Diacetyl fermentation coupled with pervaporation using oleyl alcohol supported liquid membrane

Pervaporation using oleyl alcohol supported liquid membrane was successfully applied to diacetyl fermentation by immobilized lactic acid bacteria. Diacetyl productivity was about 10 g·m⁻³·h⁻¹, while productivity during batch fermentation was about 6 g·m⁻³·h⁻¹. Diacetyl yield from consumed glucose was about 0.04 g·g⁻¹ which was 4 times as large as that of batch fermentation. The pervaporation functioned favorably on actual fermentation broth. The flux of the permeate and the diacetyl separation factor for the pervaporation were about 9 g·m⁻²·h⁻¹ and 36, respectively, and these values were maintained at almost constant levels during fermentation. Diacetyl concentration in the permeate was about 2 kg·m⁻³, which is sufficiently high for commercial use.     

Continuous butanol/isopropanol fermentation in down-flow column reactor coupled with pervaporation using supported liquid membrane

Continuous butanol/isopropanol fermentation with immobilized Clostridium isopropylicum was performed in a downflow column reactor using molasses as the substrate. In order to prevent product inhibition and at the same time obtain high concentration of the products, the column reactor was coupled with a pervaporation module using a supported liquid membrane. The liquid membrane was prepared with oleyl alcohol nontoxic to the microorganism. In comparison with the continuous fermentation without product removal, the specific butanol production rate was 2 times higher. The butanol concentration in the permeate was 230 kg/m(3), which was about 50 times higher than that in the culture broth. A numerical investigation suggested a further increase in the productivity by improving the module construction.     

Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes

A simultaneous extraction-stripping process is proposed for separating volatile products from fermentation broths, it is based on pervaporation through a liquid membrane supported with a hydrophobic porous membrane. The liquid membrane prepared with oleyl alcohol was selected as the most suitable for separating volatile products resulting from acetone-butanol fermentation. The separation performance and stability of the oleyl alcohol liquid membrane were investigated by using dilute aqueous butanol and acetone solutions. The oleyl alcohol liquid membrane was found to be superior by far in both selectivity and permeability of butanol to the better known silicone rubber membrane in its high selectivity for alcohols. Using the oleyl alcohol liquid membrane, the dilute aqueous butanol solutions of around 4 g/L obtained in acetone-butanol fermentation could be concentrated up to 100 times. The stability of this liquid membrane was also quite good as long as the surface tension of the feed solution was less than the critical surface tension of the support membrane. No change in the separation performance was found after the continuous usage in a long period of 100 h.     

Ethanol stripping by pervaporation using porous PTFE membrane

In a shell-and-tube type of module containing either porous or nonporous tubular membranes, the sweeping action of a flow inert gas in the shell side was used to strip ethanol from an aqueous ethanol solution flowing countercurrently in the tube side. A calculation of the overall mass transfer coefficient, K_G, of the membrane used was made for this system. In ethanol stripping tests using a module containing polytetrafluoreethylene (PTFE) tubular membranes, the K_G was found to be more affected by the liquid flow rate than the gas flow rate. Moreover, the gas side mass transfer coefficient, k_G, was estimated to be about 5×10⁻⁵ mol/cm²·s·atm. The liquid side mass transfer coefficient, k_L, on the other hand, was found to increase linearly with the linear velocity of the aqueous solution. Also, at an average solution temperature range of 21 to 32°C, no significant change in the K_G was observed. Comparison of the K_G of different tubular membranes revealed that the K_G of the PTFE membrane was higher than that of polypropylene or silicone membranes under the given experimental conditions.     

Increase of substrate conversion by pervaporation in the continuous butanol fermentation

Summary In a continuous fermentation of glucose to butanol and isopropanol by immobilized Clostridium beyerinckii cells the products were removed continuously by pervaporation. Both the glucose conversion and the reactor productivity were 65–70% higher than in a continuous fermentation without product removal.     

Ethanol production from starch in a pervaporation membrane bioreactor using Clostridium thermohydrosulfuricum

To attain both high productivity and efficient recovery of ethanol from broth, a membrane bioreactor consisting of a jar fermentor and a pervaporation system was applied to the direct production of ethanol from uncooked starch with a thermophilic anaerobic bacterium, Clostridium thermohydrosulfuricum. From four types of ethanol-selective membranes tested, microporous polytetrafluoroethylene (PTFE) membrane, the pores of which are impregnated with silicone rubber, was chosen for its large flux, high ethanol selectivity, and high stability. During fed-batch fermentation with pervaporation in the membrane bioreactor, ethanol was continuously extracted and concentrated in two traps with concentrations at 5.6%-6.2% (w/w) in trap 1 (20 degrees C) and 27%-32% (w/w) in trap 2 (liquid N(2)), while the ethanol concentration in the broth was maintained at 0.85-0.9% (w/w). Due to the low ethanol concentration in the broth, and the immobilization of bacterial cells by the membrane, the number of viable cells, and, eventually, the ethanol productivity, increased in the membrane bioreactor.     

