechnology since lysophospholipids are strong bioemulsifiers. The aim of the present work was to study the kinetic behaviour and properties of immobilized phospholipase A₂ from bee venom adsorbed into an ion exchange support. The enzyme had high affinity for CM-Sephadex^® support and the non-covalent interaction was optimum at pH 8. The activity of immobilized phospholipase A₂ was comparatively evaluated with the soluble enzyme using a phospholipid/Triton X-100 mixed micelle as assay system. The immobilized enzyme showed high retention activity and excellent stability under storage. The activity of the immobilized system remained almost constant after several cycles of hydrolysis. Immobilized phospholipase A₂ was less sensitive to pH changes compared to soluble form. The kinetic parameters obtained (V_max 883.4 μmol mg⁻¹ min⁻¹ and a K_m 12.9 mM for soluble form and V_max = 306 μmol mg⁻¹ min⁻¹ and a K_m = 3.9 for immobilized phospholipase A₂) were in agreement with the immobilization effect. The results obtained with CM-Sephadex^®-phospholipase A₂ system give a good framework for the development of a continuous phospholipid bioconversion process.     

The potential of enzyme recycling during the hydrolysis of a mixed softwood feedstock

Despite recent improvement in cellulase enzymes properties, the high cost associated with the hydrolysis step remains a major impediment to the commercialization of full-scale lignocellulose-to-ethanol bioconversion process. As part of a research effort to develop a commercial process for bioconversion of softwood residues, we have examined the potential for recycling enzymes during the hydrolysis of mixed softwood substrate pretreated by organosolv process. We have used response surface methodology to determine the optimal temperature, pH, ionic strength, and surfactant (Tween 80) concentration for maximizing the recovery of bound protein and enzyme activity from the residual substrates after hydrolysis. Data analysis showed that the temperature, pH and surfactant concentration were the major factors governing enzyme desorption from residual substrate. The optimized conditions were temperature 44.4 °C, pH 5.3 and 0.5% Tween 80. The optimal conditions significantly increased the hydrolysis yield by 25% after three rounds of hydrolysis. This bound enzyme desorption combining with free enzyme re-adsorption is a potential method to recover cellulase enzymes and reduce the cost of enzymatic hydrolysis.     

Microbacterium trichotecenolyticum enzyme mediated transformation of arteannuin B to artemisinin

Artemisinin, a sesquiterpene lactone containing an endoperoxide bridge, isolated from Artemisia annua L. is effective against both drug resistant and cerebral malaria causing strains of Plasmodium falciparum. The relative low yields of artemisinin in plants are a serious limitation to the commercialization of the drug. An alternative approach by microbial bioconversion of arteannuin B to artemisinin was carried out by Microbacterium trichotecenolyticum isolated from soil. Crude enzyme extract from cell free extracts were capable of microbial bioconversion of arteannuin B, the immediate precursor of artemisinin, to artemisinin. Attempts have been made to partially purify the proteins involved in bioconversion by ion exchange chromatography. Detection of artemisinin was done by thin layer chromatography, and quantified by HPLC.     

Efficacy of a hot washing process for pretreated yellow poplar to enhance bioethanol production

