A stirred bath technique for diffusivity measurements in cell matrices

A stirred bath technique was developed for determining effective diffusivities in cell matrices. The technique involves cell immobilization in a dilute gel which has negligible effect on solute diffusion. Agar and collagen were tested as immobilizing gels. Agar gel was shown to have minor interactions with the diffusion of various biological molecules, and was used for immobilization of Ehrlich Ascites Tumor (EAT) cells. Diffusivities of glucose and lactic acid were measured in EAT matrices for cell loadings between 20 and 45 vol %. Treatment with glutaraldehyde was effective in quenching the metabolic activity of the cells while preserving their physical properties and diffusive resistance. The measured data agree favorably with predictions based on Maxwell's equation for effective diffusion in a periodic composite material. The stirred bath technique is useful for diffusivity determinations in immobilized matrices or free slurries, and is applicable to both microbial and mammalian cell systems.

An attempt towards simultaneous biobased solvent based extraction of proteins and enzymatic saccharification of cellulosic materials from distiller's grains and solubles

Distiller's grains and solubles (DGS) is the major co-product of corn dry mill ethanol production, and is composed of 30% protein and 30-40% polysaccharides. We report a strategy for simultaneous extraction of protein with food-grade biobased solvents (ethyl lactate, d-limonene, and distilled methyl esters) and enzymatic saccharification of glucan in DGS. This approach would produce a high-value animal feed while simultaneously producing additional sugars for ethanol production. Preliminary experiments on protein extraction resulted in recovery of 15-45% of the protein, with hydrophobic biobased solvents obtaining the best results. The integrated hydrolysis and extraction experiments showed that biobased solvent addition did not inhibit hydrolysis of the cellulose. However, only 25-33% of the total protein was extracted from DGS, and the extracted protein largely resided in the aqueous phase, not the solvent phase. We hypothesize that the hydrophobic solvent could not access the proteins surrounded by the aqueous phase inside the fibrous structure of DGS due to poor mass transfer. Further process improvements are needed to overcome this obstacle.

Optimizing ammonia processing conditions to enhance susceptibility of legumes to fiber hydrolysis: alfalfa

An ammonia process was applied at several ammonia loadings, moisture contents, temperatures, and dwell times. A cellulase loading of 5 FPU/g dry matter and a 24 h incubation time were used to produce the sugars, which were measured as reducing sugars and by HPLC. Optimal processing conditions caused a 76% of theoretical yield (2.9-fold above untreated). Cellulose and hemicellulose conversions were 68 and 85% (vs 38 and 34% in untreated, respectively). The short hydrolysis time and relatively low enzyme loading suggests great potential to produce sugars from alfalfa.

Optimizing ammonia processing conditions to enhance susceptibility of legumes to fiber hydrolysis: Florigraze rhizoma peanut

A warm-season legume, Florigraze rhizoma peanut (FRP), was used as the source of fiber to produce sugars. FRP was subjected to several ammonia-processing conditions using temperature, biomass moisture content, and ammonia loading as process variables during a 5-min treatment. A cellulase loading of 2 FPU/g DM and 24 h incubation were used to produce the sugars. Total sugar yield was 3.34-fold higher in the optimal treatment (1.5 g ammonia/g DM-60%-90 degrees C) compared to untreated and was 65.3% of theoretical. Cellulose and hemicellulose conversions increased from 30 and 15.5% in untreated FRP to 78 and 34% in treated FRP.

Enzymatic hydrolysis of ammonia-treated sugar beet pulp

Sugar beet pulp is a carbohydrate-rich coproduct generated by the table sugar industry. Beet pulp has shown promise as a feedstock for ethanol production using enzymes to hydrolyze polymeric carbohydrates and engineered bacteria to ferment sugars to ethanol. In this study, sugar beet pulp underwent an ammonia pressurization depressurization (APD) pretreatment in which the pulp was exploded by the sudden evaporation of ammonia in a reactor vessel. APD was found to substantially increase hydrolysis efficiency of the cellulose component, but when hemicellulose- and pectin-degrading enzymes were added, treated pulp hydrolysis was no better than the untreated control.

Optimizing ammonia pressurization/depressurization processing conditions to enhance enzymatic susceptibility of dwarf elephant grass

An ammonia pressurization/depressurization process was investigated to evaluate the potential of producing reducing sugars from dwarf elephant grass, a warm-season forage. Moisture, temperature, and ammonia loading affected sugar yield (p < 0.0001). At optimal conditions, ammonia processing solubilized 50.9% of the hemicellulose and raised the sugar yield (percentage of theoretical) from 18 to 83%. Glucose and xylose production were increased 3.2- and 8.2-fold, respectively. The mild processing conditions of the ammonia treatment (90-100 degrees C, 5 min), the low enzyme loading (2 international filter paper units/g), and the short hydrolysis time (24 h), greatly enhance the potential of using forages to produce sugars valuable for several applications.

