Structural Base for Enzymatic Cyclodextrin Hydrolysis

Cyclodextrins resist hydrolysis by burying all bridge oxygens at their interior. Still, the rings can be opened by a small group of specialized enzymes, the cyclomaltodextrinases. Among them, the enzyme from Flavobacterium sp. no. 92 was mutated, crystallized and soaked with cyclodextrins, giving rise to four complex structures. One of them showed an α-cyclodextrin at the outer rim of the active center pocket. In the other complexes, α-, β-and γ-cyclodextrins were bound in a competent mode in the active center. The structures suggest that Arg464 functions as a chaperone guiding the substrates from the solvent into the active center. Over the last part of this pathway, the cyclodextrins bump on Phe274, which rotates the glucosyl group at subsite (+1) by about 120° and fixes it in the new conformation. This induced fit was observed with all three major cyclodextrins. It makes the bridging oxygen between subsites (+1) and (−1) available for protonation by Glu340, which starts the hydrolysis. The mechanism resembles a spring-lock. The structural data were supplemented by activity measurements, quantifying the initial ring opening reaction for the major cyclodextrins and the transglucosylation activity for maltotetraose. Further activity data were collected for mutants splitting the tetrameric enzyme into dimers and for active center mutants.     

Enzymatic Hydrolysis of Esters Containing a Tetrazole Ring

The lipase‐catalyzed enantioselective hydrolysis of acetates containing tetrazole moiety was studied. Among all tested lipases, Novozyme SP 435 allowed to obtain optically active 4‐(5‐aryl‐2H‐tetrazol‐2yl)butan‐2‐ol and 1‐(5‐aryl‐2H‐tetrazol‐2yl)‐propan‐2‐ol and their acetates with the highest optical purities (ee = 95%‐99%) and excellent enantioselectivity (E>100). Some of the synthesized tetrazole derivatives were screened for their antifungal activity. Racemic mixtures of 4‐[5‐(4‐chlorophenyl)‐2H‐tetrazol‐2‐yl)butan‐2‐ol as well as pure enantiomers of this compound showed promising antifungal activity against F. sambucinum, F. oxysporum, C. coccodes, and A. niger. Chirality 26: 811–816, 2014. © 2014 Wiley Periodicals, Inc.     

酶水解制备花生粕多肽工艺的优化

目的：优化研究花生粕制备多肽的工艺。方法：采用酶法水解提取多肽、用总蛋白试剂盒（TP）双缩脲比色法在540nm处测定其含量。结果：用木瓜蛋白酶水解花生粕蛋白得到多肽的最佳工艺条件为：加酶量6 300u/g原料、温度45℃、底物浓度10%、酶水解时间5h。     

Controlled Enzymatic Hydrolysis: A New Strategy for the Discovery of Antimicrobial Peptides

The use of antimicrobial peptides (AMPs) is an alternative to traditional antibiotics. AMPs are obtained using different methods such as bacterial synthesis, chemical synthesis and controlled enzymatic hydrolysis. The later is an interesting approach that deserves our attention because of the yields gathered and peptides engineered. Usually, activities of AMPs obtained in such a way are tightly dependent on the hydrolysis mechanism used. This paper deals with the hydrolysis of hemoglobin mechanism as a potential source of AMPs. Production of AMPs from hemoglobin using enzymatic controlled system is linked to hemoglobin structure. Further, we show that bovine hemoglobin, which is sensitive to peptic hydrolysis, results upon enzymatic digestion as a great source of AMPs. The hemoglobin in native and denatured states was hydrolyzed by “one-by-one” and “zipper” mechanisms, respectively. Nevertheless, a new mechanism named “semi-zipper” mechanism is obtained when protein is in molten globule structural state, constituting an original strategy for AMPs production. Seventy seven percentage of the peptides obtained by this new strategy showed antibacterial activity against nine strains.     

