Effects of linear and branched polyethylene glycol on PEGylation of recombinant hirudin: Reaction kinetics and in vitro and in vivo bioactivities

To improve the therapy efficacy of recombinant hirudin variant-2 (HV2), its PEGylation was investigated using linear mPEG-succinimidyl carbonate (mPEG-SC) and branched mPEG₂-N-hydroxysuccinimide (mPEG₂-NHS). The reaction mixtures of PEGylation were analyzed by RP-HPLC and the mono-PEG-HV2 products were purified by anion exchange chromatography (IEC). Effects of linear and branched PEG on the hydrolysis kinetics of the PEG reagent, the PEGylation kinetics of HV2 and the in vitro and in vivo bioactivity of mono-PEG-HV2 were investigated. The RP-HPLC and IEC analyses showed that linear and branched PEG-HV2 with identical molecular weight had different chromatographic behaviors. The reaction kinetics showed that branched mPEG₂-NHS displayed higher hydrolysis rate but lower PEGylation rates than linear mPEG-SC. Consequently, HV2 conjugated with mPEG₂-NHS required a greater molar ratio of PEG to HV2 than that of mPEG-SC to achieve the identically desired yield of mono-PEG-HV2. The in vitro and in vivo bioactivities of mono-PEG-HV2 showed that branched PEG-HV2 had higher therapeutic efficacy than linear PEG-HV2 with identical molecular weight. The in vivo bioactivity of mono-B-PEG40k-HV2 (mono-PEG-HV2 derived from 40 kDa branched mPEG₂-NHS) had a markedly longer duration in rabbits than did unmodified HV2, which showed its potential to be developed as a candidate antithrombotic drug.     

In situ PEGylation of recombinant hirudin on an anion exchange chromatography column

In this study, an integrated process was developed for successive solid-phase PEGylation of recombinant hirudin variant-2 (HV2) and separation of PEGylated HV2 species on an anion exchange chromatography column (so-called in situ PEGylation). The effects of different PEG sizes, ion exchange resins and reaction conditions on in situ PEGylation were investigated. The results showed that in situ PEGylation efficiently integrates the reaction, separation and purification into a single-unit operation using the same column. In situ PEGylation could improve the selectivity of PEGylation reactions by significantly reducing the formation of multi-PEG-HV2. The pore sizes and internal surface structures of different resins had a significant impact on the yield of mono-PEG-HV2. In contrast to liquid-phase PEGylation, the yield of mono-PEG-HV2 decreased as PEG size increased during the in situ PEGylation process, indicating that in situ PEGylation is a pore diffusion-controlled process. The in vitro and in vivo anticoagulant activities of mono-PEG-HV2 derived from in situ PEGylation were higher than those from liquid-phase PEGylation, indicating that in situ PEGylation could enhance the bioactivity retention of mono-PEG-HV2. The results of this study demonstrated that in situ PEGylation can be used as an effective approach for the development of PEGylated protein drugs.     

Combined optimization of N‐terminal site‐specific PEGylation of recombinant hirudin using response surface methodology and kinetic analysis

In this study, a combined optimization method was developed to optimize the N‐terminal site‐specific PEGylation of recombinant hirudin variant‐2 (HV2) with different molecular weight mPEG‐propionaldehyde (mPEG‐ALD), which is a multifactor‐influencing process. The HV2‐PEGylation with 5 kDa mPEG‐ALD was first chosen to screen significant factors and determine the locally optimized conditions for maximizing the yield of mono‐PEGylated product using combined statistical methods, including the Plackett–Burman design, steepest ascent path analysis, and central composition design for the response surface methodology (RSM). Under the locally optimized conditions, PEGylation kinetics of HV2 with 5, 10, and 20 kDa mPEG‐ALD were further investigated. The molar ratio of polyethylene glycol to HV2 and reaction time (the two most significant factors influencing the PEGylation efficiency) were globally optimized in a wide range using kinetic analysis. The data predicted by the combined optimization method using RSM and kinetic analysis were in good agreement with the corresponding experiment data. PEGylation site analysis revealed that almost 100% of the obtained mono‐PEGylated‐HV2 was modified at the N‐terminus of HV2. This study demonstrated that the developed method is a useful tool for the optimization of the N‐terminal site‐specific PEGylation process to obtain a homogeneous mono‐PEGylated protein with desirable yield.     

