Regulation of O-acetylserine sulfhydrylase B by L-cysteine in Salmonella typhimurium.

A technique based on resistance to azaserine was used to isolate mutants lacking O-acetylserine sulfhydrylase B, one of two enzymes in Salmonella typhimurium capable of synthesizing L-cysteine from O-acetyl-L-serine and sulfide. The mutant locus responsible for this defect has been designated cysM, and genetic mapping suggests that cysM is very close to and perhaps contiguous with cysA. Strains lacking either O-acetylserine sulfhydrylase B or the second sulfhydrylase, O-acetylserine sulfhydrylase A (coded for by cysK), are cysteine prototrophs, but cysK cysM double mutants were found to require cysteine for growth. O-Acetylserine sulfhydrylase B was depressed by growth on a poor sulfur source, and depression was dependent upon both a functional cysB regulatory gene product and the internal inducer of the cysteine biosynthetic pathway, O-acetyl-L-serine. Furthermore, a cysBc strain, in which other cysteine biosynthetic enzymes cannot be fully repressed by growth on L-cystine, was found to be constitutive for O-acetylserine sulfhydrylase B as well. Thus O-acetylserine sulfhydrylase B is regulated by the same factors that control the expression of O-acetylserine sulfhydrylase A and other activities of the cysteine regulon. It is not clear why S. typhimurium has two enzymes whose physiological function appears to be to catalyze the same step of L-cysteine biosynthesis.     

Sulphur metabolism in Paracoccus denitrificans. Purification, properties and regulation of serine transacetylase, O-acetylserine sulphydrylase and beta-cystathionase.

1. Serine transacetylase, O-acetylserine sulphydrylase and beta-cystathionase were purified from Paracoccus denitrificans strain 8944. 2. Serin transacetylase was purified 150-fold. The enzyme has a pH optimum between 7.5 and 8.0, is specific for L-serine and is inhibited by sulphydryl-group reagents. The apparent Km values for serine and acetyl-CoA are 4.0 - 10(-4) and 1.0 - 10(-4) M, respectively. Serine transacetylase is strongly inhibited by cysteine. 3. O-Acetylserine sulphydrylase was purified 450-fold. The enzymes has a sharp pH optimum at pH 7.5. In addition to catalysing the synthesis of cysteine, O-acetylserine sulphydrylase catalyses the synthesis of selenocysteine from O-acetylserine and selenide. The Km values for sulphide and O-acetylserine are 2.7 - 10(-3) and 1.25 - 10(-3) M, respectively. The enzyme was stimulated by pyridoxal phosphate and was inhibited by cystathionine, homocysteine and methionine. 4. beta-Cystathionase was purified approx. 50-fold. beta-Cystathionase has a pH optimum between pH 9.0 and 9.5, is sensitive to sulphydryl-group reagents, required pyridoxal phosphate for maximum activity and has an apparent Km for cystathionine of 4.2 - 10 (-3) M. beta-Cystathionase also catalyses the release of keto acid from lanthionine, djenkolic acid and cystine. Cysteine, O-acetylserine, homocysteine and glutathione strongly inhibit beta-cystathionase activity and homocysteine and methionine represses enzyme activity. 5. O-Acetylserine lyase was identified in crude extracts of Paracoccus denitrificans. The enzyme is specific for O-acetyl-L-serine, requires pyridoxal phosphate and is inhibied by KCN and hydroxylamine. The enzyme has a high Km value for O-acetylserine (50--100 mM).     

L-cysteine biosynthesis in Escherichia coli: nucleotide sequence and expression of the serine acetyltransferase (cysE) gene from the wild-type and a cysteine-excreting mutant

Serine acetyltransferase (SAT) from Escherichia coli is subject to feedback inhibition by L-cysteine. A mutant was isolated which excretes L-cysteine because of a lesion in cysE, the structural gene for SAT, rendering the enzyme less feedback sensitive. To analyse the structural basis for this mutation the cysE genes both from wild-type E. coli and the mutant strain were cloned and their nucleotide sequences determined. The cysE gene contained an open reading frame consisting of 819 bp, equivalent to a protein of 273 amino acids. The mutant gene showed a single base change in position 767 resulting in a methionine to isoleucine substitution. A causal connection between this SAT sequence alteration, feedback insensitivity and L-cysteine excretion was demonstrated. The SAT from the wild-type strain was purified. It was composed of a single polypeptide chain migrating in SDS gels according to an Mr of 34,000. As in Salmonella typhimurium, the enzyme was associated in a bifunctional complex with O-acetylserine (thiol)-lyase.     