Enhancement of Enzymatic Adipyl-7-ADCA Hydrolysis

We studied enzymatic adipyl-7-ADCA hydrolysis as a new process for the production of 7-aminodeacetoxycephalosporanic acid (7-ADCA), one of the building blocks for cephalosporin antibiotics like cephalexin and cefadroxil. Adipyl-7-ADCA hydrolysis carried out with immobilised glutaryl acylase was considerably enhanced by addition of phenylglycine amide, the side-chain donor used for cephalexin synthesis; unlike reactions carried out with free enzyme. The rate enhancing effect was not specifically related to phenylglycine amide; we found a linear relationship between the reaction rate and the buffering capacity of the added substance. These observations can be explained by a pH-gradient in the immobilised enzyme, the pH inside the particle being lower (corresponding to low enzyme activity) than outside. It was concluded that the buffer reduced the pH-gradient inside the biocatalyst, and therewith, caused the reaction rate enhancing effects. Further, chloride ions decreased the reaction rate strongly, while sodium, magnesium, sulphate, and potassium did not influence the reaction rate much. For an actual process, it is important to use a buffer that is appropriate for the reaction-pH. In that way the amount of enzyme required in a process can be reduced considerably, in our case a factor of three was found.     

Enhancement of Enzymatic Adipyl-7-ADCA Hydrolysis

We studied enzymatic adipyl-7-ADCA hydrolysis as a new process for the production of 7-aminodeacetoxycephalosporanic acid (7-ADCA), one of the building blocks for cephalosporin antibiotics like cephalexin and cefadroxil. Adipyl-7-ADCA hydrolysis carried out with immobilised glutaryl acylase was considerably enhanced by addition of phenylglycine amide, the side-chain donor used for cephalexin synthesis; unlike reactions carried out with free enzyme. The rate enhancing effect was not specifically related to phenylglycine amide; we found a linear relationship between the reaction rate and the buffering capacity of the added substance. These observations can be explained by a pH-gradient in the immobilised enzyme, the pH inside the particle being lower (corresponding to low enzyme activity) than outside. It was concluded that the buffer reduced the pH-gradient inside the biocatalyst, and therewith, caused the reaction rate enhancing effects. Further, chloride ions decreased the reaction rate strongly, while sodium, magnesium, sulphate, and potassium did not influence the reaction rate much. For an actual process, it is important to use a buffer that is appropriate for the reaction-pH. In that way the amount of enzyme required in a process can be reduced considerably, in our case a factor of three was found.     

蛋白质的酶水解过程研究

进行了蛋白质酶水解过程的研究。结果表明木瓜蛋白酶对混合蛋白质的亲和力最强 ,而 1398蛋白酶的亲和力最弱。也表明作用位点和亲和力之间有一定的对应关系 ,Km值和作用位点氨基酸含量比例的相关系数为 0 .90 9。温度影响结果表明温度较低时温度升高加速水解反应过程处主要地位 ;当温度较高时 ,酶失活过程处主导地位。在一定水解时间内的讨论最适温度条件具有更明确的针对性 ,从本研究的采用胰酶 (胰蛋白酶和胰凝乳蛋白酶 )水解 4h的条件下 ,反应温度控制在45～ 5 0℃之间最适     

Enzymatic Hydrolysis of Esters of Alkali Labile Carotenols

Esters of alkali labile carotenols were hydrolyzed enzymatically with pig liver esterase in Tris-HCl buffer containing 10-85% methanol or acetone.

The natural acetates peridinin, fucoxanthin, 19'-butanoyloxyfucoxanthin, pyrrhoxanthin and synthetic actinioerythrol diacetate provided the corresponding carotenols in 85%, 45%, (5 + 5 + 30)%, 65% and (30 + 3)% of the recovered carotenoid with total pigment recoveries 60%, 73%, 88%, 52% and 66%, respectively.

(3RS, 3'RS)-Astaxanthin dipalmitate was converted enzymatically with lipase in low yield to the monopalmitate and free astaxanthin (5% + 6%, pigment recovery 93%) with a preferred hydrolysis of the S-ester. The (R,R:R,S:S,S) ratio of substrate dipalmitate and product astaxanthin changed from 1:2:1 to 1:5:3.     

