Ethanol Production Using Concentrated Oak Wood Hydrolysates and Methods to Detoxify

Ethanol production from concentrated oak wood hydrolysate was carried out to obtain a high ethanol concentration and a high ethanol yield. The effect of added inhibitory compounds, which are typically produced in the pretreatment step of steam-explosion on ethanol fermentation, was also examined. p-Hydroxybenzoic aldehyde, a lignin-degradation product, was the most inhibitory compound tested in this study. Compounds with additional methyl groups had reduced toxicity and the aromatic acids were less toxic than the corresponding aldehydes. The lignin-degradation products were more inhibitory than the sugar-derived products, such as furfural and 5-hydroxymethylfurfural (HMF). Adaptation of yeast cells to the wood hydrolysate and detoxification methods, such as using charcoal and overlime, had some beneficial effects on ethanol production using the concentrated wood hydrolysate. After treatment with charcoal and low-temperature sterilization, the yeast cells could utilize the concentrated wood hydrolysate with 170 as well as 140 g/L glucose, and produce 69.9 and 74.2 g/L ethanol, respectively, with a yield of 0.46-0.48 g ethanol/g glucose. In contrast, the cells could not completely utilize untreated wood hydrolysate with 100 g/L glucose. Low-temperature sterilization, with or without charcoal treatment, was very effective for ethanol production when highly concentrated wood hydrolysates were used. Low-temperature sterilization has advantages over traditional detoxification methods, such as using overlime, ion exchange, and charcoal, because of the reduction in the total cost of ethanol production.

Effect of post-induction nutrient feeding strategies on the production of bioadhesive protein in Escherichia coli

The effect of post-induction nutrient feeding strategies on the production of bioadhesive protein using an IPTG inducible expression system in Escherichia coli was investigated. Cells were cultured in an exponential fed-batch mode to the OD600 of ca. 100 (48 gDCW/L) prior to induction. Six different post-induction nutrient feeding strategies (pH-stat, exponential, constant and linear change in feeding rate with three different slopes) were then applied, and bioadhesive protein production was examined. It was found that post-induction cell growth was independent of nutrient feeding rate. However, bioadhesive protein production was significantly affected by post-induction feeding strategies. Linearly changing post-induction feeding rate with a suitable slope allowed production of bioadhesive protein up to 5.3 g/L, which was higher than that obtained by the other post-induction feeding strategies.

Desulfurization of diesel oils by a newly isolated dibenzothiophene-degrading Nocardia sp. strain CYKS2

A dibenzothiophene (DBT)-degrading bacterial strain was isolated from dyeing industry wastewater and identified as Nocardia sp. CYKS2. The newly isolated bacterial strain Nocardia sp. CYKS2 was able to convert DBT to 2-hydroxybiphenyl (2-HBP) as the dead-end metabolite through a sulfur-specific pathway. Other organic sulfur compounds, such as thiophene derivatives, thiazole derivatives, sulfides, and disulfides were also desulfurized by Nocardia sp. CYKS2. In batch culture, 0.2 mM DBT was completely desulfurized in 60 h. After DBT was depleted, neither cell growth nor 2-HBP production was observed. When a model oil which DBT was dissolved in hexadecane was treated with growing cells, DBT was desulfurized from 10 mM to about 2 mM in 80 h. In this case, desulfurization rate was 0.279 mg-sulfur/(L-dispersion.h), which was about 2.5 times higher than that in the previous case of batch culture. When diesel oil was treated, the sulfur content decreased from 0.3 to 0.24 wt % in 48 h. A volumetric phase ratio of oil to water was 1/10 in this case. The sulfur decreased from 0.3 to 0.2 wt % in 48 h, when the volumetric phase ratio was 1/20. The desulfurization rates were 0.909 and 0.992 mg-sulfur/(L-dispersion.h), respectively.