Cost reductions for pretreatment and bioconversion processes are key objectives necessary to the successful deployment of a bioethanol industry. These unit operations have long been recognized for their impact on the production cost of ethanol. One strategy to achieve this objective is to improve the pretreatment process to produce a pretreated substrate resulting in reduced bioconversion time, lower cellulase enzyme usage, and/or higher ethanol yields. Previous research produced a highly digestible pretreated yellow poplar substrate using a multistage, continuously flowing, very dilute sulfuric acid (0.07% (w/v)) pretreatment. This process reduced the time required for the bioconversion of pretreated yellow poplar sawdust to ethanol. This resulted in a substantially improved yield of ethanol from cellulose. However, the liquid volume requirements, steam demand, and complexity of the flow-through reactor configuration were determined to be serious barriers to commercialization of that process. A reconfigured process to achieve similar performance has been developed using a single-stage batch pretreatment followed by a separation of solids and liquids and washing of the solids at a temperatures between 130 and 150 degrees C. Separation and washing at the elevated temperature is believed to prevent a large fraction of the solubilized lignin and xylan from reprecipitating and/or reassociating with the pretreated solids. This washing of the solids at elevated temperature resulted in both higher recovered yields of soluble xylose sugars and a more digestible pretreated substrate for enzymatic hydrolysis. Key operating variables and process performance indicators included acid concentration, temperature, wash volume, wash temperature, soluble xylose recovery, and performance of the washed, pretreated solids in bioconversion via simultaneous saccharification and fermentation (SSF). Initial results indicated over a 50% increase in ethanol yield at 72 h for the hot washed material as compared to the control (no washing, no separation) and a 43% reduction of in the bioconversion time required for a high ethanol yield from cellulose     

Screening and selection of a microbial lipase for the stereospecific hydrolysis of Verlukast

Summary A search was implemented for a microbial lipase capable of bioconverting a diester (dimethyl 5-(3-(2-(7-chloroquinolin-2-yl)ethyl)phenyl)4,6-dithianon to its S-ester acid, an intermediate in the production of Verlukast (a leukotriene receptor antagonist). Required properties of the sought-after enzyme included a high enantiomeric selectivity (e.e. >98%), the formation of only trace amounts of diacid and a high bioconversion rate. This search yielded 57 lipase-producing microorganisms, 18 of which presented detectable bioconversion activity. Thirteen of these microbes were selected for further study based upon their lipase production level and enzyme stability at harvest. Despite their common enzymatic property, namely the hydrolysis of triglycerides, these lipase preparations presented diverse ester acid specific synthesis rates (from <0.01 g/unit/h to 0.98 g/unit/h) and diacid formation levels (from 0% to 35%). One of these microbes, identified asPseudomonas aeruginosa (strain MB 5001), was found to produce a lipase having all of the above-listed required properties. The initial fermentation process developed in shake flasks was rapidly and successfully scaled up in 23-liter labora bioreactors, achieving a maximum production of 35 units/ml of lipase after 48 h of cultivation.     

A rapid microassay to evaluate enzymatic hydrolysis of lignocellulosic substrates

Current attempts to produce ethanol from lignocellulosic biomass are focused on the optimization of pretreatment to reduce substrate recalcitrance and the improvement of enzymes for hydrolysis of the cellulose and hemicellulose components to produce fermentable sugars. Research aimed at optimizing both aspects of the bioconversion process involves assessment of the effects of multiple variables on enzyme efficiency, resulting in large factorial experiments with intensive assay requirements. A rapid assay for lignocellulose hydrolysis has been developed to address this need. Pretreated lignocellulose is formed into handsheets, which are then used to prepare small disks that are easily dispensed into microtiter plates. The hydrolysis of cellulose to glucose is estimated using an enzyme-coupled spectrophotometric assay. Using disks prepared from ethanol organosolv pretreated yellow poplar, it is shown that the assay generates data comparable with those produced by hydrolysis of pretreated yellow poplar pulp in Erlenmeyer flasks, followed by HPLC analysis of glucose. The assay shows considerable time and cost benefits over the standard assay protocol and is applicable to a broad range of lignocellulosic substrates.     

The state of the art in the production of fructose from inulin enzymatic hydrolysis

