Algal biomass production,N uptake and N2 fixation in a synthetic medium

An experiment was conducted in the growth chamber to quantify the biomass production, N removal and N₂ fixation from a synthetic medium by Chlamydomonas reinhardtii and Anabaena flos-aquae. Nitrogen was supplied at a concentration of 100 mg liter⁻¹ of NO₃⁻−¹⁵N and NH₄⁺−¹⁵ (3·5 atom %), respectively. After 21 days Chlamydomonas reinhardtii removed an average of 83·8 and 78·7 mg N liter⁻¹ as NO₃⁻ and NH₄⁺, respectively. Averages of 0·89 and 0·71 g liter⁻¹ (first batch), 1·63 and 0·95 g liter⁻ (second batch) algal biomass were collected from NO₃⁻ and NH₄⁺ media, respectively. Uptake rates of 0·11 mg ¹⁵N g⁻¹ algae day⁻¹ from NO₃⁻ medium and 0·10 mg ¹⁵N g⁻¹ algae day⁻¹ from NH₄⁺ medium were calculated. Algal cells grown in NO₃⁻ and NH₄⁺ medium contained 71 and 65 g N kg⁻¹ (first batch), 39 and 58 g N kg⁻¹ (second batch), respectively. Anabaena flos-aquae produced averages of 0·58 and 0·46 g liter⁻¹ (first batch), 0·55 and 0·48 g liter⁻¹ (second batch) after 14 days of growth from NO₃⁻ and NH₄⁺ media, respectively. Blue-green algal biomass contained higher N (81–98 g kg⁻¹) than green algae. Isotope dilution method for determining N₂ fixation indicated that 55% and 77% of total N of blue-green algae grown in NO₃⁻ and NH₄⁺ media, respectively, was derived from the atmosphere.     

Fermentation of a wheat straw acid hydrolysate by Bacillus stearothermophilus T-13 in continuous culture with partial cell recycle

The effects of pretreatment by overliming and addition of nutrients (yeast extract, tryptone and ammonium chloride) on fermentation of mixed sugars derived by acid hydrolysis of the hemicellulose fraction of wheat straw with Bacilllus stearothermophilus strain T-13, an l-lactate dehydrogenase deficient mutant was investigated in continuous culture with partial cell recycle. Pretreatment and addition of nutrients to the hydrolysate improved the fermentation considerably. Sugar utilization, ethanol yields and productivities obtained in the treated hydrolysate with added nutrients were comparable to those obtained in a synthetic medium. Sugar utilization in the synthetic medium and treated and crude hydrolysates with added nutrients were 86%, 89% and 56%, respectively, compared with 45% in the treated hydrolysate without extra nutrients. Ethanol yields obtained were 0.32 g g⁻¹ sugars and 0.38 g g⁻¹ sugars in the treated hydrolysate with and without extra nutrients, respectively, compared with 0.24 g g⁻¹ sugars in the crude hydrolysate with added nutrients. Continuous culture with partial cell recycle significantly increased the rate of ethanol production (0.60–1.02 g litre⁻¹ h⁻¹) in the various media and the stability of the mutant strain compared with conventional continuous culture.     

Microbial production of squalene by a nicotinic acid-resistant mutant derived from Fusarium sp. no. 5-128B

A nicotinic acid-resistant mutant, designated NA201, was obtained from Fusarium sp. no. 5-128B by treatment with ultraviolet light. This mutant strain could grow in the presence of up to 500 mM nicotinic acid in the culture medium, although the parent strain could not grow at concentrations of nicotinic acid above 200 mM. The NA201 strain exhibited morphological mutations, neither forming aerial hyphae nor secreting a red-brown pigment. However, it retained the resistance to kabicidin at 25 mg l^−t of the parent strain. The mutant NA201 cells contained high levels of squalene and low levels of ergosterol, about 53 times higher and five to six times lower, respectively, than those of the parent strain under standard culture conditions. The volumetric oxygen transfer coefficient (Kd) affected the level of squalene in the mutant cells. The Kd for the maximum production of squalene by the mutant was 24 mmol O₂I⁻¹h⁻¹atm⁻¹ and the level of squalene in the mutant cells was 26 mg (g cell)⁻¹ on a dry weight basis. The greatest accumulation of squalene by the NA201 strain, corresponding to 323 mg per liter of culture medium and 35 mg (g cell)⁻¹ on a dry weight basis, was achieved in a culture in which the Kd was changed from a high to a low value on the third day, with the simultaneous addition of 3% glucose (w/v).     

