Selective removal of linolenic acid from soybean oil by lipase-catalyzed interesterification at low temperature

Summary Linolenic acid, the component responsible for flavour instability of soybean oil could be reduced to 3% or less by interesterification (acidolysis) of the oil using lipases as catalysts at 10°C.     

Production of acetic acid by Clostridium thermoaceticum in batch and continuous fermentations

Batch and continuous fermentations with Clostridium thermoaceticum (ATCC 39073) using automatic pH control were conducted. The value of mu(max) obtained from batch fermentation was about 0.14 h(-1); acetate yield, which was both growth and non-growth associated, was about 2 mole of acetic acid/mole of glucose, compared with a theoretical maximum value of 3. This low yield, compared with literature data, may be explained by glucose loss through a combination of degradation routes. Continuous fermentation could be sustained for 1600 h or more without contamination problems. Continuous fermentation at high dilution rates indicates that mu(max) may be well above 0.17 h(-1) when fresh feed medium is used. Acetate yields in continuous fermentation were about 77% of theoretical or 2.3 mole of acetic acid/mole of glucose.     

Modification of the nutritional properties of fats using lipase catalysed directed interesterification

Summary A method for producing a monounsaturated cooking oil from beef tallow has been investigated. Immobilised lipases were used to interesterify tallow during fractional crystallisation from melted tallow, both with and without hexane present. Significant increases in the unsaturated fatty acid content of the liquid fractions were achieved by the use of upases. The water content of the enzyme beads appeared to have a large effect on reaction rates and free fatty acid formation. The presence of hexane greatly improved the efficiency of the reaction by improving the efficiency of crystal filtration.     

Production of gramicidin S in batch and continuous culture

A mathematical model for the production of gramicidin S in batch and continuous culture is proposed. It is based on the division of the age of a cell into two phases—an immature and a mature one. A nongrowth associated product, such as an antibiotic, is assumed to be produced when the organism is in the older of these two phases, the mature state. The parameters describing the model were evaluated from batch and single stage transient continuous culture of Bacillus brevis, which produces the antibiotic gramicidin S. The predictive value of the model was studied in steady-state single stage continuous culture and in a transient two stage system. Good agreement between the theoretical curves and the experimental results was found in the transient response of both the first and second stage systems, although at high dilution rates (0.34 hr^?1) in the first stage, deviations from the predicted response were observed in the second stage. These may have been due to chemostat instability at dilution rates close to washout, lags in cell growth, and a metabolic lag on going from stage one to stage two.     

Production of citric acid in batch culture

Work has been carried out on the production of citric acid in batch culture using Aspergillus foetidus. It is shown that the dry weight increases throughout the fermentation. The supply of nitrogen is exhausted early and the subsequent increase in dry weight is due to accumulation of carbon by the cells. It appears that the exhaustion of nitrogen is a necessary prerequisite for the production of citric acid, which is produced by carbon-storing cells. The pH history in the early part of the fermentation did not affect the final yields.     

Preparation of medium and long chain triacylglycerols by lipase-catalyzed interesterification in a solvent-free system

Synthesis of medium and long chain triacylglycerols (MLCTs) by lipase-catalyzed interesterification of soybean oil with medium chain triacylglycerols (MCTs) in a solvent-free system is investigated in this study. Firstly, reaction conditions of the interesterification were optimized. Under the optimum conditions (Lipozyme 435 of 8% as catalyst, substrate ratio of 40:60, heating temperature of 90 °C, reaction time of 6 h), MLCTs were obtained in a 74.9% yield Secondly, a two-step purification was conducted to reduce acid, peroxide values and diacylglycerol content to acceptable levels. After the deacidification by the neutralization and silica gel absorption, acid, peroxide values and diacylglycerol content were reduced to 0.14 mg/g, 1.5 mmol/kg and 1.2%, respectively. The determined levels of physicochemical parameters of purified MLCTs fell within the permitted ranges of the Chinese national standard specification for MLCTs. After a two-step purification, a qualified product was produced and can be used in pharmaceutical industry as a component of fat emulsion injection. The process for the preparation of MLCTs is scalable. Differently from previous studies, the aim of this study is to obtain MLCTs products meeting the national standard JX20070100 for structured triacylglycerols.     

