Biodesulfurization of dibenzothiophene by a newly isolated Rhodococcus erythropolis strain

A new dibenzothiophene (DBT) desulfurizing bacterium was isolated from oil-contaminated soils in Iran. HPLC analysis and PCR-based detection of the presence of the DBT desulfurization genes (dszA, dszB and dszC) indicate that this strain converts DBT to 2-hydroxybiphenyl (2-HBP) via the 4S pathway. The strain, identified as Rhodococcus erythropolis SHT87, can utilize DBT, dibenzothiophene sulfone, thiophene, 2-methylthiophene and dimethylsulfoxide as a sole sulfur source for growth at 30 °C.The maximum specific desulfurization activity of strain SHT87 resting cells in aqueous and biphasic organic–aqueous systems at 30 °C was determined to be 0.36 and 0.47 μmol 2-HBP min⁻¹ (g dry cell)⁻¹, respectively. Three mM DBT was completely metabolized by SHT87 resting cells in the aqueous and biphasic systems within 10 h. The rate and the extent of the desulfurization reaction by strain SHT87 suggest that this strain can be used for the biodesulfurization of diesel oils.     

Optimization of the copy number of dibenzothiophene desulfurizing genes to increase the desulfurization activity of recombinant Rhodococcus sp.

Dibenzothiophene (DBT) degradation activity of recombinant Rhodococcus sp. T09/pRKPP was increased by about 3.5-fold by introduction of the NAD(P)H/FMN oxidoreductase gene (dszD), while DBT desulfurization activity remained the same with production of dibenzo[1,2]oxathiin-6-oxide, which was caused by insufficient activity of the last desulfurization step involving a desulfinase. Introduction of an additional dsz operon resulted in a 3.3-fold increase DBT desulfurization activity (31 mol g dry cell^–1 h^–1) compared with that of T09/pRKPP (9.5 mol g dry cell^–1 h^–1). Furthermore, optimization of DBT at 25 mg l^–1 and glucose at 10 g l^–1, increased the total DBT desulfurization activity 2- to 3-fold due to increases in the DBT desulfurizing specific activity and the final cell concentration.     

Combining co-culturing of Paenibacillus strains and Vitreoscilla hemoglobin expression as a strategy to improve biodesulfurization

Enhancement of the desulfurization activities of Paenibacillus strains 32O-W and 32O-Y were investigated using dibenzothiophene (DBT) and DBT sulfone (DBTS) as sources of sulphur in growth experiments. Strains 32O-W, 32O-Y and their co-culture (32O-W plus 32O-Y), and Vitreoscilla hemoglobin (VHb) expressing recombinant strain 32O-Yvgb and its co-culture with strain 32O-W were grown at varying concentrations (0·1–2 mmol l⁻¹) of DBT or DBTS for 96 h, and desulfurization measured by production of 2-hydroxybiphenyl (2-HBP) and disappearance of DBT or DBTS. Of the four cultures grown with DBT as sulphur source, the best growth occurred for the 32O-Yvgb plus 32O-W co-culture at 0·1 and 0·5 mmol l⁻¹ DBT. Although the presence of vgb provided no consistent advantage regarding growth on DBTS, strain 32O-W, as predicted by previous work, was shown to contain a partial 4S desulfurization pathway allowing it to metabolize this 4S pathway intermediate.     

Desulfurization of dibenzothiophene by lyophilized cells of Pseudomonas delafieldii R-8 in the presence of dodecane

Several parameters that influence the dibenzothiophene (DBT) desulfurization by lyophilized cells of Pseudomonas delafieldii R-8 were studied in the presence of dodecane. The aqueous media tested with pH range in 4.6–8.5 made no obvious difference on the desulfurization activity. The rate and extent of desulfurization were strongly dependent on the volume ratio of oil-to-water, DBT concentration and the cell concentration. The specific desulfurization rate of DBT and 4,6-dimethyl DBT (4,6-DMDBT) could reach 11.4 and 9.4 mmol sulfur kg⁻¹ dry cells (DCW) h⁻¹, respectively. The desulfurization pattern of DBT was represented by the Michaelis–Menten equation. The kinetic parameters, the limiting maximal velocity (V_max) and Michaelis constant (K_m), for desulfurization of DBT were calculated.     

