Reduction of Cerebral Edema via an Osmotic Transport Device Improves Functional Outcome after Traumatic Brain Injury in Mice.

Traumatic brain injury (TBI), the foremost cause of morbidity and mortality in persons under 45 years of age worldwide, leads to about 200,000 victims requiring hospitalization and approximately 52,000 deaths per year in the United States. TBI is characterized by cerebral edema leading to raised intracranial pressure, brain herniation, and subsequent death. Current therapies for TBI treatment are often ineffective, thus novel therapies are needed. Recent studies have shown that an osmotic transport device (OTD) is capable of reducing brain water content and improving survival in mice with severe cerebral edema. Here we compare the effects of a craniectomy and an OTD plus craniectomy on neurological function in mice after TBI. Animals treated with a craniectomy plus an OTD had significantly better neurological function 2 days after TBI compared with those treated with craniectomy only. This study suggests that an OTD for severe brain swelling may improve patient functional outcome. Future studies include a more comprehensive neurological examination, including long-term memory tests.

Electrostatic properties of confluent Caco-2 cell layer correlates to their microvilli growth and determines underlying transcellular flow.

Recently, Rajapaksa et al. (2010) showed that the rate of uptake of potential vaccine delivery nanoparticles in the mucosal layer is a function of the electrostatic properties of the corresponding solvent. This fundamentally implies that the dominant driving forces that may be capitalized on for mucosal vaccine strategies are electrostatic in nature. We hypothesize that the driving force normal to the cell (in the direction from apical to basolateral across the cell) is of particular importance. In addition, it has been theoretically shown that the electrostatic properties of mucosal cells are directly related to their development of brush border. Here we correlate the development of brush border on a human mucosal epithelial model (Caco-2) cultured in DMEM on 3.0 µm pore sized polycarbonate membranes to their corresponding electrostatic properties characterized by measuring their normal zeta potential. Properties of normal streaming potential, hydraulic permeability, and brush border development (as determined by size and number) were monitored for 2, 6, and 16 days (after cells were confluent). Human endothelial cells (HECs), which lack brush border, were used as the control. Our results demonstrate that normal zeta potential of Caco-2 cells significantly changed from -5.7 ± 0.11 mV to -3.4 ± 0.11 mV for a period between 2 and 16 days, respectively. The zeta potential of the control cell line, HECs, stayed constant (statistically not different, P > 0.05) for the duration of the experiments. Our results show that the calculated increase in surface area of the Caco-2 cells with microvilli from 6 to 16 days was directly proportional to the corresponding measured zeta potential difference. These results imply that microvilli alter the electrostatic local environment around Caco-2 cells and, hence, enhance the normal electrostatic selective transport of solute across the mucosal barrier.

Protein interaction affinity determination by quantitative FRET technology.

The dissociation constant, K(d) , is an important parameter for characterizing protein-protein interaction affinities. SUMOylation is one of the important protein post-translational modifications and it involves a multi-step enzymatic cascade reaction, resulting in peptide activation and substrate conjugation. Multiple covalent and non-covalent protein-protein interactions are involved in this cascade. Techniques involving Förster resonance energy transfer (FRET) have been widely used in biological studies in vitro and in vivo, and they are very powerful tools for elucidating protein interactions in many regulatory cascades. In our previous studies, we reported the attempt to develop a new method for the determination of the K(d) by FRET assay using the interaction of SUMO1 and its E2 ligase, Ubc9 as a test system. However, the generality and specifications of this new method have not been fully determined. Here we report a systematic approach for determining the dissociation constant (K(d) ) in the SUMOylation cascade and for further sensitivity and accuracy testing by the FRET technology. From a FRET donor to acceptor concentration ratio range of 4-40, the K(d) s of SUMO1 and Ubc9 consistently agree well with values from surface plasmon resonance and isothermal titration calorimetry. These results demonstrate the high sensitivity and accuracy of the FRET-based K(d) determination approach. This technology, therefore, can be used in general for protein-protein interaction dissociation constant determination.

Development and applications of a concentrating membrane osmometer for colloid solutions.

The membrane concentration osmometer coupled with multiple sample preparations has been used for over a century to determine a number of colloidal properties. At the dilute region, this method has been used to determine solute molecular mass. When the solution is proteinaceous, in the intermediate region, the osmotic pressure profile provides the second virial coefficient, useful for estimating protein crystallization and salting out. At the most crowded concentrations, it provides insight into protein hydration and protein-ion interaction. One of the most critical factors in generating the osmotic pressure profile is minimizing the quantity of protein used and reducing the error in preparing samples. Here, we introduce a membrane concentrating osmometer that allows one to measure osmotic pressure over a wide concentration range from a single sample. A test study was performed using the osmotic pressure profile of self-crowded bovine serum albumin solutions. The resulting profile was in good agreement with previous data in the literature obtained from multiple sample studies. The osmotic pressure profile was further used with a free solvent-based osmotic pressure model to determine protein hydration and ion binding. These results were in excellent agreement with literature values. This concentrating osmometer has several advantages over a conventional concentration osmometer for obtaining the osmotic pressure profile for proteinaceous solutions: (1) the amount of protein required is significantly decreased, (2) the potential for experimental error in sample preparation diminishes, and (3) the time for generating the osmotic pressure profile is substantially reduced.

