Comparative studies of physiological and environmental effects on the production of cyclosporin A in suspended and immobilized cells of Tolypocladium inflatum

Process improvement of the production of cyclosporin A (Cy A), a powerful immunosuppressive fungal metabolite, has been undertaken by analyzing suspended and immobilized cell cultures in parallel. Conidiospores of the producer microorganism, Tolypocladium inflatum, were entrapped into porous celite particles. Easier germination of the entrapped spores and more active growth of the immobilized cells were manifested when compared with free cell cultures initiated with spores or with mycelial inocula. Significant differences in precursor flow between the immobilized and free cell systems were evident when the effects of L-valine (a constituent amino acid of the Cy A molecule) on Cy A biosynthesis were compared in the two systems. For the freely suspended cells, L-valine supplemented early in the fermentation served as a possible precursor or stimulator of Cy A biosynthesis. A significant increase in specific production and Cy A yield on carbon source was observed in this system relative to suspended cultures supplemented with L-valine during or after exponential growth. In contrast to the free cell cultures, the addition of L-valine during the initial stage of immobilized cell growth had a negative effect on Cy A production but resulted in somewhat increased cell growth. This suggests an incompatibility between primary and secondary metabolic networks involved in Cy A biosynthesis in the immobilized state upon external addition of the amino acid.     

Continuous rhamnolipid production using denitrifying Pseudomonas aeruginosa cells in hollow‐fiber bioreactor

Rhamnolipids are high‐value effective biosurfactants produced by Pseudomonas aeruginosa. Large‐scale production of rhamnolipids is still challenging especially under free‐cell aerobic conditions in which the highly foaming nature of the culture broth reduces the productivity of the process. Immobilized systems relying on oxygen as electron acceptor have been previously investigated but oxygen transfer limitation presents difficulties for continuous rhamnolipid production. A coupled system using immobilized cells and nitrate instead of oxygen as electron acceptor taking advantage of the ability of P. aeruginosa to perform nitrate respiration was evaluated. This denitrification‐based immobilized approach based on a hollow‐fiber setup eliminated the transfer limitation problems and was found suitable for continuous rhamnolipid production in a period longer than 1,500 h. It completely eliminated the foaming difficulties related to aerobic systems with a comparable specific productivity of 0.017 g/(g dry cells)‐h and allowed easy recovery of rhamnolipids from the cell‐free medium. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 346–351, 2013     

Effect of a Pseudomonas rhamnolipid biosurfactant on cell hydrophobicity and biodegradation of octadecane.

In this study, the effect of a purified rhamnolipid biosurfactant on the hydrophobicity of octadecane-degrading cells was investigated to determine whether differences in rates of octadecane biodegradation resulting from the addition of rhamnolipid to four strains of Pseudomonas aeruginosa could be related to measured differences in hydrophobicity. Cell hydrophobicity was determined by a modified bacterial adherence to hydrocarbon (BATH) assay. Bacterial adherence to hydrocarbon quantitates the preference of cell surfaces for the aqueous phase or the aqueous-hexadecane interface in a two-phase system of water and hexadecane. On the basis of octadecane biodegradation in the absence of rhamnolipid, the four bacterial strains were divided into two groups: the fast degraders (ATCC 15442 and ATCC 27853), which had high cell hydrophobicities (74 and 55% adherence to hexadecane, respectively), and the slow degraders (ATCC 9027 and NRRL 3198), which had low cell hydrophobicities (27 and 40%, respectively). Although in all cases rhamnolipid increased the aqueous dispersion of octadecane at least 10(4)-fold, at low rhamnolipid concentrations (0.6 mM), biodegradation by all four strains was initially inhibited for at least 100 h relative to controls. At high rhamnolipid concentrations (6 mM), biodegradation by the fast degraders was slightly inhibited relative to controls, but the biodegradation by the slow degraders was enhanced relative to controls. Measurement of cell hydrophobicity showed that rhamnolipids increased the cell hydrophobicity of the slow degraders but had no effect on the cell hydrophobicity of the fast degraders. The rate at which the cells became hydrophobic was found to depend on the rhamnolipid concentration and was directly related to the rate of octadecane biodegradation.(ABSTRACT TRUNCATED AT 250 WORDS)     

