Growth models of cultures with two liquid phases. 8. Experimental observations on droplet size and interfacial area

Because of the importance of the drop she distribution and interfacial area of the dispersed liquid phase in hydrocarbon fermentations, experiments were carried out to determine the drop size distribution and the interfacial area during batch fermentations of Candida lipolytica on gas oil and on n-hexadecane dissolved in dewaxed gas oil. The effects of cell concentration and dispersed phase volume fraction on size distribution and interfacial area were investigated. Measurements of interfacial tensions, densities, viscosities, and fatty acid concentrations were also made. The results show that the size distribution is skewed and that the Sauter mean diameter is in the range of 10 to 30 μ. Both the Sauter mean diameter and the interfacial area increased during the course of a batch fermentation; however, they decreased at the end of the fermentation. The interfacial area also increased with inoculum size.     

Continuous culture of Candida lipolytica on n-hexadecane

Candida lipolytica was grown continuously on n-hexadecane as the main source of carbon. A transient continuous-culture experiment was also conducted to investigate hydrocarbon-limited growth; the hydrocarbon feed flow rate was stopped for several hours and then resumed at a reduced steady-state flow rate. Interfacial tension, Sauter mean diameter, pseudosolubility, fraction of cells in the aqueous phase, oil-phase volume fraction, and cell concentration were measured to characterize the system. The microorganisms appear to utilize both the submicron drops and the microscopic drops. The effects of interfacial tension, pseudosolubility, and unoccupied interfacial area on the kinetics of hydrocarbon fermentation are discussed here. A conceptual model for hydrocarbon uptake is presented and discussed.     

Growth models of cultures with two liquid phases. V. Substrate dissolved in dispersed phase—experimental observations

The effects of inoculum size, dispersed phase volume and substrate concentration on the batch growth of Candida lipolytica are investigated in a model system composed of n-hexadecane dissolved in dewaxed gas oil. Tabular values and parameters are presented for 16 different experiments. All of the batch growth curves exhibited a linear growth region with the length of the region ranging from 1.5 to 9.5 hours. The rate of linear growth varied both with change in dispersed phase volume and initial dispersed phase substrate concentration. A qualitative analysis of the results is presented and possible explanations for the observed linear growth rates are discussed.     

The effects of carbon sources and micronutrients in fermented whey on the biodegradation of n-hexadecane in diesel fuel contaminated soil

Fermented whey has previously been shown to stimulate biodegradation of n-hexadecane in diesel contaminated soils. The proposed explanation for the stimulatory effect is that fermented whey provides easily accessible carbon and micronutrients, which give rise to an increased degrading biomass.The objective of this work has been to investigate the role of the different carbon sources and vitamins in fermented whey on the microbial degradation of n-hexadecane in soil.The effects of lactose, lactate, vitamins and free amino acids were tested in combinations according to a full factorial design experiment, at concentrations corresponding to those present in fermented whey. The target substance was ¹⁴C-labeled n-hexadecane in nutrient amended soil microcosms contaminated with 5000 mg diesel fuel kg⁻¹ dw. Biodegradation was monitored by determination of evolved ¹⁴CO₂.Significant effects on the biodegradation of n-hexadecane were observed for lactate and amino acids additions in a sandy soil. Lactate showed both an inhibitory effect in the early phase of the experiment and a stimulatory effect in the later phase. The effect of amino acids was slightly stimulatory, mainly evident as a shortening of the lag time.The degree of n-hexadecane degradation at the end of the experiment was correlated with the total concentration of organic compounds added to the soil.

Scientific relevance

There are a handful papers describing the potential of using organic amendments (often industrial by-products) with a content of both easily accessible carbon and micronutrients, to enhance the bioremediation of polluted soils. Enhanced biodegradation is often reported and the proposed explanations are that the combination of easily accessible carbon and micronutrients increases the degrading biomass.In this paper, we examine the effect of fermented whey on the degradation of n-hexadecane and correlate the observed effects on the biodegradation with the main components lactate, amino acids, lactose and B-vitamins. This has to our knowledge never been done before.     