Optimal Bioreactor Operational Policies for the Enzymatic Hydrolysis of Sugarcane Bagasse

The consolidation of the industrial production of second-generation (2G) bioethanol relies on the improvement of the economics of the process. Within this general scope, this paper addresses one aspect that impacts the costs of the biochemical route for producing 2G bioethanol: defining optimal operational policies for the reactor running the enzymatic hydrolysis of the C6 biomass fraction. The use of fed-batch reactors is one common choice for this process, aiming at maximum yields and productivities. The optimization problem for fed-batch reactors usually consists in determining substrate feeding profiles, in order to maximize some performance index. In the present control problem, the performance index and the system dynamics are both linear with respect to the control variable (the trajectory of substrate feed flow). Simple Michaelis–Menten pseudo-homogeneous kinetic models with product inhibition were used in the dynamic modeling of a fed-bath reactor, and two feeding policies were implemented and validated in bench-scale reactors processing pre-treated sugarcane bagasse. The first approach applied classical optimal control theory. The second policy was defined with the purpose of sustaining high rates of glucose production, adding enzyme (Accellerase® 1500) and substrate simultaneously during the reaction course. A methodology is described, which used economical criteria for comparing the performance of the reactor operating in successive batches and in fed-batch modes. Fed-batch mode was less sensitive to enzyme prices than successive batches. Process intensification in the fed-batch reactor led to glucose final concentrations around 200 g/L.     

Effect of Maize Biomass Composition on the Optimization of Dilute-Acid Pretreatments and Enzymatic Saccharification

At the core of cellulosic ethanol research are innovations leading to reductions in the chemical and energetic stringency of thermochemical pretreatments and enzymatic saccharification. In this study, key compositional features of maize cell walls influencing the enzymatic conversion of biomass into fermentable sugars were identified. Stem samples from eight contrasting genotypes were subjected to a series of thermal dilute-acid pretreatments of increasing severity and evaluated for glucose release after enzymatic saccharification. The biochemically diverse set of genotypes displayed significant differences in glucose yields at all processing conditions evaluated. The results revealed that mechanisms controlling biomass conversion efficiency vary in relation to pretreatment severity. At highly severe pretreatments, cellulose conversion efficiency was primarily influenced by the inherent efficacy of the thermochemical process, and maximum glucose yields were obtained from cellulosic feedstocks harboring the highest cellulose contents per dry gram of biomass. When mild dilute-acid pretreatments were applied, however, maximum bioconversion efficiency and glucose yields were observed for genotypes combining high stem cellulose contents, reduced cell wall lignin and highly substituted hemicelluloses. For the best-performing genotype, glucose yields under sub-optimal processing regimes were only 10 % lower than the genotype-set mean at the most stringent processing conditions evaluated, while furfural production was reduced by approximately 95 %. Our results ultimately established that cellulosic feedstocks with tailored cell wall compositions can help reduce the chemical and energetic intensity of pretreatments used in the industry and improve the commercial and environmental performance of biomass-to-ethanol conversion technologies.     

牦牛骨蛋白的酶解条件研究

以蛋白质水解度为评价指标,辅以固形物溶出率,比较了中性蛋白酶、菠萝蛋白酶和木瓜蛋白酶对牦牛骨蛋白的水解效果,研究了酶用量、料液比(底物浓度)、酶解时间对水解度的影响,采用正交试验对酶解条件进行了优化。结果显示,木瓜蛋白酶是牦牛骨蛋白水解的适宜催化剂。在一定条件下,样品水解度随酶用量和酶解时间的增加而增大,底物浓度过低或过高均不利于原料中蛋白质的酶解。木瓜蛋白酶水解牦牛骨蛋白最佳条件为:酶解温度60℃,酶解时间8 h,酶用量3500 U/g蛋白质,料液比1:25(g:m l)。     

Optimization of Enzymatic Hydrolysis of Steam Pretreated Triticale Straw

Efficient conversion of the carbohydrates into fermentable sugars is crucial for industrial implementation of 2G biofuels such as bioethanol. The main objective of this study was to improve the enzymatic hydrolysis of steam pretreated triticale straw (slurry, pressed-slurry or water insoluble solids (WIS)) by optimal combination of cellulase (Cellic® CTec2) and hemicellulase (Cellic® HTec2) and incubation period for a target glucan conversion of 80 %. Among the three substrates evaluated, pressed-slurry and WIS resulted in similar sugar yields but WIS presented lower enzyme requirements. Different combinations of cellulase and endo-xylanase could provide an 80 % of glucan conversion depending on the weight assigned to constrain. The selected enzyme combination, 0.1 mL Cellic®CTec2/g WIS and 0.2 mL Cellic®HTec2/g WIS, could achieve a glucan conversion of 80 % in 45 h (desirability of 0.9). Doubling the enzyme dosage could further improve the saccharification productivity by reducing the incubation period to 37 h. The optimisation of enzymatic hydrolysis of lignocellulosic substrates, to reduce the cost of sugars production, is a compromise between substrate, enzyme dosage, incubation time and the benchmark yield, although a more favourable response can be generated with an optimised combination of enzymes.     

