Induced accumulation of oleanolic acid and ursolic acid in cell suspension cultures of <Emphasis Type="Italic">Uncaria tomentosa</Emphasis>

Increasing sucrose from 20 to 50 g l⁻¹ in Uncaria tomentosa cell suspension cultures enhanced ursolic acid and oleanolic acid production from 129 ± 61 to 553 ± 193 μg g⁻¹ cell dry wt. The maximal concentration of both triterpenes (1680 ± 39 μg g⁻¹ cell dry wt) was 8 days after elicitation by jasmonic acid, while yeast extract or citrus pectin treatments produced 1189 ± 20 or 1120 ± 26 μg g⁻¹ cell dry wt, respectively. The ratio of ursolic acid:oleanolic acid was constant at 70:30.     

Enhancing biological nitrogen removal from tannery effluent by using the efficient Brachymonas denitrificans in pilot plant operations

Summary Laboratory scale and pilot plant reactors were inoculated with an efficient denitrifier, Brachymonas denitrificans(CCUG 45880), in order to evaluate whether a bio-augmentation approach can be used to enhance biological nitrogen removal from tannery effluents. To determine the effectiveness of the introduced strain, denitrifying activity in the activated sludge was monitored by nitrate uptake rate (NUR) measurement of NO₃-N. Fluorescent in situ hybridization (FISH) technique was used to monitor the growth of the augmented species. The laboratory scale nitrate removal efficiency with the introduced B. denitrificans (3.7±0.6 mg NO₃-N gVSS ⁻¹ h ⁻¹) was higher than that of the activated sludge without the addition of the bacteria (3.5±0.7 mg NO₃-N gVSS ⁻¹ h ⁻¹); the NUR in the pilot plant after and before the introduction of the strain was also of the magnitude of 12.0±1.4 and 10.6±1.4 mg NO₃-N gVSS ⁻¹ day ⁻¹ , respectively. In situ hybridization results revealed that the introduced denitrifying bacteria significantly facilitated the development of a dense denitrifying bacterial population in the activated sludge, which enhanced in situ denitrification activity. FISH data indicated that once introduced, B. denitrificans remained abundant throughout the experimental period. The ability to seed a bioreactor with bacterial strain capable of removing target pollutants from tannery effluents in a mixed microbial community suggests that this approach could have commercial applications.     

The nonenzymic hydrolysis of Δ-thiazoline-2-carboxylate: The product of the suspected physiological reaction catalyzed by -amino acid oxidase

Δ²-Thiazoline-2-carboxylate, the product of the suspected physiological reaction catalyzed by -amino acid oxidase, is stable to hydrolysis at 37°C and pH 7 or above, but it hydrolyzes readily at pH 5 or below to give a mixture of N- and S-oxalylcysteamines; the N-oxalyl derivative predominates at pH's above 1 while the S-oxyalyl compound is the major product at high acidities. The pH-rate profile looks like the superposition of two bell-shaped curves. The initial increase in the rate as the pH is lowered is controlled by a pK_a of 3.95 and from pH 1 to 3 the rate is relatively constant (k = 6.7 × 10⁻⁴s⁻¹ at 37°C and ionic strength 0.5 ). Below pH 1 the rate increases again to a maximum in 1 HCl and then decreases in more highly acidic solutions. The rate of conversion of S-oxalylcysteamine to N-oxalylcysteamine is inversely proportional to the hydrogen ion concentration from pH 3 to 5 but becomes largely independent of pH from pH 1 to 2. In the pH-independent region the rate is comparable with that observed by others for S-acetylcysteamine but in the pH-dependent region the rate is 20 to 25 times faster for the oxalyl derivative than for the acetyl compound. At pH 1, N-oxalylcysteamine is partially converted to the S-oxalyl derivative but the rate of hydrolysis (k = 1.0 × 10⁻⁵s⁻¹ at 37°C) to cysteamine and oxalate of this partially equilibrated system occurs at a comparable rate. The results of this investigation are rationalized in terms of what is known about other thiazoline hydrolyses and intramolecular S to N acyl migrations. The main differences in the present case are presumably due to the fact that thiazoline-2-carboxylate can undergo hydrolysis by two reaction manifolds, one with the carboxyl unprotonated and the other with it protonated. The relevance of these results to possible reactions of thiazoline-2-carboxylate in vivo is briefly considered.     