Continuous hydrocarbon fermentation with colloidal emulsion feed. A kinetic model for two-liquid phase culture

Candida tropicalis was cultured in a chemostat-type fermentor with n-hexadecane, dispersed in water as submicron droplets, as the only carbon substrate. The emulsion as well as the aqueous medium were fed continuously into the fermentor. A Monod-type equation can correlate the specific group rate in the continuous fermentor with the concentration of submicron droplets. The same equation can also be fitted to the data for the conventional-type batch culture in the same fermentor in which an oil phase as well as an aqueous phase existed, if the hydrocarbon concentration in the aqueous phase excluding oil drops is employed as the substrate concentration. This demonstrates that Candida tropicalis takes up only submicron droplets of n-hexadecane as the carbon substrate.     

Growth models of cultures with two liquid phases. VII. Substrate dissolved in dispersed phase; effect of dispersed phase volume and temperature

The effects of dispersed phase volume and temperature on the batch growth of Candida lipolytica on gas oil are investigated. Growth parameters are presented for two sets of experiments. The shape of growth curves was basically similar to the system composed of n-hexadecane dissolved in dewaxed gas oil, in spite of the complex nature of the substance. All of the batch growth curves exhibited a linear growth region. The rate of linear growth and its length varied with change in dispersed phase volume. The effect of temperature on growth rate was investigated for temperatures ranging from 23°C to 34°C. The results show a smaller activation energy during linear growth than during the early stages of batch growth. These results are analyzed from the viewpoint of growth models presented previously. The results indicate that growth at drop surfaces is important and that segregation effects may be important.     

Growth models of cultures with two liquid phases. VI. Parameter estimation and statistical analysis

Parameter estimation studies have been conducted employing mathematical models developed previously by the investigators and experimental data collected by the last author. A batch fermentation process in which Candida lipolytica were cultured on n-hexadecane dissolved in dewaxed gas oil was employed to obtain the experimental data. The kinetic data from a number of batch experiments conducted at different initial substrate concentrations and different dispersed phase volume fractions were analyzed assuming that, the basic model parameters (maximum specific growth rate, saturation constant, substrate phase equilibrium constant, adsorption constant, desorption constant, etc.) did not change from experiment to experiment. The Gauss-Newton method with modification by Greenstadt, Eisenpress, Bard, and Carroll was used to minimize the conventional sum of squares criterion on the IBM 300/50 computer. The individual confidence intervals were obtained for each individual parameter. Tin- models were compared employing the F-test for equality of variances and an analysis of residuals. For the two best models, the estimated parameter values were compared with available experimental information. The results showed good agreement between the experimental data and the values predicted by the mathematical models. The results presented in this work did suggest that growth on small segregated drops may be more important than continuous phase growth on dissolved substrate.     

Distribution of dispersed oil phase in hydrocarbon fermentations

Recent experimental results show that the spreading coefficient frequently becomes positive when Candida lipolytica is cultivated on n-hexadecane. The effects of oil spreading at the surface of air bubbles in an airlift fermentor are examined using a mathematical model. The distribution of the oil phase with position and among the phases is determined using computer simulation. The simulation results qualitatively explain some of the experimental observations which have been previously reported.     

The effects of carbon sources and micronutrients in fermented whey on the biodegradation of n-hexadecane in diesel fuel contaminated soil

Fermented whey has previously been shown to stimulate biodegradation of n-hexadecane in diesel contaminated soils. The proposed explanation for the stimulatory effect is that fermented whey provides easily accessible carbon and micronutrients, which give rise to an increased degrading biomass.The objective of this work has been to investigate the role of the different carbon sources and vitamins in fermented whey on the microbial degradation of n-hexadecane in soil.The effects of lactose, lactate, vitamins and free amino acids were tested in combinations according to a full factorial design experiment, at concentrations corresponding to those present in fermented whey. The target substance was ¹⁴C-labeled n-hexadecane in nutrient amended soil microcosms contaminated with 5000 mg diesel fuel kg⁻¹ dw. Biodegradation was monitored by determination of evolved ¹⁴CO₂.Significant effects on the biodegradation of n-hexadecane were observed for lactate and amino acids additions in a sandy soil. Lactate showed both an inhibitory effect in the early phase of the experiment and a stimulatory effect in the later phase. The effect of amino acids was slightly stimulatory, mainly evident as a shortening of the lag time.The degree of n-hexadecane degradation at the end of the experiment was correlated with the total concentration of organic compounds added to the soil.Scientific relevanceThere are a handful papers describing the potential of using organic amendments (often industrial by-products) with a content of both easily accessible carbon and micronutrients, to enhance the bioremediation of polluted soils. Enhanced biodegradation is often reported and the proposed explanations are that the combination of easily accessible carbon and micronutrients increases the degrading biomass.In this paper, we examine the effect of fermented whey on the degradation of n-hexadecane and correlate the observed effects on the biodegradation with the main components lactate, amino acids, lactose and B-vitamins. This has to our knowledge never been done before.     