Purification and Kinetic Properties of Serine Acetyltransferase Free of O-Acetylserine(thiol)lyase from Spinach Chloroplasts

Serine acetyltransferase, a key enzyme in the L-cysteine biosynthetic pathway, was purified over 300,000-fold from the stroma of spinach (Spinacia oleracea) leaf chloroplasts. The purification procedure consisted of ammonium sulfate precipitation, anion-exchange chromatography (Trisacryl M DEAE and Mono Q HR10/10), hydroxylapatite chromatography, and gel filtration (Superdex 200). The purified enzyme exhibited a specific activity higher than 200 units mg-1 and a subunit molecular mass of about 33 kD upon polyacrylamide gel electrophoresis in the presence of sodium dodecyl sulfate. Moreover, the purified serine acetyltransferase appeared to be essentially free of O-acetyleserine(thiol)lyase, another enzyme component in the L-cysteine biosynthetic pathway. A steady-state kinetic analysis indicated that the mechanism of the enzyme-catalyzed reaction involves a double displacement. The apparent Km for the two substrates, L-serine and acetyl-coenzyme A, were 2.29 [plus or minus] 0.43 and 0.35 [plus or minus] 0.02 mM, respectively. The rate of L-cysteine synthesis in vitro was measured in a coupled enzyme assay using extensively purified O-acetylserine(thiol)lyase and serine acetyltransferase. This rate was maximum when the assay contained approximately a 400-fold excess of O-acetylserine(thiol)lyase over serine acetyltransferase. Measurements of the relative level of O-acetylserine(thiol)lyase and serine acetyltransferase activities in the stroma indicated that the former enzyme was present in much larger quantities than the latter. Thus, the activity ratio for these two enzymes [O-acetylserine(thiol)lyase activity/serine acetyltransferase activity] measured in the stromal protein extract was 345. This strongly suggested that all the O-acetylserine(thiol)lyase and serine acetyltransferase activities in the stroma are involved in bringing a full synthesis of L-cysteine in the chloroplast.     

Autotrophic denitrification via a novel membrane-attached biofilm reactor

AIMS: A laboratory-scale autotrophic membrane-attached biofilm reactor was developed to remove nitrate from drinking water. METHODS AND RESULTS: Hydrogen and carbon dioxide flowed together into the lumem side of a gas-permeable silicone tube. The gases diffused through the membrane wall to feed Alcaligenes eutrophus that formed a biofilm on the surface of the silicone tube for autotrophic denitrification. Hydrogen provided the energy source, and carbon dioxide, besides serving as the carbon source, was employed to neutralize the alkalinity from denitrification. The optimal carbon dioxide concentration in the silicone tube was between 20% and 50%. CONCLUSION: This study has demonstrated that a gas-permeable silicone tube is a convenient and efficient method to feed A. eutrophus for autotrophic denitrification. Supplying a suitable amount of carbon dioxide together with hydrogen into the silicone tube solved the problem that alkalinity formation caused during denitrification. The pH of the bioreactor was maintained at about 7 to avoid nitrite accumulation, and then the nitrogen removal rate was increased. A high specific nitrogen removal rate (1.6-5.4 g Nm(2)d(-1-1) of surface area of silicone tube) was achieved. SIGNIFICANCE AND IMPACT OF THE STUDY: In addition to combining the advantages of the hydrogenotrophic denitrification process and a membrane feeding substrate bioreactor (MFSB), this bioreactor achieved a high nitrogen removal rate and is simple to operate. It therefore is highly promising in drinking-water treatment.     