Taxol (paclitaxel) production using free and immobilized cells of Taxus cuspidata

The production characteristics for Taxol (paclitaxel) using free and immobilized cells of Taxus cuspidata were investigated in a perfusion culture bioreactor. Although the cell growth was inhibited by higher dilution rates, the specific production rate of Taxol was increased by perfusion compared with that using batch operation. Perfusion cultures using a nylon-mesh cell separator for free suspension cells showed similar production profiles to those obtained using immobilized cells. Continuous Taxol production was successfully obtained at an approximate specific production rate of 0.3 mg/g DCW (dry cell weight) per day for up to 40 days. (c) 1997 John Wiley & Sons, Inc.     

Enhanced hydrocarbon biodegradation by a newly isolated Bacillus subtilis strain

The relation between hydrocarbon degradation and biosurfactant (rhamnolipid) production by a new Bacillus subtilis 22BN strain was investigated. The strain was isolated for its capacity to utilize n-hexadecane and naphthalene and at the same time to produce surface-active compound at high concentrations (1.5 - 2.0 g l(-1)). Biosurfactant production was detected by surface tension lowering and emulsifying activity. The strain is a good degrader of both hydrocarbons used with degradability of 98.3 +/- 1% and 75 +/- 2% for n-hexadecane and naphthalene, respectively. Measurement of cell hydrophobicity showed that the combination of slightly soluble substrate and rhamnolipid developed higher hydrophobicity correlated with increased utilization of both hydrocarbon substrates. To our knowledge, this is the first report of Bacillus subtilis strain that degrades hydrophobic compounds and at the same time produces rhamnolipid biosurfactant.     

Immobilization of Escherichia coli JM103[pUC8] in kappa-carrageenan coupled with recombinant protein release by in situ cell membrane permeabilization.

Immobilization of Escherichia coli JM103[pUC8] was carried out with kappa-carrageenan as the support matrix. Substantial natural excretion of beta-lactamase, attributable to the less intact membrane of plasmid-harboring cells, was observed in immobilized cell cultures. Nevertheless, a significant portion of the beta-lactamase produced was retained in the cells. As compared to suspension cultures, much higher beta-lactamase activities, especially in the extracellular liquid, and much longer retention of plasmid-bearing cells (improved plasmid stability) were observed in immobilized cell cultures. Further enhancement in excretion of the recombinant protein (beta-lactamase) was achieved by permeabilization of cell membrane by periodic exposure of the immobilized cell cultures to ethylenediaminetetraacetic acid (EDTA). While the presence of EDTA led to some suppression of cell growth in suspension cultures, cell growth in gel beads was not affected by EDTA to the same extent, possibly due to lesser exposure of immobilized cells to EDTA. Exposure of immobilized cell cultures to EDTA presumably inhibited plasmid replication and led in turn to diversion of cellular resources for the support of expression of plasmid genes. Indeed, treatment of the immobilized cell cultures with EDTA resulted in increased production of beta-lactamase when compared to the enzyme production in EDTA-free cultures. More frequent addition of EDTA increased the period of retention of plasmid-bearing cells in these cultures but did not have any noticeable adverse effect on synthesis of beta-lactamase. Improvement in plasmid stability in EDTA-treated immobilized cell cultures was ascribed to the reduction in the growth rate differential between plasmid-free and plasmid-bearing cells, since plasmid-free cells were subject to more reduction in specific growth rate than were plasmid-bearing cells.     

The production of monoclonal antibody in growth-arrested hybridomas cultivated in suspension and immobilized modes.