Evidence for the role of zinc on the performance of dibenzothiophene desulfurization by <Emphasis Type="Italic">Gordonia alkanivorans</Emphasis> strain 1B

Gordonia alkanivorans strain 1B is able to desulfurize dibenzothiophene (DBT) to 2-hydroxybiphenyl (2-HBP), the final product of the 4S pathway. However, both the cell growth and the rate of desulfurization can be largely affected by the nutrient composition of the growth medium due to cofactor requirements of many enzymes involved in the biochemical pathways. In this work, the effect of several metal ions on the growth and DBT desulfurization by G. alkanivorans was studied. From all the metal ions tested, only the absence of zinc significantly affected the cell growth and the desulfurization rate. By increasing the concentration of Zn from 1 to 10 mg L⁻¹, 2-HBP productivity was improved by 26%. The absence of Zn²⁺, when sulfate was also used as the only sulfur source, did not cause any difference in the bacterial growth. Resting cells grown in the presence of Zn²⁺ exhibited a 2-HBP specific productivity of 2.29 μmol g⁻¹ (DCW) h⁻¹, 7.6-fold higher than the specific productivity obtained by resting cells grown in the absence of Zn²⁺ (0.30 μmol g⁻¹ (DCW) h⁻¹). These data suggests that zinc might have a key physiological role in the metabolism of DBT desulfurization.     

Elucidation of 2-hydroxybiphenyl effect on dibenzothiophene desulfurization by Microbacterium sp. strain ZD-M2

The effect of 2-hydroxybiphenyl (2-HBP), the end product of dibenzothiophene (DBT) desulfurization via 4S pathway, on cell growth and desulfurization activity was investigated by Microbacterium sp. The experimental results indicate that 2-HBP would inhibit the desulfurization activity. Providing 2-HBP was added in the reaction media, the DBT degradation rate decreased along with the increase of 2-HBP addition. By contrast, cell growth would be promoted in the addition of 2-HBP at a low concentration (<0.1mM). At high concentration of 2-HBP, the inhibition on the cell growth occurred. Meanwhile, the inhibitory effect of 2-HBP on DBT desulfurization activity was tested both in the oil/aqueous two-phase system and the aqueous system. A mathematical model was developed to explain the product formation kinetics with DBT as the sole sulfur source. The predicted results were close to the experimental data, it elucidated that along with the 2-HBP accumulation, the inhibitory effect of 2-HBP on DBT desulfurization and cell growth was enhanced.     

Proteomics and Metabolomics Analyses to Elucidate the Desulfurization Pathway of Chelatococcus sp.

