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Ho Nam Chang

Publications and source records attributed to Ho Nam Chang.

13 recordsLinked to original sources

Crosslinked enzyme aggregates in hierarchically-ordered mesoporous silica: a simple and effective method for enzyme stabilization.

alpha-chymotrypsin (CT) and lipase (LP) were immobilized in hierarchically-ordered mesocellular mesoporous silica (HMMS) in a simple but effective way for the enzyme stabilization, which was achieved by the enzyme adsorption followed by glutaraldehyde (GA) crosslinking. This resulted in the formation of nanometer scale crosslinked enzyme aggregates (CLEAs) entrapped in the mesocellular pores of HMMS (37 nm), which did not leach out of HMMS through narrow mesoporous channels (13 nm). CLEA of alpha-chymotrypsin (CLEA-CT) in HMMS showed a high enzyme loading capacity and significantly increased enzyme stability. No activity decrease of CLEA-CT was observed for 2 weeks under even rigorously shaking condition, while adsorbed CT in HMMS and free CT showed a rapid inactivation due to the enzyme leaching and presumably autolysis, respectively. With the CLEA-CT in HMMS, however, there was no tryptic digestion observed suggesting that the CLEA-CT is not susceptible to autolysis. Moreover, CLEA of lipase (CLEA-LP) in HMMS retained 30% specific activity of free lipase with greatly enhanced stability. This work demonstrates that HMMS can be efficiently employed as host materials for enzyme immobilization leading to highly enhanced stability of the immobilized enzymes with high enzyme loading and activity.

Chymotrypsin↗

Array-based mutation detection of BRCA1 using direct probe/target hybridization.

We describe here an efficient microarray-based multiplex assay to detect Korean-specific mutations in breast cancer susceptibility gene BRCA1 using direct probe/target hybridization. Allele-specific oligonucleotides were covalently immobilized on an aldehyde-activated glass slide to prepare an oligonucleotide chip. From a wild-type sample, a two-step method was used to generate labeled multiplex polymerase chain reaction (PCR) amplification products of genomic regions containing the mutation sites. Amino allyl-dUTP, an amine-modified nucleotide, was incorporated during multiplex PCR amplifications and a monofunctional form of cyanine 3 dye was subsequently attached to the reactive amine group of the PCR products. Hybridization of the labeled PCR products to the oligonucleotide chip successfully identified all of the genotypes for the selected mutation sites. This work demonstrates that oligonucleotides chip-based analysis is a good candidate for efficient clinical testing for BRCA1 mutations when combined with the indirect strategy to prepare labeled target samples.

BRCA1 Protein↗

Simple synthesis of hierarchically ordered mesocellular mesoporous silica materials hosting crosslinked enzyme aggregates.

Hierarchically ordered mesocellular mesoporous silica materials (HMMS) were synthesized using a single structure-directing agent. The mesocellular pores are synthesized without adding any pore expander; the pore walls are composed of SBA-15 type mesopores. Small-angle X-ray scattering revealed the presence of uniform pore structures with two different sizes. Using HMMS as a nanoscopic template, hierarchically ordered mesocellular mesoporous carbon (HMMC) and polymer (HMMP) materials were synthesized. HMMS was used as a host for enzyme immobilization. To improve the retention of enzymes in HMMS, we adsorbed enzymes, and then employed crosslinking using glutaraldehyde (GA). The resulting crosslinked enzyme aggregates (CLEAs) show an impressive stability with extremely high enzyme loadings. For example, 0.5 g alpha-chymotrypsin (CT) could be loaded in 1 g of silica with no activity decrease observed with rigorous shaking over one month. In contrast, adsorbed CT without GA treatment resulted in a lower loading, which further decreased due to continuous leaching of adsorbed CT under shaking. The activity of crosslinked CT aggregates in HMMS was approximately 10 times higher than that of the adsorbed CT, which represents a 74-fold increase in activity per unit weight of HMMS due to higher CT loading.

Adsorption↗

High cell density fed-batch cultivation of Escherichia coli using exponential feeding combined with pH-stat.

A new feeding strategy in fed-batch culture, exponential feeding combined with pH-stat is suggested to avoid the accumulation of substrate in culture broth. Exponential feeding was stopped whenever a predetermined amount of limiting substrate was supplied and then pH change was observed. When pH rose above an upper limit due to the depletion of substrate, feeding was restarted. With this feeding strategy, recombinant Escherichia coli could be grown to 101 g/l by controlling the specific growth rate at 0.1 h(-1).

Acetic Acid↗

Selective extraction of acetic acid from the fermentation broth produced by Mannheimia succiniciproducens.

Acetic acid is by-product from fermentation processes for producing succinic acid using Mannheimia succiniciproducens . To obtain pure succinic acid from the final fermentation broth, acetic acid was selectively removed based on the different extractability of succinic acid and acetic acid with pH using tri-n-octylamine (TOA) as extractant. When successive batch extractions were performed using 0.25 mol TOA kg(-1) dissolved in 1-octanol at pH 5, the mol ratio of succinic acid to acetic acid before extraction was 4.9 and the final ratio after the fourth batch was 9.4.