Isolation of hexavalent chromium resistant bacteria from industrial saline effluents and their ability of bioaccumulation

The mixed cultures has been isolated from industrial saline wastewater contaminated with chromium(VI), using enrichment in the presence of 50 mg l⁻¹ chromium(VI) and 4% (w/v) NaCl at pH 8. In this study, the molasses (M) medium was selected a suitable medium for the effective chromium bioaccumulation by the mixed cultures. Eleven pure isolates obtained from mixed cultures and some of them showed high bioaccumulation in the M media containing about 100 mg l⁻¹ chromium(VI) and 4% NaCl. The strain 8 (99.3%) and 10 (99.1%) were able to bioaccumulate more efficient than the mixed culture (98.9%) in this media. But the highest specific Cr uptake was obtained by the mixed cultures followed by strain 8 and 10 with 56.71, 33.14 and 21.7 mg g⁻¹, respectively. Bioaccumulation of chromium(VI) ions by the strain 8 growing in the media with chromium(VI) and NaCl was studied in a batch system as a function of initial chromium(VI) (86.6–547.6 mg l⁻¹) and NaCl (0, 2, 4, 6% w/v) concentrations. During all the experiments, the uptake yield of the strain 8 was highly affected from NaCl concentrations in the medium at high initial chromium(VI) concentrations. But at low chromium(VI) concentration, strain 8 was not affected from NaCl concentrations in the medium. The maximum uptake yield were obtained in the M media with 2% NaCl as 98.8% for 110.0 mg l⁻¹, 98.6% for 217.1 mg l⁻¹, 98.6% for 381.7 mg l⁻¹ and 98.2% for 547.6 mg l⁻¹ initial chromium(VI) concentrations. The strain 8 tolerated a 6% (w/v) NaCl concentration was able to bioaccumulate more than 95% of the applied chromium(VI) at the 97.6–224.4 mg l⁻¹ initial chromium(VI) concentrations. The results presented in this paper was shown that these pure and mixed cultures might be of use for the bioaccumulation of chromium(VI) from saline wastewater.     

Influence of specific growth rate over the secretory expression of recombinant potato carboxypeptidase inhibitor in fed-batch cultures of Escherichia coli

A high cell density cultivation protocol was developed for the secretory production of potato carboxypeptidase inhibitor (PCI) in Escherichia coli. The strain BW25113 (pIMAM3) was cultured in fed-batch mode employing minimal media and an exponential feed profile where the specific growth rate was fixed by limitation of the fed carbon source (glycerol). Plasmid loss rates were found to be proportional to the specific growth rate. Distribution of PCI along the cell compartments and the culture media was also dependent on the fixed growth rate. When specific growth rate was kept at μ = 0.10 h⁻¹, 1.4 g PCI L⁻¹ were obtained when adding the product present in periplasmic extracts and supernatant fractions, with a 50% of the total expressed protein recovered from the extracellular medium. This constituted a 1.2-fold increase compared to growth at μ = 0.15 h⁻¹, and 2.0-fold compared to μ = 0.25 h⁻¹. Last, a cell permeabilization treatment with Triton X-100 and glycine was employed to direct most of the product to the culture media, achieving over 81% of extracellular PCI. Overall, our results point out that production yields of secretory proteins in fed-batch cultures of E. coli can be improved by means of process variables, with applications to the production of small disulfide-bridged proteins. Overall, our results point out that control of the specific growth rate is a successful strategy to improve the production yields of secretory expression in fed-batch cultures of E. coli, with applications to the production of small disulfide-bridged proteins.     

Factors affecting l-arginine production in the continuous culture of an l-arginine producer of Corynebacterium acetoacidophilum

The effects of culture conditions on l-arginine production by continuous culture were studied using a stable l-arginine hyperproducing strain of Corynebacterium aceto-acidophilum, SC-190. Strain SC-190 demonstrated a volumetric productivity of 35 g l⁻¹·h⁻¹ at a dilution rate of 0.083h⁻¹ and feeding sugar concentration of 8%, and a product yield of 29.2% at a dilution rate 0.021h⁻¹ and feeding sugar concentration of 15%. The corresponding values for fed-batch culture are 0.85 g·l⁻¹·h⁻¹ and 26%. However, the product yield decreased with an increase in the volumetric productivity. To achieve stable l-arginine production, aeration and agitation conditions sufficient to maintain an optimal level of redox potential (>−100 mV) were necessary. The addition of phosphate to the feeding medium led to a decrease in l-arginine production. It was confirmed in the steady state that growth and l-arginine formation were inhibited by a high concentration of l-arginine.     

