Toxicity of organic solvents used in situ in microbial fermentation

Summary Toxicity of organic solvents for in situ solvent extraction of carboxylic acids from aqueous solutions was studied on bacteria Bacillus subtillis and Acetobacter spp., yeasts Kluyveromyces marxianus and Pichia fermentans and fungi Aspergillus terreus and Rhizopus arrhizus. It has been found that trialkylamine and tributylphosphate are much more toxic than other carriers as trialkylphosphineoxide, triisobutylphosphinesulfide and trihexylphosphate. For R. arrhizus trihexylphosphate was found to be the less toxic solvent.     

Toxicity of organic solvents used in situ in fermentation of lactic acid by Rhizopus arrhizus

Of 17 organic phases, some containing one of the five extractants for solvent extraction of lactic acid from Rhizopus arrhizus broth, solvents containing tertiary amines (Hostarex A327, trioctylamine) and secondary amine with isotridecanol modifier and trihexylphosphate, are from point of view of toxicity suitable for the in situ or on-line extraction. Pentaphosphinedipentylester is highly toxic. Toxicity of alcohols used as modifiers, decreases with an increase in the number of carbons in a molecule. Isotridecanol is medium toxic. Octanol and isodecanol and solvents containing them are toxic.This revised version was published online in October 2005 with corrections to the Cover Date.     

In situ recovery of fermentation products

In situ recovery of fermentation products can increase the rate of product inhibited fermentations, reduce costs of waste-water treatment and minimize product degradation. Some methods of in situ recovery show more potential than others for the production of chemicals and pharmaceuticals by fermentation.     

Use of silica gel polymer for DNA extraction with organic solvents

Phenol and chloroform are the standard solvents used for DNA extraction. These solvents aid in the removal of protein and lipid from crude or partially purified cell extracts. Although the procedure is well established, the solvents are noxious, caustic, and unpleasant. We describe in this paper the use of a special blood collection tube to isolate the offensive organic solvents. With the use of silica gel polymer containing tubes, phenol, phenol:chloroform, or chloroform can be separated from the DNA containing aqueous phase in a rapid and safe manner. The method permits higher yields of DNA since the DNA is poured from the tube rather than aspirated with pipet.     

Two-phase systems: potential for in situ extraction of microalgal products

Algae are currently used for production of niche products and are becoming increasingly interesting for the production of bulk commodities, such as biodiesel. For the production of these goods to become economically feasible, production costs will have to be lowered by one order of magnitude. The application of two-phase systems could be used to lower production costs. These systems circumvent the costly step of cell harvesting, whilst the product is extracted and prepared for downstream processing. The mechanism of extraction is a fundamental aspect of the practical question whether two-phase systems can be applied for in situ extraction, viz, simultaneous growth, product formation and extraction, or as a separate downstream processing step. Three possible mechanisms are discussed; 1) product excretion 2) cell permeabilization, and 3) cell death. It was shown that in the case of product excretion, the application of two-phase systems for in situ extraction can be very valuable. With permeabilization and cell death, in situ extraction is not ideal, but the application of two-phase systems as downstream extraction steps can be part of a well-designed biorefinery process. In this way, processing costs can be decreased while the product is mildly and selectively extracted.Thus far none of the algal strains used in two-phase systems have been shown to excrete their product; the output has always been the result of cell death. Two-phase systems can be a good approach as a downstream processing step for these species. For future applications of two-phase in situ extraction in algal production processes, either new species that show product excretion should be discovered, or existing species should be modified to induce product excretion.     

