Enhanced exopolysaccharide production and biological activity of Lactobacillus rhamnosus ZY with calcium and hydrogen peroxide

Exopolysaccharides (EPS) are important food and drug additives with beneficial antioxidant, anticancer, and immune-related effects on human health. However, the EPS is limited by low yields and the need for complex culture conditions in fermentation. Here, we report that hydrogen peroxide and calcium stimulated probiotic activity and production of crude exopolysaccharide (c-EPS) by Lactobacillus rhamnosus ZY. Accordingly, supplementation with 3 mM H₂O₂ allowed c-EPS biosynthesis to reach 567 mg/L after 24 h. Addition of both CaCl₂ and H₂O₂ resulted in a c-EPS yield of 2498 mg/L after 12 h, over 9-fold higher than that of an anaerobic culture. We observed that exposure to calcium and hydrogen peroxide made the cells more hydrophobic and led to the over-expression of GroEL, NADH peroxidase, and glyceraldehyde 3-phosphate dehydrogenase, thus increasing energy storage and EPS production. Chromatographic analysis revealed c-EPS was composed mainly of mannose (5.1%), galactose (15.3%), glucose (20–30%), and rhamnose (50–60%). Preliminary in vitro tests revealed that H₂O₂ and CaCl₂ enhanced the 2,2-diphenyl-1-picrylhydrazyl and hydroxyl radical scavenging capacities, resulting in a notable protective effect against oxidative damage in NIH/3T3 cells. Our study provides a simple and cost-effective approach for achieving high yields of good quality EPS using Lactobacillus rhamnosus.     

In vitro metabolic engineering of hydrogen production at theoretical yield from sucrose

Hydrogen is one of the most important industrial chemicals and will be arguably the best fuel in the future. Hydrogen production from less costly renewable sugars can provide affordable hydrogen, decrease reliance on fossil fuels, and achieve nearly zero net greenhouse gas emissions, but current chemical and biological means suffer from low hydrogen yields and/or severe reaction conditions. An in vitro synthetic enzymatic pathway comprised of 15 enzymes was designed to split water powered by sucrose to hydrogen. Hydrogen and carbon dioxide were spontaneously generated from sucrose or glucose and water mediated by enzyme cocktails containing up to15 enzymes under mild reaction conditions (i.e. 37 °C and atm). In a batch reaction, the hydrogen yield was 23.2 mol of dihydrogen per mole of sucrose, i.e., 96.7% of the theoretical yield (i.e., 12 dihydrogen per hexose). In a fed-batch reaction, increasing substrate concentration led to 3.3-fold enhancement in reaction rate to 9.74 mmol of H₂/L/h. These proof-of-concept results suggest that catabolic water splitting powered by sugars catalyzed by enzyme cocktails could be an appealing green hydrogen production approach.     

Two-step acid and alkaline ethanolysis/alkaline peroxide fractionation of sugarcane bagasse and rice straw for production of polylactic acid precursor

Sugarcane bagasse and rice straw were subjected to acid and alkaline ethanolysis and sequential enzymatic hydrolysis to produce glucose for lactic acid production. Influence of physico-chemical treatments using ultrasonic bath and ultrasonic probe was studied compared with mechanical stirring. The results showed that the highest glucose yield with least contamination of xylose was obtained from acid ethanolysis fractionation (5 N H₂SO₄ + 50%, v/v ethanol) when stirred at 90 °C for 4 h. Alkaline ethanolysis accomplished high amount of both glucose and xylose released, however it was not favorable substrate for homofermentative lactic acid bacteria. In order to enhance enzymatic hydrolysis of acid ethanolysis fractionated samples, lignin was subsequently removed by the second step alkaline/peroxide delignification. The maximum lactic acid was obtained at 23.6 ± 0.2 g/L from Lactobacillus casei fermentation after 72 h when hydrolysate from two-step acid hydrolysis and alkaline/peroxide fractionated sugarcane bagasse containing 24.6 g/L initial glucose concentration was used as substrate.     