Synthesis of a New Tri-Branched PEG-IFNα2 and Its Impact on Anti Viral Bioactivity

Efficacy of proteins can be enhanced by using polyethylene glycol (PEG) conjugation (PEGylation) to the protein molecules. Mobile non-toxic PEG chains conjugated to bio-therapeutics increase their hydrodynamic volume and in turn can prolong their plasma retention time and increase their solubility. An important aspect of PEGylation is the selection of PEG molecule with suitable structure and molecular weight. In this study, conceiving the idea that branched PEG-conjugates show superior efficacy over the linear PEG-conjugates, a tri-branched PEG-interferon (mPEG₃L₂-IFN) was synthesized by reacting a 30 KDa tri-branched mPEG₃L₂-NHS reagent with IFN to improve its pharmacokinetic properties and reduce the loss of in vitro bioactivity (which is generally exhibited by PEGylation) of the conjugated protein to some extent. The PEGylation procedure was optimized in terms of concentration and molar ratios of reactants, reaction time, temperature and pH conditions of the reaction mix. The conjugate was purified by cation exchange chromatography and characterized by SDS-PAGE and SE-HPLC. Trypsin digestion of mPEG₃L₂-IFN indicated a single site specificity of PEGylation. Anti viral bioactivity of mPEG₃L₂-IFN was found to be 2.38 × 10⁷ IU/mg which is approximately 9.52% of native IFNα2 (2.5 × 10⁸ IU/mg) and better than PEGasys from Roche Pharma. Therefore, it is reported that the tri-branched mPEG₃L₂-NHS reagent has the potential to be used to conjugate proteins for the promising therapeutic results.     

Chemical modification of recombinant hirudin with palmitic acid in mixed aqueous-organic solutions

In this study, chemical modification of recombinant hirudin variant-2 (HV2) with palmitic acid (PAL) was proposed as an alternative approach to circumvent the limitations of PEGylation. To facilitate a sufficient contact of the hydrophilic HV2 to the hydrophobic PAL, thereby improving the reaction specificity to achieve the desired mono-PAL-HV2 with high retained bioactivity, the reaction was developed in mixed aqueous-organic solutions. Compared with HV2 conjugation with PAL-benzotriazole (PAL-BTA) in mixed aqueous-NMP solution, the conjugation of HV2 with PAL-N-hydroxysuccinimide (PAL-NHS) in mixed aqueous-DMSO solution could improve the site-specific conjugation of one PAL molecule to a particular lysine residue. Furthermore, the reaction mixture of the latter was further purified by preparative liquid chromatography. Three mono-PAL-HV2 isomers were obtained and retained 36%, 4% and 89% of the in vitro anticoagulant activity of unmodified HV2, respectively. One of the mono-PAL-HV2 isomers, namely, mono-PAL-HV2-3, was isolated with the highest selectivity and exhibited the highest in vitro anticoagulant bioactivity. Modification site analysis of mono-PAL-HV2-3 revealed that a single PAL molecule was conjugated at Lys27 of HV2. This study presented a successful PAL modification in which site-specific reaction was improved to achieve the desired mono-PAL-HV2 with highly retained bioactivity in mixed aqueous-organic solutions.     

PEG chain length impacts yield of solid-phase protein PEGylation and efficiency of PEGylated protein separation by ion-exchange chromatography: Insights of mechanistic models

The mechanisms behind protein PEGylation are complex and dictated by the structure of the protein reactant. Hence, it is difficult to design a reaction process which can produce the desired PEGylated form at high yield. Likewise, efficient purification processes following protein PEGylation must be constructed on an ad hoc basis for each product. The retention and binding mechanisms driving electrostatic interaction-based chromatography (ion-exchange chromatography) of PEGylated proteins (randomly PEGylated lysozyme and mono-PEGylated bovine serum albumin) were investigated, based on our previously developed model Chem. Eng. Technol. 2005, 28, 1387–1393. PEGylation of each protein resulted in a shift to a smaller elution volume compared to the unmodified molecule, but did not affect the number of binding sites appreciably. The shift of the retention volume of PEGylated proteins correlated with the calculated thickness of PEG layer around the protein molecule. Random PEGylation was carried out on a column (solid-phase PEGylation) and the PEGylated proteins were separated on the same column. Solid-phase PEGylation inhibited the production of multi-PEGylated forms and resulted in a relatively low yield of selective mono-PEGylated form. Pore diffusion may play an important role in solid-phase PEGylation. These results suggest the possibility of a reaction and purification process development based on the mechanistic model for PEGylated proteins on ion exchange chromatography.     