Acetic Acid↗

Inhibitory effect of carbon dioxide on the fed-batch culture of Ralstonia eutropha: evaluation by CO2 pulse injection and autogenous CO2 methods.

In order to see the effect of CO(2) inhibition resulting from the use of pure oxygen, we carried out a comparative fed-batch culture study of polyhydroxybutyric acid (PHB) production by Ralstonia eutropha using air and pure oxygen in 5-L, 30-L, and 300-L fermentors. The final PHB concentrations obtained with pure O(2) were 138.7 g/L in the 5-L fermentor and 131.3 g/L in the 30-L fermentor, which increased 2.9 and 6.2 times, respectively, as compared to those obtained with air. In the 300-L fermentor, the fed-batch culture with air yielded only 8.4 g/L PHB. However, the maximal CO(2) concentrations in the 5-L fermentor increased significantly from 4.1% (air) to 15.0% (pure O(2)), while it was only 1.6% in the 30-L fermentor with air, but reached 14.2% in the case of pure O(2). We used two different experimental methods for evaluating CO(2) inhibition: CO(2) pulse injection and autogenous CO(2) methods. A 10 or 22% (v/v) CO(2) pulse with a duration of 3 or 6 h was introduced in a pure-oxygen culture of R. eutropha to investigate how CO(2) affects the synthesis of biomass and PHB. CO(2) inhibited the cell growth and PHB synthesis significantly. The inhibitory effect became stronger with the increase of the CO(2) concentration and pulse duration. The new proposed autogenous CO(2) method makes it possible to place microbial cells under different CO(2) level environments by varying the gas flow rate. Introduction of O(2) gas at a low flow rate of 0.42 vvm resulted in an increase of CO(2) concentration to 30.2% in the exit gas. The final PHB of 97.2 g/L was obtained, which corresponded to 70% of the PHB production at 1.0 vvm O(2) flow rate. This new method measures the inhibitory effect of CO(2) produced autogenously by cells through the entire fermentation process and can avoid the overestimation of CO(2) inhibition without introducing artificial CO(2) into the fermentor.

Bioreactors↗

Characterization of an oxygen-dependent inducible promoter, the Escherichia coli nar promoter, in gram-negative host strains.

The Escherichia coli nar promoter is maximally induced under anaerobic conditions in the presence of nitrate ion or under anaerobic only conditions, depending on the genotype of the E. coli nar promoter. Previously, we found that the E. coli nar promoter has some desirable characteristics as an inducible promoter in the E. coli host strains. In this study, the E. coli nar promoter with lacZ gene at the downstream was cloned onto a broad-host-range Gram-negative vector, pBBR122. It was then induced in some other Gram-negative host strains, such as Agrobacterium, Pseudomonas, and Rhizobium, to determine whether the E. coli nar promoter could be used as an inducible promoter in these strains. From shake-flask experiments it was found that the wild-type E. coli nar promoter cloned onto pBBR122, pNW61, was suppressed under aerobic conditions in an Agrobacterium host strain, was partially induced under microaerobic only conditions, and was maximally induced under microaerobic conditions in the presence of nitrate ion. Whereas the mutant-type E. coli nar promoter cloned onto pBBR122, pNW618, was suppressed under aerobic conditions and was maximally induced under microaerobic conditions, regardless of the presence of nitrate ion. This kind of induction pattern observed for the E. coli nar promoters in the Agrobacterium host strain was similar to that observed for the E. coli nar promoters in the E. coli host strain. On the other hand, it was found that both of the E. coli nar promoters, pNW61 and pNW618, in a Pseudomonas host strain were partially induced under aerobic conditions and were maximally induced under microaerobic conditions, regardless of the presence of nitrate. Finally, it was found that both of the E. coli nar promoters in a Rhizobium host strain were minimally induced, regardless of the presence of oxygen or nitrate ion. Similar induction patterns for the three strains were also observed from fermentor experiments in which the dissolved oxygen (DO) level was tightly controlled. From an evolutionary point of view, the results from the three Gram-negative host strains indicate that the E. coli nar promoter system, including the promoter and regulatory proteins, was best conserved in the Agrobacterium host strain and the least conserved in the Rhizobium host strain. From an industrial point of view, the results indicate that the E. coli nar promoter system can be used as an oxygen-dependent inducible promoter in both Agrobacterium and Pseudomonas host strains.

Cloning, Molecular↗

Poly(3-hydroxybutyrate) synthesis in fed-batch culture of Ralstonia eutropha with phosphate limitation under different glucose concentrations.