Process Modeling of Enzymatic Hydrolysis of Wet-Exploded Corn Stover

The aim of this work was to investigate the optimal process conditions leading to high glucose yield (over 80 %) after wet explosion (WEx) pretreatment and enzymatic hydrolysis. The study focused on determining the “sweet spot” where the glucose yield obtained is optimized compared to the cost of the enzymes. WEx pretreatment was conducted at different temperatures, times, and oxygen concentrations to determine the best WEx pretreatment conditions for the most efficient enzymatic hydrolysis. Enzymatic hydrolysis was further optimized at the optimal conditions using central composite design of response surface methodology with respect to two variables: Cellic® CTec2 loading [5 to 40 mg enzyme protein (EP)/g glucan] and substrate concentration (SC) (5 to 20 %) at 50 °C for 72 h. The most efficient and economic conditions for corn stover conversion to glucose were obtained when wet-exploded at 170 °C for 20 min with 5.5 bar oxygen followed by enzymatic hydrolysis at 20 % SC and 15 mg EP/g glucan (5 filter paper units) resulting in a glucose yield of 84 %.     

Biological Pretreatment with Two Bacterial Strains for Enzymatic Hydrolysis of Office Paper

The cellulose-hydrolyzing strains, Sphingomonas paucimobilis MK1 and Bacillus circulans MK2, were separated from soil and were grown together in a single culture plate. Growth B. circulans MK2 in liquid culture required symbiosis with S. paucimobilis MK1. Biological pretreatment with the combined strain suspension after the liquid culture improved enzymatic hydrolysis of office paper from municipal wastes. Sugar recovery by S. paucimobilis MK1 (51%) was 1.4 times higher than that of the untreated sample (30%) and in the strain combination with B. circulans MK2, recovery was further improved by 2.5 times (75%). The sugar recovery in maximum condition was enhanced up to 94% for office paper. Furthermore, biological pretreatment effects were confirmed for more than 1 day less time. In X-ray diffraction patterns for the crystallinity of cellulose in office paper changed after biological pretreatment, the crystallinity was increased in comparison to that in untreated paper. The mechanism of biological pretreatment effect was explained by the fact that the strain acted as an endoglucanase, which hydrolyzes amorphous areas randomly.     

六种蛋白酶酶解效果的研究

本实验利用六种蛋白酶(1、2、3、4、5、6号蛋白酶)分别对豆粕、玉米芽粕、花生粕、菜籽粕、酒糟、黄粉虫、地鳖虫进行酶解,以肽含量为指标研究六种蛋白酶的酶解效果.结果显示,3号蛋白酶对酒糟、黄粉虫、地鳖虫酶解效果明显,酶解液肽含量最高可达12.6 mg·L-1、17.66 mg· L-1和36 mg·L-1;4号蛋白酶对豆粕酶解效果明显,酶解豆粕肽含量达到17.47 mg·L一1;5号蛋白酶对花生粕酶解效果明显,酶解花生粕肽含量最高可达18.45 mg·L1;六种蛋白酶均能酶解菜籽粕,酶解液肽含量均在15 mg·L-1以上,且差异不大.     