Kinetics of glucose transport in human erythrocytes: zero-trans efflux and infinite-trans efflux at 0°C

The kinetic features of glucose transport in human erythrocytes have been the subject of many studies, but no model is consistent with both the kinetic observations and the characteristics of the purified transporter. In order to reevaluate some of the kinetic features, initial rate measurements were performed at 0°C. The following kinetic parameters were obtained for fresh blood: zero-trans efflux K_m = 3.4 mM, V_max = 5.5 mM/min; infinite-trans efflux K_m = 8.7 mM, V_max = 28 mM/min. For outdated blood, somewhat different parameters were obtained: zero-trans efflux K_m = 2.7 mM, V_max = 2.4 mM/min; infinite-trans efflux K_m = 19 mM, V_max = 23 mM/min. The K_m values for fresh blood differ from the previously reported values of 16 mM and 3.4 mM for zero-trans and infinite-trans efflux, respectively (Baker, G.F. and Naftalin, R.J. (1979) Biochim. Biophys. Acta 550, 474–484). The use of 50 mM galactose rather than 100 mM glucose as the infinite-trans sugar produced no change in the infinite-trans efflux K_m values but somewhat lower V_max values. Simulations indicate that initial rates were closely approximated by the experimental conditions. The observed time courses of efflux are inconsistent with a model involving rate-limiting dissociation of glucose from hemoglobin (Naftalin, R.J., Smith, P.M. and Roselaar, S.E. (1985) Biochim. Biophys. Acta 820, 235–249). The results presented here support the adequacy of the carrier model to account for the kinetics.     

Kinetic models and process parameters for ultrasound-assisted extraction of water-soluble components and polysaccharides from a medicinal fungus

This study was on the kinetics and process parameters for ultrasound-assisted extraction (UAE) of water-soluble components and polysaccharides (PS) from the dry mycelium of a medicinal fungus, Cordyceps sinensis Cs-HK1. Four process variables (factors) were evaluated at different levels, ultrasound intensity (2.44–44.1 W/cm²), temperature (40–70 °C), solid particle size (156.5–750 μm), and solid-to-liquid ratio (1/30–1/70 g/mL). The experimental data of yields versus time in most cases were fitted closely to two empirical kinetic models for solid–liquid extraction, parabolic diffusion equation (y = y_o + y₁t^1/2) and power law (y = βtⁿ) with high correlation coefficients (R²) of 0.95–0.99 for total extract yield, and 0.90–0.96 for PS yield. The PS yield was increased more significantly than the total extract yield with the ultrasound intensity. Reducing the particle size and increasing the extraction temperature led to a higher yield and extraction rate; increasing the solid-to-liquid ratio (or decreasing the liquid volume) increased the PS yield and extraction rate but had little influence on the total extract. Significant correlations were found between extraction rate (dy/dt) and ultrasound power density (P/V), and between extract yield (y) and energy density (Pt/V). The kinetic and process parameters are useful for rational design and efficient operation of UAE processes.     

Regulation by Phospholipids and Kinetic Studies of Plant Membrane-Bound UDP-Glucose Sterol beta-d-Glucosyl Transferase

Solubilization and partial purification of the microsomal UDP-glucose sterol glucosyl transferase activity from maize coleoptiles by chromatography on DEAE-cellulose resulted in a highly delipidated (>95%) and inactive enzymic preparation. Addition of sterols revealed part of the activity and subsequent addition of phospholipids further increased the activity. Negatively charged phospholipids were shown to be by far the best activators. The purification step also produced the elimination of two interfering microsomal enzymic activities: UDPase and steryl glucoside acyl transferase. The removal of these two enzymic activities was a prerequisite for kinetic studies including product-inhibition studies, since the substrates of these two latter enzymes are the products of UDPG-SGTase activity. The results of the kinetic studies strongly suggest an ordered bi-bi mechanism for the glucosylation of sterols. Finally the effect of different phospholipids on the kinetic parameters of the reaction was studied. Both phosphatidylcholine and phosphatidylglycerol significantly decrease K_m-sterol (and not K_m-UDPglucose) and increase the reaction V_max. The decrease of K_m-sterol is similar with both phospholipids whereas the increase of V_max is much greater with phosphatidylglycerol than with phosphatidylcholine.     