Biological hydrogen production from CO: Bioreactor performance

This paper presents an alternative solution to the current problem faced by the world; diminishing of fossil fuel. Bioconversion of synthesis gas to hydrogen as clean fuel was catalyzed by a photosynthetic bacterium, Rhodospirillum rubrum. The clean fuel production was biologically mediated by the water–gas shift reaction in a 2 l bioreactor. The work performed was on agitation effects on hydrogen production, K_La and power consumption. The results show that 500 rpm was the suitable agitation rate to be employed. The hydrogen production was optimized at 0.44 ± 0.023 atm giving a K_La of 86.4 ± 3.5 h⁻¹. The production rate was 9.6 mmol H₂/h. The maximum light conversion efficiency at agitation speed of 800 rpm, light intensity of 500 lux (732 kW/m²) and 4 g/l inlet acetate concentration was about 10.84 ± 1.73%. At this condition, the maximum CO conversion efficiency was found to be 81 ± 5.6%. The ratio of power per volume was calculated to be 322.30 ± 12.14 kW/m³ and foaming problem was successfully avoided. The corresponding power consumption was estimated to be about 0.64 ± 0.03 kW, while the output hydrogen energy was determined to be 643.2 ± 26 kW. A prolonged operation of continuous hydrogen production employing a microsparger showed stable behaviour for a duration of 27 days.     

Production of hemicellulosic sugars and glucose from residual corrugated cardboard

Corrugated cardboard samples were subjected to two-step saccharification. A first prehydrolysis stage was carried out to solubilise the hemicellulosic fraction as hemicellulosic sugars, and the solid phase from prehydrolysis was used as a substrate for the enzymic hydrolysis of cellulose. The prehydrolysis step was carried out for 0–180 min in media containing 1–3 wt.% of H₂SO₄ and the fraction of solid recovered after treatments and the compositions of solid and liquid phases from treatments were measured. The susceptibility of prehydrolysed solids towards the enzymic hydrolysis was assessed in further experiments. Under selected prehydrolysis conditions (3% H₂SO₄, 180 min), 78.2% of initial hemicelluloses was saccharified, leading to liquors containing up to 10 g hemicellulosic sugars/l and 9.2 g glucose/l. The corresponding solid phase, enriched in cellulose, showed good susceptibility towards enzymatic hydrolysis, leading to solutions containing up to 17.9 g glucose/l (conversion yield=63.6%) and a glucose/total sugar ratio of 0.93 g/g. Mathematical models assessing the effects of the operational conditions on both the prehydrolysis stage and the susceptibility of substrates towards enzymic hydrolysis have been developed.     

Enzymatic hydrolysis of corncob and ethanol production from cellulosic hydrolysate

 Enzymatic hydrolysis of corncob and ethanol fermentation from cellulosic hydrolysate were investigated. After corncob was pretreated by 1% H₂SO₄ at 108 °C for 3 h, the cellulosic residue was hydrolyzed by cellulase from Trichoderma reesei ZU-02 and the hydrolysis yield was 67.5%. Poor cellobiase activity in T. reesei cellulase restricted the conversion of cellobiose to glucose, and the accumulation of cellobiose caused severe feedback inhibition to the activities of β-1,4-endoglucanase and β-1,4-exoglucanase in cellulase system. Supplementing cellobiase from Aspergillus niger ZU-07 greatly reduced the inhibitory effect caused by cellobiose, and the hydrolysis yield was improved to 83.9% with enhanced cellobiase activity of 6.5 CBU g⁻¹ substrate. Fed-batch hydrolysis process was started with a batch hydrolysis containing 100 g l⁻¹ substrate, with cellulosic residue added at 6 and 12 h twice to get a final substrate concentration of 200 g l⁻¹. After 60 h of reaction, the reducing sugar concentration reached 116.3 g l⁻¹ with a hydrolysis yield of 79.5%. Further fermentation of cellulosic hydrolysate containing 95.3 g l⁻¹ glucose was performed using Saccharomyces cerevisiae 316, and 45.7 g l⁻¹ ethanol was obtained within 18 h. The research results are meaningful in fuel ethanol production from agricultural residue instead of grain starch.     