The present work reviews the main advancements achieved in the last decades in the study of the fructose production process by inulin enzymatic hydrolysis. With the aim of collecting and clarifying the majority of the knowledge in this area, the research on this subject has been divided in three main parts: a) the characteristics of inulin (the process reactant); b) the properties of the enzyme inulinase and its hydrolytic action; c) the advances in the study of the applications of inulinases in bioreactors for fructose production. Many vegetable sources of inulin are reported, including information about their yields in terms of inulin. The properties of inulin that appear relevant for the process are also summarized, with reference to their vegetable origin. The characteristics of the inulinase enzyme that catalyzes inulin hydrolysis, together with the most relevant information for a correct process design and implementation, are described in the paper. An extended collection of data on microorganisms capable of producing inulinase is reported. The following characteristics and properties of inulinase are highlighted: molecular weight, mode of action, activity and stability with respect to changes in temperature and pH, kinetic behavior and effect of inhibitors. The paper describes in detail the main aspects of the enzyme hydrolysis reaction; in particular, how enzyme and reactant properties can affect process performance. The properties of inulinase immobilized on various supports are shown and compared to those of the enzyme in its native state. Finally, a number of applications of free and immobilized inulinases and whole cells in bioreactors are reported, showing the different operating procedures and reactor types adopted for fructose production from inulin on a laboratory scale.     

The membrane ATPase of Escherichia coli I. Ion dependence and ATP-ADP exchange reaction

The properties of the membrane-bound ATPase (EC 3.6.1.3) of Escherichia coli have been reexamined using membranes obtained by mechanical disruption of exponentially growing cells.

The activity exhibited an absolute requirement for Mg²⁺ in the neutral pH range, while Ca²⁺ was found able to activate ATPase at more alkaline pH. Optimal activity was observed at pH 7.5, with a Mg/ATP ratio of 0.5.

ADP was found to inhibit ATP hydrolysis and to transform the Michaelian ATP concentration dependence with a K_m of 0.5 mM into a sigmoid curve with increasing K_m and decreasing V.

In contrast ADP activated an ATP-ADP exchange process and this shift from hydrolysis to exchange was stimulated by high Mg²⁺ and by orthophosphate.

All nucleoside triphosphates tested interfered with ATP hydrolysis, all could be hydrolyzed and could donate their terminal phosphate group to ADP. The relative efficiencies of nucleoside triphosphates in these three processes varied in parallel with minor discrepancies.

ATP hydrolysis was inhibited by N,N′-dicyclohexylcarbodiimide (DCCD) Dio 9, NaN₃ and pyrophosphate, the first two being ineffective against ATP-ADP exchange, the third being stimulatory and the last inhibitory.

ATP hydrolysis and ATP-ADP exchange are tentatively attributed to the terminal enzyme of oxidative phosphorylation.     

Microbiological transformation of mycophenolic acid

In our microbial screening program, we have isolated a fungal strain which produced mycophenolic acid (MPA). This compound is a selective inhibitor of guanine synthesis and, therefore, it has antibacterial, antiviral, antitumor and selective immunosuppressive activities, too. This last effect was utilised by Roche-Syntex to develop a derivative of MPA to the immunosuppressive drug CellCept®.

In order to obtain novel derivatives of MPA with an enhanced activity, we applied bioconversion of MPA with various microorganisms. TLC with densitometric evaluation and HPLC methods were developed for measurement of MPA derivatives. In the course of the bioconversion of MPA by using various types of microorganisms amidation of the carboxyl group, hydroxylation of the C₄-methyl group and formation of glycoside derivatives from the hydroxyl group located on C₇ were observed as the most frequently occurring transformations. The structures of bioconversion products were determined by UV, IR, ¹H NMR, ¹³C NMR and mass spectroscopic methods.

The taxonomic features of cultures of the species applied in the bioconversion were also determined.     

Improvement of corn stover bioconversion efficiency by using plant glycoside hydrolase

Plant cell wall is the most abundant substrate for bioethanol production, and plants also represent a key resource for glycoside hydrolase (GH). To exploit efficient way for bioethanol production with lower cellulase loading, the potential of plant GH for lignocellulose bioconversion was evaluated. The GH activity for cell wall proteins (CWPs) was detected from fresh corn stover (FCS), and the synergism of which with Trichoderma reesei cellulase was also observed. The properties for the GH of FCS make it a promising enzyme additive for lignocellulose biodegradation. To make use of the plant GH, novel technology for hydrolysis and ethanol fermentation was developed with corn stover as substrate. Taking steam-exploded corn stover as substrate for hydrolysis and ethanol fermentation, compared with T. reesei cellulase loaded alone, the final glucose and ethanol accumulation increased by 60% and 63% respectively with GH of FCS as an addition.     