Hydrocarbon recovery and biocompatibility of solvents for extraction from cultures of Botryococcus braunii

Various water-immiscible solvents were tested for biocompatibility and hydrocarbon recovery under different contact conditions with the hydrocarbon-rich microalga Botryococcus braunii. Eighteen solvents were first selected from a database of 1500 compounds (compiled for solvent selection for ethanol recovery from Saccharomyces cerevisiae fermentation). Nine of these candidate solvents were shown to be biocompatible with B. braunii following short contact times. This biocompatibility tends to be associated with high molecular weights and high boiling points but strongly depends on solvent chemical structure. A low polarity is essential to biocompatibility and calculated octanol-water partition coefficients, or capacity factors determined by reversed-phase high-performance liquid chromatography (HPLC), are suitable predictors of biocompatibility with B. braunii. High recoveries of hydrocarbons directly from the algal culture require relatively polar solvents and are, therefore, inimical with maintenance of cell viability. The inaccessibility of weakly polar solvents to the cell surface appears to protect the algae but also prevents substantial recovery of the hydrocarbons stored in B. braunii outer walls. In order to achieve a high recovery, contact with the solvent must be carried out on algae concentrated by filtration. Then, a large fraction of B. braunii hydrocarbons can be recovered, after a short contact time, without impairing cell viability. Under these conditions, the pertinent solvent property is affinity for the nonpolar hydrocarbons, and the highest recovery yield, approximately 70% after contact for 30 min, is achieved with hexane.     

Optimal selection of organic solvents for biocompatible extraction of beta-carotene from Dunaliella salina

In the aim of beta-carotene biocompatible extraction, toxicity of various pure solvents belonging to different homologous series has been investigated for Dunaliella salina. The results showed that solvents having logP(oct) > 5 or having a molecular weight over 150 g/mol can be considered biocompatible for this microalga. The membrane critical solvent concentration for each series of solvents has been calculated applying Osborne's model, showing that the aliphatic chlorinated hydrocarbon is the most toxic family studied. Mixtures of a biocompatible solvent (decane) with a toxic solvent (CH(2)Cl(2), MEK, MTBE) have been studied. The beta-carotene extraction ability of CH(2)Cl(2)-decane mixture was found six times more efficient than with pure decane. It has been demonstrated that the extraction ability of solvent depends on its affinity with the product extracted and on its concentration incorporated in the cellular membrane.     

Selection of salt hydrate pairs for use in water control in enzyme catalysis in organic solvents

The water activities (a(w)) of 13 salt hydrate pairs were determined from vapor pressure measurements; a(w) values for a subset were also estimated from a study of water transfer to isopropylether. The application of salt hydrates as water buffers was investigated in two models: (i) effect of hydration on the initial rate of subtilisincatalyzed transesterification of the nitrophenol ester of CBZ-alanine with butanol; and (ii) effect of hydrates on the equilibrium concentrations of reactants in the esterification of dodecanol and decanoic acid, catalyzed by lipase. Transfer of ions from salt to enzyme particles was also demonstrated. The implications of the results for the successful use of salt hydrates as water buffers are discussed. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 367-374, 1997.     

In situ extraction versus the use of an external column in fermentation

Summary Organic extraction of 2,3-butanediol produced by Klebsiella oxytoca fermentation was studied to determine if the use of an external column offered advantages over in situ extractive fermentation. Dodecanol was chosen from 24 tested solvents, 11 of which were non-toxic to K. oxytoca. Although growth occurred in all shakeflask experiments containing dodecanol, growth was never observed when dodecanol was used in an in situ arrangement in a fermentor. Using dodecanol in an external column, however, resulted in a cell yield of 0.10 g/g d-xylose, and a 2,3-butanediol yield of 0.32 g/g d-xylose, similar to results obtained in control (solventless) experiments. Although the partitioning of 2,3-butanediol in the organic phase was low, this study suggests that external columns, with recycling to the fermentor, can offer substantial advantages over in situ extraction.     

Proteins in organic solvents

Catalysis in organic solvents and the mapping of protein surfaces using multiple solvent crystal structures are two rapidly developing areas of research. Recent advances include the study of protein folding and stability in different solvents, and the demonstration that it is possible to qualitatively rank the affinities of protein binding sites for a given organic solvent using the multiple solvent crystal structures method.     