Potential of the genetically transformed root cultures of Plumbago europaea for biomass and plumbagin production

Plumbago europaea L. is the main source of plumbagin which is a well-known pharmacological active compound. In this investigation, genetically transformed roots of P. europaea were obtained by improving some factors affecting the efficiency of Agrobacterium rhizoigenes-mediated transformation such as explant type, A. rhizoigenes strain, bacterial infection period, co-cultivation period and acetosyringone concentration. The leaf, hypocotyl and stem explants from in vitro grown plantlets were infected with bacterial strains (A4, ATCC15834, MSU440 and A13). The highest transformation rate of 69.3% was achieved after 7–9 days by inoculating A. rhizogenes MSU440 strain onto the 3-week-old stem explants followed by a co-cultivation period of 2 days on a medium containing 100 μM acetosyringone. To investigate the existence of the rolB gene, polymerase chain reaction was carried out using specific primers. Effects of growth media (MS, 1/2 MS, MS-B5 and ½ MS-B5), different sucrose concentrations and illumination on biomass production and plumbagin biosynthesis in P. europaea hairy root cultures were analyzed using stem explants after infection with MSU440 strain. ½ MS-B5 liquid medium containing 30 g L⁻¹ sucrose incubated in the dark resulted in the efficient biomass production of transformed hairy roots (12.5 g fresh weight, 1.8 g dry weight) with 3.2 mg g⁻¹ DW plumbagin accumulation. This procedure provides a framework for large-scale cultivation of hairy roots for plumbagin production. This is the first report describing the establishment of P. europaea hairy root culture with special emphasis on plumbagin production.     

Cascaded valorization of brown seaweed to produce l-lysine and value-added products using Corynebacterium glutamicum streamlined by systems metabolic engineering

Seaweeds emerge as promising third-generation renewable for sustainable bioproduction. In the present work, we valorized brown seaweed to produce l-lysine, the world's leading feed amino acid, using Corynebacterium glutamicum, which was streamlined by systems metabolic engineering. The mutant C. glutamicum SEA-1 served as a starting point for development because it produced small amounts of l-lysine from mannitol, a major seaweed sugar, because of the deletion of its arabitol repressor AtlR and its engineered l-lysine pathway. Starting from SEA-1, we systematically optimized the microbe to redirect excess NADH, formed on the sugar alcohol, towards NADPH, required for l-lysine synthesis. The mannitol dehydrogenase variant MtlD D75A, inspired by 3D protein homology modelling, partly generated NADPH during the oxidation of mannitol to fructose, leading to a 70% increased l-lysine yield in strain SEA-2C. Several rounds of strain engineering further increased NADPH supply and l-lysine production. The best strain, SEA-7, overexpressed the membrane-bound transhydrogenase pntAB together with codon-optimized gapN, encoding NADPH-dependent glyceraldehyde 3-phosphate dehydrogenase, and mak, encoding fructokinase. In a fed-batch process, SEA-7 produced 76 g L⁻¹ l-lysine from mannitol at a yield of 0.26 mol mol⁻¹ and a maximum productivity of 2.1 g L⁻¹ h⁻¹. Finally, SEA-7 was integrated into seaweed valorization cascades. Aqua-cultured Laminaria digitata, a major seaweed for commercial alginate, was extracted and hydrolyzed enzymatically, followed by recovery and clean-up of pure alginate gum. The residual sugar-based mixture was converted to l-lysine at a yield of 0.27 C-mol C-mol⁻¹ using SEA-7. Second, stems of the wild-harvested seaweed Durvillaea antarctica, obtained as waste during commercial processing of the blades for human consumption, were extracted using acid treatment. Fermentation of the hydrolysate using SEA-7 provided l-lysine at a yield of 0.40 C-mol C-mol⁻¹. Our findings enable improvement of the efficiency of seaweed biorefineries using tailor-made C. glutamicum strains.     