Reduction in swimming performance in juvenile rainbow trout (Oncorhynchus mykiss) following sublethal exposure to pyrethroid insecticides

While the lethal toxicity of pyrethroid insecticides to fish is well documented, their sublethal physio-behavioral effects remain poorly characterized. Known pyrethroid-associated changes to insect neuromuscular function may translate into similar effects in fish, thereby altering swimming ability and affecting foraging, predator avoidance, and migration. Three experiments were conducted using critical (U_crit) and burst (U_max) swimming speeds to assess the sublethal effects of the pyrethroids permethrin and deltamethrin in juvenile rainbow trout (Oncorhynchus mykiss). Fish were exposed to deltamethrin (100, 200, or 300 ng/L) or permethrin (1, 2, or 3 μg/L) in water for 4 d, and assessed for swimming performance. Deltamethrin (200 and 300 ng/L) reduced U_crit, but not U_max, while both swim performance measurements were unaffected by permethrin. Subsequent experiments used only U_crit to assess deltamethrin exposure. In a time course experiment, deltamethrin (300 ng/L) reduced U_crit after 1 and 4 d of exposure, but after 7 d of exposure U_crit was fully recovered. Finally, deltamethrin (1, 2, or 3 μg/L) reduced U_crit after 1 h bath exposures similar to recommended protocols for deltamethrin based sea-lice treatment in aquaculture. The real-world implications of the revealed pyrethroid-associated swimming ability reductions in salmon may be important in areas close to aquaculture facilities.     

Triazine Resistance without Reduced Vigor in Phalaris paradoxa

A triazine-resistant (R) biotype of Phalaris paradoxa L. (hood canarygrass) was superior to a triazine-susceptible (S) biotype in seed-germinability and seedling emergence. It was equal or superior to the S-biotype in growth under noncompetitive conditions. Rates of CO₂ uptake by R-plants were similar to those of S-plants, except at very low photon flux densities, where S-plants exhibited higher rates of CO₂ uptake. Fluorescence induction curves of chloroplasts isolated from R-plants indicated an alteration in photosystem II. Analysis of the light dependence of electron transport shows a reduction in quantum yield (Q_y) in R- compared to S-chloroplasts. The same analysis, however, shows for R-chloroplasts an increase in the light-saturated electron transport rate (V_max). The increase in V_max compensates for the reduction of Q_y over a wide range of photon flux densities, which may explain the similarity between R- and S-biotypes in photosynthetic potential and growth.     

Calculation of Km and Vmax from Substrate Concentration Versus Time Plot

A simple method for the calculation of kinetic parameters (K_m, V_max) under conditions of changing substrate concentrations is presented. An application of the method to detect shifts in groups involved in the utilization of a substrate in a mixed microbial culture is given.     

Experimental studies and two-dimensional modelling of a packed bed bioreactor used for production of galacto-oligosaccharides (GOS) from milk whey

In the present study, extensive experimental investigations and detailed theoretical analysis of a two-dimensional packed bed bioreactor, employed for the production of galacto-oligosaccharides (GOS) from milk whey were performed. Model equations, in one- and two-dimensions, capable of predicting the substrate concentration distribution in the bioreactor were developed by coupling mass balance equation with appropriate velocity distribution equation and solved numerically. Validation of the proposed model equations was done by a set of experimental data obtained from the bioreactor. The effects of reactor to catalyst particle diameter ratio (d _t/d _p), feed flowrate (10^?6–10^?9 m³ s^?1), and initial lactose concentration (50–200 kg m^?3) on substrate concentration distribution were investigated in detail. While, the distribution of substrate concentration in axial direction was independent of d _t/d _p, it was observed that for d _t/d _p <40, significant radial concentration distribution existed. It was further observed that the substrate conversion and product yield obtained experimentally showed an excellent agreement (97 ± 2 %) with the results predicted by the two-dimensional model equation, whereas, the results predicted by the one-dimensional model equation did not lie within the desired confidence level (<90 %). The results were confirmed by both curve fitting and statistical analysis. The prediction of substrate concentration distribution in axial and radial directions using the developed two-dimensional model equation is necessary for computing the bioreactor volume to achieve the desired GOS yield.     