Effect of glutathione L-cystein and L-djenkolic acid in the synthesis and mutagenicity of azide metabolite in Bacillus subtilis ATCC 6633 strain.

The Bacillus subtilis ATCC 6633 strain synthesizes a mutagenic metabolite from sodium azide and O-acetylserine. Mutagenicity of azide was decreased in growth media containing 10(-4) M glutathione, L-cysteine or L-djenkolic acid whereas dithiothritol (DTT) added at the same concentration did not reduce the mutagenicity of azide. Likewise, glutathione, L-cysteine, L-djenkolic acid, and DTT were found to have no effect in reducing the mutagenicity of the in vitro produced metabolite using bacterial cell-free extract. These results suggest that O-acetyl-serine sulfhydrylase catalyzes the reaction of azide and O-acetylserine to form a mutagenic metabolite, which is ninhydrin positive and migrates in TLC to an Rf value similar to that of azidoalanine in both acidic and basic solvent systems.     

Enzymatic production of L-serine with a feedback control system for formaldehyde addition

Serine hydroxymethyltransferase (SHMT) in the form of crude extract from a recombinant strain of Klebsiella aerogenes was used for the production of L-serine from glycine and formaldehyde (HCHO). A stirred tank bio-reactor with a continuous feed of HCHO (37%) was employed. Since the performance of the serine bioreactor was heavily dependent on how HCHO was fed, an automatic feedback control system was developed for HCHO delivery utilizing the phenomenon of formol titration. This control procedure was based on the following circumstance: as a bioconversion proceeded, if the rate of HCHO feed was balanced by the rate of serine synthesis so that HCHO concentration was maintained near zero, then there was no pH change in the bioreactor. Once the rate of HCHO addition exceeded that of serine synthesis, the HCHO concentration built up and the excess HCHO reacted with the amino group of an amino acid (e.g. glycine or serine) to produce a Schiff base and a proton which lowered the pH. A pH controller detected and relayed this pH change to the on-off switch of the HCHO feed pump. Thus, HCHO infusion stopped when the pH was lower than the set point, which was the initial pH of the reaction. With this control system, the maximum concentration of HCHO that was reached in the bioreactor was only 1mM-3.3mM depending on the pH and amino acid composition in the bioreactor. Moreover, a decrease in pH also signaled the use of a slower feed rate at which HCHO was to be, delivered once the pH resumed its initial value after excess HCHO was consumed by the reaction. Employing this control system, we have optimized the performance of the serine bioreactor to give a serine titer of 450 g/L with an 88% molar conversion of glycine at a volumetric serine productivity of 8.9 g/L/h.     

Purification and characterization of O-acetylserine (thiol) lyase from spinach chloroplasts.

O-Acetylserine (thiol) lyase, the last enzyme in the cysteine biosynthetic pathway, was purified to homogeneity from spinach leaf chloroplasts. The enzyme has a molecular mass of 68,000 and consists of two identical subunits of Mr 35,000. The absorption spectrum obtained at pH 7.5 exhibited a peak at 407 nm due to pyridoxal phosphate, and addition of O-acetylserine induced a considerable modification of the spectrum. The pyridoxal phosphate content was found to be 1.1 per subunit of 35,000, and the chromophore was displaced from the enzyme by O-acetylserine, leading to a progressive inactivation of the holoenzyme. Upon gel filtration chromatography on Superdex 200, part of the chloroplastic O-acetylserine (thiol) lyase eluted in association with serine acetyltransferase at a position corresponding to a molecular mass of 310,000 (such a complex called cysteine synthase has been characterized in bacteria). The activity of O-acetylserine (thiol) lyase was optimum between pH 7.5 and 8.5. The apparent Km for O-acetylserine was 1.3 mM and for sulfide was 0.25 mM. The calculated activation energy was 12.6 kcal/mol at 10 mM O-acetylserine. The overall amino-acid composition of spinach chloroplast O-acetylserine (thiol) lyase was different than that determined for the same enzyme (cytosolic?) obtained from a crude extract of spinach leaves. A polyclonal antibody prepared against the chloroplastic O-acetylserine (thiol) lyase exhibited a very low cross-reactivity with a preparation of mitochondrial matrix and cytosolic proteins suggesting that the chloroplastic isoform was distinct from the mitochondrial and cytosolic counterparts.     