Fed-batch cultivation of an oxygen-dependent inducible promoter system, the nar promoter in Escherichia coli with an inactivated nar operon

The nar promoter of Escherichia coli is maximally induced under anaerobic or microaerobic conditions in the presence of nitrate. We previously demonstrated in batch experiments that the intact nar promoter of E. coli cloned into a pBR322-based plasmid serves as a high-level expression system in a nar mutant of E. coli (Lee et al., 1996b). In this study, we extend characterization of the nar promoter expression system to the fed-batch culture mode, which is widely used in industrial-scale fermentation. From these experiments, it was found that the specific beta-galactosidase activity expressed from the lacZ gene fused to the nar promoter was maximal when host cells were grown under aerobic conditions [dissolved oxygen, (DO) = 80%] to absorbance at 600 nm (OD600) = 35 before induction of the nar promoter by lowering DO to 1-2% with alternating microaerobic and aerobic conditions. Approximately 15 h after induction, the OD600 of the culture reached 135 and the specific beta-galactosidase activity increased to 40,000 Miller units, equivalent to approximately 35% of the total cellular proteins. The specific beta-galactosidase activity before induction was approximately 1,000 Miller units, giving an induction ratio of approximately 40. Based on these results, we conclude that the nar promoter provides a convenient and effective high level expression system under conditions of fed-batch culture.

Angiogenesis and osteogenesis in an orthopedically expanded suture

The purpose of this study was to examine the angiogenic and the subsequent osteogenic responses during a 96-hour time-course after sutural expansion. Fifty rats were divided into: (1) a control group that received only angiogenic induction through injection of 5 ng/gm recombinant human endothelial cell growth factor (rhECGF); (2) an experimental group that received orthopedic expansion and rhECGF; (3) a sham group that received expansion and sodium chloride (NaCl) injection; and (4) a baseline group that received no expansion or injection. All rats were injected with 3H-thymidine (1.0 microCi/gm) 1 hour before death to label the DNA of S-phase cells. Demineralized sections (4 microm thick) were stained with hematoxylin and eosin. Angiogenesis and cell migration were analyzed with a previously established cell kinetics model. Analysis of variance was used to test the hypothesis that enhancement of angiogenesis stimulates reestablishment of osteogenic capability. Blood vessel number, area, and endothelial cell-labeled index significantly increased in experimental groups, but no difference was found between control and baseline groups. Labeled-pericyte index and activated pericyte numbers in the experimental group were also higher than in the sham groups. These results show that supplemental rhECGF enhances angiogenesis in expanded sutures but not in nonexpanded sutures. Data also suggest that pericytes are the source of osteoblasts in an orthopedically expanded suture.

Angiogenic induction and cell migration in an orthopaedically expanded maxillary suture in the rat

The purpose was to examine the effect of an angiogenic factor on cell migration patterns and osteoblast histogenesis during the 96 h following orthopaedic expansion of the anterior maxillary suture. Fifty rats were divided into four groups: (1) a control group that received only angiogenic induction via injection of 5 ng/g body wt recombinant human endothelial-cell growth factor; (2) an experimental group that received orthopaedic expansion and angiogenic induction; (3) a sham group that received orthopaedic expansion and normal saline injection; and (4) a baseline group that received no expansion or injection. The experimental and sham groups were subdivided to conduct experiments over 1, 2, 3 or 4 days. The anterior portion of each maxilla was dissected free and demineralized. Sections (4 microns thick) were cut from every block and stained with Mayer's haematoxylin and eosin. Cell migration was analysed using a previously established cell-kinetics model. The osteoprogenitor cells were divided into four categories according to nuclear volume: A cells (40-79 microns3), B cells (80-119 microns3), C cells (120-169 microns3) and D cells (> or = 169 microns3 A' cells are the portion of the A cell population that responds to osteogenic stimulus. As previously defined in periodontal ligament, the reciprocal association of a decreasing number of less differentiated (A + A) cells and an increasing number of C + D cells, as a function of distance from the nearest major blood vessel, was consistently found in all groups. This suggests a vascularly oriented gradient of progressively more differentiated osteoprogenitor cells. Also, A + A' cells were predominately located within 20 microns of the nearest major blood vessel whereas the C + D cells were found at a distance > 30 microns from the nearest major blood vessel. These results suggest that the A'-->C shift occurs 20-30 microns from the nearest major blood vessel. In the angiogenic induction groups, the numbers of committed osteoprogenitors (A + A') were significantly higher than in the sham group at day 1. At day 3, the numbers of preosteoblasts (C + D) in angiogenic sutures were significantly higher than in the sham groups. This enhancement of preosteoblast population strongly suggests the possible role of activated pericytes in expanded sutures as a source of osteoprogenitor cells.