Batch kinetics and oxygen consumption ofCandida lipolytica 4-1 onn-alkanes

Detailed batch kinetics ofCandida lipolytica 4-1 onn-hexadecane for varying dispersed phase volume from 0.5 to 5% v/v is presented. All batch growth curves exhibited a linear growth region, indicating a substrate uptake limit. System productivities derived from the linear region were correlated to the dispersed phase volume. The correlation coefficient was identical with that obtained on gas oil. This implies that a correlation coefficient of interfacial area to the dispersed phase volume is identical for both systems. Dissolved oxygen profile and uptake of oxygen from gas phase were also measured. The oxygen uptake rate, volumetric oxygen transfer rate and oxygen demand (requirement) were calculated by means of the balance method. Under limiting dissolved oxygen concentration the maximal oxygen transfer of the fermenter was assessed.     

Fed-batch hydrocarbon fermentation with colloidal emulsion feed

Candida tropicalis was cultured with n-hexadecane, dispersed in water as submicron droplets, as the only carbon substrate; the emulsion being fed continuously into a fermentor containing only an aqueous medium (fed-batch culture). The results have demonstrated that the organism takes up hydrocarbon accommodated in the aqueous phase as submicron droplets. The cell/substrate yield for the linear growth phase, where growth was limited by the supply of the substrate, was much higher than the yield for the exponential growth phase.     

Hydrocarbon uptake in hydrocarbon fermentations

Candida lipolytica (strain ATCC 8662) was grown on a simple defined medium with n-hexadecane as the main carbon Source under batch fermentation conditions. The relative importance of the cells growing in the aqueous phase on the overall kinetics was studied. The effect of interfacial tension, unoccupied interfacial area, and pseudosolubility on the specific growth was also studied. Results are presented and discussed here.     

Effects of hydrocarbon additions on gas-liquid mass transfer coefficients in biphasic bioreactors

The effects of aliphatic hydrocarbons (n-hexadecane andn-dodecane) on the volumetric oxygen mass transfer coefficient (k _L a) were studied in flat alveolar airlift reactor and continuous stirred tank reactors (CSTRs). In the flat alveolar airlift reactor, high aeration rates (>2 vvm) were required in order to obtain efficient organic-aqueous phase dispersion and reliablek _L a measurements. Addition of 1% (v/v)n-hexadecane orn-dodecane increased thek _l a 1.55-and 1.33-fold, respectively, compared to the control (superficial velocity: 25.8×10⁻³ m/s, sparger orifice diameter: 0.5 mm). Analysis of the gas-liquid interfacial areaa and the liquid film mass transfer coefficientk _L suggests that the observedk _L a increase was a function of the media's liquid film mass transfer. Addition of 1% (v/v)n-hexadecane orn-dodecane to analogous setups using CSTRs led to ak _L a increase by a factor of 1.68 and 1.36, respectively (superficial velocity: 2.1×10⁻³ m/s, stirring rate: 250 rpm). These results propose that low-concentration addition of oxygen-vectors to aerobic microbial cultures has additional benefit relative to incubation in purely aqueous media.     

Increased shikonin production by hairy roots of Lithospermum erythrorhizon in two phase bubble column reactor

Summary Plant hairy root cultures of Lithospermum erythrorhizon were carried out to produce shikonin derivatives by employing in situ extraction with n-hexadecane in a shake flask and a bubble column bioreactor. Over 95 % shikonin produced was recovered in the n-hexadecane layer. In flask cultures the maximum concentration of shikonin with n-hexadecane extraction was 3 times higher than that obtained without extraction. In the two phase bubble column reactor, 572.6 mg/L of shikonin and 15.6 g/L of dry cell mass were obtained after 54 days. Shikonin was produced at a constant level of 10.6 mg/L day during this period.     

Protein-like Activator for n-Alkane Oxidation by Pseudomonas aeruginosa S7B1

During the study of the n-alkane oxidation by Pseudomonas aeruginosa S₇B₁, a nondialysable activator for n-alkane oxidation was discovered in the culture broth of the strain. The activator was purified, as judged by cellulose acetate membrane electrophoresis, by ammonium sulfate precipitation and chromatography on DEAE-Sephadex, CM-Sephadex and Sephadex G-75 columns.