Optimization of ω-3 fatty acid production by microalgae: crossover effects of CO2 and light intensity under batch and continuous cultivation modes

The microalga Pavlova lutheri is a potential source of economically valuable docosahexaenoic and eicosapentaenoic acids. Specific chemical and physical culture conditions may enhance their biochemical synthesis. There are studies relating the effect of CO₂ on growth; however, this parameter should not be assessed independently, as its effect strongly depends on the light intensity available. In this research, the combined effects of light intensity and CO₂ content on growth and fatty acid profile in P. lutheri were ascertained, in order to optimize polyunsaturated fatty acid production. The influence of the operation mode was also tested via growing the cultures by batch and by continuous cultivation. Higher light intensities associated with lower dilution rates promoted increases in both cell population and weight per cell. Increased levels of CO₂ favored the total lipid content, but decreased the amounts of polyunsaturated fatty acids. Mass productivities of eicosapentaenoic acid (3.61 ± 0.04 mg · L⁻¹ · d⁻¹) and docosahexaenoic acid (1.29 ± 0.01 mg · L⁻¹ · d⁻¹) were obtained in cultures supplied with 0.5% (v/v) CO₂, at a dilution rate of 0.297 d⁻¹ and a light intensity of 120 μE · m⁻² · s⁻¹.     

Mechanism of Extracellular Thiol Nitrosylation by N2O3 Produced by Activated Macrophages

Reactive nitrogen intermediates are synthesized by activated macrophages. These molecules, and nitrous anhydride (N₂O₃) in particular, are known to be potent nitrosylating species. We investigated the role of macrophage-derived N₂O₃ in extracellular nitrosylation. We used dilution experiments to demonstrate the intracellular production of N₂O₃ and its export into the extracellular medium, with a rate constant k_ex = 6.8 × 10⁶ M s⁻¹. The kinetics of the competition between extracellular hydrolysis of N₂O₃ and its reaction with added glutathione were also studied. We obtained a value of the rate constant k_GSH for the latter reaction of 4.4 × 10⁷ M⁻¹ s⁻¹, consistent with earlier determinations in cell-free systems. The implications of these results in human albumin nitrosylation were investigated. Nitrosylated albumin was detected in activated macrophages supernatants using an anti-NO-acetylated cysteine antibody. It was estimated that 10% of N₂O₃ produced by activated cells participate in extracellular nitrosylation. N₂O₃ thus appears to be a new effector molecule of the immune system, as an agent for the nitrosylation of albumin, the main nitric oxide carrier in vivo.     

Cells of <Emphasis Type="BoldItalic">Candida utilis</Emphasis> for <Emphasis Type="BoldItalic">in vitro</Emphasis> (<Emphasis Type="BoldItalic">R</Emphasis>)-phenylacetylcarbinol production in an aqueous/octanol two-phase reactor

(R)-Phenylacetylcarbinol (PAC), a pharmaceutical precursor, was produced from benzaldehyde and pyruvate by pyruvate decarboxylase (PDC) of Candida utilis in an aqueous/organic two-phase emulsion reactor. When the partially purified enzyme in this previously established in vitro process was replaced with C. utilis cells and the temperature was increased from 4 to 21 °C, a screen of several 1-alcohols (C4–C9) confirmed the suitability of 1-octanol as the organic phase. Benzyl alcohol, the major by-product in the commercial in vivo conversion of benzaldehyde and sugar to PAC by Saccharomyces cerevisiae, was not formed. With a phase volume ratio of 1:1 and 5.6 g C. utilis l⁻¹ (PDC activity 2.5 U ml⁻¹), PAC levels of 103 g l⁻¹ in the octanol phase and 12.8 g l⁻¹ in the aqueous phase were produced in 15 h at 21 °C. In comparison to our previously published process with partially purified PDC in an aqueous/octanol emulsion at 4 °C, PAC was produced at a 4-times increased specific rate (1.54 versus 0.39 mg U⁻¹ h⁻¹) with simplified catalyst production and reduced cooling cost. Compared to traditional in vivo whole cell PAC production, the yield on benzaldehyde was 26% higher, the product concentration increased 3.9-fold (or 6.9-fold based on the organic phase), the productivity improved 3.1-fold (3.9 g l⁻¹ h⁻¹) and the catalyst was 6.9-fold more efficient (PAC/dry cell mass 10.3 g g⁻¹).*Dedicated with gratitude to Prof. Dr. Franz Lingens – “Theo”.     

Significant enhancement of oleanolic acid accumulation by biotic elicitors in cell suspension cultures of Calendula officinalis L.