Recycling cellulases during the hydrolysis of steam exploded and ethanol pretreated Lodgepole pine

Recycling of cellulases is one way of reducing the high cost of enzymes during the bioconversion process. The effects of surfactant addition on enzymatic hydrolysis and the potential recycling of cellulases were studied during the hydrolysis of steam exploded Lodgepole pine (SELP) and ethanol pretreated Lodgepole pine (EPLP). Three cellulase preparations (Celluclast, Spezyme CP, and MSUBC) were evaluated to determine their hydrolysis efficiencies over multiple rounds of recycling. The surfactant, Tween 80, significantly increased the yield from 63% to 86% during the hydrolysis of the SELP substrate. The addition of surfactant to the hydrolysis of the EPLP substrate increased the free enzymes in the supernatant from 71% of the initial protein to 96%. Based on the Langmuir adsorption constants, cellulases (Celluclast and Spezyme CP) from Trichoderma reesei showed a higher affinity (3.48 mL/mg and 3.17 mL/mg) for the EPLP substrate than did the Penicillium enzyme (0.62 mg/mg). The Trichoderma reesei enzyme was used in four successive rounds of enzyme recycling using surfactant addition and readsorption onto fresh substrates during the hydrolysis of EPLP. In contrast, the Penicillium-derived enzyme preparation (MSUBC) could only be recycled once. When the same recycling strategy was carried out using the SELP substrate, the hydrolysis yield declined during each enzyme recycling round. These results suggested that the higher lignin content of the SELP substrate, and the low affinity of cellulases for the SELP substrate limited enzyme recycling by readsorption onto fresh substrates.     

The State of the Art in the Production of Fructose from Inulin Enzymatic Hydrolysis

ABSTRACT

The present work reviews the main advancements achieved in the last decades in the study of the fructose production process by inulin enzymatic hydrolysis. With the aim of collecting and clarifying the majority of the knowledge in this area, the research on this subject has been divided in three main parts: a) the characteristics of inulin (the process reactant); b) the properties of the enzyme inulinase and its hydrolytic action; c) the advances in the study of the applications of inulinases in bioreactors for fructose production.

Many vegetable sources of inulin are reported, including information about their yields in terms of inulin. The properties of inulin that appear relevant for the process are also summarized, with reference to their vegetable origin.

The characteristics of the inulinase enzyme that catalyzes inulin hydrolysis, together with the most relevant information for a correct process design and implementation, are described in the paper. An extended collection of data on microorganisms capable of producing inulinase is reported. The following characteristics and properties of inulinase are highlighted: molecular weight, mode of action, activity and stability with respect to changes in temperature and pH, kinetic behavior and effect of inhibitors. The paper describes in detail the main aspects of the enzyme hydrolysis reaction; in particular, how enzyme and reactant properties can affect process performance. The properties of inulinase immobilized on various supports are shown and compared to those of the enzyme in its native state.

Finally, a number of applications of free and immobilized inulinases and whole cells in bioreactors are reported, showing the different operating procedures and reactor types adopted for fructose production from inulin on a laboratory scale.     

Simultaneous Bioconversion of Cellulose and Hemicellulose to Ethanol

ABSTRACT:?