Polyvinyl alcohol–silica nanohybrids: An efficient carrier matrix for amylase immobilization

Polyvinyl alcohol (PVA)–silica nanohybrids have been synthesized in a modified Stöber process. The bioactivities of the enzyme loaded hybrids were monitored and the optimum activity sample (H) was calcined at 300 °C in N₂ to obtain hybrid gel (H₃) with improved performance. The synthesized hybrids have been characterized by Fourier Transform Infra Red spectroscopy, X-ray diffraction, scanning electron microscopy, thermogravimetric analysis and BET surface area analysis. Under the optimized conditions, the bioactivity of the enzyme impregnated H₃ (H₃-Enz) was 21.823 U/mg. On recycling, H₃-Enz retained 88% of its initial bioactivity in the sixth cycle. The kinetic parameters of soluble starch hydrolysis for the immobilized (K_M = 4.137 mg mL^?1; V_max = 5.95 mg mL^?1 min^?1) and free enzyme (K_M = 10.667 mg mL^?1; V_max = 6.0557 mg mL^?1 min^?1) indicated that the immobilization has nearly doubled the enzyme's affinity for the substrate, while the maximum rate of the enzymatic reaction at the saturation point was not much affected. The immobilized enzyme showed greater shelf life in comparison to the free enzyme.     

Termination of a toxic Alexandrium bloom with hydrogen peroxide

The dinoflagellate Alexandrium ostenfeldii is a well-known harmful algal species that can potentially cause paralytic shellfish poisoning (PSP). Usually A. ostenfeldii occurs in low background concentrations only, but in August of 2012 an exceptionally dense bloom of more than 1 million cells L⁻¹ occurred in the brackish Ouwerkerkse Kreek in The Netherlands. The A. ostenfeldii bloom produced both saxitoxins and spirolides, and is held responsible for the death of a dog with a high saxitoxin stomach content. The Ouwerkerkse Kreek routinely discharges its water into the adjacent Oosterschelde estuary, and an immediate reduction of the bloom was required to avoid contamination of extensive shellfish grounds. Previously, treatment of infected waters with hydrogen peroxide (H₂O₂) successfully suppressed cyanobacterial blooms in lakes. Therefore, we adapted this treatment to eradicate the Alexandrium bloom using a three-step approach. First, we investigated the required H₂O₂ dosage in laboratory experiments with A. ostenfeldii. Second, we tested the method in a small, isolated canal adjacent to the Ouwerkerkse Kreek. Finally, we brought 50 mg L⁻¹ of H₂O₂ into the entire creek system with a special device, called a water harrow, for optimal dispersal of the added H₂O₂. Concentrations of both vegetative cells and pellicle cysts declined by 99.8% within 48 h, and PSP toxin concentrations in the water were reduced below local regulatory levels of 15 μg L⁻¹. Zooplankton were strongly affected by the H₂O₂ treatment, but impacts on macroinvertebrates and fish were minimal. A key advantage of this method is that the added H₂O₂ decays to water and oxygen within a few days, which enables rapid recovery of the system after the treatment. This is the first successful field application of H₂O₂ to suppress a marine harmful algal bloom, although Alexandrium spp. reoccurred at lower concentrations in the following year. The results show that H₂O₂ treatment provides an effective emergency management option to mitigate toxic Alexandrium blooms, especially when immediate action is required.     