The relationship of aging to endotoxin shock and to production of TNF-alpha

BACKGROUND

Aged people are considered prone to gram-negative bacteremia and septic shock. This relationship was tested in murine endotoxin shock.

METHODS

Balb/c mice of various ages (1.4-13.4 months) were intraperitoneally injected with lipopolysaccharide (LPS), and rates of survival were observed. The production of TNF-alpha in vivo induced by LPS was measured.

RESULTS

The survival rates were the smallest in the oldest and youngest groups. Production of TNF-alpha attained a maximum at 2 h after LPS injection and was smaller in the oldest group; it had a reciprocal relationship to survival rates in each group except the youngest group.

CONCLUSION

Old and young mice had smaller rates of survival and greater production of TNF-alpha following endotoxin shock induced by LPS.

Production of poly(3-hydroxybutyric acid) by recombinant Escherichia coli strains: genetic and fermentation studies

A number of Escherichia coli strains including K12, B, W, XL1-Blue, DH5 alpha, HB101, JM109, and C600 were transformed with the stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid biosynthesis genes, and were subsequently compared for their ability to synthesize and accumulate poly(3-hydroxybutyric acid) (PHB). The rate of PHB synthesis, the extent of PHB accumulation, and PHB yield from glucose varied considerably from one strain to another. Strains XL1-Blue and B harboring pSYL105 synthesized PHB at the highest rate to a final concentration of ca. 7 g/L in complex medium containing 20 g glucose/L. With an aim to reduce the cost of the medium, the effect on PHB accumulation of supplementing a defined medium with complex nitrogen sources was examined. A PHB concentration of 81 g/L could be obtained in 41 h from a pH-stat fed-batch culture of XL1-Blue(pSYL105) in a semidefined medium. When the availability of acetyl-CoA was increased by supplementing the medium with complex nitrogen sources, amino acids, or oleic acid, PHB synthesis by recombinant E. coli was enhanced.

Hypersensitivity to mosquito bite: a case report

Severe hypersensitivity to mosquito bites is very rare. A 18-year-old girl student has had multiple hemorrhagic bullae with atrophic scars on both limbs and left side of the face due to mosquito bites for 16 years. When she was seven years old, she noticed a severe local reaction with bloody bullae formation, chills, and fever several hours after the mosquito bite. The bullae developed into ulcers which finally became scars. This patient was confirmed to be hypersensitive to mosquito bites by the mosquito bite test. This case is the first record of mosquito allergy in Taiwan.

Production of poly(hydroxyalkanoic acid)

Poly(hydroxyalkanoic acid) [PHA] is accumulated by numerous microorganisms as an energy reserve material under unbalanced growth conditions in the presence of excess carbon source. In spite of being a good candidate for biodegradable thermoplastics, their high price compared with conventional plastics currently in use has limited their availability in a wide range of applications. With the aim of reducing the high production cost of PHA, much effort is currently being devoted to improve productivity by employing various microorganisms and by developing efficient culture techniques. Several processes recently developed and employed for the production of PHA by various bacteria are described.

Shikonin production by extractive cultivation in transformed-suspension and hairy root cultures of Lithospermum erythrorhizon

Effects of in situ extraction, fungal elicitation, a permeabilizing agent, and the oxygen transfer rate on shikonin production in transformed suspension and hairy root cultures of Lithospermum erythrorhizon were studied. Shikonin production with in situ extraction in transformed cell and hairy root cultures by n-hexadecane was 7.6 and 3 times higher than those of the control culture. Shikonin production of transformed L. erythrohizon increased with the enhanced gas exchange, and in situ extraction also increased sucrose consumption and shikonin production. The optimal volume of n-hexadecane in the hairy root culture was similar to that in the transformed cell cultures. In situ extraction at an earlier stage significantly enhanced shikonin production both in transformed cell and hairy root cultures. Dimethylsulfoxide used as a permeabilizing agent was harmful to cell growth and shikonin production, and permeabilizing was unnecessary when in situ extraction was applied. This occurred because with the solvent addition, most shikonin was spontaneously released from the cells and was dissolved in the solvent layer. The combined addition of n-hexadecane of the extract of the fungus Penicillium as an elicitor seemed to result in a higher production of shikonin both in cell suspensions and transformed root cultures. However, an increase of shikonin induction by fungal elicitation in a hairy root culture was not significant in comparison with that of normal cell cultures.

