Enteric methane emissions are the single largest source of direct greenhouse gas emissions (GHG) in beef and dairy value chains and a substantial contributor to anthropogenic methane emissions globally. In late 2019, the World Wildlife Fund (WWF), the Advanced Research Projects Agency-Energy (ARPA-E) and the Foundation for Food and Agriculture Research (FFAR) convened approximately 50 stakeholders representing research and production of seaweeds, animal feeds, dairy cattle, and beef and dairy foods to discuss challenges and opportunities associated with the use of seaweed-based ingredients to reduce enteric methane emissions. This Perspective article describes the considerations identified by the workshop participants and suggests next steps for the further development and evaluation of seaweed-based feed ingredients as enteric methane mitigants. Although numerous compounds derived from sources other than seaweed have been identified as having enteric methane mitigation potential, these mitigants are outside the scope of this article.

Contemporary consumers demand healthier and more nourishing food, and thus, alternative foods that are low-calorie in fats and/or sugars are preferred. These desired properties may be attained by substituting the fatty acid esters of erythritol and pentaerythritol due to their antioxidant action and low toxicity for humans. In this work, the catalyzed hydrolysis of five fatty acid tetraesters of erythritol and/or pentaerythritol by both porcine pancreas type VI-s lipase (PPL) and Candida antarctica lipase-B (CALB) were studied kinetically. In all cases, except the hydrolysis of pentaerythritol tetrastearate by CALB, Michaelis–Menten kinetics were observed. In addition, the pKa values of the fatty acids released due to the catalyzed hydrolysis of the studied tetraesters by CALB were estimated. In the course of the aforementioned procedures, it was found that the CALB-catalyzed hydrolysis was incomplete to various degrees among four of the five studied tetraesters (excluding erythritol tetraoleate), and one or more estimated apparent pKa values were obtained. These results are novel, and by means of applied methodology, they reveal that erythritol and/or pentaerythritol tetraesters of medium- and long-chain fatty acids are suitable candidates for use as beneficial alternatives to butter and/or sweeteners.

Nowadays, enzyme kinetics and modeling of enzymatic systems are tightly connected and interacting. Nevertheless, a step-by-step approach to both of these two main fields demands an in-depth analytical description of their many particular issues and features. In the beginning, some preliminary knowledge and concepts were considered necessary, whereas the systematic approach to the main course of this chapter starts with a section devoted to the comprehension of fundamentals of enzyme kinetics. Subsequently, a series of important operating methodologies applicable to enzyme kinetics are comprehensively described. This chapter ends with a detailed analysis and description of the modern in-silico modeling of enzymatic systems, which is preceded by a concise section in which we explain the coupling of enzyme kinetics and modeling.

Immobilized Lipase-B from Candida antarctica catalyzed the esterification of butyric acid and ethanol under anhydrous solvent-free reaction conditions toward the synthesis of ethyl butyrate, a compound significant as food and perfume flavoring, as well as biofuel. The proton inventory technique was efficiently applied in mixtures of the anhydrous polar solvents ethanol and deuterated ethanol (CH3CH2OD). Subsequently, and by suitable analysis of the experimental data, the aforementioned synthetic procedure seems likely to follow the kinetic mechanism ordered bi-bi involving single substrate dead-end inhibition by ethanol, whereas were estimated values of important parameters. So far is the first experimental evidence that the synthesis of ethyl butyrate, which is catalyzed by immobilized lipase, it follows an entirely different mechanism when it is performed in anhydrous solvent-free system vs. that in anhydrous n-hexane; then it may be constructive for the industrial production of fixed quality of ethyl butyrate.

