Caspase cleavage product lacking amino-terminus of IkappaBalpha sensitizes resistant cells to TNF-alpha and TRAIL-induced apoptosis

In response to a diverse array of signals, IkappaBalpha is targeted for phosphorylation-dependent degradation by the proteasome, thereby activating NF-kappaB. Here we demonstrate a role of the cleavage product of IkappaBalpha in various death signals. During apoptosis of NIH3T3, Jurkat, Rat-1, and L929 cells exposed to tumor necrosis factor (TNF)-related apoptosis-inducing ligand (TRAIL), Fas, serum deprivation, or TNF-alpha, respectively, IkappaBalpha was cleaved in a caspase-dependent manner. In vitro and in vivo cleavage assays and site-directed mutagenesis showed that caspase-3 cleaved IkappaBalpha between Asp31 and Ser32. Expression of the cleavage product lacking amino-terminus (1-31), DeltaIkappaBalpha, sensitized otherwise resistant NIH3T3 fibroblast cells to apoptosis induced by TNF-alpha or TRAIL, and HeLa tumor cells to TNF-alpha. DeltaIkappaBalpha was more pro-apoptotic compared to wild type or cleavage-resistant (D31E)IkappaBalpha mutant and the sensitization elicited by DeltaIkappaBalpha was as effective as that by the dominant negative mutant, (S32,36A)IkappaBalpha, in NIH3T3 cells. DeltaIkappaBalpha suppressed the transactivation of NF-kappaB induced by TNF-alpha or TRAIL, as reflected by luciferase-reporter activity. Conversely, expression of the p65 subunit of NF-kappaB suppressed TNF-alpha-, TRAIL-, and serum deprivation-induced cell death. On the contrary, DeltaIkappaBalpha was less effective at increasing the death rate of HeLa cells that were already sensitive to death signals including TRAIL, etoposide, or taxol. These results suggest that DeltaIkappaBalpha generated by various death signals sensitizes cells to apoptosis by suppressing NF-kappaB activity.     

Versatile macrolide-responsive mammalian expression vectors for multiregulated multigene metabolic engineering

The novel macrolide-inducible and -repressible mammalian gene regulation systems (E.REX) have been cloned into a variety of sophisticated expression configurations including (1) multi-purpose expression vectors, (2) pTRIDENT-based artificial operons, (3) dual-regulated expression strategies for independent control of two different transgenes, (4) autoregulated vectors for one-step installation of adjustable multigene expression, and (5) oncoretroviral and lentiviral plasmids for transduction of macrolide-, streptogramin- and tetracycline-dependent transactivators and production of cell lines supporting independent control of three different transgenes. This vector portfolio represents a construction kit-like toolbox for efficient installation of adjustable gene expression responsive to clinically licensed antibiotics and enables the design of multiregulated multigene metabolic engineering strategies required for biopharmaceutical manufacturing, gene therapy, and tissue engineering.     

Impact of coexpression and coamplification of sICAM and antiapoptosis determinants bcl-2/bcl-x(L) on productivity,cell survival,and mitochondria number in CHO-DG44 grown in suspension and serum-free media

We have engineered dihydrofolate reductase-negative (dhfr-/-) Chinese hamster ovary (CHO) DG44 cells adapted for growth in serum-free suspension cultures for simultaneous expression of the common cold therapeutic, the soluble intercellular adhesion molecule 1 (sICAM), and the antiapoptosis determinants bcl-2 or bcl-x(L). Detailed analyses of titer and antiapoptosis characteristics of these production cell lines included an independent (sICAM; bcl-2/bcl-x(L)) as well as a cocistronic (sICAM-(bcl-2/bcl-x(L))) expression set-up in which translation-initiation of the survival cistron is driven by an internal ribosome entry site (IRES) of the encephalomyocarditis virus (EMCV). In transient transfections or stable mixed populations and in comparison to isogenic sICAM-only control vectors, both bcl-x(L)-encoding configurations achieved higher sICAM yields while bcl-2 over-expression resulted in decreased product levels. Overall, the death-protective impact of bcl-2 and bcl-x(L) in engineered CHO-DG44 was not significant under typical batch-mode operation, an observation that was confirmed by clonal analysis. bcl-2 and bcl-x(L) displayed their antiapoptosis potential only following dhfr-based amplification in sICAM-producing CHO-DG44 cell lines. In all cases, bcl-x(L) outperformed bcl-2 in its cell death-protective capacity. Amplification-dependent high-level expression of mitochondria-localized bcl-2 family members required for successful antiapoptosis engineering may be essential to compensate for increased mitochondria numbers found to be associated with production cell lines grown in serum-free medium.     