Structure, mechanism, and conformational dynamics of O-acetylserine sulfhydrylase from Salmonella typhimurium: comparison of A and B isozymes

O-Acetylserine sulfhydrylase is a pyridoxal 5'-phosphate-dependent enzyme that catalyzes the final step in the cysteine biosynthetic pathway in enteric bacteria and plants, the replacement of the beta-acetoxy group of O-acetyl-l-serine by a thiol to give l-cysteine. Two isozymes are found in Salmonella typhimurium, with the A-isozyme expressed under aerobic and the B-isozyme expressed under anaerobic conditions. The structure of O-acetylserine sulfhydrylase B has been solved to 2.3 A and exhibits overall a fold very similar to that of the A-isozyme. The main difference between the two isozymes is the more hydrophilic active site of the B-isozyme with two ionizable residues, C280 and D281, replacing the neutral residues S300 and P299, respectively, in the A-isozyme. D281 is above the re face of the cofactor and is within hydrogen-bonding distance to Y286, while C280 is located about 3.4 A from the pyridine nitrogen (N1) of the internal Schiff base. The B-isozyme has a turnover number (V/Et) 12.5-fold higher than the A-isozyme and an approximately 10-fold lower Km for O-acetyl-l-serine. Studies of the first half-reaction by rapid-scanning stopped-flow indicate a first-order conversion of the internal Schiff base to the alpha-aminoacrylate intermediate at any concentration of O-acetyl-l-serine. The Kd values for formation of the external Schiff base with cysteine and serine, obtained by spectral titration, are pH dependent and exhibit a pKa of 7.0-7.5 (for a group that must be unprotonated for optimum binding) with values, above pH 8.0, of about 3.0 and 30.0 mM, respectively. In both cases the neutral enolimine is favored at high pH. Failure to observe the pKa for the alpha-amines of cysteine and serine in the pKESB vs pH profile suggests a compensatory effect resulting from titration of a group on the enzyme with a pKa in the vicinity of the alpha-amine's pKa. The pH dependence of the first-order rate constant for decay of the alpha-aminoacrylate intermediate to give pyruvate and ammonia gives a pKa of about 9 for the active site lysine (K41), a pH unit higher than that of the A-isozyme. The difference in pH dependence of the pKESB for cysteine and serine, the higher pKa for K41, and the preference for the neutral species at high pH compared to the A-isozyme can be explained by titration of C280 to give the thiolate. Subtle conformational differences between O-acetylserine sulfhydrylase A and O-acetylserine sulfhydrylase B are detected by comparing the absorption and emission spectra of the internal aldimine in the absence and presence of the product acetate and of the external aldimine with l-serine. The two isozymes show a different equilibrium distribution of the enolimine and ketoenamine tautomers, likely as a result of a more polar active site for O-acetylserine sulfhydrylase B. The distribution of cofactor tautomers is dramatically affected by the ligation state of the enzyme. In the presence of acetate, which occupies the alpha-carboxylate subsite, the equilibrium between tautomers is shifted toward the ketoenamine tautomer, as a result of a conformational change affecting the structure of the active site. This finding, in agreement with structural data, suggests for the O-acetylserine sulfhydrylase B-isozyme a higher degree of conformational flexibility linked to catalysis.     

Anaerobic Hydrogen Production from Sucrose Using an Acid‐Enriched Sewage Sludge Microflora