Desulfurization of dibenzothiophene (DBT) and alkylated DBT derivatives present in transport fuel through specific cleavage of carbon-sulfur (C-S) bonds by a newly isolated bacterium Chelatococcus sp. is reported for the first time. Gas chromatography-mass spectrometry (GC-MS) analysis of the products of DBT degradation by Chelatococcus sp. showed the transient formation of 2-hydroxybiphenyl (2-HBP) which was subsequently converted to 2-methoxybiphenyl (2-MBP) by methylation at the hydroxyl group of 2-HBP. The relative ratio of 2-HBP and 2-MBP formed after 96 h of bacterial growth was determined at 4:1 suggesting partial conversion of 2-HBP or rapid degradation of 2-MBP. Nevertheless, the enzyme involved in this conversion process remains to be identified. This production of 2-MBP rather than 2-HBP from DBT desulfurization has a significant metabolic advantage for enhancing the growth and sulfur utilization from DBT by Chelatococcus sp. and it also reduces the environmental pollution by 2-HBP. Furthermore, desulfurization of DBT derivatives such as 4-M-DBT and 4, 6-DM-DBT by Chelatococcus sp. resulted in formation of 2-hydroxy-3-methyl-biphenyl and 2-hydroxy –3, 3^/- dimethyl-biphenyl, respectively as end product. The GC and X-ray fluorescence studies revealed that Chelatococcus sp. after 24 h of treatment at 37°C reduced the total sulfur content of diesel fuel by 12% by per gram resting cells, without compromising the quality of fuel. The LC-MS/MS analysis of tryptic digested intracellular proteins of Chelatococcus sp. when grown in DBT demonstrated the biosynthesis of 4S pathway desulfurizing enzymes viz. monoxygenases (DszC, DszA), desulfinase (DszB), and an NADH-dependent flavin reductase (DszD). Besides, several other intracellular proteins of Chelatococcus sp. having diverse biological functions were also identified by LC-MS/MS analysis. Many of these enzymes are directly involved with desulfurization process whereas the other enzymes/proteins support growth of bacteria at an expense of DBT. These combined results suggest that Chelatococcus sp. prefers sulfur-specific extended 4S pathway for deep-desulphurization which may have an advantage for its intended future application as a promising biodesulfurizing agent.     

Cultivation of a desulfurizing bacterium, Mycobacterium strain G3

Various carbon and sulfur sources on the growth and desulfurization activity of Mycobacterium strain G3, which is a dibenzothiophene (DBT)-degrading microorganism, were studied. Ethanol, glucose or glycerol as the sole carbon source and MgSO₄, taurine or dimethyl sulfoxide (DMSO) as the sole sulfur source were suitable for the growth. In addition, desulfurization activity was expressed in medium containing taurine, MgSO₄ or DMSO at 0.1 mM, when 217 mM ethanol was used as the sole carbon source. The highest desulfurization activity was in the stationary phase cells after 5 days' growth, rather than those harvested during active growth, when Mycobacterium G3 was cultivated in medium containing 217 mM ethanol and 0.1 mM MgSO₄. Thus alternative sulfur sources to DBT can be used for the cultivation of this desulfurizing microorganism.     

Biodesulfurization of dibenzothiophene by growing cells of Gordonia sp. in batch cultures

A new isolate, identified as Gordonia sp. ZD-7 by 16S rDNA sequence analysis, grew in n-hexadecane containing dibenzothiophene (DBT) which was degraded from 2.8 mM to 0.2 mM within 48 h. Biodesulfurization could be repeatedly performed for more than 190 h, with average desulfurization rates of 5 mmol DBT kg cells (dry wt)⁻¹ h⁻¹.     

Production of vitamin B12 in an upflow anaerobic filter continuous reactor using Acetobacterium sp.

The accumulation of biofilm by Acetobacterium sp. during continuous culture in an upflow anaerobic filter (UAF) growing on methanol-formate was the result of space velocity and inlet concentrations of substrate and Co⁺². To achieve good development of biofilm, a space velocity of 0.38 h^–1, inlet substrate concentrations of 125 mM of both methanol and formate, and Co⁺² at 0.16 mM were required. Cell productivities in the effluent of the UAF-reactor were about 6-fold higher than in chemostat cultures (0.20 g l^–1 h^–1 for UAF and 0.035 g l^–1 h^–1 for chemostat) (previous studies), and the maximum vitamin B₁₂ specific concentration was 5.1 mg g cell^–1.     