The effects of elicitors on cell growth and oleanolic acid (OA) accumulation in shaken cell suspension cultures of Calendula officinalis were investigated. Elicitors were added individually at various concentrations to 5-day-old cell cultures and their effects monitored at 24 h intervals for 4 days. Different effects on OA accumulation were observed depending on the day of treatment. Jasmonic acid was the most efficient elicitor. After 72 h of treatment with 100 μM JA, the intracellular content of OA reached its maximum value (0.84 mg g⁻¹ DW), which was 9.4-fold greater than that recorded in an untreated control cultures. The addition of chitosan at 50 mg l⁻¹ produced a 5-fold enhancement of OA accumulation (0.37 mg g⁻¹ DW) after 48 h of treatment. Treatment with yeast extract at 200 mg l⁻¹ for 96 h or with pectin at 2 mg l⁻¹ for 48 h produced identical cellular levels of OA (0.22 mg g⁻¹ DW). Lastly, 48 h elicitation with homogenate of the fungus Trichoderma viride produced a 1.8-fold increase in oleanolic acid content (0.12 mg g⁻¹ DW). In addition to significantly stimulating OA accumulation and its secretion into the culture medium, the elicitors also caused slight inhibition of cell growth.     

Purification and properties of a novel raw starch degrading-cyclodextrin glycosyltransferase from Klebsiella pneumoniae AS- 22

A novel raw starch degrading α-cyclodextrin glycosyltransferase (CGTase; E.C. 2.4.1.19), produced by Klebsiella pneumoniae AS-22, was purified to homogeneity by ultrafiltration, affinity and gel filtration chromatography. The specific cyclization activity of the pure enzyme preparation was 523 U/mg of protein. No hydrolysis activity was detected when soluble starch was used as the substrate. The molecular weight of the pure protein was estimated to be 75 kDa with SDS-PAGE and gel filtration. The isoelectric point of the pure enzyme was 7.3. The enzyme was most active in the pH range 5.5–9.0 whereas it was most stable in the pH range 6–9. The CGTase was most active in the temperature range 35–50°C. This CGTase is inherently temperature labile and rapidly loses activity above 30°C. However, presence of soluble starch and calcium chloride improved the temperature stability of the enzyme up to 40°C. In presence of 30% (v/v) glycerol, this enzyme was almost 100% stable at 30°C for a month. The K_m and k_cat values for the pure enzyme were 1.35 mg ml⁻¹ and 249 μM mg⁻¹ min⁻¹, respectively, with soluble starch as the substrate. The enzyme predominantly produced α-cyclodextrin without addition of any complexing agents. The conditions employed for maximum α-cyclodextrin production were 100 g l⁻¹ gelatinized soluble starch or 125 g l⁻¹ raw wheat starch at an enzyme concentration of 10 U g⁻¹ of starch. The α:β:γ-cyclodextrins were produced in the ratios of 81:12:7 and 89:9:2 from gelatinized soluble starch and raw wheat starch, respectively.     

Biochemical characterization of arabidopsis developmentally regulated G-proteins (DRGs)

Developmentally regulated G-proteins (DRGs) are a highly conserved family of GTP-binding proteins found in archaea, plants, fungi and animals, indicating important roles in fundamental pathways. Their function is poorly understood, but they have been implicated in cell division, proliferation, and growth, as well as several medical conditions. Individual subfamilies within the G-protein superfamily possess unique nucleotide binding and hydrolysis rates that are intrinsic to their cellular function, and so characterization of these rates for a particular G-protein may provide insight into its cellular activity. We have produced recombinant active DRG protein using a bacterial expression system and refolding, and performed biochemical characterization of their GTP binding and hydrolysis. We show that recombinant Arabidopsis thaliana atDRG1 and atDRG2a are able to bind GDP and GTP. We also show that DRGs can hydrolyze GTP in vitro without the assistance of GTPase-activating proteins and guanine exchange factors. The atDRG proteins hydrolyze GTP at a relatively slow rate (0.94 × 10⁻³ min⁻¹ for DRG1 and 1.36 × 10⁻³ min⁻¹ for DRG2) that is consistent with their nearest characterized relatives, the Obg subfamily. The ability of DRGs to bind nucleotide substrates without assistance, their slow rate of GTP hydrolysis, heat stress activation and domain conservation suggest a possible role as a chaperone in ribosome assembly in response to stress as it has been suggested for the Obg proteins, a different but related G-protein subfamily.     