Mass spectrometry assay for studying kinetic properties of dipeptidases: characterization of human and yeast dipeptidases

Chemical modifications of substrate peptides are often necessary to monitor the hydrolysis of small bioactive peptides. We developed an electrospray ionization mass spectrometry (ESI–MS) assay for studying substrate distributions in reaction mixtures and determined steady-state kinetic parameters, the Michaelis–Menten constant (K_m), and catalytic turnover rate (V_max/[E]_t) for three metallodipeptidases: two carnosinases (CN1 and CN2) from human and Dug1p from yeast. The turnover rate (V_max/[E]_t) of CN1 and CN2 determined at pH 8.0 (112.3 and 19.5 s⁻¹, respectively) suggested that CN1 is approximately 6-fold more efficient. The turnover rate of Dug1p for Cys-Gly dipeptide at pH 8.0 was found to be slightly lower (73.8 s⁻¹). In addition, we determined kinetic parameters of CN2 at pH 9.2 and found that the turnover rate was increased by 4-fold with no significant change in the K_m. Kinetic parameters obtained by the ESI–MS method are consistent with results of a reverse-phase high-performance liquid chromatography (RP–HPLC)-based assay. Furthermore, we used tandem MS (MS/MS) analyses to characterize carnosine and measured its levels in CHO cell lines in a time-dependent manner. The ESI–MS method developed here obviates the need for substrate modification and provides a less laborious, accurate, and rapid assay for studying kinetic properties of dipeptidases in vitro as well as in vivo.     

Aldehyde PEGylation kinetics: a standard protein versus a pharmaceutically relevant single chain variable fragment

The mPEG-aldehyde PEGylation with two different PEG sizes and two proteins was experimentally determined with respect to yield, conversion, and selectivity. The kinetic behavior of these PEGylation reactions was simulated using a numerically solved set of differential equations. We show that the assumption of an inactivation of mPEG-aldehyde is crucial for the simulation of the overall PEGylation and that the inactivation is pH-dependent. We further demonstrate that ideal PEGylation parameters such as pH, temperature, reaction time, and protein concentration need to be chosen carefully depending on the protein and PEG size. In terms of selectivity and yield, we show that the reaction should be stopped before the highest mono-PEG concentration is reached. Moreover, room temperature and a slightly acidic pH of approximately 6 are good starting points. In conclusion, selectivity can be optimized choosing a shorter reaction time and a reduced reaction temperature.     

Dissecting the Catalytic Mechanism of Trypanosoma brucei Trypanothione Synthetase by Kinetic Analysis and Computational Modeling

In pathogenic trypanosomes, trypanothione synthetase (TryS) catalyzes the synthesis of both glutathionylspermidine (Gsp) and trypanothione (bis(glutathionyl)spermidine (T(SH)₂)). Here we present a thorough kinetic analysis of Trypanosoma brucei TryS in a newly developed phosphate buffer system at pH 7.0 and 37 °C, mimicking the physiological environment of the enzyme in the cytosol of bloodstream parasites. Under these conditions, TryS displays K_m values for GSH, ATP, spermidine, and Gsp of 34, 18, 687, and 32 μm, respectively, as well as K_i values for GSH and T(SH)₂ of 1 mm and 360 μm, respectively. As Gsp hydrolysis has a K_m value of 5.6 mm, the in vivo amidase activity is probably negligible. To obtain deeper insight in the molecular mechanism of TryS, we have formulated alternative kinetic models, with elementary reaction steps represented by linear kinetic equations. The model parameters were fitted to the extensive matrix of steady-state data obtained for different substrate/product combinations under the in vivo-like conditions. The best model describes the full kinetic profile and is able to predict time course data that were not used for fitting. This system''s biology approach to enzyme kinetics led us to conclude that (i) TryS follows a ter-reactant mechanism, (ii) the intermediate Gsp dissociates from the enzyme between the two catalytic steps, and (iii) T(SH)₂ inhibits the enzyme by remaining bound at its product site and, as does the inhibitory GSH, by binding to the activated enzyme complex. The newly detected concerted substrate and product inhibition suggests that TryS activity is tightly regulated.     

A new approach to DNA polymerase kinetics

Little is known of the detailed mechanisms of the polymerization reactions carried out by RNA and DNA polymerases. Besides technical reasons, there are mathematical difficulties not encountered in traditional enzymology. The product of the reaction after one polymerization step is also the substrate of the next step. A number of polymerases, isolated from various sources, have an exonuclease activity. The chain which is being synthesized may be either elongated or trimmed, and its growth has the character of a random walk. In this case, although the overall reaction scheme is more complex, the experiments are more informative, as every dNTP may be transformed into two distinct products: incorporated, or free dNMP.Having solved some of the mathematical difficulties of the random walk problem, we are able to propose a strategy for the study of the polymerization/excision kinetics. We measure the amount y(t) of nucleotide that is polymerized at time tand the amount x(t) of nucleoside monophosphate that has accumulated. When $\text{d}\text{y}\text{d}\text{x}$ is plotted against the concentration of dNTP, a curve is obtained with a characteristic shape, a straight line in a large number of cases. From there, kinetic constants can be estimated.The analysis is made in terms of four possible kinetic schemes. In the most elementary model there are only two rate constants, one for incorporation and one for excision. This model is a limiting case of all other models. The frayed-unfrayed model of Brutlag & Kornberg (1972), Hopfield's kinetic proofreading scheme (Hopfield, 1974), and the delayed-escape scheme (Ninio, 1975) are examined in detail, and we show how the kinetic experiments may in principle distinguish between the schemes. Our approach is illustrated with three experiments in which Escherichia coli DNA polymerase I acts on poly(dC), and poly(dT) · oligo(dA)₁₀.     