Production of butanol by Clostridium puniceum in batch and continuous culture

Summary The pink-pigmented, amylolytic and pectinolytic bacterium Clostridium puniceum in anaerobic batch culture at pH 5.5 and 25–30°C produced butan-1-ol as the major product of fermentation of glucose or starch. The alcohol was formed throughout the exponential phase of growth and surprisingly little acetone was simultaneously produced. Furthermore, acetic and butyric acids were only accumulated in low concentrations, and under optimal conditions were completely re-utilised before the fermentation ceased. Thus, in a minimal medium containing 4% w/v glucose as sole source of carbon and energy, after 65 h at 25°C, pH 5.5 all of the glucose had been consumed to yield (g product/100 g glucose utilised) butanol 32, acetone 3 and ethanol 2. Butanol was again the major product of glucose fermentation during phosphate-limited chemostat culture wherein, although the organism eventually lost its capacity to sporulate and to synthesize granulose, production of butanol continued for at least 100 volume changes. Under no growth condition was the organism capable of producing more than 13.3 g l^-1 of butanol. At pH 5.5, growth on pectin was slow and yielded a markedly lesser biomass concentration than when growth was on glucose or starch; acetic acid was the major fermentation product with lower concentrations of methanol, acetone, butanol and butyric acid. At pH 7, growth on all substrates produced virtually no solvents but high concentrations of both acetic and butyric acids.     

Production of optically pure L-alanine in batch and continuous stirred tank reactors using immobilized Pseudomonas sp.

A process to obtain optically pure l-alanine has been developed using batch and continuous stirred tank reactors with a new l-aminoacylase-producing bacterium Pseudomonas sp. BA2 immobilized in calcium alginate beads coated with glutaraldehyde. The maximum production of l-alanine in a continuous stirred tank reactor was 11.26 g after 2 days of operation which is higher than that previously reported.     

Kinetics of growth and lactic acid production in continuous and batch culture

Summary In a lactic acid fermentation by Streptococcus faecalis, the specific consumption rate of glucose (v) and the specific production rate of lactic acid () were represented by the following simple equations as functions of the specific growth rate (): 1/=(1/) + 1/ = (1/) + By use of data from a batch culture, these two equations were derived from enzyme kinetics of the product inhibition. These equations were successfully applied to the results of batch culture and chemostat culture. In addition, calculation of ATP yield by these equations agreed with the experimental results better than the conventional Leudeking-Piret type equation, which includes two terms associated with growth and not with growth. Correspondence to: H. Ohara     

Ethanol production in multistage continuous, single stage continuous, Lactobacillus-contaminated continuous, and batch fermentations

Saccharomyces cerevisiae-based ethanol fermentations were conducted in batch culture, in a single stage continuous stirred tank reactor (CSTR), a multistage CSTR, and in a fermentor contaminated with Lactobacillus that corresponded to the first fermentor of the multistage CSTR system. Using a glucose concentration of 260 g l^–1 in the medium, the highest ethanol concentration reached was in batch (116gl^–1), followed by the multistage CSTR (106gl^–1), and the single stage CSTR continuous production system (60gl^–1). The highest ethanol productivity at this sugar concentration was achieved in the multistage CSTR system where a productivity of 12.7gl^–1h^–1 was seen. The other fermentation systems in comparison did not exceed an ethanol productivity of 3gl^–1h^–1. By performing a continuous ethanol fermentation in multiple stages (having a total equivalent working volume of the tested single stage), a 4-fold higher ethanol productivity was achieved as compared to either the single stage CSTR, or the batch fermentation.     

Amino acid consumption by Chloroflexus aurantiacus in batch and continuous cultures

Amino acid consumption was studied with batch and continuous chemostat cultures of Chloroflexus aurantiacus grown phototrophically in complex medium with casamino acids (Pierson and Castenholz 1974). Amino acids like Arg, Asx, Thr, Ala, Tyr, which were utilized during the early exponential phase by cells grown in batch cultures were consumed in chemostat cultures essentially at any of the dilution rates employed (0.018–0.104 h^-1). Those amino acids which were taken up during subsequent phases of growth were consumed in chemostat cultures preferentially at low dilution rates. For example, the consumption of Glx was enhanced during the late exponential phase and at low dilution rates. At high dilution rates Glx was not consumed at all. Since Glx utilization largely paralleled bacteriochlorophyll formation, it is discussed that formation of the photopigment depends on the intracellular availability of Glu as the exclusive precursor for tetrapyrrole synthesis.     