β-carotene production from soap stock by loofa-immobilized Rhodotorula rubra in an airlift photobioreactor

In this study, the soap stock as a sole carbon source was used for growing a carotenoid producing yeast (Rhodotorula rubra). The application of soap stock resulted in increase of carotenoids yield up to 5.36 folds when compared with the grown cultures on glucose. On the best Monod equation fitted on the specific growth rate (μ) data, the maximum specific growth rate (μ_m) and half-saturation concentration (K_S) were respectively determined at 0.064 h⁻¹ and 3.26 g L⁻¹ for total fatty acids presented in soap stock. Further tests on the carotenogenesis process were carried out in a cell-immobilized airlift photobioreactor where the natural loofa sponge was used for immobilization of the cells. The performance of the bioreactor was statistically studied by the response surface methodology (RSM) where aeration rate of 0.11 vvm and light irradiation intensity of 2517 Lx provided an optimum condition for producing β-carotene with a specific production rate of 22.65 mg g_cell⁻¹ day⁻¹.     

Desulfurization of model and diesel oils by resting cells of Gordona sp.

The desulfurization activity of the resting cells of Gordona sp. CYKS1 was strongly depended on harvest time and the highest value when the cells had been harvested in the early growth phase (0.12 mg sulfur g^–1 cell^–1 h^–1). For the model oil, hexadecane containing dibenzothiophene, the specific desulfurization rate decreased as the reaction proceeded. Both the specific and the volumetric desulfurization rates were not significantly affected by the aqueous-to-oil phase ratio. The diesel oils, light gas oil and a middle distillate unit feed were desulfurized at higher rates (ca. 0.34 mg sulfur g^–1 cell^–1 h^–1) than the model oil (0.12 mg sulfur g^–1 cell^–1 h^–1).     

Improvement of a mammalian cell culture process by adaptive,model-based dialysis fed-batch cultivation and suppression of apoptosis

Both conventional and genetic engineering techniques can significantly improve the performance of animal cell cultures for the large-scale production of pharmaceutical products. In this paper, the effect of such techniques on cell yield and antibody production of two NS0 cell lines is presented. On the one hand, the effect of fed-batch cultivation using dialysis is compared to cultivation without dialysis. Maximum cell density could be increased by a factor of ~5–7 by dialysis fed-batch cultivation. On the other hand, suppression of apoptosis in the NS0 cell line 6A1 bcl-2 resulted in a prolonged growth phase and a higher viability and maximum cell density in fed-batch cultivation in contrast to the control cell line 6A1 (100)3. These factors resulted in more product formation (by a factor ~2). Finally, the adaptive model-based OLFO controller, developed as a general tool for cell culture fed-batch processes, was able to control the fed-batch and dialysis fed-batch cultivations of both cell lines.Abbreviations A membrane area (dm²) - c _Glc,F glucose concentration in nutrient feed (mmol L^–1) - c _Glc,FD glucose concentration in dialysis feed (mmol L^–1) - c _Glc,i glucose concentration in inner reactor chamber (mmol L^–1) - c _Glc,o glucose concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Lac,FD lactate concentration in dialysis feed (mmol L^–1) - c _Lac,i lactate concentration in inner reactor chamber (mmol L^–1) - c _Lac,o lactate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _LS,FD limiting substrate concentration in dialysis feed (mmol L^–1) - c _LS,i limiting substrate concentration in inner reactor chamber (mmol L^–1) - c _LS,o limiting substrate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Mab monoclonal antibody concentration (mg L^–1) - F _D feed rate of dialysis feed (L h^–1) - F _Glc feed rate of nutrient concentrate feed (L h^–1) - K _d maximum death constant (h^–1) - k _d,LS death rate constant for limiting substrate (mmol L^–1) - k _Glc monod kinetic constant for glucose uptake (mmol L^–1) - k _Lac monod kinetic constant for lactate uptake (mmol L^–1) - k _LS monod kinetic constant for limiting substrate uptake (mmol L^–1) - K _Lys cell lysis constant (h^–1) - K _S,Glc monod kinetic constant for glucose (mmol L^–1) - K _S,LS monod kinetic constant for limiting substrate (mmol L^–1) - µ cell-specific growth rate (h^–1) - µ _d cell-specific death rate (h^–1) - µ _d,min minimum cell-specific death rate (h^–1) - µ _max maximum cell-specific growth rate (h^–1) - P _Glc membrane permeation coefficient for glucose (dm h^–1) - P _Lac membrane permeation coefficient for lactate (dm h^–1) - P _LS membrane permeation coefficient for limiting substrate (dm h^–1) - q _Glc cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Glc,max maximum cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Lac cell-specific lactate uptake/production rate (mmol cell^–1 h^–1) - q _Lac,max maximum cell-specific lactate uptake rate (mmol cell^–1 h^–1) - q _LS cell-specific limiting substrate uptake rate (mmol cell^–1 h^–1) - q _LS,max maximum cell-specific limiting substrate uptake rate (mmol cell ^–1 h^–1) - q _Mab cell-specific antibody production rate (mg cell^–1 h^–1) - q _MAb,max maximum cell-specific antibody production rate (mg cell^–1 h^–1) - t time (h) - V _i volume of inner reactor chamber (culture chamber) (L) - V _o volume of outer reactor chamber (dialysis chamber) (L) - X _t total cell concentration (cells L^–1) - X viable cell concentration (cells L^–1) - Y _Lac/Glc kinetic production constant (stoichiometric ratio of lactate production and glucose uptake) (–)     