The effects of the microenvironment and the nature of the limiting nutrient on culture viability and overall MAb productivity were explored using a hybridoma cell line which characteristically produces MAb in the stationary phase. A direct comparison was made of the changes in the metabolic profiles of suspension and PEG-alginate immobilized (0.8 mm beads) batch cultures upon entry into the stationary phase. The shifts in glucose, glutamine, and amino acid metabolism upon entry into the stationary phase were similar for both microenvironments. While the utilization of most nutrients in the stationary phase decreased to below 20% of that in the growth phase, antibody production was not dramatically affected. The immobilized culture did exhibit a 1.5-fold increase in the specific antibody rate over the suspension culture in both the growth and stationary phases. The role of limiting nutrient on MAb production and cell viability was assessed by artificially depleting a specific nutrient to 1% of its control concentration. An exponentially growing population of HB121 cells exposed to these various depletions responded with dramatically different viability profiles and MAb production kinetics. All depletions resulted in growth-arrested cultures and nongrowth-associated MAb production. Depletions in energy sources (glucose, glutamine) or essential amino acids (isoleucine) resulted in either poor viability or low antibody productivity. A phosphate or serum depletion maintained antibody production over at least a six day period with each resulting in a 3-fold higher antibody production rate than in growing batch cultures. These results were translated to a high-density perfusion culture of immobilized cells in the growth-arrested state with continued MAb expression for 20 days at a specific rate equal to that observed in the phosphate- and serum-depleted batch cultures.     

Effect of culture process on alkaloid production by Catharanthus roseus cells. II. Immobilized cultures.

Two processes for the production of indole alkaloids 2 l surface-immobilized bioreactor cultures of Catharanthus roseus cells using Zenk's Alkaloid Production Medium (APM) were evaluated. The 1-stage process consisted of inoculating APM containing bioreactors and incubating for 15 d. The 2-stage process involved inoculating growth medium-containing bioreactors, growing the immobilized cultures for a certain period of time and subsequently replacing this medium with APM. The production stage which lasted for 15 d. High production in 2-stage cultures required the replacement of the growth regulator 2,4-dichlorophenoxyacetic acid by indole-3-acetic acid in the growth medium and a growth stage of 6 d (late exponential phase) before production initiation. Growth, main nutrient consumption and alkaloid production were monitored. Both culture regimes resulted in similar biomass production, dw (10-13 g l-1). The 2-stage cultures yielded biomass richer in organic nutrients (200-300%) and with higher respiratory activity (approximately 250%), indicated by their lower biomass-to-carbohydrate yields (31% and 26%), as compared to 1-stage cultures (41%). Two-stage cultures produced more known products (10 as compared to 6) at yields (5 to 4800 micrograms g-1) 3 to 5 times higher than 1-stage cultures. More alkaloids were alkaloids released in the medium of 2-stage cultures, under non-lysing conditions, (20 to 4700 micrograms l-1) than in 1-stage cultures (20 to 460 micrograms l-1). These results were compared to those obtained from shake flask cultures performed at the same time, with the same C. roseus cell line and under similar regimes and reported previously. Suspension and immobilized cultures performed according to the 1-stage regime showed similar total production. However, release of known alkaloids was 2 to 3 times higher in immobilized than in suspension cultures. Total alkaloid production of 2-stage suspension cultures was 3.8-fold higher than 2-stage immobilized cultures. Two stage immobilized cultures released 4 more known alkaloids than the 2-stage suspensions. Lower oxygen availability in the 2 l immobilized cultures may explain lower specific growth rates (0.15-0.22 d-1) and total alkaloid production levels, compared to 200 ml suspension cultures (0.2-0.4 d-1) reported in our previous paper.     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Rhamnolipid production in batch and fed-batch fermentation using<Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> BYK-2 KCTC 18012P