Binding mechanisms for Thermobifida fusca Cel5A,Cel6B,and Cel48A cellulose-binding modules on bacterial microcrystalline cellulose

The family II cellulose-binding modules (CBM) from Thermobifida fusca Cel5A and Cel48A were cloned in the Escherichia coli/Streptomyces shuttle vector pD730, and the plasmids were transformed into Streptomyces lividans TKM31. CBM(Cel5A), and CBM(Cel48A), CBM(Cel6B) were expressed and purified from S. lividans. The molecular masses were determined by mass spectrometry, and the values were 10595 +/- 2, 10915 +/- 2, and 11291 +/- 2 Da for CBM(Cel5A), CBM(Cel6B), and CBM(Cel48A), respectively. Three different binding models (Langmuir, Interstice Penetration, and Interstice Saturation) were tested to describe the binding isotherms of these CBMs on bacterial microcrystalline cellulose (BMCC). The experimental binding isotherms of T. fusca family II CBMs on BMCC are best modeled by the Interstice Saturation model, which includes binding to the constrained interstice surface of BMCC as well as traditional Langmuir binding on the freely accessible surface. The Interstice Saturation model consists of three different steps (Langmuir binding, interstice binding, and interstice saturation). Full reversibility only occurred in the Langmuir region. The irreversibility in the interstice binding and saturation regions probably was caused by interstice entrapment. Temperature shift experiments in different binding regions support the interstice entrapment assumption. There was no systematic difference in binding between the two types of exocellulase CBMs--one that hydrolyzes cellulose from the nonreducing (CBM(Cel6B)) end and one that hydrolyzes cellulose from the reducing end (CBM(Cel48A)).     

Use of at-line and in-situ near-infrared spectroscopy to monitor biomass in an industrial fed-batch Escherichia coli process

One of the key goals in bioprocess monitoring is to achieve real-time knowledge of conditions within the bioreactor, i.e., in-situ. Near-infrared spectroscopy (NIRS), with its ability to carry out multi-analyte quantification rapidly with little sample presentation, is potentially applicable in this role. In the present study, the application of NIRS to a complex, fed-batch industrial E. coli (RV308/PHKY531) process was investigated. This process undergoes a series of temperature changes and is vigorously agitated and aerated. These conditions can pose added challenges to in-situ NIRS. Using the measurement of a key analyte (biomass) as an illustration, the details of the relationship between the at-line and in-situ use of NIRS are considered from the viewpoint of both theory and practical application. This study shows that NIRS can be used both at-line and in-situ in order to achieve good predictive models for biomass. There are particular challenges imposed by in-situ operation (loss of wavelength regions and noise) which meant the need for signal optimisation studies. This showed that whilst the at-line modelling process may provide some useful information for the in-situ process, there were distinct differences. This study shows that the in-situ use of NIRS in a highly challenging matrix (similar to those encountered in current industrial practice) is possible, and thus extends previous works in the area.     

Advantages of using non-isothermal bioreactors for the enzymatic synthesis of antibiotics: the penicillin G acylase as enzyme model

A new hydrophobic and catalytic membrane was prepared by immobilizing Penicillin G acylase (PGA, EC.3.5.1.11) from E. coli on a nylon membrane, chemically grafted with butylmethacrylate (BMA). Hexamethylenediamine (HMDA) and glutaraldehyde (Glu) were used as a spacer and coupling agent, respectively. PGA was used for the enzymatic synthesis of cephalexin, using D(-)-phenylglycine methyl ester (PGME) and 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) as substrates. Several factors affecting this reaction, such as pH, temperature, and concentrations of substrates were investigated. The results indicated good enzyme-binding efficiency of the pre-treated membrane, and an increased stability of the immobilized PGA towards pH and temperature. Calculation of the activation energies showed that cephalexin production by the immobilized biocatalyst was limited by diffusion, resulting in a decrease of enzyme activity and substrate affinity. Temperature gradients were employed as a way to reduce the effects of diffusion limitation. Cephalexin was found to linearly increase with the applied temperature gradient. A temperature difference of about 3 degrees C across the catalytic membrane resulted into a cephalexin synthesis increase of 100% with a 50% reduction of the production times. The advantage of using non-isothermal bioreactors in biotechnological processes, including pharmaceutical applications, is also discussed.     