Selective Desulfurization of Dibenzothiophene by Rhodococcus erythropolis D-1

A dibenzothiophene (DBT)-degrading bacterium, Rhodococcus erythropolis D-1, which utilized DBT as a sole source of sulfur, was isolated from soil. DBT was metabolized to 2-hydroxybiphenyl (2-HBP) by the strain, and 2-HBP was almost stoichiometrically accumulated as the dead-end metabolite of DBT degradation. DBT degradation by this strain was shown to proceed as DBT → DBT sulfone → 2-HBP. DBT at an initial concentration of 0.125 mM was completely degraded within 2 days of cultivation. DBT at up to 2.2 mM was rapidly degraded by resting cells within only 150 min. It was thought this strain had a higher DBT-desulfurizing ability than other microorganisms reported previously.     

Operon structure and functional analysis of the genes encoding thermophilic desulfurizing enzymes of Paenibacillus sp. A11-2

Paenibacillus A11-2 can efficiently cleave two carbon&bond;sulfur bonds in dibenzothiophene (DBT) and alkyl DBTs, which are refractory by conventional petroleum hydrodesulfurization, to remove sulfur atom at high temperatures. An 8.7-kb DNA fragment containing the genes for the DBT desulfurizing enzymes of A11-2 was cloned in Escherichia coli and characterized. Heterologous expression analysis of the deletion mutants identified three open reading frames that were required for the desulfurization of DBT to 2-hydroxybiphenyl (2-HBP). The three genes were designated tdsA, tdsB, and tdsC (for thermophilic desulfurization). Both the nucleotide sequences and the deduced amino acid sequences show significant homology to dszABC genes of Rhodococcus sp. IGTS8, but there are several local differences between them. Subclone analysis revealed that the product of tdsC oxidizes DBT to DBT-5,5'-dioxide via DBT-5-oxide, the product of tdsA converts DBT-5,5'-dioxide to 2-(2-hydroxyphenyl) benzene sulfinate, and the product of tdsB converts 2-(2-hydroxyphenyl)benzene sulfinate to 2-HBP. Cell-free extracts of a recombinant E. coli harboring all the three desulfurization genes converted DBT to 2-HBP at both 37 and 50 degrees C. In vivo and in vitro exhibition of desulfurization activity of the recombinant genes derived from a Paenibacillus indicates that an E. coli oxidoreductase can be functionally coupled with the monooxygenases of a gram-positive thermophile.     