The purified activator, which was positive in protein color reactions, remarkable stimulated only the oxidation of n-hexadecane, though it was not observed in case of palmitic acid or glucose oxidation.

Co-operative action between the activator and rhamnolipid, which had been isolated as a growth stimulant of P. aeruginosa S₇B₁ on n-hexadecane by the authors, was observed not only in the oxidation of n-hexadecane but also in the growth on n-hexadecane.     

Data consistency,yield, maintenance,and hysteresis in batch cultures of Candida lipolytica cultured on n-hexadecane

Candida lipolytica was cultured batchwise using n-hexadecane as the main carbon source. Biomass production, n-hexadecane consumption, oxygen consumption, and carbon dioxide evolution were measured to follow the fermentation. The consistency of the measured data was examined using integrated and instantaneous available electron and carbon balances. Values of the “true” growth yield, η_max, and maintenance coefficient, m_e were estimated using three different sets of data (biomass and n-hexadecane, oxygen and biomass, and CO₂ and biomass), and the results were compared with estimates obtained from literature data. Hysteresis patterns were observed in plots of specific rates of oxygen consumption and carbon dioxide evolution versus specific growth rate.     

Method for Improving the Reliability of Learning Machine

Optimization of learning machine prediction has been attempted by the addition of a “width” parameter proposed by Wangen et al. Predictions were made for the production of phenazine compounds, the utilizations of d-sorbitol, of n-hexadecane, and of histamine by pseudomonads. In all but one cases examined, the “stability” of prediction was much improved when a high positive value was assigned to the parameter. A slight increase was often found in the hit-to-miss ratio, but the χ² test revealed that it was statistically insignificant.     

Influence of n-hexadecane on penicillin fermentation with Penicillium chrysogenum: The morphological effect

Summary In addition to acting as an oxygen transfer enhancer, n-hexadecane plays an important role in dominating the mycelial morphology of Penicillium chrysogenum in a submerged penicillin fermentation. The cell morphology is related to the timing of adding n-hexadecane to the culture. n-Hexadecane also has a function of suppressing foaming and thus can be employed as an antifoam agent in the fermentation.     

Synthesis of dl-Phyllostine

“Protein-like activator (PA)” for n-alkane oxidation was formed by Pseudomonas aeruginosa S₇B₁ from long-chain n-alkanes, 1-hexadecene and cetyl alcohol but not from glucose, glycerol and palmitic acid. The molecular weight and the total amino acid residues of PA were estimated at about 14,300 and 147, respectively. PA was relatively stable to low pH and high temperature, and completely inactivated upon heating at 98°C for 45 min. The cultural fluid obtained from n-hexadecane medium stimulated the growth of the strain on n-hexadecane. The degree of the growth stimulation by the fluid depended on the amount of PA and rhamnolipid (RL) in the fluid. The heat-treated PA lost the growth-stimulaing effect and the emulsifying power on the n-hexadecane medium in the presence of RL.     

Oxygen transfer in mechanically agitated aqueous systems containing dispersed hydrocarbon

The effect of dispersed n -dodecane or n -hexadecane on the air-to-aqueous phase overall volumetric oxygen transfer coefficient in a simulated (cell-free) stirred-tank fermentor is described. The oil volume fraction ranged from zero to 0.10; the ionic strength of the aqueous phases was varied from 0 to 0.45. The air-to-aqueous phase coefficients in both oil-free (K_La) and oil-bearing (K_La*) systems were evaluated from unsteady-state experiments using a membrane-covered probe to follow the aqueous phase dissolved oxygen tension. For all systems studied, K_La*/K_La was found to be independent of P/V and v_s for all practical purposes. However, for a particular aqueous phase and at a given P/V and v_s, the ratio K_La*K_La generally differed from unity. Depending on the combination of hydrocarbon type and volume fraction and the aqueous-phase ionic strength employed, the dispersed hydrocarbon may, in some cases, reduce the rate of oxygen transfer and in others enhance it relative to that of the corresponding oil-free gas–liquid dispersion. Enhancement of the air-to-aqueous transfer rate by such negative spreading coefficient hydrocarbons has not been reported previously.