A novel and high‐rate anaerobic sequencing bath reactor (ASBR) process was used to evaluate the hydrogen productivity of an acid‐enriched sewage sludge microflora at a temperature of 35 °C. In this ASBR process a 4 h cycle, including feed, reaction, settle, and decant steps, was repeatedly performed in a 5 L reactor. The sucrose substrate concentration was 20 g COD/L; the hydraulic retention time (HRT) was maintained at 12–120 h at the initial period and thereafter at 4–12 h. The reaction/settle period ratio, which is the most important parameter for ASBR operation was 1.7. The experimental results indicated that the hydrogenic activity of the sludge microflora was HRT‐dependent and that proper pH control was necessary for a stable operation of the bioreactor. The peak hydrogenic activity value was attained at an HRT of 8 h and an organic loading rate of 80 kg COD/m³ × day. Each mole of sucrose in the reactor produced 2.8 mol of hydrogen and each gram of biomass produced 39 mmol of hydrogen per day. An overly‐short HRT might deteriorate the hydrogen productivity. The concentration ratios of butyric acid to’acetic acid, as well as volatile fatty acid and soluble microbial products to alkalinity can be used as monitoring indicators for the hydrogenic bioreactor.     

Oscillatory behavior of Saccharomyces cerevisiae in continuous culture: I. Effects of pH and nitrogen levels

The appearance of sustained oscillations in bioreactor variables (biomass and nutrient concentrations) in continuous cultures of Saccharomyces cerevisiae indicates the complex nature of microbial systems, the inadequacy of current growth kinetic models, and the difficulties which may arise in bioprocess control and optimization. In this study we investigate continuous bioreactor behavior over a range of operating conditions (dilution rate, feed glucose concentration, feed ammonium concentration, dissolved oxygen, and pH) to determine the process requirements which lead to oscillatory behavior. We present new results which indicate that high feed ammonium concentrations may eliminate oscillations and that under oscillatory conditions ammonium levels are generally low and oscillatory as well. The effects of pH are complex and oscillations were only observed at pH values 5.5 and 6.5; no oscillations were observed at a pH of 4.5. Under our nominal operating conditions (feed glucose concentration 10 g/L, dilution rate 0.145 h(-1), feed ammonium concentration 0.0303M, dissolved oxygen level 50%, pH 5.5, and T = 30 degrees C) we found two possible final bioreactor states depending on the transient used to reach the nominal operating conditions. One of the states was oscillatory and characteristic of oxidative metabolism and the other was nonoscillatory and fermentative.     

The snowball effect in fed-batch bioreactions

The bioreactor will play an important role in future biological manufacturing. For economic profit, important profiles of the feed rate in fed-batch cultures have been discussed. Unfortunately, the optimal feed rate is less robust. In these studies there exists the snowball effect in a substrate-inhibited bioprocess, in which substrate is accumulated due to uncertain parameters in the model or feed-rate error. The snowball effect also exists in multi-substrate-limited processes. In further studies, the interaction between the substrates has been higher in essential substrates than in growth-enhancing substrates. In a typical fed-batch bioreactor, the amount of the product can be reduced to 1% or less when the snowball effect arises. A new control structure, i.e., an off-line optimized feedforward controller added to a gain-scheduling PI(2)D feedback controller, is proposed to eliminate the troublesome snowball effect. The proposed control strategy recovers the yield up to 95%. Moreover, the robustness of the proposed control structure is demonstrated by simulation.     

Purification and characterization of polyphenol oxidase from nettle (Urtica dioica L.) and inhibitory effects of some chemicals on enzyme activity

Polyphenol oxidase (PPO) of nettle (Urtica dioica L.) was extracted and purified through (NH4)2SO4 precipitation, dialysis, and CM-Sephadex ion-exchange chromatography and was used for its characterization. The PPO showed activity to catechol, 4-methylcatechol, L-3,4-dihydroxyphenylalanine (L-DOPA), L-tyrosine, p-cresol, pyrogallol, catechin and trans-cinnamic acid. For each of these eight substrates, optimum conditions such as pH and temperature were determined and L-tyrosine was found to be one of the most suitable substrates. Optimum pH and temperature were found at pH 4.5 and 30 degrees C respectively and Km and Vmax values were 7.90 x 10(-4) M, and 11290 EU/mL for with L-tyrosine as substrate. The inhibitory effect of several inhibitors, L-cysteine chloride, sodium azide, sodium cyanide, benzoic acid, salicylic acid, L-ascorbic acid, glutathione, thiourea, sodium diethyl dithiocarbamate, beta-mercaptoethanol and sodium metabisulfite were tested. The most effective was found to be sodium diethyl dithiocarbamate which acted as a competitive inhibitor with a Ki value of 1.79 x 10(-9)M. In addition one isoenzyme of PPO was detected by native polacrylamide slab gel electrophoresis.     