The optimization of culture conditions for the bacteriumPseudomonas aeruginosa BYK-2 KCTC 18012P, was performed to increase its rhamnolipid production. The optimum level for carbon, nitrogen sources, temperature and pH, for rhamnolipid production in a flask, were identified as 25 g/L fish oil, 0.01% (w/v) urea, 25 and pH 7.0, respectively. Optimum conditions for batch culture, using a 7-L jar fermentor, were 200 rpm of agitation speed and a 2.0 L/min aeration rate. Under the optimum conditions, on fish oil for 216 h, the final cell and rhamnolipid concentrations were 5.3 g/L and 17.0 g/L respectively. Fed-batch fermentation, with different feeding conditions, was carried out in order to increase, cell growth and rhamnolipid production by thePseudomonas aeruginosa, BYK-2 KCTC 18012P. When 2.5 g of fish oil and 100 mL basal salts medium, containing 0.01% (w/v) urea, were fed intermittently during the fermentation, the final cell and rhamnolipid concentrations at 264 h, were 6.1 and 22.7 g/L respectively. The fed-batch culture resulted in a 1.2-fold increase in the dry cell mass and a 1.3-fold increase in rhamnolipid production, compared to the production of the batch culture. The rhamnolipid production-substrate conversion factor (0.75 g/g) was higher than that of the batch culture (0.68 g/g).     

Production of monoclonal antibody using free-suspended and immobilized hybridoma cells: Effect of serum

The effect of serum on cell growth and monoclonal antibody (MAb) productivity was studied in a repeated fedbatch mode using both free-suspended and immobilized S3H5/gamma2bA2 hybridoma cells. In the suspension culture, serum influenced the cell growth rate but not the specific MAb productivity. The average specific growth rate of the suspension culture in medium containing 10% serum was approximately 0.99 +/- 0.12 day(-1) (+/-standard deviation), while that in medium containing 1% serum was approximately 0.73 +/- 0.12 day(-1). The specific MAb productivity was almost constant at 3.69 +/- 0.57 mug/10(6) cells/day irrespective of serum concentration reached a maximum at ca. 1.8 x 10(6) cells/mL of medium in 10% serum medium, and the cell concentration was gradually reduced to 1%. The specific MAb productivity of the immobilized cells was more than three times higher than that of the free-suspended cells. The amount of serum in the medium did not influence the specific MAb production rate of the immobilized cells. The maintenance of high cell concentration and the enhanced specific MAb productivity of the immobilized cell culture resulted in a higher volumetric MAb productivity. In addition, MAb yield in the immobilized cell culture with medium containing 1% serum was 2.2 mg/mL of serum, which was approximately three times higher than that in the suspension culture.     

Enhanced degradation of petrol (Slovene diesel) in an aqueous system by immobilized Pseudomonas fluorescens

The rate of degradation of n -alkanes C₁₂-C₁₈, in petrol (Slovene diesel) in an aqueous system, by free and immobilized Pseudomonas fluorescens in shaking flasks was investigated. Cells were immobilized to a biosupport, Biofix, and a biosorbant, Drizit. Analysis of cellular growth of the free and immobilized bacteria over 8 d of incubation with diesel as the sole carbon source, showed a reduction in the lag phase in the immobilized cultures in comparison to the free system. The free system degraded 52·3% of C₁₂ and 11·6% of C₁₃, but C₁₄-C₁₈ were not degraded. In comparison to the free system and diesel which had not been exposed to experimental conditions (unexposed), the immobilized systems degraded significantly more of C₁₃-C₁₈. Biofix-immobilized cells degraded 14·8% of C₁₂ and an average of 53·5% of C₁₃-C₁₈. Drizit-immobilized cells degraded 24·5% of C₁₂, 52·4% of C₁₃ and an average of 91·2% of C₁₄-C₁₈. This study shows the successful use of immobilized bacteria technology to enhance the degradation of diesel in an aqueous system.     