Prompt repair of hydrogen peroxide-induced DNA lesions prevents catastrophic chromosomal fragmentation

Iron-dependent oxidative DNA damage in vivo by hydrogen peroxide (H₂O₂, HP) induces copious single-strand(ss)-breaks and base modifications. HP also causes infrequent double-strand DNA breaks, whose relationship to the cell killing is unclear. Since hydrogen peroxide only fragments chromosomes in growing cells, these double-strand breaks were thought to represent replication forks collapsed at direct or excision ss-breaks and to be fully reparable. We have recently reported that hydrogen peroxide kills Escherichia coli by inducing catastrophic chromosome fragmentation, while cyanide (CN) potentiates both the killing and fragmentation. Remarkably, the extreme density of CN + HP-induced chromosomal double-strand breaks makes involvement of replication forks unlikely. Here we show that this massive fragmentation is further amplified by inactivation of ss-break repair or base-excision repair, suggesting that unrepaired primary DNA lesions are directly converted into double-strand breaks. Indeed, blocking DNA replication lowers CN + HP-induced fragmentation only ∼2-fold, without affecting the survival. Once cyanide is removed, recombinational repair in E. coli can mend several double-strand breaks, but cannot mend ∼100 breaks spread over the entire chromosome. Therefore, double-strand breaks induced by oxidative damage happen at the sites of unrepaired primary one-strand DNA lesions, are independent of replication and are highly lethal, supporting the model of clustered ss-breaks at the sites of stable DNA-iron complexes.     

Effects of intraspecific competition on growth and photosynthesis of Atriplex prostrata

We investigated the effect of intraspecific competition on growth parameters and photosynthesis of the salt marsh species Atriplex prostrata Boucher in order to distinguish the effects of density-dependent growth inhibition from salt stress. High plant density caused a reduction of 30% in height, 82% in stem dry mass, 80% in leaf dry mass, and 95% in root dry mass. High density also induced a pronounced 72% reduction in leaf area, 29% decrease in length of mature internodes and 50% decline in net photosynthetic rate. The alteration of net photosynthesis paralleled growth inhibition, decreasing from 7.6 ± 0.9 μmol CO₂ m⁻² s⁻¹ at low density to 3.5 ± 0.4 μmol CO₂ m⁻² s⁻¹ at high density, indicating growth inhibition caused by intraspecific competition is mainly due to a decline in net photosynthesis rate. Plants grown at high density also exhibited a reduction in stomatal conductance from 0.7 ± 0.1 mol H₂O m⁻² s⁻¹ at low density to 0.3 ± 0.1 mol H₂O m⁻² s⁻¹ at high density and a reduction in transpiration rate from 6.0 ± 0.3 mmol H₂O m⁻² s⁻¹ at low density to 4.3 ± 0.3 mmol H₂O m⁻² s⁻¹ at high density. Biomass production was inhibited by an increase in plant density, which reduced the rate of photosynthesis, stomatal conductance and leaf area of plants.     

The first crenarchaeon capable of growth by anaerobic carbon monoxide oxidation coupled with H2 production

The ability to grow by anaerobic CO oxidation with production of H₂ from water is known for some thermophilic bacteria, most of which belong to Firmicutes, as well as for a few hyperthermophilic Euryarchaeota isolated from deep-sea hydrothermal habitats. A hyperthermophilic, neutrophilic, anaerobic filamentous archaeon strain 1505 = VKM B-3180 = KCTC 15798 was isolated from a terrestrial hot spring in Kamchatka (Russia) in the presence of 30% CO in the gas phase. Strain 1505 could grow lithotrophically using carbon monoxide as the energy source with the production of hydrogen according to the equation CO + H₂O → CO₂ + H₂; mixotrophically on CO plus glucose; and organotrophically on peptone, yeast extract, glucose, sucrose, or Avicel. The genome of strain 1505 was sequenced and assembled into a single chromosome. Based on 16S rRNA gene sequence analysis and in silico genome-genome hybridization, this organism was shown to be closely related to the Thermofilum adornatum species. In the genome of Thermofilum sp. strain 1505, a gene cluster (TCARB_0867-TCARB_0879) was found that included genes of anaerobic (Ni,Fe-containing) carbon monoxide dehydrogenase and genes of energy-converting hydrogenase ([Ni,Fe]-CODH–ECH gene cluster). Compared to the [Ni,Fe]-CODH–ECH gene clusters occurring in the sequenced genomes of other H₂-producing carboxydotrophs, the [Ni,Fe]-CODH–ECH gene cluster of Thermofilum sp. strain 1505 presented a novel type of gene organization. The results of the study provided the first evidence of anaerobic CO oxidation coupled with H₂ production performed by a crenarchaeon, as well as the first documented case of lithotrophic growth of a Thermofilaceae representative.     