Characteristics of butanol metabolism in alcohol dehydrogenase-deficient deermice.

Deermice lacking the low-Km alcohol dehydrogenase eliminated butan-1-ol, a substrate for microsomal oxidation but not for catalase, at 117 mumol/min per kg body wt. Microsomal fractions and hepatocytes metabolized butan-1-ol also (Vmax. = 6.7 nmol/min per nmol of cytochrome P-450, Km = 0.85 mM; Vmax. = 5.3 nmol/min per 10(6) cells, Km = 0.71 mM respectively). These results are consistent with alcohol oxidation by the microsomal system in these deermice.     

Increased productivity of <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis> fermentation of acetone,butanol, and ethanol by pervaporation through supported ionic liquid membrane

Pervaporation proved to be one of the best methods to remove solvents out of a solvent producing Clostridium acetobutylicum culture. By using an ionic liquid (IL)-polydimethylsiloxane (PDMS) ultrafiltration membrane (pore size 60 nm), we could guarantee high stability and selectivity during all measurements carried out at 37°C. Overall solvent productivity of fermentation connected with continuous product removal by pervaporation was 2.34 g l⁻¹ h⁻¹. The supported ionic liquid membrane (SILM) was impregnated with 15 wt% of a novel ionic liquid (tetrapropylammonium tetracyano-borate) and 85 wt% of polydimethylsiloxane. Pervaporation, accomplished with the optimized SILM, led to stable and efficient removal of the solvents butan-1-ol and acetone out of a C. acetobutylicum culture. By pervaporation through SILM, we removed more butan-1-ol than C. acetobutylicum was able to produce. Therefore, we added an extra dose of butan-1-ol to run fermentation on limiting values where the bacteria would still be able to survive its lethal concentration (15.82 g/l). After pervaporation was switched off, the bacteria died from high concentration of butan-1-ol, which they produced.     

Water and oleyl alcohol as stationary liquid phases in gas—liquid chromatography : Determination of partition coefficients of volatile substances for analysis of quantitative structure—activity relationships

Indirect determination of partition coefficients of volatile substances in the system oleyl alcohol—water for analysis of quantitative structure—activity relationships is discussed. Water and oleyl alcohol were used as stationary liquid phases in gas—liquid chromatography. In order to correct the results for adsorption effects, two new procedures using a standard substance were suggested. The procedures were compared with a procedure used by Conder et al. Comparison of molar hydration enthalpies and entropies derived from experimental results of a series of aliphatic alcohols with calorimetric data proved that all procedures under consideration yielded true partition coefficients.     

Fast and efficient protein purification using membrane adsorber systems

The purification of proteins from complex cell culture samples is an essential step in proteomic research. Traditional chromatographic methods often require several steps resulting in time consuming and costly procedures. In contrast, protein purification via membrane adsorbers offers the advantage of fast and gentle but still effective isolation. In this work, we present a new method for purification of proteins from crude cell extracts via membrane adsorber based devices. This isolation procedure utilises the membranes favourable pore structure allowing high flow rates without causing high back pressure. Therefore, shear stress to fragile structures is avoided. In addition, mass transfer takes place through convection rather than diffusion, thus allowing very rapid separation processes. Based on this membrane adsorber technology the separation of two model proteins, human serum albumin (HSA) and immungluboline G (IgG) is shown. The isolation of human growth hormone (hGH) from chinese hamster ovary (CHO) cell culture supernatant was performed using a cation exchange membrane. The isolation of the enzyme penicillin acylase from the crude Escherichia coli supernatant was achieved using an anion exchange spin column within one step at a considerable purity. In summary, the membrane adsorber devices have proven to be suitable tools for the purification of proteins from different complex cell culture samples.     

Energy saving electron pathways in proteins

This paper is a contribution to the discussion of whether the general architecture of electron transfer sites in blue copper proteins is mainly a result of the structural preferences of the metal ion or is induced by the protein. Although the site is probably stable only when protected by the protein, there appears to be no strain from the latter on the structure in the vicinity of the copper atom. For an operative redox site it is further required that the geometry of the site is acceptable for both oxidation states, to avoid high reorganization energy. The site must also be connected to the outer world by suitable tunneling pathways. The blue copper sites appear to fulfill these requirements, but it is difficult to assess the role of evolutionary pressure to form electron transfer proteins in general.     