Production and recovery of recombinant protease inhibitor α1-antitrypsin

Human α₁-antitrypsin (AAT) was produced in the recombinant yeast Saccharomyces cerevisiae ATCC 20699 grown in batch and fed-batch culture. The final biomass concentration and antitrypsin concentration attained were 55 g·L⁻¹ and 1.23 g·L⁻¹, respectively, in the fed-batch. The maximum productivities of biomass and antitrypsin were 1.6 and > 0.04 g L⁻¹h⁻¹, respectively, or substantially greater than the highest productivity values reported in the past. For recovering the antitrypsin, the cell slurry was concentrated 4-fold (231 g·L⁻¹ biomass, 122 min of processing) by cross-flow microfiltration and the cells were disrupted by bead milling (3 passes of 3 min total retention time). The cell homogenate was treated with aluminum chloride or PBS (pH 7) to aid separation of the cell debris by flocculation and sedimentation. The clarified cell homogenate was subjected to ammonium sulfate fractionation to precipitate the recombinant antitrypsin. The AAT precipitated at 45–75% saturation of ammonium sulfate, depending on the age of the homogenate. The crude AAT in the homogenate degraded at room temperature (25°C), with a zero order deactivation rate of 1.815 × 10⁻³ ± 3.43 × 10⁻⁴ g AAT L⁻¹h⁻¹.     

d-Amino acid production by E. coli co-expressed three genes encoding hydantoin racemase, d-hydantoinase and N-carbamoyl-d-amino acid amidohydrolase

Three genes respectively encoding d-specific hydantoinase (DHHase), N-carbamoyl-d-amino acid amidohydrolase (DCHase) and hydantoin racemase (HRase) were co-expressed in E. coli in a system designed for the efficient enzymatic production of d-amino acids via a combination of hydantoin hydrolysis and hydantoin racemization. With the use of whole cells, the d-forms of eight amino acids – d-phenylalanine, d-tyrosine, d-tryptophan, O-benzyl-d-serine, d-valine, d-norvaline, d-leucine and d-norleucine – were efficiently converted from the corresponding dl-5-monosubtituted hydantoin compounds.     

Purification and properties of a wheat leaf N-acetyl-β-d-hexosaminidase

An N-acetyl-β-d-hexosaminidase has been purified from primary wheat leaves (Triticum aestivum L.) by freeze-thawing, (NH₄)₂SO₄ precipitation, methanol precipitation, gel filtration, cation exchange chromatography and affinity chromatography on concanavalin A-Sepharose. The activity of the purified preparations could be stabilised by addition of Triton X-100 and the enzyme was stored at -20°C without significant loss of activity. The enzyme hydrolysed pNP-β-d-GlcNAc (optimum pH 5.2, K_m 0.29 mM, V_max 2.56 μkat mg⁻¹) and pNP-β-d-GalNAc (optimum pH 4.4, K_m 0.27 mM, V_max 2.50 μkat mg⁻¹). Five major isozymes were identified, with isoelectric points in the range 5.13–5.36. All five isozymes possessed both N-acety-β-d-glucosaminidase and N-acetyl-β-d-galactosaminidase activity. Inhibition studies and mixed substrate analysis suggested that both substrates are catalysed by the same active site. Both activities were inhibited by GlcNAc, 2-acetamido-2-deoxygluconolactone, GalNAc and the ions of mercury, silver and copper. The K_is for inhibition of N-acetyl-β-d-glucosaminidase activity were: GlcNAc (15.3 mM) and GalNAc (3.4mM). For inhibition of N-acety-β-d-galactosaminidase activity the corresponding values were: GlcNAc (18.2 mM) and GalNac (2.5 mM). The enzyme was considerably less active at releasing pNP from pNP-β-d-(GlcNAc)₂ and pNP-β-d-(GlcNAc)₃ than from pNP-β-d-GlcNAc. The ability of the N-acetyl-β-d-hexosaminidase to relase GlcNAc from chitin oligomers (GlcNAc)₂ (optimum pH 5.0) and (GlcNAc)₃₋₆ (optimum pH 4.4) was also low. Analysis of the reaction products revealed that the initial products from the hydrolysis of (GlcNAc)_n were predominantly (GlcNAc)_n−1 and GlcNAc.     