Plant cell bioreactor for the production of protoberberine alkaloids from immobilized Thalictrum rugosum cultures

Cultured Thalictrum rugosum cells were immobilized using a glass fiber substratum previously shown to provide optimum immobilization efficiency based on spontaneous adhesion mechanisms. When cultivated in shake flasks, immobilized cells exhibited decreased growth and protoberberine alkaloid production rates in comparison to freely suspended cells. Since alkaloid production is growth associated in T. rugosum, the decreased specific production rate was a function of the slower growth rate. Cells immobilized on glass fiber mats appear to be amenable for extended culture periods. Maximum biomass and protoberberine alkaloid levels were maintained for at least 14 days in immobilized cultures. In contrast, fresh weight, dry weight, and total alkaloid content decreased in suspension cultures following the linear growth phase.Glass fiber mats were incorporated in to a 4.5-L plant cell bioreactor as horizontal disks supported on a central rod. Mixing in the reactor was provided by the combined actions of a magnetic impeller and a cylindrical sparging colum. fThe magnetic impeller and a cylindrical sparging column. The entire inoculum biomass of T. rougosum, introduced as suspension, was spontaneously immobilized with in 8h. During liner phase, the growth rate of bioreactor cultivated immobilized cells (mu = 0.06 day(-1)) was 50% that immobilized cell viability in both systems was determined to be similar. The increase in specific production of protoberberine alklodis was initially similar in bioreactor-and culture period. The increase in specific production of protoberberine alkaloids was initially similar in bioreactor-and shake-flask-cultivated immobilized cells. However, the maximum specific production of bioreactor grown cultures was lower. The scale up potential of an immobilization strategy based on the spontaneous adhesion of immobilization strategy based on the spontaneous adhesion of cultured plant cells to glass fiber is demonstrated.     

Oxygen uptake by entrapped hybridoma cells

Oxygen consumption by hybridoma cells immobilized in 1- and 3.9-mm-diameter calcium alginate beads was measured. The entrapped cells consumed oxygen at about 10 mumol/min per 10(9) cells, regardless of the bead size and cell loading. In contrast, the same cells in suspension culture respire at specific rates of 3-8 mumol/min per 10(9) cells (depending on the cell density). The growth rate of the immobilized cells was significantly reduced, while specific antibody production was comparable to that of free cells.     

Ethanol production at 45°C by alginate-immobilized Kluyveromyces marxianus IMB3 during growth on lactose-containing media

The thermotolerant yeast strain Kluyveromyces marxianus IMB3 was immobilized in calcium alginate and this was used in batch-fed reactor systems to convert lactose (4?g/l) to ethanol. Production of ethanol by the free and immobilized biocatalyst in the presence and absence of Mn²⁺ was compared. In systems containing the free microorganism in the presence and absence of Mn²⁺, ethanol increased to a maximum of 8?g/l within 40 hours with no significant difference in production by both systems. Ethanol production by the immobilized system in the absence of Mn²⁺ increased to a maximum of 13?g/l within 40 hours and then decreased to 9?g/l within 80 hours. Ethanol production by the immobilized system in the presence of Mn²⁺ increased to 14?g/l within 60 hours and this decreased to 13?g/l at 80 hours. When all systems were re-fed at 80 hours, ethanol production by systems containing the free biocatalyst increased to a maximum of 3?g/l while the immobilized system in the presence of Mn²⁺ increased to a maximum of 12?g/l. Subsequent experiments involving re-feeding the system at shorter time intervals demonstrated that ethanol production by the immobilized system on lactose-containing media at 45?°C was far superior to ethanol production by the free biocatalyst.     

Rhamnolipid (biosurfactant) effects on cell aggregation and biodegradation of residual hexadecane under saturated flow conditions.

The objective of this research was to evaluate the effect of low concentrations of a rhamnolipid biosurfactant on the in situ biodegradation of hydrocarbon entrapped in a porous matrix. Experiments were performed with sand-packed columns under saturated flow conditions with hexadecane as a model hydrocarbon. Application of biosurfactant concentrations greater than the CMC (the concentration at which the surfactant molecules spontaneously form micelles or vesicles [0.03 mM]) resulted primarily in the mobilization of hexadecane entrapped within the sand matrix. In contrast, application of biosurfactant concentrations less than the CMC enhanced the in situ mineralization of entrapped hexadecane; however, this effect was dependent on the choice of bacterial isolate. The two Pseudomonas isolates tested, R4 and ATCC 15524, were used because they exhibit different patterns of biodegradation of hexadecane, and they also differed in their physical response to rhamnolipid addition. ATCC 15524 cells formed extensive multicell aggregates in the presence of rhamnolipid while R4 cells were unaffected. This behavior did not affect the ability of the biosurfactant to enhance the biodegradation of hexadecane in well-mixed soil slurry systems but had a large affect on the extent of entrapped hexadecane biodegradation in the sand-packed-column system that was used in this study.     