Simultaneous determination of hydroxocobalamin and its cyanide complex cyanocobalamin in human plasma by high-performance liquid chromatography application to pharmacokinetic studies after high-dose hydroxocobalamin as an antidote for severe cyanide poisoning

Hydroxocobalamin (OHCbl) is a powerful antidote for cyanide poisoning, via the formation of non-toxic cyanocobalamin (CNCbl). Plasmatic cobalamins were measured at 361 nm, after enrichment and purification on a short C₁₈ precolumn (1% acetic acid; 1 ml min⁻¹; 2 min), by back-flush elution on a C₁₈ ODS-2 column [0.1 M sodium dihydrogenphosphate-methanol (63:27, v/v) (pH 4.0); 0.80 ml min⁻¹]. The precision was 3.21 and 3.54% for 10 μM OHCbl and CNCbl, respectively. The method was used to study the pharmacokinetics of OHCbl and the formed CNCbl in severely poisoned patients.     

pspK acquisition contributes to the loss of capsule in pneumococci: molecular characterisation of non-encapsulated pneumococci

With the introduction of the pneumococcal conjugate vaccine (PCV), the number of cases of non-vaccine type pneumococci and non-encapsulated Streptococcus pneumoniae (NESp) infection have increased. In order to clarify how pspK-harbouring NESp might have emerged, we characterised NESp and analysed the correlation between transformation and non-encapsulation. A total of 26 NESp strains were used in this study. The genetic backgrounds were compared using multilocus sequence typing (MLST). The ΔpspK::ermB strain, in which pspK was replaced by ermB in NESp, was constructed by homologous recombination. The genomic DNA of the ΔpspK::ermB strain was transformed into two types of encapsulated S. pneumoniae via transformation. The fitness of the parent and non-encapsulated transformants was compared using the growth curve. All NESp had pspK instead of capsular coding regions and were classified into 14 types by MLST, which indicated that NESp had several genetic backgrounds. Transformation of ΔpspK::ermB genomic DNA resulted in 10⁻⁴‒10⁻⁵ non-encapsulated transformants. Non-encapsulated transformants could grow faster than the encapsulated parent strain. The acquisition of pspK region via transformation contributed to the loss of encapsulation with high frequency. The present results suggest that non-encapsulation through pspK acquisition could be a potential mechanism to evade PCV.     

Metabolic engineering of Clostridium acetobutylicum for butyric acid production with high butyric acid selectivity

A typical characteristic of the butyric acid-producing Clostridium is coproduction of both butyric and acetic acids. Increasing the butyric acid selectivity important for economical butyric acid production has been rather difficult in clostridia due to their complex metabolic pathways. In this work, Clostridium acetobutylicum was metabolically engineered for highly selective butyric acid production. For this purpose, the second butyrate kinase of C. acetobutylicum encoded by the bukII gene instead of butyrate kinase I encoded by the buk gene was employed. Furthermore, metabolic pathways were engineered to further enhance the NADH-driving force. Batch fermentation of the metabolically engineered C. acetobutylicum strain HCBEKW (pta⁻, buk⁻, ctfB⁻ and adhE1⁻) at pH 6.0 resulted in the production of 32.5 g/L of butyric acid with a butyric-to-acetic acid ratio (BA/AA ratio) of 31.3 g/g from 83.3 g/L of glucose. By further knocking out the hydA gene (encoding hydrogenase) in the HCBEKW strain, the butyric acid titer was not further improved in batch fermentation. However, the BA/AA ratio (28.5 g/g) obtained with the HYCBEKW strain (pta⁻, buk⁻, ctfB⁻, adhE1⁻ and hydA⁻) was 1.6 times higher than that (18.2 g/g) obtained with the HCBEKW strain at pH 5.0, while no improvement was observed at pH 6.0. These results suggested that the buk gene knockout was essential to get a high butyric acid selectivity to acetic acid in C. acetobutylicum.     

Li+ effect on the cell wall of the yeast Saccharomyces cerevisiae as probed by FT-IR spectroscopy

The effect of Li⁺ ions as a transformation inducing agent on the yeast cell wall has been studied. Two Saccharomyces cerevisiae strains, p63-DC5 with a native cell wall, and strain XCY42-30D(mnn1) which contains structural changes in the mannan-protein complex, were used. Fourier transform infrared (FT-IR) spectroscopy has been used for the characterization of the yeast strains and for determination of the effect of lithium cations on the cell wall. A comparison of the carbohydrate absorption band positions in the 970–1185 cm^?1 range, of Na⁺ and Li⁺ treated yeast cells has been estimated. Absorption band positions of the cell wall carbohydrates of p63-DC5 were not influenced by the studied ions. On the contrary, the treatment of XCY42-30D(mnn1) cells with Li⁺ ions shifted glucan band positions, implying that the cell wall structure of strain XCY42-30D(mnn1) is more sensitive to Li⁺ ion treatment.     