Cloning, overexpression, purification, and characterization of O-acetylserine sulfhydrylase-B from Escherichia coli

O-Acetylserine sulfhydrylase-B (OASS-B, EC 2.5.1.47) is one of the two isozymes produced by Escherichia coli that catalyze the synthesis of L-cysteine from O-acetyl-L-serine and sulfide. The cysM gene encoding OASS-B was cloned and the enzyme was overexpressed in E. coli using pUC19 with a lacUV5 promoter. The enzyme was purified to homogeneity, as evidenced by SDS-PAGE. Approximately 300 mg of purified OASS-B was obtained from 1600 mL of culture broth with a purification yield of 60% or higher. The purified OASS-B was characterized and its properties compared with OASS-A. OASS-B did not form a complex with E. coli serine acetyltransferase (SAT, EC 2.3.1.30) and showed a wide range of substrate specificity in nonproteinaceous amino acid synthesis.     

Subcellular Location of O-Acetylserine Sulfhydrylase Isoenzymes in Cell Cultures and Plant Tissues of Datura innoxia Mill

O-Acetylserine sulfhydrylase (OASS; EC 4.2.99.8) catalyzes the formation of L-cysteine from O-acetylserine and inorganic sulfide. Three OASS isoenzymes that differ in molecular mass and subunit structure are present in shoot and root tissues and in cadmium-resistant and cadmium-susceptible cell cultures of Datura innoxia Mill. Different OASS forms predominate in leaves, roots, and suspension-cell cultures. To determine the subcellular location of the OASS isoenzymes, purified mitochondria, chloroplasts, and cytosolic fractions from protoplasts were obtained. The isoenzymes are compartmentalized in D. innoxia cells, with a different isoenzyme predominant in the chloroplast, cytosol, and mitochondria, suggesting that they serve different functions in the plant cell. The chloroplast form is most abundant in green leaves and leaf protoplasts. The cytosolic form is most abundant in roots and cell cultures. A mitochondrial form is abundant in cell cultures, but is a minor form in leaves or roots. Cadmium-tolerant cell cultures contain 1.8 times as much constitutive OASS activity as the wild-type cell line, and 2.9 times more than the cadmium-hypersensitive cell line. This may facilitate rapid production of glutathione and metal-binding phytochelatins when these cultures are exposed to cadmium.     

Analysis and control of proteolysis of a fusion protein in Pichia pastoris fed-batch processes

A fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A and lipase B from Candida antarctica (CALB), was produced by Pichia pastoris Mut(+) in high-cell density bioreactor cultures. The production was induced by switching from growth on glycerol to growth on methanol. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 1.3 g x l(-1) of CBM-CALB. However, only about 40% of the product was of full-length according to Western blot analysis. This loss was due to a cleavage of the protein in the linker between the CBM and the CALB moieties. The cleavage was catalyzed by serine proteases in the culture supernatant. The CALB-moiety was subjected to further slow degradation by cell-associated proteolysis. Different strategies were used to reduce the proteolysis. Previous efforts to shorten the linker region resulted in a stable protein but with ten times reduced product concentration in bioreactor cultures (Gustavsson et al. 2001, Protein Eng. 14, 711-715). Addition of rich medium for protease substrate competition had no effect on the proteolysis of CBM-CALB. The kinetics for the proteolytic reactions, with and without presence of cells were shown to be influenced by pH. The fastest reaction, cleavage in the linker, was substantially reduced at pH values below 5.0. Decreasing the pH from 5.0 to 4.0 in bioreactor cultures resulted in an increase of the fraction of full-length product from 40 to 90%. Further improvement was achieved by decreasing the temperature from 30 to 22 degrees C during the methanol feed phase. By combining the optimal pH and the low temperature almost all product (1.5 g x l(-1)) was obtained as full-length protein with a considerably higher purity in the culture supernatant compared with the original cultivation.     