Enzymatic Synthesis of Rhamnose Containing Chemicals by Reverse Hydrolysis

Rhamnose containing chemicals (RCCs) are widely occurred in plants and bacteria and are known to possess important bioactivities. However, few of them were available using the enzymatic synthesis method because of the scarcity of the α-L-rhamnosidases with wide acceptor specificity. In this work, an α-L-rhamnosidase from Alternaria sp. L1 was expressed in Pichia pastroris strain GS115. The recombinant enzyme was purified and used to synthesize novel RCCs through reverse hydrolysis in the presence of rhamnose as donor and mannitol, fructose or esculin as acceptors. The effects of initial substrate concentrations, reaction time, and temperature on RCC yields were investigated in detail when using mannitol as the acceptor. The mannitol derivative achieved a maximal yield of 36.1% by incubation of the enzyme with 0.4 M L-rhamnose and 0.2 M mannitol in pH 6.5 buffers at 55°C for 48 h. In identical conditions except for the initial acceptor concentrations, the maximal yields of fructose and esculin derivatives reached 11.9% and 17.9% respectively. The structures of the three derivatives were identified to be α-L-rhamnopyranosyl-(1→6'')-D-mannitol, α-L-rhamnopyranosyl-(1→1'')-β-D-fructopyranose, and 6,7-dihydroxycoumarin α-L-rhamnopyranosyl-(1→6'')-β-D-glucopyranoside by ESI-MS and NMR spectroscopy. The high glycosylation efficiency as well as the broad acceptor specificity of this enzyme makes it a powerful tool for the synthesis of novel rhamnosyl glycosides.     

Kinetic Characterization of Enzymatic Hydrolysis of Complex Protein Substrates for Producing Nutrient Media

Hydrolysis of a protein mixture from muscle and bone tissues with the enzymatic system from porcine pancreatic cell suspension was studied. Kinetic constants and the values of activation energy were determined for individual processes of the release of 15 amino acids. The kinetic characteristics of the overall enzymatic hydrolysis calculated from analysis of the changes in concentrations of terminal amino groups were compared with the characteristics obtained while studying the accumulation patterns of individual amino acids.     

直接加热膨化蔗渣酶法水解的研究

采用加热时间为２０ｍｉｎ,压力为２．０ＭＰａ,温度为１２０℃的直接加热膨化甘蔗渣为水解底物、日本ｙｓｋｕｌｔ生物化学试剂公司生产的ｏｎｏｚｕｋＲＳ型纤维纯洁酶粉进行蔗渣的酶法水解实验,考察了蔗渣中纤维素的酶解还原糖得率与反应时间、酶浓度、ｐＨ值、缓冲液种类、离子强度以及固液比的关系,结果表明：当固液比为５％（ｗ／ｖ）,酶浓度＞１．２０ｍｇ／ｍｌ时,还原糖得率随酶浓度的增加变化不显著;本实验条件下,缓冲液种类和离子强度对还原糖得率几乎没有影响;水解最适宜ｐＨ值为４．２～４．９;最佳反应温度为５０℃。     

Hydrolysis by Indigenous Plasmin: Consequences for Enzymatic Cross-Linking and Acid-Induced Gel Formation of Non-Micellar Casein

Casein is a group of milk proteins with high nutritional value, and the exploitation of its techno-functional potentials has been investigated for decades. In this study, acid casein powder was dissolved in 0.1 mol/L phosphate buffers with different pH, resulting in casein solutions with pH 5.9, 6.6 and 7.3. During preparation and storage (40 °C) of the samples, casein hydrolysis was observed in size exclusion chromatography and gel electrophoresis. The degree of hydrolysis increased with increasing pH, and treatment of casein with commercial plasmin resulted in similar polypeptides, suggesting that the hydrolysis was caused by residual indigenous plasmin present in the acid casein powder. Most polypeptides could be cross-linked by microbial transglutaminase, except for one particular fraction which appeared at constant intensity in the chromatograms. The stiffness of acid-induced gels as determined in small amplitude oscillatory shear rheology decreased with increasing degree of hydrolysis, and was also lower for cross-linked samples when the preceding casein hydrolysis was more pronounced. Enzymatic cross-linking increased the resistance of casein against plasmin-related hydrolysis, presumably because of the resulting lysine modification. However, one particular fraction of polypeptides was released by hydrolysis in spite of cross-linking, suggesting that they did not contain lysine residues that are susceptible for mTGase. The results indicate that plasmin-related hydrolysis should be taken into account for the application of acid casein or sodium caseinate as additive in food design.

     

Enzymatic Hydrolysis of Proteins from Crustaceans of the Barents Sea

Enzymatic preparations from king crab hepatopancreas were shown to be capable, in principle, of producing protein hydrolysates. Hydrolysis of protein-containing waste of deep-water prawn and king crab occurs most successfully at pH 8.0–8.5 and 50–55°C for 5–6 h in the presence of 6 g enzyme per kg substrate. The total chemical composition of the hydrolysates, the molecular weight distributions of proteins and polypeptides, and the contents of free amino acids were studied in dry hydrolysates.