Alteration of glucose consumption kinetics with progression of baculovirus infection in Spodoptera frugiperda cells

We have used the initial-rate approach to characterize changes in the glucose consumption kinetics of baculovirus-infected Spodoptera frugiperda clone 9 (Sf9) cells with the progression of the infection process. The specific glucose consumption rate (qG) of cultured baculovirus-infected Sf9 cells was measured at 4, 8, 12, 16, and 24 h postinfection (h.p.i.) in media containing 4-35 mM glucose. Higher medium glucose concentrations resulted in higher final extracellular virus and recombinant beta-galactosidase yields. qG was related to the extracellular glucose concentration by means of a Michaelis-Menten relationship. The apparent Michaelis-Menten constant (K(m)) for glucose consumption was found not to change significantly during the progression of the infection process, and remained between 6.2 and 7.2 mM. However, the maximal specific glucose consumption rate (qGmax) was found to rapidly increase after infection, peaking at 16 h.p.i. at a value four times that for uninfected Sf9 cells. The kinetic analysis of glucose consumption rates in baculovirus-infected Sf9 cells presented here will aid in the optimal design and operation of bioreactor systems for the large-scale production of recombinant products from the baculovirus/insect cell system.

MALDI-MS as a monitor of the purification and folding of synthetic eclosion hormone

Analogues of the small protein Manduca sexta eclosion hormone (62 amino acids) were synthesized by Fmoc solid-phase methodology. Matrix-assisted laser desorption ionization mass spectrometry (MALDI-MS) was used to analyze the products of the syntheses and this information was used to design an efficient purification scheme. MALDI-MS was used to monitor the target products through purification and it was also used to monitor folding of the purified materials. The folded EH analogues were shown to be biologically active proteins with an in vivo bioassay using pharate adult moths, Heliothis virescens.

Heterologous protein expression affects the death kinetics of baculovirus-infected insect cell cultures: a quantitative study by use of n-target theory

The death of cultured insect cells after baculovirus infection is a time-dependent event. Without a quantitative model, it is difficult to characterize its kinetics. Our group has shown that the cell survival rate can be characterized by use of the n-target theory, which involves only two parameters: the number of hypothetical inactivation targets (n) and the first-order death rate (k). In this study, we used different recombinant viruses to examine the effect of heterologous protein expression on the cell survival rate. The proteins expressed were beta-galactosidase, human T-cell leukemia virus type I p40x, human interleukin-2, and human tissue plasminogen activator (tPA). The survival rate was affected by protein expression, but the n value remained constant if the protein expression level was high (above 30 mg/L). Low-level expression of secreted, glycosylated tPA resulted in a reduced n value, which was restored to the normal value when the tPA signal peptide and prosequence were deleted. In addition, if the n value was normal (10-11), the level of protein expression correlated negatively with the death rate. However, if the n value was reduced by unfavorable culture conditions or foreign protein expression, the expression level correlated positively with the death rate. A dimensionless plot with kt as the dimensionless time shows that alteration of the k value while retaining constant n is equivalent to a rescaling of time. Therefore, the survival curves with constant n reduce to a single curve on the dimensionless plot.(ABSTRACT TRUNCATED AT 250 WORDS)

Design and application of NMR-compatible bioreactor circuits for extended perfusion of high-density mammalian cell cultures

MR spectroscopy of cultured cells allows non-invasive analyses of the metabolism of cells with specific phenotypes under defined conditions. This technique can be used to investigate the intracellular metabolism of cells or extended to critically evaluate phenomena observed by in vivo MRS. In this paper, a cell maintenance system is described which allows MR analyses with unparalleled spectral resolution, S/N and stability. This system consists of a 25 mm diameter hollow fiber bioreactor and a supporting circuit. The hollow fiber reactor was chosen because it yields a large filling factor which can be perfused through defined volumes. The fibers were 300 microns diameter microporous (0.2 micron) cellulose acetate/cellulose nitrate membranes with high porosity, which allow bulk convective flow throughout the extracapillary space. This flow (Starling flow) is necessary to disrupt steady-state gradients in substrates and waste products. In many respects, the design of the supporting circuit is more important than the bioreactor itself, since it provides the reactor with the proper chemical and physical environment. Hence, this circuit can be applied to a variety of bioreactor configurations. The circuit consists of a hollow fiber oxygenator and a bleed-and-feed system housed in a temperature-controlled cabinet. Culture of mammalian cells in this reactor yields 31P spectra which have excellent spectral and temporal resolution. At confluence, endogenous 31P line widths were typically < 10 Hz (at 162 MHz) and well resolved spectra were obtained in < 30 s.