The development of sensitive, easy and reliable methods for the determination of Rhizomucor pusillus rennin (MPR) activity, in free and in immobilized form, along with the elucidation of the mechanism of action, represent challenges for the widespread use of the enzyme in industrial cheese production. These could be accomplished by using highly specific and sensitive substrates, as well as direct assay methods. We designed and synthesized novel substrates based on Fluorescence Resonance Energy Transfer (FRET) for the MPR by employing computational simulation techniques and peptide synthesis in liquid phase. Three FRET-substrates (Abz-GFY-pNA, Abz-SFY-pNA and Abz-GFI-pNA) were found active, while the Abz-GFY-pNA showed the highest reliability, sensitivity and specificity among them. Subsequently, a novel mechanism of MPR action was elucidated, with the development of novel methods for assaying activity in free and immobilized form, which both may contribute in the wider use of rennin in cheese production and other biotechnological applications.

We have recently (8th February 2018) published our article entitled “Molecular, biochemical and kinetic analysis of a novel, thermostable lipase (LipSm) from Stenotrophomonas maltophilia Psi-1, the first member of a new bacterial lipase family (XVIII)” [1]. While our manuscript was going through the final stages of publication, an article by Samoylova et al. [2] was published (12th January 2018) in the journal Extremophiles , entitled “Cloning, expression and characterization of the esterase estUT1 from Ureibacillus thermosphaericus which belongs to a new lipase family XVIII”. Since we could not have known of the work of Samoylova et al. [2] when we submitted our manuscript, and in order to avoid confusion in the scientific community, we propose to reclassify LipSm as the first characterized member of the new bacterial lipase family XIX. Therefore throughout our article [1] “lipase family XVIII” should read “lipase family XIX” (title included).

The enzyme catalyzed esterification of butyric acid by ethanol under anhydrous conditions in n-hexane, through continuous removal of the formed water, follows a ping pong bi-bi reaction mechanism; immobilized lipase-B from Candida antarctica on acrylic resin (Novozyme 435) was used as biocatalyst. For first time, the kinetic data of an enzymatic bi-substrate reaction generating simultaneous double dead-end substrate inhibitions were processed by surface fitting through multiparametric non-linear equations. Both anhydrous CH3CH2OH and/or CH3CH2OD were employed in an attempt to apply the technique of kinetic isotope effects and validate the selection of the best system among two (ping pong bi-bi and ordered bi-bi), which could describe the aforementioned reaction.

In this work we suggest a methodology comprising the design and use of cost-effective, sustainable, and environmentally friendly process for biofuel production compatible with the market demands. A new generation biofuel is produced using fatty acids, which were generated from acidogenesis of industrial wastes of bioethanol distilleries, and esterified with selected alcohols by immobilized Candida antarctica Lipase-B. Suitable reactors with significant parameters and conditions were studied through experimental design, and novel esterification processes were suggested; among others, the continuous removal of the produced water was provided. Finally, economically sustainable biofuel production was achieved providing high ester yield (<97%) along with augmented concentration (3.35M) in the reaction mixtures at relatively short esterification times, whereas the immobilized lipase maintained over 90% of its initial esterifying ability after reused for ten cycles.

Delignified wheat straw was fermented by a mixed bacterial anaerobic culture obtained from a UASB reactor to produce organic acids (OAs). Kissiris was used as immobilization carrier in a 2-compartment 82 L bioreactor filled with 17 L of fermentation broth for the first 7 fermentation batches and up to 40 L for the subsequent batches. The amount of straw used was 30 g/L and the temperature was set at 37 degrees C for all experiments. The total OAs reached concentrations up to 17.53 g/L and the produced ethanol ranged from 0.3 to 1 mL/L. The main OAs produced was acetic acid (6-8 g/L) and butyric acid (3-8 g/L). The OAs were recovered from the fermentation broth by a downstream process using 1-butanol, which was the solvent with the best recovery yields and also served as the esterification alcohol. The enzymatic esterification of OAs resulted to 90% yield. (C) 2017 Elsevier Ltd. All rights reserved.