Effect of tannins on growth and amylase production by Calvatia gigantea

The effect of tannins was investigated on growth and α-amylase (α-1,4-glucan 4-glucanohydrolase, EC 3.2.1.1) production by the edible fungal species Calvatia gigantea, grown in a laboratory-scale fermenter on acorn starch media containing up to 2 g tannins l⁻¹. No inhibition of both growth and amylase excretion was observed when the fungus was cultivated on media containing 40 to 100 times higher tannin concentration than that reported to inhibit microbial growth. Amylase excretion was enhanced when starch was dry sterilized but specific growth rate was higher when starch was wet sterilized. Biomass and amylase production increased with increasing substrate concentration and specific growth rate reached its maximum value at 20 g l⁻¹ starch concentration. The optimum pH of biomass and amylase productionwas 5.0–5.5 and 6.0−6.5 respectively and that of temperature was 29–32 and 29–30°C respectively. Maximum yields of 68 250 U amylase and 0.58–0.60 g biomass g⁻¹ acorn were obtained at optimum growth conditions. A plot of reciprocal growth rate vs. reciprocal starch concentration made it possible to calculate K_s = 0.84 g acorn starch l⁻¹ and μ_max = 0.249 h⁻¹.     

Characterization of Tn5-induced symbiotically defective mutants of cowpea rhizobia

Symbiotically defective mutants of cowpea rhizobia strain IRC256 were isolated by random Tn5 mutagenesis and characterized. One auxotroph (MS1) requiring adenine and thiamine was a non-nodulating mutant (Nod⁻) and three prototrophic mutants were Nod⁺ Fix⁻ which formed small and ineffective nodules on cowpeas (Vigna unguiculata). Acetylene reduction activity of the Nod⁺ Fix⁻ mutants was reduced to 80–94% of that of the wild-type strain. The non-nodulating mutant (MS1) induced root-hair curling but did not show any nodule initiation or nodule development. Ultrastructural examination of nodules formed by Fix⁻ mutants showed that these contained few bacteroids, indicating either early senescence or a reduction in bacterial release into the cytoplasm of the host cell. DNA hybridization of total DNAs from a representative number of Tn5 mutants showed that each of them had one copy of the transposon Tn5 which was randomly inserted into the genome of cowpea rhizobia.     

One-pot production of d-allulose from inulin by a novel identified thermostable exoinulinase from Aspergillus piperis and Dorea sp. d-allulose 3-epimerase

Inulin has been widely used as a cheap bioresource for producing many valuable products by enzymatic hydrolysis or microbial fermentation, such as high-fructose syrup and fructooligosaccharides. In this work, a one-pot two-enzyme reaction system was developed to produce d-allulose from inulin using A. piperis exoinulinase and Dorea sp. d-Allulose 3-epimerase. The exoinulinase that was identified from Aspergillus piperis CBS 112811 was cloned and intracellularly expressed in Escherichia coli. The enzyme displayed the maximal activity as 3750 U mg⁻¹ at pH 6.0 and 55 °C. For the effects of different cations, Mn²⁺ simulated the enzyme activity by 41 %. When 10 g L⁻¹ inulin was hydrolyzed by A. piperis exoinulinase, the conversion rate reached 98 % within 6 h. Furthermore, the optimum pH, temperature and the ratio of the two enzymes loaded for one-pot reaction were measured to be pH 6.0, 60 °C and 15/15 U mL⁻¹, respectively. The conversion rate of inulin to d-allulose reached 23.3 % after reaction for 4 h with 10 g L⁻¹ inulin. When adding 100 g L⁻¹ as a substrate, 21.4 g L⁻¹ d-allulose was produced using the two-enzyme system.     

Immobilization of lipase in organic solvent in the presence of fatty acid additives