Immunoblot analysis of components of Penicillium citrinum recognized by human IgE and IgG antibodies

Penicillium species are well-known indoor fungi and have been considered as one of the causative agents of extrinsic bronchial asthma. We have identified that Penicillium citrinum is the most prevalent Penicillium species in the Taipei area. In the present study, components of this airborne fungus recognized by human IgE and IgG antibodies were analyzed by immunoblotting. Eight components ranging in MWs from 112 to 17.5 kD reacted with IgE antibodies in 11 serum samples. The component with an MW of about 33 kD showed the highest frequency (81.8%) of IgE-binding. However, 11 components of P. citrinum showed IgG-immunoblotting activity, and the component with an MW of about 66 kD revealed the highest frequency (58.3%) of IgG-binding. Only 3 of the 9 serum samples which reflected IgE antibody activity to the 33 kD component of P. citrinum showed IgG-immunoblotting activity to the same 33 kD component. Furthermore, 4 of the 5 serum samples obtained from healthy laboratory personnel demonstrated IgG responses, but none had IgE antibody activity to components of p. citrinum. The discrepancy observed between IgE and IgG responses to the same allergenic extract requires further investigation.

Construction of plasmids, estimation of plasmid stability, and use of stable plasmids for the production of poly(3-hydroxybutyric acid) by recombinant Escherichia coli

Plasmids containing the Alcaligenes eutrophus poly(3-hydroxybutyric acid) (PHB) biosynthetic genes were constructed for the production of PHB in Escherichia coli and plasmid stability was investigated by repeated subculturing without antibiotic pressure. Both pSYL101 (high copy) and pSYL102 (medium copy) were unstable during the subcultures. Higher instability was observed when cells were accumulating PHB. Segregational instability was aggravated by the faster growth of plasmid-free cells and by appearance of non-dividing cells harboring large amount of PHB during the fed-batch culture. Two derivatives, pSYL103 and pSYL104, were then developed by cloning the parB locus of plasmid R1 into pSYL102 and pSYL101, respectively. They showed 100% stability even during PHB synthesis and accumulation over 110 generations. All four plasmids were structurally stable. The final cell mass, PHB concentration, and PHB per dry cell weight (P/X, w/w, %) of 101.4 g l-1, 81.2 g l-1, and 80.1%, respectively, were obtained in 39 h by high cell density culture of XL1-Blue (pSYL104). The final PHB concentration was lower using XL1-Blue (pSYL103), which suggested that high gene dosage was required for the synthesis and accumulation of PHB to a high concentration in E. coli.

High density cell culture by membrane-based cell recycle

Enhancement of productivity of a bioprocess necessitates continuous operation of bioreactors with high biomass concentrations than are possible in conventional batch, fedbatch or continuous modes of culture. Membrane-based cell recycle has been effectively used to maintain high cell concentrations in bioreactors. This review compares membranebased cell recycle operation with other such high density cell culture systems as immobilized cell reactors and reactors with cell recycle by centrifugation or gravity sedimentation. A theoretical of production of primary and secondary metabolites in membrane-based recycle systems is presented. Operation of this type of system is discussed with examples from aerobic and anaerobic fermentations.

Bench-scale production of acrylamide using the resting cells of Brevibacterium sp. CH2 in a fed-batch reactor

Effects of various organic acids and salts on the stabilization of nitrile hydratase were investigated. The stability of the nitrile hydratase of Brevibacterium CH2 during storage was greatly enhanced by the addition of n-butyric acid. Effects of temperature, pH, and concentrations of acrylonitrile and n-butyric acid on acrylamide production by the resting cells were also investigated. Acrylamide production per unit dry weight of the cells increased 1.33 times by the addition of 0.05% n-butyric acid. A 20% acrylamide solution was successfully produced in a bench-scale reactor (12 l) with only a trace amount of salts after 10 h of hydration reaction under optimum reaction conditions without using an isotonic substrate. The conversion yield was nearly 100%, and acrylic acid as a by-product was not produced. Final acrylamide production of 400 g g-1 cells and productivity of 20 g/(g cells l-1 x h-1) were obtained.