Identification of novel quinazolin-4(3H)-ones as inhibitors of thermolysin,the prototype of the M4 family of proteinases

A combinatorial series of novel quinazolin-4(3H)-ones were synthesised and their structures were established based on spectroscopic data (IR, NMR, EI-MS, and FAB-MS). The compounds were tested for inhibition of the zinc metalloproteinase thermolysin (TLN) utilizing a chemical array-based approach. Some of the compounds were found to inhibit TLN, with IC₅₀ values ranging from 0.0115 μM (compound 3) to 122,637 μM (compound 29). Compound 3 [3-phenyl-2-(trifluoromethyl) quinazolin-4(3H)-one] (IC₅₀ = 0.0115 μM) and compound 35 [3-(isopropylideneamino)-2,2-dimethyl-2,3-dihydroquinazolin-4 (1H)-one] (IC₅₀ = 0.2477 μM) were found to be the most potent inhibitors.     

Optimization of short-term storage of pikeperch semen: an applicable approach

Contamination of semen with urine and asynchronous maturation of males and females are main obstacles in artificial reproduction of pikeperch Sander lucioperca. The objective of this study was to overcome these obstacles using optimization of a procedure for short-term storage of pikeperch semen at 4 °C using two immobilizing media (IM): (a) IM1, 180 mM NaCl, 2.68 mM KCl, 1.36 mM CaCl₂ ⋅ 2H₂O and 2.38 mM NaHCO₃, 343 mOsm/kg; and (b) IM2, 200 mM NaCl, 2.68 mM KCl, 1.36 mM CaCl₂ ⋅ 2H₂O and 2.38 mM NaHCO₃, 381 mOsm/kg. Undiluted sperm was used as the control. At 6 h poststorage, there were no substantial changes in spermatozoa motility and velocity at 30 s postactivation in all groups. Over 48 h of storage, the highest spermatozoa motility and velocity were obtained in sperm diluted in IM2 compared to the other groups. IM2 could maintain a significantly higher ATP content of diluted sperm than IM1 and undiluted treatment for 2 days. Similarly, the highest values of eyeing and hatching rates were observed in sperm diluted in IM2 compared to sperm in the other studied groups. It can be concluded that the obtained result is a novel and applicable approach to maintain semen quality of pikeperch during short-term storage, suggesting IM2 as a promising medium for short-term storage. The present study also opens possibilities for ensuring a reliable source of semen as a convenient approach for increasing genetic diversity in hatcheries.     

Identification of 2,3-dihydro-1H-pyrrolo[3,4-c]pyridine-derived ureas as potent inhibitors of human nicotinamide phosphoribosyltransferase (NAMPT)

Potent nicotinamide phosphoribosyltransferase (NAMPT) inhibitors containing 2,3-dihydro-1H-pyrrolo[3,4-c]pyridine-derived ureas were identified using structure-based design techniques. The new compounds displayed improved aqueous solubilities, determined using a high-throughput solubility assessment, relative to previously disclosed urea and amide-containing NAMPT inhibitors. An optimized 2,3-dihydro-1H-pyrrolo[3,4-c]pyridine-derived compound exhibited potent anti-NAMPT activity (18; BC NAMPT IC₅₀ = 11 nM; PC-3 antiproliferative IC₅₀ = 36 nM), satisfactory mouse PK properties, and was efficacious in a PC-3 mouse xenograft model. The crystal structure of another optimized compound (29; NAMPT IC₅₀ = 10 nM; A2780 antiproliferative IC₅₀ = 7 nM) in complex with the NAMPT protein was also determined.     