In this study porcine pancreatic lipase (PPL) was covalently immobilized on cross-linked polyvinyl alcohol (PVA) in organic media in the presence of fatty acid additives in order to improve its immobilized activity. The effects of fatty acid additions to the immobilization media were investigated choosing tributyrin hydrolysis in water and ester synthesis by immobilized PPL in n-hexane. Various fatty acids which are also the substrates of lipases in esterification reactions were used as active site protecting agents during the immobilization process in an organic solvent. The obtained results showed that covalent immobilization carried out in the presence of fatty acids as protective ligands improved the hydrolytic and esterification activity of immobilized enzyme. A remarkable increase in activity of the immobilized PPL was obtained when octanoic acid was used as an additive and the hydrolytic activity was increased from 5.2 to 19.2 μmol min⁻¹ mg⁻¹ as compared to the non-additive immobilization method. With the increase of hydrolytic activity of immobilized lipase in the presence of octanoic acid, in an analogous manner, the rate of esterification for the synthesis of butyl octanoate was also increased from 7.3 to 26.3 μmol min⁻¹ g⁻¹ immobilized protein using controlled thermodynamic water activities with saturated salt solutions. In addition, the immobilized PPL activity was maintained at levels representing 63% of its original activity value after 5 repeated uses. The proposed method could be adopted for a wide variety of other enzymes which have highly soluble substrates in organic solvent such as other lipases and esterases.     

Over expression of GroESL in Cupriavidus necator for heterotrophic and autotrophic isopropanol production

We previously reported a metabolic engineering strategy to develop an isopropanol producing strain of Cupriavidus necator leading to production of 3.4 g L⁻¹ isopropanol. In order to reach higher titers, isopropanol toxicity to the cells has to be considered. A toxic effect of isopropanol on the growth of C. necator has been indeed observed above a critical value of 15 g L⁻¹. GroESL chaperones were first searched and identified in the genome of C. necator. Native groEL and groES genes from C. necator were over-expressed in a strain deleted for PHA synthesis. We demonstrated that over-expressing groESL genes led to a better tolerance of the strain towards exogenous isopropanol. GroESL genes were then over-expressed within the best engineered isopropanol producing strain. A final isopropanol concentration of 9.8 g L⁻¹ was achieved in fed-batch culture on fructose as the sole carbon source (equivalent to 16 g L⁻¹ after taking into account evaporation). Cell viability was slightly improved by the chaperone over-expression, particularly at the end of the fermentation when the isopropanol concentration was the highest. Moreover, the strain over-expressing the chaperones showed higher enzyme activity levels of the 2 heterologous enzymes (acetoacetate carboxylase and alcohol dehydrogenase) of the isopropanol synthetic operon, translating to a higher specific production rate of isopropanol at the expense of the specific production rate of acetone. Over-expressing the native chaperones led to a 9–18% increase in the isopropanol yield on fructose.     

Enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by Flavobacterium sp.

An enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by the action of hydantoinase and carbamoylase has been investigated. A strain identified as (Flavobacterium) sp. I-3 isolated from soil was found to form l-tryptophan from dl-5-indolylmethylhydantoin. Cultural conditions for the formation of the l-tryptophan-forming activity were investigated, and the highest activity of 0.81 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth (hydantoinase, 3.6 μmol min⁻¹of N-carbamoyl-l-tryptophan formed per 1 ml of culture broth; carbamoylase, 0.92 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth) was obtained. These activities were found to be inducible and intracellular. Optimization of the parameters of the conversion reaction resulted in accumulation of 50 mg of l-tryptophan per 1 ml of cultural broth per day. The conversion yield from dl-5-indolylmethylhydantoin was about 100%. Accumulated l-tryptophan was readily isolated in pure form by ordinary procedures.     

Survivability of indigenous microflora and a Salmonella typhimurium marker strain in poultry mash treated with buffered propionic acid

Buffered propionic acid (BPA) was evaluated as a potential treatment for the elimination of Salmonella spp. in poultry mash. A primary poultry isolate marker strain of Salmonella typhimurium was added as either a broth or in a dry chalk carrier form to poultry mash containing soybean meal as a protein supplement. The mash was supplemented with buffered propionic acid at 2, 4, 6, 8, 10, 20, 30, 50 and 100 g kg⁻¹ diet and samples were enumerated for indigenous aerobic bacteria, fungi and the S. typhimurium marker strain. Total indigenous aerobic bacteria and fungal populations were generally decreased by addition of more than 20 g BPA kg⁻¹, but an addition of 100 g BPA kg⁻¹ mash was usually required to achieve reductions of approximately 90% of indigenous aerobic bacteria and 99% of indigenous fungi. After 7 days of storage, 8 g BPA kg⁻¹ mash also reduced S. typhimurium populations by more than 90% in mash inoculated via chalk, while at least 50 g BPA kg⁻¹ mash was required to provide the same level of reduction in mash inoculated with a liquid culture of S. typhimurium. Although BPA does not appear to be an overly effective antimicrobial agent with respect to indigenous aerobic bacterial populations in animal feed, higher concentrations may have the potential for reducing fungal and Salmonella spp. contamination in poultry mash.