Analysis of biodesulfurization of model oil system by the bacterium,strain RIPI-22

The execution of 4S process (sulfur-specific pathway) by growing cells of the newly isolated strain RIPI-22 and its resting cells in both aqueous reaction system and in two-phase system were investigated. The time for maximum desulfurization activity of the strain in resting state and in model oil system (hexadecane containing dibenzothiophene) was 7 h. Using taguchi design procedure the effects of cell density, pH and phase ratio on the desulfurization reaction were studied. The extent of desulfurization was hardly dependent on the pH where as the volume ratio of hydrocarbon-aqueous phase significantly affected the desulfurization activity.On the basis of the determined optimum desulfurizing conditions, the biodesulfurization pattern of DBT was studied and kinetic parameters were calculated.     

Alginate molecular mass produced by <Emphasis Type="Italic">Azotobacter vinelandii</Emphasis> in response to changes of the O<Subscript>2</Subscript> transfer rate in chemostat cultures

Alginate production by Azotobacter vinelandii growing in chemostat cultures was evaluated under different O₂ transfer rates (OTR). As a result of modifying the culture’s agitation rate from 300 to 500 rpm, the OTR increased from 9 to 15.1 mmol l⁻¹ h⁻¹ and a slight variation in the alginate production (1.7–2.2 g l⁻¹) was observed. At a constant growth rate (0.1 h⁻¹), the mean molecular mass of the alginate was strongly influenced by changes in the OTR, varying from 860 to 1,690 kDa. These results support a possible relationship between alginate polymerization-depolymerization process and the O₂ uptake rate.     

Nutrient uptake and alkaline phosphatase (ec 3:1:3:1) activity of emiliania huxleyi (PRYMNESIOPHYCEAE) during growth under n and p limitation in continuous cultures

Emiliania huxleyi (strain L) expressed an exceptional P assimilation capability. Under P limitation, the minimum cell P content was 2.6 fmol P·cell^?1, and cell N remained constant at all growth rates at 100 fmol N·cell^?1. Both, calcification of cells and the induction of the phosphate uptake system were inversely correlated with growth rate. The highest (cellular P based) maximum phosphate uptake rate (V_max^P) was 1400 times (i.e. 8.9 h^?1) higher than the actual uptake rate. The affinity of the P‐uptake system (dV/dS) was 19.8 L·μmol^?1·h^?1 at μ = 0.14 d^?1. This is the highest value ever reported for a phytoplankton species. V_max and dV/dS for phosphate uptake were 48% and 15% lower in the dark than in the light at the lowest growth rates. The half‐saturation constant for growth was 1.1 nM. The coefficient for luxury phosphate uptake (Q_maxt/Q_min) was 31. Under P limitation, E. huxleyi expressed two different types of alkaline phosphatase (APase) enzyme kinetics. One type was synthesized constitutively and possessed a V_max and half‐saturation constant of 43 fmol MFP·cell^?1·h^?1 and 1.9 μM, respectively. The other, inducible type of APase expressed its highest activity at the lowest growth rates, with a V_max and half‐saturation constant of 190 fmol MFP·cell^?1·h^?1 and 12.2 μM, respectively. Both APase systems were located in a lipid membrane close to the cell wall. Under N‐limiting growth conditions, the minimum N quotum was 43 fmol N·cell^?1. The highest value for the cell N‐specific maximum nitrate uptake rate (V_max^N) was 0.075 h^?1; for the affinity of nitrate uptake, 0.37 L·μmol^?1·h^?1. The uptake rate of nitrate in the dark was 70% lower than in the light. N‐limited cells were smaller than P‐limited cells and contained 50% less organic and inorganic carbon. In comparison with other algae, E. huxleyi is a poor competitor for nitrate under N limitation. As a consequence of its high affinity for inorganic phosphate, and the presence of two different types of APase in terms of kinetics, E. huxleyi is expected to perform well in P‐controlled ecosystems.     