Structural and mechanistic insights were revealed for the reversible inhibition of Porcine Pancreatic Elastase (PPE); the kinetics of uninhibited and inhibited hydrolysis of substrate Suc-AAA-pNA was analyzed thoroughly. Additionally, the interactions between PPE and its inhibitor were studied by computational techniques. The uninhibited hydrolysis of Suc-AAA-pNA by PPE proceeds through a virtual transition state, involving an inferior physical and another dominating chemical step, where two stabilized reactant states precede the predominant acyl-enzyme. Different kinds of bonding with the PPE-backbone residues, including those of the catalytic triad, were found during the MD simulation of 5 ns, as key interactions favoring a higher stabilization of the best ranked complex PPE-CF3C(O)-KA-NHPh-p-CF3. The proton inventories of the inhibited hydrolysis of Suc-AAA-pNA by PPE, were ruled out the existence of any virtual transition state and thus they argue for a different mode of catalysis involving a structurally disturbed PPE molecule. Thereafter, a novel inhibition mechanism was suggested.

An economic evaluation of an integrated technology for industrial scale new generation biofuel production using whey, vinasse, and lignocellulosic biomass as raw materials is reported. Anaerobic packed-bed bioreactors were used for organic acids production using initially synthetic media and then wastes. Butyric, lactic and acetic acid were predominately produced from vinasse, whey, and cellulose, respectively. Mass balance was calculated for a 16,000L daily production capacity. Liquid-liquid extraction was applied for recovery of the organic acids using butanol-1 as an effective extraction solvent which serves also as the alcohol for the subsequent enzyme-catalyzed esterification. The investment needed for the installation of the factory was estimated to about 1.7million€ with depreciation excepted at about 3months. For cellulosics, the installation investment was estimated to be about 7-fold higher with depreciation at about 1.5years. The proposed technology is an alternative trend in biofuel production.

The kinetics of immobilized enzymes can not be analyzed by means of the simple Michaelis-Menten concept, which generally fails to describe the immobilized state due to both its probable barriers, and because the active concentration of the enzyme approaches, or even exceeds this of its substrate(s). In such cases, the various experimental data are usually treated by complex rate equations comprising too many parameters acquiring different natures and meanings, depending on both the properties of the immobilization state and the experimental conditions; thus, more likely, only apparent values of the Michaelis-Menten kinetic parameters can be estimated experimentally. Likewise, immobilization is often a key method in optimizing the operational performance of enzymes, in both laboratory and industrial scale, and affects considerably the kinetics in non-aqueous and non-conventional media due to several issues as the structural changes of the enzyme molecule, the heterogeneity of the system, and the partial or total absence of water. In this work a theoretical approach is described on the formulation of simplified rate equations, reflecting also the actual mass balances of the reactants, in the case where esterification synthetic reactions are catalyzed by immobilized lipases, in either a non-aqueous organic solvent or in a non-solvent system.

The aim of this work was to study the production of extracellular α-amylase by Kluyveromyces marxianus IF0 0288 using optimized nutritional and cultural conditions in a complex yeast medium under aerobic batch fermentation. By applying the conventional "one-variable-at-a-time" approach and the response surface methodology, the effect of four fermentation parameters (type of carbon source, initial culture pH, temperature, and incubation time) on the growth and α-amylase production was evaluated. The production of α-amylase during 60 h of fermentation increased 13-fold under optimized conditions (1% starch, pH 6.0, 30ºC) in comparison to the conventional optimization method. The initial pH value of 6.13 and temperature of 30.3ºC were optimal conditions by the response surface methodology, leading to further improvement (up to 13-fold) in the production of extracellular α-amylase. These results constituted first evidence that K. marxianus could be potentially used as an effective source of extracellular α-amylase.