Poly(3-hydroxybutyrate) (PHB) was produced by fed-batch cultures of Ralstonia eutropha with phosphate limitation under different glucose concentrations. When glucose was kept at 2.5 g l(-1), cell growth and PHB synthesis were limited due to the shortage of carbon source but a higher PHB content occurred in the cell-growth stage. This shows that a low glucose concentration is favorable for PHB accumulation in R. eutropha. PHB obtained with glucose at 9 g l(-1) is 1.6 times that obtained with 40 g l(-1). When glucose was in the range of 9 to 40 g l(-1), PHB concentration and productivity decreased significantly with the increase of glucose concentration. The highest PHB productivity was obtained with glucose at 9 g l(-1).

Bioreactors↗

Fed-batch cultures of Escherichia coli cells with oxygen-dependent nar promoter systems.

The recombinant proteins produced from Escherichia coli as a host cell need to be made at as low a cost as possible because of the end of the monopoly following expiry of the patent on early pharmaceutical proteins, and thus expanding applications to non-pharmaceutical large-scale products. We review in this article how the various promoters used in recombinant E. coli could affect its protein products, especially with emphasis on relatively new oxygen-dependent nar promoters for beta-galactosidase production. Several studies carried out in the authors' laboratory show that the nar promoter does not require any chemicals except 1% nitrate and oxygen for protein production. And according to recent work with the modified strains it is possible to produce the enzyme (beta-galactosidase) even without the nitrate ions at 45% of its total protein content when its cell density reached OD = 176.

Escherichia coli↗

Recovery of ammonium lactate and removal of hardness from fermentation broth by nanofiltration.

Nanofiltration (NF) was investigated as an alternative to desalting electrodialysis (ED) and ion exchange for the recovery of ammonium lactate from fermentation broth. Three commercial NF membranes, NF45, NF70, and NTR-729HF, were characterized with 50 mM NaCl, MgSO(4), and glucose solutions. NF45 membrane was selected because it showed the lowest rejection of monovalent ion, the highest rejection of divalent ion, and the highest rejection of nonpolar molecule. Effects of the operating pressure were investigated in a range of 100-400 psig, on the flux, lactate recovery, and glucose and magnesium removal from a real fermentation broth containing about 1.0 M of ammonium lactate. The flux and recovery rate increased linearly with the pressure. However, lactate rejection also increased with the pressure, lowering the recovery yield. More magnesium ions and glucose were rejected as the pressure was increased, and at 400 psig, for example, magnesium ion was almost completely rejected, highlighting the chance of obviating the necessity of ion exchange to remove hardness, by using NF instead of desalting ED. Membrane fouling was not so severe as expected, considering the complex nature and a rather high concentration of the fermentation broth treated.

Culture Media↗

Sequential feeding of glucose and valerate in a fed-batch culture of Ralstonia eutropha for production of poly(hydroxybutyrate-co-hydroxyvalerate) with high 3-hydroxyvalerate fraction.

Several important properties of poly(3-hydroxybutyric-co-3-hydroxyvaleric acids) (P(3HB-co-3HV) depend mainly on the HV unit fraction of the copolymer. Sequential and simultaneous feeding of glucose and valerate were employed to produce P(3HB-co-3HV) in a fed-batch culture of Ralstonia eutropha, and the effects of feeding models on the cell growth, 3HV unit fraction, and copolymer productivity have been investigated. The sequential feeding of glucose and then valerate resulted in a cell density of 110.2 g/L, 3HV unit fraction of 62.7 mol %, and copolymer productivity of 0.56 g/(L.h), while the latter simultaneous feeding strategy never achieved the 3HV fraction of P(3HB-co-3HV) higher than 50%. A nuclear magnetic resonance study confirmed that the production of random copolymer P(3HB-co-3HV) with high 3HV unit fraction was possible even with sequential feeding of glucose and valerate.

Bioreactors↗

Recombinant antibody production by perfusion cultures of rCHO cells in a depth filter perfusion system.

Recombinant Chinese hamster ovary cells, producing recombinant antibody against the human platelet, were cultivated in a depth filter perfusion system (DFPS). When perfusion cultures with working volume of 1 L were operated at perfusion rates of 5/d and 6/d, volumetric antibody productivities reached values 28 and 34 times higher than that of batch suspension culture in Erlenmeyer flasks and 43 and 53 times higher than that of batch culture in a controlled stirred tank reactor, respectively. Perfusion cultures in the DFPS showed stable antibody production over the whole culture period of up to 20 days. In the DFPS, inoculated cells in suspension were entrapped in a few hours within the depth filter matrix by medium circulation and retained there until the void space of the filter matrix was saturated by the cultured cells. After cells in the depth filter matrix reached saturation, overgrown viable cells at a perfusion rate of 5/d or 6/d were continuously collected into waste medium at a density of 2-4 x 10(5) cells/mL, which resulted in stable operation at high perfusion rates, maintaining values of process parameters such as glucose/lactate concentration, pH, and dissolved oxygen concentration. Because the DFPS overcomes most drawbacks observed with conventional perfusion systems, it is preferable to be used as a key culture system to produce monoclonal antibody stably for a long culture period.

Animals↗