The effect of ajmalicine spiking and resin addition timing on the production of indole alkaloids from Catharanthus roseus cell cultures

The potential for the feedback inhibition of indole alkaloid synthesis was investigated by spiking suspension cultures of Catharanthus roseus with 0, 9, or 18 mg/L ajmalicine on day 0. The production of ajmalicine, catharanthine, and serpentine were inhibited in a dose-dependent manner. The inhibition was transient as the exogenous ajmalicine was ultimately either metabolized in the medium or within the cell. The addition of neutral resin has previously been shown to enhance ajmalicine production. To minimize product inhibition and product metabolism, Amberlite XAD-7 resin was added to immobilized cultures of C. roseus starting on either day 0, 5, or 15, and fresh resin was exchanged for spent resin every 5 days. The addition of resin did not decrease the viability of the culture. Growth was reduced only in cultures with resin added on day 0. Alkaloid production was enhanced to different extents by the timing of resin addition, suggesting that feedback inhibition or product metabolism was present throughout the culture period. Ajmalicine recovery was nearly 100% when the resin was added initially either on day 0 or day 5. Ajmalicine recovery was reduced to 55% when the resin was added later in the culture period starting on day 15, presumably because of resin saturation or the inaccessibility of alkaloids trapped in the vacuole. Delaying the addition of XAD-7 resin until 5 days after the start of the culture resulted in the highest improvement in ajmalicine production, i.e approximately 70% and also resulted in the complete recovery of ajmalicine from the cell.     

Continuous isolation of plasmid DNA by annular chromatography.

Continuous chromatographic separations, especially of multicomponent mixtures, constitute interesting options for biotechnological downstream processing. Taking the separation of plasmid DNA from clearified lysates on hydroxyapatite as a pertinent example, we discuss the potential of continuous annular chromatography (CAC) in comparison with conventional (preparative) batch chromatography. In CAC the column is realized in the form of a thin (5 mm, height 210 mm) slowly rotating annulus. The performance of such a CAC column is compared to that of an ("analytical") batch column of similar thickness (diameter) and length (4 x 250 mm) and that of a ("preparative") batch column of similar cross-sectional surface area and height (50 x 210 mm). The quality of the obtained plasmid as defined by the appearance of the corresponding agarose gels (native and linearized plasmid), the 260/280 ratio and the biological activity (transient transfection of HEK 293 cells) was found to be identical in all three cases. The yields are also shown to be equivalent. The loading factor is found to be the most decisive parameter for the transfer of a given separation method between the continuous and the batch columns. Under nonoptimized conditions, plate numbers tended to be lower in the continuous compared to the batch columns. This is shown to be largely due to an artifact created by the CAC design (collection of averaged fractions at the outlets) and can be overcome by optimizing the rotation speed. Surprisingly the large batch column consistently gave better plate numbers than either the small batch or the CAC column. Compared to the preparative batch column, wall effects are more pronounced in the CAC (respectively the small diameter batch column), which may translate into better bed stability but conceivably also contributes to an increase in plate height, due to the reduction in bed density usually observed in the proximity of the wall. The CAC is shown to be a powerful approach to continuous chromatography, which allows a direct and straightforward upscale of chromatographic bioseparation methods.     

Phase separation rates of aqueous two-phase systems: correlation with system properties

The kinetics of phase separation in aqueous two-phase systems have been investigated as a function of the physical properties of the system. Two distinct situations for the settling velocities were found, one in which the light, organic-rich (PEG) phase is continuous and the other in which the heavier, salt-rich (phosphate) phase is continuous. The settling rate of a particular system is a crucial parameter for equipment design, and it was studied as a function of measured viscosity and density of each of the phases as well as the interfacial tension between the phases. Interfacial tension increases with increasing tie line length. A correlation that describes the rate of phase separation was investigated. This correlation, which is a function of the system parameters mentioned above, described the behavior of the system successfully. Different values of the parameters in the correlation were fitted for bottom-phase-continuous and top-phase-continuous systems. These parameters showed that density and viscosity play a role in the rate of separation in both top continuous- and bottom continuous-phase regions but are more dominant in the continuous top-phase region. The composition of the two-phase system was characterized by the tie line length. The rate of separation increased with increasing tie line length in both cases but at a faster rate when the bottom (less viscous) phase was the continuous phase. These results show that working in a continuous bottom-phase region is advantageous to ensure fast separation.