The reaction of oxalyl thiolesters with nucleophiles, especially thiols

Since there is evidence that oxalyl thiolesters (RSCOCOO⁻) are present in animal cells, and possibly may participate in the control of metabolism, the present study was undertaken to characterize their reactivity with nucleophiles so that one could gain a better understanding of how they might be affecting the activities of enzymes. At 25°C and neutral pH, N-acetyl-S-oxalyl-2-aminoethanethiol (NAC-S-Ox) reacts rapidly with cysteamine (2-aminoethanethiol) to give N-acetylcysteamine and N-oxalylcysteamine. Under similar conditions, other aminothiols, such as cysteine, homocysteine, penicillamine, and cysteine ethyl ester, also react rapidly with NAC-S-Ox, but non-thiol-containing amines, such as alanine, alanine ethyl ester, glycine, and S-methylcysteine, react more than four orders of magnitude less rapidly. The aminothiol reactions apparently proceed by rate-determining oxalyl transfer to the thiol followed by a rapid intramolecular S- to N-oxalyl migration. The reactions follow second-order kinetics with the thiolate anion being the reactive nucleophile. At 25°C and ionic strength 1.0 , k_N, defined in the equation, rate = k_N[RS⁻][NAC-S-Ox], has the following values ( ⁻¹ s⁻¹) for the anion of the reacting thiol: cysteamine, 170; cysteine, 260; cysteine ethyl ester, 76; homocysteine, 380. Rate data for the reaction of NAC-S-Ox with hydroxylamine, imidazole, hydroperoxide, and hydroxide were also obtained. The reaction of S-oxalyl-p-thiocresol with thiol anions under the same conditions gives the following values for k_N ( ⁻¹ s⁻¹ × 10⁻³): glutathione, 5.6; N-acetylcysteamine, 3.7; pantetheine, 4.8; 8-mercaptooctanoic acid, 4.5; 6-mercaptooctanoic acid, 1.0; dihydrolipoic acid, 8.2. These results indicate that oxalyl transfers from oxalyl thiolesters to thiol anions occur more than two orders of magnitude more rapidly than corresponding acetyl transfers, and that under physiological conditions any in vivo oxalyl thiolester would equilibrate within minutes with virtually every thiol in the cell, including those attached to enzymes. Consequently, it is proposed that one mechanism by which oxalyl thiolesters may function in vivo to alter the catalytic activities of enzymes is to covalently modify enzymic thiols by acylation with an oxalyl group.     

Synthesis, characterization and applications of graft copolymer (Chitosan-g-N,N-dimethylacrylamide)

An unreported graft copolymer of N,N-dimethylacrylamide (DMA) with chitosan has been synthesized under nitrogen atmosphere using peroxymonosulphate/mandelic acid redox pair. The effect of reaction conditions on grafting parameters i.e. grafting ratio, efficiency, conversion, add on and homopolymer has been studied. Experimental results show that maximum grafting has been obtained at 1.0 g dm⁻³ concentration of chitosan, 30 × 10⁻² mol dm⁻³ concentration of N,N-dimethylacrylamide and 7.0 × 10⁻³ mol dm⁻³ concentration of hydrogen ion. It has also been observed that grafting ratio, add on, conversion and efficiency increase upto 3.2 × 10⁻³ mol dm⁻³ of mandelic acid, 12.0 × 10⁻³ mol dm⁻³ of potassium peroxymonosulphate, 150 min of time and 40 °C of temperature. Grafted polymer has been characterized by FTIR spectroscopy and thermogravimetric analysis. Water swelling capacity of chitosan-g-N,N-dimethylacrylamide has been determined. It has been observed that the graft copolymer is thermally more stable than parent backbone.     

Antibacterial activity of lyase-depolymerized products of alginate

A series of mannuronic acid (M-block) and guluronic acid (G-block) fractions (M1–M5 and G1–G5) with different molecular weights were obtained by lyase depolymerization of alginate and evaluated for in vitro antibacterial activity against 19 bacterial strains. The antibacterial data revealed that both types of fractions generally showed activity against certain tested bacteria, whereas M-block fractions showed broader spectra and more potent inhibition than G-block fractions. Among these fractions, M3 (molecular weight 4.235 kDa) exhibited the broadest spectrum of inhibition and high inhibitory activity against Escherichia coli (minimal inhibitory concentration, MIC = 0.312 μg mL⁻¹), Salmonella paratyphi B (MIC = 0.225 μg mL⁻¹), Staphylococcus aureus (MIC = 0.016 μg mL⁻¹) and Bacillus subtilis (MIC = 0.325 μg mL⁻¹).     