Palm oil utilization for the simultaneous production of polyhydroxyalkanoates and rhamnolipids by <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis>

Direct utilization of palm oil for the simultaneous production of polyhydroxyalkanoates (PHAs) and rhamnolipids was demonstrated using Pseudomonas aeruginosa IFO3924. By secreted lipase, palm oil was hydrolyzed into glycerol and fatty acids. Fatty acids became favorable carbon sources for cell growth and PHA production via β-oxidation and glycerol for rhamnolipid production via de novo fatty acid synthesis. Both PHA and rhamnolipid syntheses started after the nitrogen source was exhausted and cell growth ceased. PHA synthesis continued until all fatty acids were exhausted, and at that time, PHA content in the cells reached a maximum, but stopped despite the remaining glycerol (<2g/l). In contrast, rhamnolipid synthesis continued until glycerol was exhausted.     

Production of gibberellins and bikaverin by cells of Gibberella fujikuroi immobilized in carrageenan

The production of gibberellins and bikaverin by immobilized and free cells of Gibberella fujikuroi strains was followed. Both types of cells, free and immobilized, produced similar titers of the secondary metabolites during the normal growth cycle. The kinetics of nutrient use and product formation by the immobilized cells lagged behind that of the free cells and this was assumed to be the result of diffusional limitations imposed on the immobilized cells. A noticeable difference was that in the immobilized cells, all of the bikaverin was excreted into the medium for both strains of G. fujikuroi tested but in the free cell fermentation 44% was excreted for strain ACC 917 and only 10% for strain GF1a. Gibberellin and bikaverin could be produced in a semi-continuous fashion with both free and immobilized cells for a period of 16 d in a resuspension medium containing 0.12 mM or 0.60 mM ammonium chloride. No definite advantage, on a productivity basis, for using immobilized cells over free cells could be seen.     

Rhamnolipid production using Shewanella seohaensis BS18 and evaluation of its efficiency along with phytoremediation and bioaugmentation for bioremediation of hydrocarbon contaminated soils

Abstract

This study reports the combined use of a rhamnolipid type biosurfactant (BS) along with phytoremediation and bioaugmentation (BA) for bioremediation of hydrocarbon-contaminated soils. Bacterial isolates obtained from hydrocarbon contaminated soil were screened for rhamnolipid production and isolate BS18, identified as Shewanella seohaensis, was selected for bioremediation experiments. Growth of BS18 in mineral salt medium (MSM) with diesel oil as the carbon source showed a maximum biomass of 8.2?g L^?1, rhamnolipid production of 2.2?mg g^?1 cell dry weight, surface tension reduction of 28.6?mN/m and emulsification potential (EI₂₄%) of 65.6. Characterization of rhamnolipid based on Fourier transmittance infrared (FTIR) analysis confirmed the presence of OH, CH₂/CH₃, C=O, and COO stretching vibrations, respectively, which are distinctive features of rhamnolipid type BSs. In bioremediation experiments, the lowest hydrocarbon concentration of 2.1?mg g^?1 of soil for non-sterilized soil and 4.3?mg g^?1 of soil for sterilized soil was recorded in the combined application of rhamnolipid, phytoremediation, and BA. This treatment also yielded the highest hydrocarbon degrading bacterial population (6.4 Log Cfu g^?1 of soil), highest plant biomass (8.3?g dry weight plant^?1), and the highest hydrocarbon uptake (512.3?mg Kg^?1 of plant).