Kinetics of l-Valine Uptake in Suspension-Cultured Cells and Protoplast-Derived Cells of Tobacco: Comparison of Wild-Type and the Val-2 Mutant

A kinetic analysis was made of l-valine uptake in protoplast-derived cells (mesophyll protoplasts cultured for 6 days) and in suspension-cultured cells of tobacco (Nicotiana tabacum L., cv Xanthi). Cells from wild-type and Val^r-2 mutant plants were compared. A low-K_m component was found in protoplast-derived cells (K_m = 45 ± 5 micromolar) as well as in suspension-cultured cells (K_m = 84 ± 21 micromolar). In the mutant cells the V_max of this component was 12- to 14-fold less than in wild-type cells. A second component (K_m = 2.4 ± 0.7 millimolar) was found in suspension-cultured cells but not in protoplast-derived cells; its V_max was the same in wild-type and mutant cells. A third component was apparently unsaturable (linear component). It was present in protoplast-derived cells but not in suspension-cultured cells, and had the same magnitude in wild-type and mutant cells. The results are discussed with reference to the uptake of l-valine in leaf tissue, in which the three kinetic components have been found simultaneously. The reduced V_max of the low-K_m component in the Val^r-2 mutant, and the differential expression of the other two components in suspension-cultured cells and protoplast-derived cells indicate that the kinetically distinguishable components represent physically distinct transport systems.     

Optimization of octreotide PEGylation by monitoring with fast reversed-phase high-performance liquid chromatography

The purpose of this study was to develop a fast reversed-phase high-performance liquid chromatography (HPLC) method for monitoring the octreotide PEGylation reaction in order to find optimal conditions for the production of the desired mono-PEGylated octreotide. The fast HPLC method could separate the positional isomers of two mono-PEGylated octreotides, di-PEGylated octreotide, and unmodified octreotide within 4.5 min. The PEGylation pattern was monitored at various pH conditions and molar ratios of reactants to allow optimization of the PEGylation reaction conditions for the production of N-terminally mono-PEGylated octreotide.     

Purification and kinetic studies on a porphobilinogen deaminase from the unicellular green alga Scenedesmus obliquus

Porphobilinogen deaminase, the enzyme condensing four molecules of porphobilinogen, was isolated and purified from light grown Scenedesmus obliquus (wild type). The purification procedure included heat treatment, ammonium sulphate fractionation, gel filtration, high-resolution anion-exchange chromatography and hydrophobic interaction chromatography. The enzyme was purified 1368-fold, compared to the initial crude extract. Its final specific activity was 6812 units · (mg · protein)^?1 at pH 7.4 with a recovery of 44%. The relative molecular mass was 33000, as determined by Sephadex G-100 gel filtration, and 35900 by lithium dodecyl sulfate-polyacrylamide-gel electrophoresis, indicating that the enzyme is a monomer. Studies of initial reaction velocities showed a linear progress curve for hydroxymethylbilane formation and a hyperbolic dependence of the initial reaction rate on substrate concentration, consistent with a sequential displacement mechanism. Apparent kinetic constants (K _m and V _max) for the conversion of porphobilinogen to hydroxymethylbilane at 37 ° C, pH 7.4, were 79 μM and 176 pmol · min^?1, respectively. Variation of both V _max and K _max with pH indicated the presence of ionizable groups in the enzyme-substrate complex(es), showing a single ionization (pK 7.15) in V _max/K _m plots. A sharp pH-profile for V _max was interpreted as a positive cooperative proton dissociation. In spite of the two pathways existing for 5-aminolevulinate biosynthesis in Scenedesmus, currently there is no indication of the existence of two porphobilinogen deaminases or even of isoenzymes.