Kinetic studies of the lactic acid fermentation in batch and continuous cultures

The fermentation kinetics of the homofermentative organism Lactobacillus delbrueckii in a glucose-yeast extract medium is studied in both batch and continuous culture under conditions of controlled pH. From a graphical analysis of the batch data, a mathematical model of the process is derived which relates bacterial growth, glucose utilization, and lactic acid formation. The parameters in the model represent the activity of the organism and are a function of pH, having a maximum value at about 5.90. In a continuous stirred tank fermentor (CSTF), the effect of pH, feed concentration, and residence time is observed. The feed medium is a constant ratio of two parts glucose to one part yeast extract plus added mineral salts. An approximate prediction of the steady-state behavior of the CSTF can be made using a method based on the kinetic model derived for the batch case. In making step changes from one steady state to another, the transient response is observed. Using the kinetic model to simulate the transient period, the calculated behavior qualitatively predicts the observed response.     

Evaluation ofl-lactic acid production in batch, fed-batch, and continuous cultures ofRhizopus sp. MK-96-1196 using an airlift bioreactor

Various processes which producel-lactic acid using ammonia-tolerant mutant strain,Rhizopus sp. MK-96-1196, in a 3 L airlift bioreactor were evaluated. When the fed-batch culture was carried out by keeping the glucose concentration at 30 g/l, more than 140 g/l ofl-lactic acid was produced with a product yield of 83%. In the case of the batch culture with 200 g/l of initial glucose concentration, 121 g/L ofl-lactic acid was obtained but the low product yield based on the amount of glucose consumed. In the case of a continuous culture, 1.5 g/l/h of the volumetric productivity with a product yield of 71% was achieved at dilution rate of 0.024 h⁻¹. Basis on these results three processes were evaluated by simple variable cost estimation including carbon source, steam, and waste treatment costs. The total variable costs of the fed-batch and continuous cultures were 88% and 140%, respectively, compared to that of batch culture. The fed-batch culture with highl-lactic acid concentration and high product yield decreased variable costs, and was the best-suited for the industrial production ofl-lactic acid.     

Utilization of substrates during batch growth of Pseudomonas fluorescens on olive oil,lard, and mutton tallow

Summary Similar amounts of cell-associated and cell-free lipase activities were present in log phase cultures of Pseudomonas fluorescens growing on fatty substrates. The rates of triglyceride hydrolysis and fatty acid utilization were balanced as free fatty acids remained at low concentrations in the culture media at all times. The time required for growth initiation and optimal growth rates of P. fluorescens were similar on olive oil, lard and mutton tallow, provided the coalesced solid fats were mechanically dispersed during the initial stages of cultivation. Although olive oil was completely consumed at the end of cultivation, substantial amounts of tri- and diglycerides, presumably bearing saturated acyl residues, remained in lard culture and, to a lesser extent, in mutton tallow culture.     

Development of high-oleic,low-linolenic acid Ethiopian-mustard (Brassica carinata) germplasm

Seed oil of current zero erucic-acid germplasm of Ethiopian mustard ( Brassica carinata A. Braun) is characterized by a low concentration of oleic acid and high concentrations of linoleic and linolenic acids. Sources of increased oleic-acid (HO) and reduced linolenic-acid (LL) concentration have been developed separately in high erucic-acid germplasm. The objectives of the present research were to study the inheritance of the HO and LL traits in crosses HO x LL, and to develop HOLL recombinants, both in high erucic-acid and zero erucic-acid backgrounds. The HO mutant N2-3591 (about 20% oleic acid compared to 9% in conventional high erucic-acid materials), was reciprocally crossed with the LL lines N2-4961 and HF-186 (both with about 5% linolenic acid compared to 12% in standard high erucic-acid materials). Increased oleic acid concentration of N2-3591 was found to be controlled by alleles at one locus (Ol), whereas three different loci for reduced linolenic-acid concentration (Ln, Ln1 and Ln2) were identified in N2-4961 and HF-186. Crosses between N2-3591 and N2-4961 generated HOLL recombinants where levels of increased oleic-acid and reduced linolenic-acid were similar to those of the parents. However, a transgressive segregation for oleic acid was observed in crosses between N2-3591 and HF-186, where F(2) seeds with up to 29.7% oleic acid were obtained, in comparison to an upper limit of 25.1% in the N2-3591 parent grown in the same environment. The transgressive increased oleic-acid was expressed in the F(3) generation and was attributed to the presence of a second locus, designated Ol2. The transgressive trait was transferred to the zero erucic-acid line 25X-1, resulting in a zero erucic-acid germplasm with very high oleic-acid concentration (83.9% compared to 32.9% in 25X-1) and low linolenic-acid concentration (5.0% compared to 16% in 25X-1). Additionally, two other lines exhibiting different stable levels of increased oleic-acid (70.7% and 79.5%, respectively) and reduced levels of linolenic-acid (7.5% and 8.7%, respectively) were isolated.     