Synthesis,crystal structure and fluorescent characterization of a novel lanthanide tetraphosphonate with a layered structure

Hydrothermal reactions of Gd(III) nitrate with N,N,N′,N′-tetramethylenephosphono-1,4-diaminobutane, (H₂O₃PCH₂)₂N–(CH₂)₄–N(CH₂PO₃H₂)₂ (H₈L), afforded a novel Gd(III) phosphonate, namely, Gd[(O₃PCH₂)(HO₃PCH₂)N(H)(CH₂)₄N(H)(CH₂PO₃H)₂] · 2H₂O, [Gd(H₅L)] · 2H₂O. Its structure was established by a single-crystal X-ray diffraction study. In this compound, the Gd(III) ion is coordinated by eight phoshonate oxygen atoms from five different phosphonate groups, which belong to five different phosphonic ligands. Each Gd atom is connected with its neighboring Gd atoms by two phosphonate oxygens, forming a gadolinium phosphonate slab along the a-axis. Such slabs are bridged by tetraphosphonate H₅L anions, resulting in a 〈0 1 1〉 layer with the butane groups toward the interlayer space. These layers are further interlinked by strong hydrogen bonds formed by uncoordinated phosphonate oxygens into a 3D supermolecular structure. Luminescent studies indicate that this compound exhibits a broad blue fluorescent emission band at 441 nm.     

Alkaline lipase from a novel strain Burkholderia multivorans: Statistical medium optimization and production in a bioreactor

An alkaline lipase from Burkholderia multivorans was produced within 15 h of growth in a 14 L bioreactor. An overall 12-fold enhanced production (58 U mL⁻¹ and 36 U mg⁻¹ protein) was achieved after medium optimization following the “one-variable-at-a-time” and the statistical approaches. The optimal composition of the lipase production medium was determined to be (% w/v or v/v): KH₂PO₄ 0.1; K₂HPO₄ 0.3; NH₄Cl 0.5; MgSO₄·7H₂O 0.01; yeast extract 0.36; glucose 0.1; olive oil 3.0; CaCl₂ 0.4 mM; pH 7.0; inoculum density 3% (v/v) and incubation time 36 h in shake flasks. Lipase production was maximally influenced by olive oil/oleic acid as the inducer and yeast extract as the additive nitrogen. Plackett–Burman screening suggested catabolite repression by glucose. Amongst the divalent cations, Ca²⁺ was a positive signal while Mg²⁺ was a negative signal for lipase production. RSM predicted that incubation time, inoculum density and oil were required at their higher levels (36 h, 3% (v/v) and 3% (v/v), respectively) while glucose and yeast extract were required at their minimal levels for maximum lipase production in shake flasks. The production conditions were validated in a 14 L bioreactor where the incubation time was reduced to 15 h.     

Application of polyethylene glycol immobilized Clostridium sp. LS2 for continuous hydrogen production from palm oil mill effluent in upflow anaerobic sludge blanket reactor

A novel polyethylene glycol (PEG) gel was fabricated and used as a carrier to immobilize Clostridium sp. LS2 for continuous hydrogen production in an upflow anaerobic sludge blanket (UASB) reactor. Palm oil mill effluent (POME) was used as the substrate carbon source. The optimal amount of PEG-immobilized cells for anaerobic hydrogen production was 12% (w/v) in the UASB reactor. The UASB reactor containing immobilized cells was operated at varying hydraulic retention times (HRT) that ranged from 24 to 6 h at 3.3 g chemical oxygen demand (COD)/L/h organic loading rate (OLR), or at OLRs that ranged from 1.6 to 6.6 at 12 h HRT. The best volumetric hydrogen production rate of 336 mL H₂/L/h (or 15.0 mmol/L/h) with a hydrogen yield of 0.35 L H₂/g COD_removed was obtained at a HRT of 12 h and an OLR of 5.0 g COD/L/h. The average hydrogen content of biogas and COD reduction were 52% and 62%, respectively. The major soluble metabolites during hydrogen fermentation were butyric acid followed by acetic acid. It is concluded that the PEG-immobilized cell system developed in this work has great potential for continuous hydrogen production from real wastewater (POME) using the UASB reactor.     