The optimized production of extracellular protease by Kluyveromyces marxianus IF0 0288 is investigated in yeast medium containing glucose as the carbon source in fully aerobic batch fermentation (150 rpm). Four parameters - type of nitrogen source, initial culture pH, temperature and length of fermentation- influencing the growth and protease production, were considered using both the “one variable at a time” approach and response surface methodology (RSM). Experimental and statistical evidence is presented for 36-fold increase in protease volumetric activity during 72 hours of fermentation with conventionally optimized nutrition (0.04% w/v bovine serum albumin) and cultivation (pH 5.5, 25oC) conditions. The optimal initial pH-value 5.46 and temperature 25.9oC were identified by the RMS and further improved on application both the volumetric activity (42.5-fold) and specific protease activity (51-fold). The results provide for the first time the evidence that K. marxianus is potentially an efficient producer of extracellular protease. Keywords: Aerobic batch fermentation, factorial design, food industry, incubation time, initial pH, Kluyveromyces marxianus, nitrogen source, optimization, process temperature, protease activity, response surface methodology, serine protease, statistical analysis, submerged fermentation, yeast

Lipase-catalyzed esterification reactions are among the most significant chemical and biochemical processes of industrial relevance. Lipases catalyze hydrolysis as well as esterification reactions. Enzyme-catalyzed esterification has acquired increasing attention in many applications, due to the significance of the derived products. More specifically, the lipase-catalyzed esterification reactions attracted research interest during the past decade, due to an increased use of organic esters in biotechnology and the chemical industry. Lipases, as hydrolyzing agents are active in environments, which contain a minimum of two distinct phases, where all reactants are partitioned between these phases, although their distribution is not fixed and changes as the reaction proceeds. The kinetics of the lipase-catalyzed reactions is governed by a number of factors. This article presents a thorough and descriptive evaluation of the applied trends and perspectives concerning the enzymatic esterification, mainly for biofuel production; an emphasis is given on essential factors, which affect the lipase-catalyzed esterification reaction. Moreover, the art of using bacterial and/or fungal strains for whole cell biocatalysis purposes, as well as carrying out catalysis by various forms of purified lipases from bacterial and fungal sources is also reviewed.

In this study, the production and optimization of extracellular lipase from Kluyveromyces marxianus IFO 0288 was investigated by using optimized nutritional and cultural conditions in a yeast medium containing glucose as the carbon source in fully aerobic batch fermentation (150 rpm). The influence of four fermentation parameters (type of lipidic source, initial culture pH, temperature, and length of fermentation) on growth and lipase production was investigated and evaluated using the conventional "one variable at a time" approach and response surface methodology. An 18-fold increase in lipase production during 65 h of fermentation was obtained with optimized nutritional (0.5 % olive oil) and cultivation (pH 6.5, 35 °C) conditions by employing the conventional optimization method. By applying the response surface methodology technique the initial pH value of 6.4 and temperature of 32.5 °C were identified as optimal and led to further improvements (up to 18-fold) of extracellular lipase production. The results provide, for the first time, evidence that K. marxianus has the potential to be used as an efficient producer of extracellular lipase with prospective application in a variety of industrial and biotechnological areas.

A novel extracellular hydrolase of ∼45kDa molecular mass was purified from Kluyveromyces marxianus IFO 0288 cultures and characterized as serine protease. The K(m)-value of protease (designated protease-KM-IFO-0288-A), which was found active in media containing elevated [NaCl] but lacking EDTAK(2), decreased with increasing [Ca(2+)]. The protease maintained considerable activity at the range of 10-60°C and pH 6.00-10.25, with optimum k(cat)/K(m)-value at 35.5°C and pH 7.75. It was strongly affected by specific irreversible inhibitors of serine proteases while was unaffected by inhibitors of cysteine proteases. Significant rate constants, activation energies, and proton inventories were estimated from the profiles of Michaelis-Menten parameters, versus pH, temperature and deuterium atom fraction, in the hydrolysis of Suc-AAPF-pNA showing that protease-KM-IFO-0288-A performs catalysis via a charge-relay system. The properties of protease-KM-IFO-0288-A suggest that K. marxianus represents a valuable source of extracellular protease of biotechnological interest which, given its GRAS status, could find several important applications.