Identification and functional analysis of the genes encoding dibenzothiophene-desulfurizing enzymes from thermophilic bacteria

Thermophilic bacteria Bacillus subtilis WU-S2B and Mycobacterium phlei WU-F1 desulfurize dibenzothiophene (DBT) and alkylated DBTs through specific cleavage of the carbon-sulfur bonds over a temperature range up to 52°C. In order to identify and functionally analyze the DBT-desulfurization genes, the gene cluster containing bdsA, bdsB, and bdsC was cloned from B. subtilis WU-S2B. The nucleotide and amino acid sequences of bdsABC show homologies to those of the other known DBT-desulfurization genes and enzymes; e.g. a nucleotide sequence homology of 61.0% to dszABC of the mesophilic bacterium Rhodococcus sp. IGTS8 and 57.8% to tdsABC of the thermophilic bacterium Paenibacillus sp. A11-2. Deletion and subcloning analysis of bdsABC revealed that the gene products of bdsC, bdsA and bdsB oxidized DBT to DBT sulfone (DBTO₂), converted DBTO₂ to 2-hydroxybiphenyl-2-sulfinate (HBPSi), and desulfurized HBPSi to 2-hydroxybiphenyl (2-HBP), respectively. Resting cells of a recombinant Escherichia coli JM109 harboring bdsABC converted DBT to 2-HBP over a temperature range of 30–52°C, indicating that the gene products of bdsABC were functional in the recombinant. The activities of DBT degradation at 50°C and DBT desulfurization (2-HBP production) at 40°C in resting cells of the recombinant were approximately five times and twice, respectively, as high as those in B. subtilis WU-S2B. The recombinant E. coli cells also degraded alkylated DBTs, such as 2,8-dimethylDBT and 4,6-dimethylDBT. The nucleotide sequences of B. subtilis WU-S2B bdsABC and the corresponding genes from M. phlei WU-F1 were found to be completely identical to each other although the strains are genetically different.     

EFFECTS OF NH4+ ASSIMILATION ON DARK CARBON FIXATION AND β-1,3-GLUCAN METABOLISM IN THE MARINE DIATOM SKELETONEMA COSTATUM (BACILLARIOPHYCEAE)

The effects of NH₄⁺ assimilation on dark carbon fixation and β-1,3-glucan metabolism in the N-limited marine diatom Skeletonema costatum (Grev.) Cleve (Bacillariophyceae) were investigated by chemical analysis of cell components and incorporation of ¹⁴C-bicarbonate. The diatom was grown in pH-regulated batch cultures with a 14:10 h LD cycle until N depletion. The cells were then incubated in the dark with ¹⁴C-bicarbonate, but without a source of N for 2 h, then in the dark with 63 μmol·L⁻¹ NH₄⁺ for 3 h. Without N, the cellular concentration of free amino acids was almost constant (∼4.5 fmol·cell⁻¹). Added NH₄⁺ was assimilated at a rate of 12 fmol·cell⁻¹·h⁻¹, and the cellular amino acid pool increased rapidly (doubled in <1 h, tripled in <3 h). The glutamine level increased steeply (45× within 3 h), and the Gln/ Glu ratio increased from 0.1 to 2.4 within 3 h. The rate of dark C fixation during N depletion was only 1.0 fmol·cell⁻¹·h⁻¹. The addition of NH₄⁺ strongly stimulated dark C fixation, leading to an assimilation rate of 4.0 fmol·cell⁻¹·h⁻¹, corresponding to a molar C/N uptake ratio of 0.33. Biochemical fractionation of organic ¹⁴C showed no significant ¹⁴C fixation into amino acids during N depletion, but during the first 1–2 h of NH₄⁺ assimilation, amino acids were rapidly radiolabeled, accounting for virtually all net ¹⁴C fixation. These results indicate that anaplerotic β-carboxylation is activated during NH₄⁺ assimilation to provide C₄ intermediates for amino acid biosynthesis. The level of cellular β-1,3-d-glucan was constant (16.5 pg·cell⁻¹) during N depletion, but NH₄⁺ assimilation activated a mobilization of 28% of the reserve glucan within 3 h. The results indicate that β-1,3-glucan in diatoms is the ultimate substrate for β-carboxylation, providing precursors for amino acid biosynthesis in addition to energy from respiration.