Activation of nylon net and its application to a biosensor for determination of glucose in human serum

A glucose biosensor using a glucose oxidase (GO_x)-immobilized nylon net with glutaraldehyde as cross-linking reagent and an oxygen (O₂) electrode for the determination of glucose has been fabricated. The detection scheme was based on the utilization of dissolved O₂ in oxidation of glucose by the membrane bound GO_x. Crucial factors including O-alkylation temperature, reaction times of nylon net with dimethyl sulfate, l-lysine, and glutaraldehyde, and enzyme loading were examined to determine the optimal enzyme immobilization conditions for the best sensitivity of the developed glucose biosensor. In addition, the effects of pH and concentration of phosphate buffer on the response of the biosensor were studied. The glucose biosensor had a linear range of 18 μM to 1.10 mM with the detection limit of 9.0 μM (S/N = 3) and response time of 80 s. The biosensor exhibited both good operational stability with over 200 measurements and long-term storage stability. The results from this biosensor compared well with those of a commercial glucose assay kit in analyzing human serum glucose samples.     

Superoxide dismutase (SOD) in boar spermatozoa: Purification,biochemical properties and changes in activity during semen storage (16 °C) in different extenders

The antioxidant system in semen is composed of enzymes, low-molecular weight antioxidants and seminal plasma proteins. Loss of enzymatic activity of superoxide dismutase (SOD) during semen preservation may cause insufficient antioxidant defense of boar spermatozoa. The aim of this study was to isolate and characterize SOD molecular forms from spermatozoa and to describe changes in SOD activity in boar sperm during preservation at 16 °C. Sperm extracts were prepared from fresh or diluted semen and used for SOD purification or activity measurement. Ion-exchange chromatography and gel filtration was used to purify SOD molecular forms. BTS, Dilu Cell, M III and Vitasem were used as diluents for 5-day storage of semen at +16 °C. The molecular form of SOD released from spermatozoa after cold shock and homogenization had a molecular weight of approximately 67 kDa. The activity of the SOD form was the highest at pH 10 within the temperature range between 20 and 45 °C. The enzymatic activity of form released after cold shock was inhibited by H₂O₂ and diethyldithiocarbamate (DDC; by 65 and 40%, respectively). The SOD form released by homogenization was inhibited by H₂O₂ and DDC (40%). The molecular form released after urea treatment was a 30 kDa protein with maximum activity at 20 °C and pH 10. Enzymatic activity of this form was inhibited by H₂O₂ by 35%, DDC by 80% and 2-mercaptoethanol by 15%. The antigenic determinants of SOD isolated from boar seminal plasma and spermatozoa were similar to each other. Susceptibility of spermatozoa to cold shock increased during storage, but the differences between extenders were statistically non-significant.     

Response surface analysis for enzymatic decolorization of Congo red by manganese peroxidase

The enzymatic decolorization process of manganese peroxidase (MnP) is a complex system, which is greatly affected by the concentrations of H₂O₂, Mn²⁺, dye and enzyme. This work aimed to study these factors and investigate the combined interactions between them by applying response surface methodology (RSM) for decolorization of Congo red with MnP from Schizophyllum sp. F17, meanwhile conventional one-factor-at-a-time analysis was carried out. Through the one-factor-at-a-time analysis the optimized H₂O₂, Mn²⁺, Congo red and MnP extract was 0.2 mM, 0.5 mM, 50 mg/l and 0.8 ml, respectively, and the maximum decolorization attained under such conditions was 24.2%. Response surface analysis was conducted through Box–Behnken design and a second-order polynomial model (R² = 0.8565) was generated to describe the combined effect and the interactions quantificationally. ANOVA analysis indicated that the interactions between H₂O₂ and MnP, between dye and MnP were significant; the optimum condition through RSM was found to be 0.35 mM H₂O₂, 0.5 mM Mn²⁺, 75 mg/l Congo red and 1.4 ml MnP extract, for maximum decolorization of 30.8%.