FTIR evidence for alcohol binding and dehydration in phospholipid and ganglioside micelles

We theorize that intoxicants and modern anesthetics bind at the membrane-water interface and displace (dehydrate) bound water molecules by breaking the hydrogen bonds. We tested this hypothesis by examining the effect of butanol on the binding of water to the polar regions of lipids in reversed micelles. Understanding the mechanisms of intoxication requires studies in physiologically relevant systems such as systems containing sialoglycoconjugates, especially gangliosides, which concentrate in the synapses of neural tissue. Therefore, we compared butanol effects on phospholipid with effects on ganglioside. Hydrogen-bond breaking activity of 1-butanol was studied in reversed micelles made of dipalmitoylphosphotidylcholine (DPPC), ganglioside (GM1 and GT1b) or the lipid mixture in a D2O-CCl4 medium. Fourier transform infrared spectroscopy (FTIR) data indicated that 1-butanol binds to DPPC and to gangliosides. Adding GM1 to the DPPC micelles introduces a new binding site for the alcohol. GT1b binds more butanol than GM1, because of more binding sites provided by extra sialic acid moieties. Spectral red shifts indicate that both water and butanol bind to the C = O group of sialic acid. Butanol partially releases the surface-bound water by disrupting hydrogen bonds, as indicated by an appearance of a sharp new free OD stretching band of the released D2O molecules. However, control studies with lipid-free systems in CCl4 revealed that a free OD peak could occur from a deuterium exchange reaction between D2O and 1-butanol(ol-h).(ABSTRACT TRUNCATED AT 250 WORDS)

Iteration of hybridoma growth and productivity in hollow fiber bioreactors using 31P NMR

Applications of nuclear magnetic resonance (NMR) spectroscopy to isolated or cultured mammalian cells have been limited because of technical difficulties in maintaining cultures at the extremely high densities required by NMR. Among the well-engineered systems available for such analyses, hollow fiber bioreactors (HFBRs) can maintain the greatest cell density. This attribute of HFBRs makes them ideal for application to NMR-based studies. These systems are currently being applied in biotechnology, where they are used for the production of mammalian cell-derived products, such as monoclonal antibodies. In this paper, the application of a HFBR system designed especially for NMR-based investigations is described. Performance of this system is monitored by NMR and the resulting stability and density of hybridoma cultures are reported. The resulting signal-to-noise per unit time is the highest seen to date for a mammalian cell system.

Nuclear magnetic resonance spectroscopy of dense cell populations for metabolic studies and bioreactor engineering: a synergistic partnership

Commercial exploitation of the fruits of recombinant DNA and cell fusion technologies is significantly limited by the lack of fundamental metabolic information on the cell lines of interest, whether these are plant, animal, insect, or microbial cells. NMR can help to provide this information and thereby improve bioreactor design and operation. However, in the case of on-line NMR of dense cell culture devices for metabolic studies, these devices are inherently heterogeneous bioreactors. To ensure that the metabolic information generated is reliable, a number of precautions should be taken. These are the same precautions that should be taken to ensure that commercial bioreactors operate in a reaction-controlled regime. Therefore, reactor engineering methodologies, particularly diffusion and reaction analyses and reaction monitoring by whole-cell NMR must go hand in hand, each extending, complementing, and validating the other.

Experimental and theoretical evidence for convective nutrient transport in an immobilized cell support

Even though immobilized-cell reactors possess several engineering advantages over free-cell reactors, their full potential has not been realized because mass transfer often limits the rate of nutrient supply and product removal from immobilized cell supports. We studied the interaction between mass transfer and reaction kinetics in the anaerobic conversion of glucose to CO2 and ethanol by yeast immobilized in a porous rotating disk on the agitator shaft of a conventional CSTR. A Sherwood number correlation was used to show that external mass-transfer resistances were negligible under typical operating conditions. The modulus of Weisz based on observable reaction parameters was used to gauge the importance of pore diffusion limitations. Under conditions for which significant pore diffusion effects and hence low effectiveness factors (eta = ca. 0.1) would be predicted, the observed reaction rates were much higher than expected (eta = ca. 1), suggesting that pore diffusion limitations were at least partially relieved by convective transport of glucose into the support. Two possible mechanisms of convective transport are discussed. We hypothesize that gas evolution was responsible for the convective enhancement of glucose supply.

Degradation of ribonucleic acid by immobilized ribonuclease

An immobilized enzyme (pancreatic ribonuclease bound to porous titania) was investigated for the degradation of purified yeast ribonucleic acid as a substrate. The immobilized enzyme is active and stable in the pH range 4--8. Dependence of enzymatic activity on ionic strength, pH, temperature, fluid flow rate, and substrate concentration were investigated. A cumulative fluid residence time of 6 sec is sufficient for 50% substrate conversion at 25 degrees C and pH 7.0. The critical flow rate (i.e., the fluid flow rate necessary to remove film diffusion resistance) approximately doubles with each 10 degree C rise in reaction temperature. The critical flow rates obtained in this study are about 40 times greater than those obtained for a similar study on immobilized glucose oxidase. Arrhenius plots gave activation energies of -9.6 and -7.1 kcal/g mol at pH 4.6 and 7.0, respectively. The work reported herein is a bench-scale investigation of an immobilized enzyme with primary emphasis on the mass transfer and kinetic characteristics of the system. The rapid reaction rates obtainable at relatively low temperatures offer a potential alternative method of purifying yeast single cell protein (SCP) with miminum loss of desired protein. The key questions are how such a system would react in a yeast homogenate, what conditions in such a system must be controlled, and what type of immobilized reactor should be utilized, if such further work continued to show promise.