Growth characteristics of Geotrichum ingens on propionic acid and acetic acid in batch and continuous culture

Growth of Geotrichum ingens in batch cultures was completely inhibited by 47 g acetic acid/l or 33 g propionic acid/I. With mixtures of acetic and propionic acids, however, growth only ceased at 55 g/l. Acetic acid inhibited growth linearly, whereas propionic acid inhibited growth non-linearly. In continuous culture, two steady states at each dilution rate were observed at high dilution rates for acetic acid and propionic acid. The highest yield coefficient (0.69 g cells/g substrate) was achieved with propionic acid as substrate. On both substrates and their mixtures, the protein content of the biomass increased when the dilution rate was increased.The authors are with the Department of Microbiology and Biochemistry, University of the Orange Free State, P.O. Box 339, Bloemfontein 9300, South Africa     

Production of citric acid in continuous culture

Work has been carried out on the production of citric acid by Aspergillus foetidus in single-stage continuous culture, operated under nitrogen-limiting conditions at dilution rates between 0.04 to 0.21 hr^?1. Citric acid concentration increased rapidly as the dilution rate decreased and appears to be critically dependent on the pH in the culture vessel and the nitrogen concentration in the feed. A mathematical model based on a distinction between basic cells, which require nitrogen but do not produce citric acid, and stroage cells, which accumulate carbon and simultaneously produce citric acid, is proposed.     

Production of L- AND D-lactate by Pediococcus pentosaceus in batch and steady-state continuous culture

The fast growth and acid production of a strain of Pediococcus pentosaceus , used as a starter culture in the production of dry sausages, was dependent on the presence of acetate. In a batch culture on a mixture of glucose and sucrose both sugars were consumed simultaneously. Similar growth rates and product yields were obtained on glucose and sucrose, d - AND l -lactate were produced via a D- and L-lactate dehydrogenase (LDH), respectively, and no racemase was present. In batch cultures about 15% of the lactic acid produced was the D-isomer, whereas in a sucrose-limited, continuous culture the fraction of D-lactic acid increased with decreasing dilution rate. The results are discussed in relation to the two LDH activities.     

Production of thermostable xylanases in batch and continuous culture by Thermomonospora fusca KW 3

Summary The actinomycete Thermomonospora fusca KW 3 produced novel thermostable xylanases in batch and continuous cultures in media containing insoluble xylan. The production of xylanases could be induced with oat spelt or beech xylan. Very low activities were detected when the strain was grown on glucose or xylose. In continuous cultivations, mycelial wall growth could be prevented using a stirrer speed controller. Homogeneous mixing of the insoluble substrate was obtained by vibrating the flexible tubes. T. fusca KW 3 could be grown on insoluble xylan at growth rates as high as 0.23 h^–1, equivalent to a doubling time of 3 h. Xylanase activity decreased from maximum levels of 2.5 units (U) ml^–1 with increasing dilution rate and was nearly constant at a level of 0.5 U ml^–1 with dilution rates greater than 0.1 h^–1. Correspondence to: P. Röthlisberger     

Production of medium chain glycerides from coconut and palm kernel fatty acid distillates by lipase-catalyzed reactions

Medium chain glycerides (MCGs) containing C_8:0 and C_10:0 fatty acids is very much important for medicinal and nutritional applications. Coconut and palm kernel fatty acid distillates (FADs) can be utilized to produce MCGs by a combination of lipase-catalyzed hydrolysis and esterification reactions. The neutral glycerides present in coconut and palm kernel FADs are hydrolyzed by Candida rugosa lipase. The hydrolysates were then subjected to steam distillation under vacuum (at 120–140 °C) to get fractions rich in medium chain fatty acids (MCFAs). The fractions, from coconut and palm kernel FADs (75.2 and 76.2% MCFAs, respectively), were esterified with Rhizomucor miehei (Lipozyme RM IM) lipase to produce MCGs. Products from coconut FAD contained 64.7–67.5% diacylglycerol (DG), followed by 18.8–22.9% monoacylglycerol (MG) and 9.8–9.3% triacylglycerol (TG). Similarly, products from palm kernel FAD contained 63.5–66.7% DG, 19.1–23.6% MG and 9.5–10.1% TG.