Efficient purification of DNA fragments using a protein binding membrane

A novel and efficient method has been developed for isolation of correctly digested DNA fragments without the use of classic size-dependent electrophoretic separation methods. To achieve this, DNA fragments are end-labelled by haptens. After specific endonuclease digestion of the hapten-labelled DNA, the DNA is incubated with a protein that specifically binds to the hapten. The incubation mixture is then passed through a cartridge containing a protein-binding membrane that does not bind DNA. Undigested and partly digested DNA are retained on the membrane, while correctly digested DNA is selectively recovered for use in further downstream applications.     

Enhanced purification of plasmid DNA using Q-Sepharose by modulation of alcohol concentrations

Ion-exchange chromatography is one of the most commonly used methods for plasmid preparation. In this study a modified method was used to purify plasmid from bacterial lysate using Q-Sepharose. Incorporation of alcohols into the washing buffers enhanced the separation of plasmid from RNA and proteins. The use of isopropanol and ethanol achieved a high yield and purity whereas the use of methanol failed to improve the plasmid purification using Q-Sepharose by batch adsorption-desorption. Stepwise elution containing various concentrations of isopropanol and NaCl was used in preparative chromatography to enhance the plasmid purification. The same stepwise elution was applied to the chromatography columns packed with 0.5, 20, and 200 ml of Q-Sepharose for plasmid purification from 7.5, 300, and 3000 ml bacterial broth, respectively. Complete separation of DNA from RNA and proteins was achieved under gravity flow by modulation of the alcohol concentrations in the stepwise elution. These three scales of chromatography maintained an approximate plasmid yield and the purified plasmid contained undetectable levels of RNA and protein.     

Ethanol production in a continuous fermentation/membrane pervaporation system

The productivity of ethanol fermentation processes, predominantly based on batch operation in the U.S. fuel ethanol industry, could be improved by adoption of continuous processing technology. In this study, a conventional yeast fermentation was coupled to a flat-plate membrane pervaporation unit to recover continuously an enriched ethanol stream from the fermentation broth. The process employed a concentrated dextrose feed stream controlled by the flow rate of permeate from the pervaporation unit via liquid-level control in the fermentor. The pervaporation module contained 0.1 m² commercially available polydimethylsiloxane membrane and consistently produced a permeate of 20%–23% (w/w) ethanol while maintaining a level of 4%–6% ethanol in a stirred-tank fermentor. The system exhibited excellent operational stability. During continuous operation with cell densities of 15–23 g/l, ethanol productivities of 4.9–7.8 gl^–1 h^–1 were achieved utilizing feed streams of 269–619 g/l glucose. Pervaporation flux and ethanol selectivities were 0.31–0.79 lm^–2 h^–1 and 1.8–6.5 respectively.     

Simulating the effect of alcohol on the structure of a membrane

Adsorption of alcohol molecules or other small amphiphilic molecules in the cell membrane can induce significant changes in the structure of the membrane. To understand the molecular mechanisms underlying these structural changes, we developed a mesoscopic membrane model. Molecular simulations on this model nicely reproduce the experimental phase diagrams. We find that alcohol can induce an interdigitated structure in which the normal bilayer structure changes into a monolayer in which the alcohol molecules screen the hydrophobic tails from the water phase. We compute the effect of the chain length of the alcohol on the phase behaviour of the membrane. At low concentrations of alcohol, the membrane has domains of the interdigitated phase that are in coexistence with the normal membrane phase. We use our model to clarify some of the experimental questions related to the structure of the interdigitated phase and put forward a simple model that explains the alcohol chain length dependence of the stability of this interdigitated phase.     

Continuous production of butanol from a glucose/xylose mixture with an immobilized cell system coupled to pervaporation

Summary Glucose and xylose can be converted continuously and simultaneously to butanol using immobilized cells. Xylose is only converted when glucose is completely consumed and the biocatalyst is not fully inhibited by butanol. With pervaporation for in-situ butanol recovery the complete conversion of a feed containing 60 kg/m³ of mixed sugars is achieved.     

Rapid purification of yeast alcohol dehydrogenase

Making use of the unusual stability of yeast alcohol dehydrogenase in the presence of ethanol, a simple, rapid procedure for isolating this enzyme in high yield is presented. Once-crystallized enzyme is obtained within 5 h of commencing the procedure; this is undegraded and substantially free of proteolytic activity.