A comparative study of gel entrapped and membrane attached microbial reactors for biodegrading phenol

A comparative study between two reactors, one using microorganisms entrapped in calcium alginate gel, and the other using microorganisms attached on the surface of a membrane (polymeric microporous sheeting, MPS^TM) to biodegrade phenol is performed. Results indicate that the alginate bead bioreactor is efficient at higher phenol concentrations while the membrane bioreactor shows better performance at lower phenol concentrations. This unique response is primarily attributed to the different techniques by which the microorganisms are immobilized in the two reactors.In batch mode, below a starting concentration of 100 ppm phenol, biodegradation rates in the membrane bioreactor are (7.58 to 12.02 mg phenol/h · g dry biomass) atleast 10 times the rates in alginate bead bioreactor (0.74 to 1.32 mg phenol/h · g dry biomass). Biodegradation rates for the two reactors match at a starting concentration of 250 ppm phenol. Above 500 ppm phenol, the rates in the alginate bead bioreactor are (7.3 to 8.1 mg phenol/h · g dry biomass) on an average 5.5 times the corresponding rates in the membrane bioreactor (2.18 to 1.03 mg phenol/h · g dry biomass).In continuous feed mode the steady state degradation rates in the membrane bioreactor are one to two orders of magnitude higher than the alginate bead bioreactor below 150 ppm inlet phenol concentration. At an inlet concentration around 250 ppm phenol the rates are comparable. Above 500 ppm of phenol the rates in the alginate bioreactor are an order of magnitude high than the membrane bioreactor.Due to substrate inhibition, and its inability to sustain a high biomass concentration, the membrane bioreactor shows poor efficiencies at phenol concentrations above 250 ppm. At low phenol concentrations the apparent reaction rates in the alginate bead bioreactor decrease due to the diffusional resistance of the gel matrix, while biodegradation rates in the membrane bioreactor remain high due to essentially no external diffusional resistance.Results indicate that a combined reactor system can be more effective for bioremediation than either separate or attached microbial reactors.     

Long-term Continuous Production of Monoclonal Antibody by Hybridoma Cells Immobilized in a Fibrous-Bed Bioreactor

The kinetics and long-term stability of continuous production of monoclonal antibody IgG2b by hybridoma HD-24 cells immobilized in a fibrous-bed bioreactor (FBB) were studied for a period of ～8 months. The cells were immobilized in the fibrous bed by surface attachment of cells and entrapment of large cell clumps in the void space of the fibrous matrix. A high viable cell density of 1.01 × 10⁸/ml was attained in the bioreactor, which was about 63 times higher than those in conventional T-flask and spinner flask cultures. The continuous FBB produced IgG at a concentration of ～0.5 g/l, with reactor productivity of ～7 mg/h·l, which was about 23 times higher than those from conventional T-flask and spinner flask cultures. The IgG concentration can be further increased to ～0.67 g/l by using higher feed (glucose and glutamine) concentrations and running the reactor at a recycle batch or fed-batch mode. The long-term performance of this bioreactor was also evaluated. For a period of 36 days monitored, the MAb produced in the continuous well-mixed bioreactor at 50 h retention time (0.02/h dilution rate) was maintained at a steady concentration level of ～0.3 g/l with less than 8% drift. At the end of the study, it was found that ～25% of the cells were strongly attached to the fiber surfaces and the other ～75% entrapped or weakly immobilized in the fibrous matrix. The strongly attached cells had a high viability of ～90%, compared to ～75% for cells weakly immobilized and only ～1.4% for freely suspended cells, suggesting that the fibrous matrix preferentially retained and protected the viable (productive) cells. The FBB thus was able to maintain its long-term productivity because nonviable and dead cells were continuously washed off from the fibrous matrix. The high MAb concentration and production rate and excellent stability for continuous long-term production obtained in this study compare favorably to other bioreactor studies reported in the literature. The reactor performance can be further improved by providing better pH and aeration controls at higher feed concentrations. The FBB is easy to operate and scale-up, and thus can be used economically for industrial production of MAb.