Characteristics of fed-batch cultures of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> containing human-like collagen cDNA at different specific growth rates

Fed-batch cultures of recombinant Escherichia coli BL21 for producing human-like collagen were performed at different specific growth rates (0.1~0.25 h⁻¹) before induction and at a constant value of 0.05 h⁻¹ after induction by the method of pseudo-exponential feeding. Although the final biomass (around 69 g l⁻¹) was almost the same in all fed-batch cultures, the highest product concentration (13.6 g l⁻¹) was achieved at the specific growth rate of 0.15 h⁻¹ and the lowest (9.6 g l⁻¹) at 0.25 h⁻¹. The mean productivity of human-like collagen was the highest at 0.15 h⁻¹ (0.57 g l⁻¹ h⁻¹) and the lowest at 0.1 h⁻¹ (0.35 g l⁻¹ h⁻¹). In the phase before induction, the cell yield coefficient (Y_X/S) decreased when the specific growth rate increased, while the formation of acetic acid increased upto 2.5 g l⁻¹ at 0.25 h⁻¹. The mean product yield coefficient (Y_P/S) also decreased with specific growth rate increasing. The respiration quotient (RQ) increased slightly with specific growth rate increasing before induction, and the mean value of RQ was around 72%. The optimum growth rate for human-like collagen production was 0.15~0.2 h⁻¹.     

Comparison of the hydrolysis of Zn-PPi and the MgPPi as substrates and the effect of free cations upon membrane-bound pyrophosphatase of Rhodospirillum rubrum

The hydrolytic activity of chromatophore membrane-bound pyrophosphatase with Zn-PPi²⁻ as substrate was studied and compared with Mg-PPi²⁻ hydrolysis. The pH profile of Zn-PPi²⁻ hydrolysis is a bell shaped curve with an optimum at 5.25. This behavior is different from the sigmoidal profile obtained for Mg-PPi²⁻ hydrolysis, which has a plateau from pH 6.5 to 9.0. Zn-PPi²⁻ hydrolytic activity is inhibited by 1-butanol and methylene-diphosphate but not by NaF. The enzyme has no activity when free Zn²⁺ concentration is lower than 7.5 pM (at 0.9–1.2 mm Zn-PPi²⁻ and therefore free Zn²⁺ is an essential activator of Zn-PPi²⁻ hydrolytic activity. Free Mg²⁺, on the contrary, acts as an inhibitor of Zn-PPi²⁻ hydrolysis. The dependence of the reaction rate on the Zn-PPi²⁻ concentration is sigmoidal.     

Artifacts associated with the use of thiocyanate and valinomycin/K+ as permeant ions in oxidant pulse experiments on denitrifying bacteria

By means of¹⁵N-tracer and oxidant pulse methods and with nitrate-grownParacoccus denitrificans it was found that KSCN completely inhibited reduction of N₂O and nitrate in the 1 to 10 mM range, but had little or no effect on reduction of O₂ or nitrite at 150 mM. These observations confirm a previous report. Potassium thiocyanate was insufficiently permeant across the cytoplasmic membrane ofParacoccus denitrificans andPseudomonas denitrificans even at 150 mM to prevent membrane polarization when oxidant pulses were large. Polarization and inhibition artifacts due to KSCN have created some confusion in the literature. Whereas valinomycin had little direct effect on reduction of nitrite, N₂O, and O₂ individually byPa. denitrificans, it caused a temporary nitrite-dependent inhibition of N₂O reduction. Under nonpolarizing conditions the H⁺/2e^– ratios for O₂, N₂O, and nitrite (8.0, 4.3, and 4.5, respectively) confirmed those reported previously from this laboratory. The present results largely but not entirely agree with data from another laboratory.     

Using porphyritic andesite as a new additive for improving hydrolysis and acidogenesis of solid organic wastes

The effects of porphyritic andesite on the hydrolysis and acidogenesis of solid organic wastes were investigated by batch and continuous experiments using a rotational drum fermentation system. The results of the batch experiment show that if porphyritic andesite (1%, 3%, and 5% reactants) is added initially, the pH level increases and hydrolysis and acidogenesis are accelerated. The highest surface based hydrolysis constant (26.4 × 10⁻³ kg m⁻² d⁻¹) and volatile solid degradation ratio (43.3%) were obtained at a 1% porphyritic andesite addition. In the continuous experiment, porphyritic andesite elevated the first order hydrolysis constant from 13.10 × 10⁻³ d⁻¹ to 18.82 × 10⁻³ d⁻¹. A particle mean diameter reduction rate of 33.05 μm/d and a volatile solid degradation rate of 3.53 g/L d⁻¹ were obtained under the hydraulic retention time of 4, 8, 12 and 16 d.