Lignocellulosic materials containing cellulose, hemicellulose, and lignin as their main constituents are the most abundant renewable organic resource present on Earth. The conversion of both cellulose and hemicellulose for production of fuel ethanol is being studied intensively with a view to develop a technically and economically viable bioprocess. The fermentation of glucose, the main constituent of cellulose hydrolyzate, to ethanol can be carried out efficiently. On the other hand, although bioconversion of xylose, the main pentose sugar obtained on hydrolysis of hemicellulose, to ethanol presents a biochemical challenge, especially if it is present along with glucose, it needs to be fermented to make the biomass-to-ethanol process economical. A lot of attention therefore has been focussed on the utilization of both glucose and xylose to ethanol. Accordingly, while describing the advancements that have taken place to get xylose converted efficiently to ethanol by xylose-fermenting organisms, the review deals mainly with the strategies that have been put forward for bioconversion of both the sugars to achieve high ethanol concentration, yield, and productivity. The approaches, which include the use of (1) xylose-fermenting yeasts alone, (2) xylose isomerase enzyme as well as yeast, (3) immobilized enzymes and cells, and (4) sequential fermentation and co-culture process are described with respect to their underlying concepts and major limitations. Genetic improvements in the cultures have been made either to enlarge the range of substrate utilization or to channel metabolic intermediates specifically toward ethanol. These contributions represent real significant advancements in the field and have also been adequately dealt with from the point of view of their impact on utilization of both cellulose and hemicellulose sugars to ethanol.     

微生物转化连翘苷制备连翘脂素的研究

本文旨在开发一种微生物转化工艺,将连翘苷转化为活性更高的连翘脂素.结果从土壤中分离筛选到一株桔青霉(Penicillium citrinum)LB菌株,转化连翘苷为连翘脂素的专一性较高.经培养基主要组成和转化条件优化,得出较佳的产酶培养组成为:蔗糖7 g/L,(NH4)2 SO45 g/L,NaCl 5 g/L,KH2 PO45 g/L,MgSO41 g/L,MnSO40.5 g/L,pH 6.0.LB菌株经产酶培养后,过滤收集菌体悬浮于2倍发酵液体积的磷酸盐缓冲液中,加入2 g/L的底物连翘苷,于30℃、200 r/min转化20 h,连翘脂素的转化得率可达94.1%.利用微生物将连翘苷转化为连翘脂素,具有方法简单、转化得率高、产物容易纯化和副产物少等优点,有潜在的工业化应用价值.     

Sulfamoyloxy-substituted 2-phenylindoles: antiestrogen-based inhibitors of the steroid sulfatase in human breast cancer cells

Estrone sulfate (E1S) is an endogenous prodrug that delivers estrone and, subsequently, estradiol to the target cells following the hydrolysis by the enzyme estrone sulfatase which is active in various tissues including hormone dependent breast cancer cells. Blockade of this enzyme should reduce the estrogen level in breast cancer cells and prevent hormonal growth stimulation. Sulfamates of a variety of phenolic compounds have been shown to be inhibitors of estrone sulfatase. Our rational is based on findings that these inhibitors can undergo hydrolysis and the pharmacological effects of the free hydroxy compounds contribute to the bioactivity of the sulfamates. A desirable action of the metabolites would be an estrogen antagonism to block stimulatory effects of residual amounts of estrogens. Thus, we synthesized a number of sulfamoyloxy-substituted 2-phenylindoles with side chains at the indole nitrogen that guarantee antiestrogenic activity. All of the new sulfamates were studied for their inhibitory effects on the enzyme estrone sulfatase from human breast cancer cells and their (anti)hormonal activities in stably transfected human MCF-7/2a mammary carcinoma cells. The hormonal profile of the sulfamates was partly reflected by the properties of the corresponding hydroxy precursors. Some of the sulfamoylated antiestrogens strongly inhibited estrone sulfatase activity with IC₅₀ values in the submicromolar range. They were devoid of agonist activity and suppressed estrone sulfate-stimulated gene expression mainly by blocking the enzyme. Examples are the disulfamates of the indoles ZK 119, 010 and ZK 164, 015. Their IC₅₀s for sulfatase inhibition were 0.3 and 0.2 μM, respectively, and 50 and 80 nM, respectively, for the inhibition of E1S-stimulated luciferase expression in transfected MCF-7 cells. With some of the new sulfamates an additional direct antiestrogenic effect was noticed which might be due to a partial hydrolysis during incubation and would improve the growth inhibitory effect on estrogen-sensitive breast cancer cells.     