Production of monoclonal antibodies against human chorionic gonadotropin by hybridoma cultures in calcium alginate capsules

A new method of making microcapsules with calcium alginate gel was developed and the cultivation of the encapsulated hybridoma cells producing monoclonal antibodies against human chorionic gonadotropin was investigated. A high cell density of 2.0 x 10(8) cells/cm3 in the capsules led to a high dilution rate of 0.67 per hour and resulted in the high volumetric monoclonal antibody productivity of 652.8 mg/l/day, which was 20-30 times higher than those of traditional continuous suspension cultures. However, long-term continuous culture was not achieved with this capsule system probably because of the limitation in nutrient supply and the accumulation of waste products. Also the analysis of oxygen transfer in this system showed that oxygen supply was not enough to support such a high cell density.

Continuous production of 6-APA in an aqueous two-phase system

An aqueous two-phase system of polyethylene glycol (PEG) and potassium phosphate provided a favorable environment for bioconversion of penicillin G to 6-aminopenicillanic acid (6-APA). The recombinant E. coli cells containing penicillin acylase were partitioned in the phosphate-rich bottom phase, and the product 6-APA in the PEG-rich top phase, which protected the enzyme from deactivation for a longer period of time. The continuous production of 6-APA by recycling the bottom phase showed a slight decrease in enzyme activity from initial 80 mM of 6-APA production to 61 mM during the eight days of operation at a space velocity of 0.12 hours-1. This work showed a possibility that the aqueous two-phase whole-cell enzyme bioconversion could serve as an alternative to immobilized cells on solid matrices.

Removal of hydrogen sulfide by Chlorobium thiosulfatophilum in immobilized-cell and sulfur-settling free-cell recycle reactors

Bioconversion of hydrogen sulfide to elementary sulfur by the photosynthetic bacterium Chlorobium thiosulfatophilum was studied in immobilized-cell and sulfur-settling free-cell recycle reactors. The cells immobilized in strontium alginate beads excreted elementary sulfur and accumulated it as crystal in the bead matrices, which made it possible that the reactor broth remained clear and the light penetrated the reactor deeper than with the free cells. In comparison with the free cells, the immobilized cells required 30% less light energy at a H2S removal rate of 2 mM/(L.h) and showed an activity of 2.4 times that of the free cells. However, in 40 h after the reaction the deterioration of the H2S removal efficiency became significant due to the accumulation of sulfur in the beads. The scanning electron micrograph (SEM) and energy-dispersive X-ray spectrometer (EDS) studies showed that the sulfur in the beads existed within a layer of 0.4 mm from the bead surface. In the sulfur-settling free-cell recycle reactor, about 80% of the sulfur excreted by the free cells could be removed in a settler. The 4-L fed batch reactor with the settler improved the light transmission to result in a H2S removal rate of 3 mumol/(mg of protein.h), 50% higher than that without it. The settling recycle reactor was much better in the removal of H2S than the immobilized-cell reactor because the former was a continuous system with the constant removal of sulfur particles by settling and of spent medium by supplying fresh medium at the same rate as the filtering rate of the reactor broth, while the latter was essentially a batch system where toxic metabolites and produced sulfur could not be removed.

Membrane bioreactors: present and prospects

Membrane bioreactors have a very handy in-situ separation capability lacking in other types of bioreactors. Combining various functions of membrane separations and biocatalyst characteristics of enzymes, microbial cells, organelles, animal and plant tissues can generate quite a number of membrane bioreactor systems. The cell retaining property of membranes and selective removal of inhibitory byproducts makes high cell density culture possible and utilizes enzyme catalytic activity better, which leads to high productivity of bioreactors. Enzyme reactions utilizing cofactors and hydrolysis of macromolecules are advantageous in membrane bioreactors. Anaerobic cell culture may be efficiently carried out in membrane cell recycle systems, while aerobic cultures work well in dual hollow fiber reactors. Animal and plant cells have much a better chance of success in membrane reactors because of the protective environment of the reactor and the small oxygen uptake rate of these cells. Industrial use of these reactors are still in its infancy and limited to enzyme and animal tissue culture, but applications will expand as existing problems are resolved.