Rules for optimization of biocatalysis in organic solvents

General rules for the optimization of different biocatalytic systems in various types of media containing organic solvents are derived by combining data from the literature, and the logarithm of the partition coefficient, log P, as a quantitative measure of solvent polarity. (1) Biocatalysis in organic solvents is low in polar solvents having a log P < 2, is moderate in solvents having a log P between 2 and 4, and is high in a polar solvents having a log P > 4. It was found that this correlation between polarity and activity parallels the ability of organic solvents to distort the essential water layer that stabilizes the biocatalysts. (2) Further optimization of biocatalysis in organic solvents is achieved when the polarity of the microenvironment of the biocatalyst (log P(i)) and the continuous organic phase (log P(cph)) is tuned to the polarities of both the substrate (log P(s)) and the product (log P(p)) according to the following rules: |log P(i) - log P(s)| and |log P(cph) - log P(p)| should be minimal and |log P(cph) - log P(s)| and |log P(i) - log P(p)| should be maximal, with the exception that in the case of substrate inhibition log P(i), should be optimized with respect to log P(s) In addition to these simple optimization rules, the future developments of biocatalysis in organic solvents are discussed.     

Ethanol production by anaerobic thermophilic bacteria: Kinetics in fed-batch cultures ofClostridium thermohydrosulfuricum

Summary Fed-batch fermentations ofClostridium thermohydrosulfuricum are carried out using medium rich in nitrogen source and with glucose as growth limiting factor. The ethanol/lactate yield increases as the specific growth rate and specific rate of consumption of glucose diminish. Under the experimental conditions chosen here this yield attained 3.66 moles. mole^–1 with a maximal ethanol concentration of 12 g.l^–1. In batch fermentation, the maximum concentration of ethanol did not exceed 8 g.l^–1, independent of the concentration in glucose or nitrogen source applied.     

Antibody-antigen binding in organic solvents

We describe, for the first time, the action of antibodies in anhydrous organic solvents. It has been demonstrated that the binding of a hapten, 4-aminobiphenyl, to the immobilized monoclonal antibody 2E11 is strong and specific not only in water but also in a variety of non-aqueous media. Further, the strength of interaction between antibody and hapten has been related to the hydrophobicity of the solvent: the more hydrophobic the solvent, the weaker the protein-ligand interaction.     

Designing enzymes for use in organic solvents.

Enzymes are routinely used in organic solvents where numerous reactions of interest to synthetic and polymer chemists can be performed with high selectivity. Recently, it has become apparent that the catalytic properties of an enzyme can be tailored to a specific catalytic requirement by the use of solvent and protein engineering. The former involves altering the polarity, hydrophobicity, water content, etc., of the organic milieu, while the later applies site-directed mutagenesis to alter the physicochemical properties of the biocatalyst. The dominant effects of organic solvents on enzyme structure and function, and the potential of solvent and protein engineering to design enzymes to function optimally in organic media, are the major foci of this review.     

Isolation of choline esters from aqueous solutions by extraction with sodium tetraphenylboron in organic solvents

1. The method is based on the observation that choline esters and sodium tetraphenylboron (Kalignost) form complexes that are insoluble in water but soluble in organic solvents such as nitriles, higher ketones and benzyl alcohol. 2. The extraction procedure is an example of liquid cation exchange where tetraphenylboron is the cation-exchange group. 3. The proportion of choline esters extracted depends on the type and total amount of cation in the aqueous phase and the amount of sodium tetraphenylboron in the organic solvent. 4. The proportion of choline esters extracted is independent of the choline ester concentration, the pH (between 8 and 3) and the relative volumes of the two phases. 5. The affinity of sodium tetraphenylboron for choline esters increases with an increase in the size of the acyl group. 6. The choline ester extracted can be released into an aqueous solution by treatment with strong acids, silver salts and anion-exchange resins.