Bile Salt Stimulated Human Milk Lipase Catalyzed Ester Hydrolysis in Detergentless Microemulsion Media

Bile salt stimulated human milk lipase (E.C.3.1) has been used to catalyze the hydrolysis of 4-nitrophenylalkanoates (alkyl C-chain length, n = 2, 3, 4, 6, 10, 12 and 16) in a detergentless microemulsion medium of n-hexane/iso-propanol/water (71.1:27.7:1.2 vol%) containing 2 mM taurocholate at 37°C. The rate of hydrolysis of the esters with n = 2, 3, or 4 was nearly equal but the rate then fell rapidly with increasing alkyl-chain length. No activity was observed with the palmitate ester. Three dimensional surfaces were built up to represent both the catalytic activity and the rate constant of inactivation for the enzyme catalyzed hydrolysis of 4-nitrophenylpropionate in a range of compositions of the ternary system n-hexane/wo-propanol/water at 37 °C. Maximum activation and maximum inactivation were observed in the ternary region of the phase diagram. In the stable; transparent micro-emulsion region another smaller maximum in activity was observed and, at this same solvent composition, minimum inactivation occurred. Values of K_m lay in the range 1.37-8.98 mM while V_max varied from 0.25-7.59 umol.min.mg^-1 and the rate constant of inactivation k_in ranged from (0.01-1.18). 10^-3 s^-1 over the three-dimensional surfaces. The most important result is that the enzyme retains its activity in microemulsion media containing less than two volume percent water content.     

Factors affecting cellulose and hemicellulose hydrolysis of alkali treated brewers spent grain by Fusarium oxysporum enzyme extract

The enzymatic degradation of polysaccharides to monosaccharides is an essential step in bioconversion processes of lignocellulosic materials. Alkali treated brewers spent grain was used as a model substrate for the study of cellulose and hemicellulose hydrolysis by Fusarium oxysporum enzyme extract. The results obtained showed that cellulose and hemicellulose conversions are not affected by the same factors, implementing different strategies for a successful bioconversion. Satisfactory cellulose conversion could be achieved by increasing the enzyme dosage in order to overcome the end-product inhibition, while the complexity of hemicellulose structure imposes the presence of specific enzyme activities in the enzyme mixture used. All the factors investigated were combined in a mathematical model describing and predicting alkali treated brewers spent grain conversion by F. oxysporum enzyme extract.     

Enantioconvergent bioconversion of p-chlorostyrene oxide to (R)-p-chlorophenyl-1,2-ethandiol by the bacterial epoxide hydrolase of Caulobacter crescentus

The enantioselective hydrolysis of eight racemic styrene oxide derivatives has been investigated by using the recombinant cell containing epoxide hydrolase (EH) of Caulobacter crescentus. Some styrene oxide derivatives were hydrolyzed via enantioconvergent manner so that enantiopure diol products could be prepared with a 100% theoretical yield. The recombinant cell containing C. crescentus EH exhibited an ability to hydrolyze racemic p-chlorostyrene oxide the most enantioconvergently, thus affording the formation of the corresponding (R)-diol with enantiomeric excess (ee) as high as 95% and a 72% yield in preparative-scale (16.8 g/l) bioconversion.     

ON THE PHOSPHOLIPASE A2 ACTIVITY OF HUMAN CEREBRAL CORTEX

Abstract— Preparations of phospholipase Az have been obtained from human cerebral cortex. The enzyme was extracted from acetone-dried tissue and purified by heat-treatment and gel filtration on Sephadex.
Although heating at 65°C or 70°C destroys most of the phospholipase A₁ activity that is present in crude extracts, a small proportion remains associated with the A₂ activity during these procedures. The heat-treated extracts hydrolyse lecithin in preference to phosphatidyl-ethanolamine but have no action on lysolecithin or neutral lipids. The results suggest that A₂ activity and the heat-stable component of A₁ may both be due to a single phospholipase A that can hydrolyse diacylglycerophosphatides at either the 2-or the 1-position, to form a mixture of isomeric lysoderivatives.
A molecular weight of 55,000 was calculated for the enzyme.