Characterizing short-term release and neovascularization potential of multi-protein growth supplement delivered via alginate hollow fiber devices.

Multi-protein (10-250 kDa) endothelial cell growth supplement (ECGS) contains growth factors of varying sizes resulting in advanced release rates from diffusion-based drug delivery devices. As a result, the biochemical stimulus provided by ECGS for neovascularization in the critical initial stages of cell transplantation in artificial organs may differ from that for single growth factor delivery. In this study, both in vitro and in vivo studies were conducted with ECGS to correlate in vitro release of multiple angiogenic growth factors to vascularization potential in vivo. The short-term release of ECGS from calcium alginate gels supported in the lumen of polypropylene (PP) hollow fibers was investigated in vitro for up to 142 h. The overall time constant increased from 2, 2.2 and 6.3 h as the alginate concentration was increased from 1.5%, 2% and 3%, respectively. However, time constants for individual species ranged from 1.5 to 77 h. The in vivo bioactivity of released ECGS was assessed for up to 21 days using a Lewis rat model implanted with 1.5% calcium alginate gels supported in PP and polysulfone hollow fibers. For the ECGS-releasing PP hollow fiber system, a two-fold increase in neovascularization with respect to the control was observed for the period between 7 and 17 days post-implantation at the device-tissue interface (p<0.05).

The rate of cellular hydrogen peroxide removal shows dependency on GSH: mathematical insight into in vivo H2O2 and GPx concentrations.

Although its concentration is generally not known, glutathione peroxidase-1 (GPx-1) is a key enzyme in the removal of hydrogen peroxide (H2O2) in biological systems. Extrapolating from kinetic results obtained in vitro using dilute, homogenous buffered solutions, it is generally accepted that the rate of elimination of H2O2 in vivo by GPx is independent of glutathione concentration (GSH). To examine this doctrine, a mathematical analysis of a kinetic model for the removal of H2O2 by GPx was undertaken to determine how the reaction species (H2O2, GSH, and GPx-1) influence the rate of removal of H2O2. Using both the traditional kinetic rate law approximation (classical model) and the generalized kinetic expression, the results show that the rate of removal of H2O2 increases with initial GPx(r), as expected, but is a function of both GPx(r) and GSH when the initial GPx(r) is less than H2O2. This simulation is supported by the biological observations of Li et al. Using genetically altered human glioma cells in in vitro cell culture and in an in vivo tumour model, they inferred that the rate of removal of H2O2 was a direct function of GPx activity x GSH (effective GPx activity). The predicted cellular average GPx(r) and H2O2 for their study are approximately GPx(r) < or =1 microm and H2O2 approximately 5 microm based on available rate constants and an estimation of GSH. It was also found that results from the accepted kinetic rate law approximation significantly deviated from those obtained from the more generalized model in many cases that may be of physiological importance.

A new paradigm: manganese superoxide dismutase influences the production of H2O2 in cells and thereby their biological state.

The principal source of hydrogen peroxide in mitochondria is thought to be from the dismutation of superoxide via the enzyme manganese superoxide dismutase (MnSOD). However, the nature of the effect of SOD on the cellular production of H(2)O(2) is not widely appreciated. The current paradigm is that the presence of SOD results in a lower level of H(2)O(2) because it would prevent the non-enzymatic reactions of superoxide that form H(2)O(2). The goal of this work was to: a) demonstrate that SOD can increase the flux of H(2)O(2), and b) use kinetic modelling to determine what kinetic and thermodynamic conditions result in SOD increasing the flux of H(2)O(2). We examined two biological sources of superoxide production (xanthine oxidase and coenzyme Q semiquinone, CoQ(*-) that have different thermodynamic and kinetic properties. We found that SOD could change the rate of formation of H(2)O(2) in cases where equilibrium-specific reactions form superoxide with an equilibrium constant (K) less than 1. An example is the formation of superoxide in the electron transport chain (ETC) of the mitochondria by the reaction of ubisemiquinone radical with dioxygen. We measured the rate of release of H(2)O(2) into culture medium from cells with differing levels of MnSOD. We found that the higher the level of SOD, the greater the rate of accumulation of H(2)O(2). Results with kinetic modelling were consistent with this observation; the steady-state level of H(2)O(2) increases if K<1, for example CoQ(*-)+O(2)-->CoQ+O(2)(*-). However, when K>1, e.g. xanthine oxidase forming O(2)(*-), SOD does not affect the steady state-level of H(2)O(2). Thus, the current paradigm that SOD will lower the flux of H(2)O(2) does not hold for the ETC. These observations indicate that MnSOD contributes to the flux of H(2)O(2) in cells and thereby is involved in establishing the cellular redox environment and thus the biological state of the cell.

Using TEM to couple transient protein distribution and release for PLGA microparticles for potential use as vaccine delivery vehicles.

In the development of tunable PLGA microparticles as vaccine delivery vehicles, it is important to understand the drug distribution within the microparticle over time as well as the long-term release of the drug during polymer degradation. This study addresses the transient 3-D drug distribution in PLGA microparticles during in vitro degradation. Specifically, poly (lactide-co-glycolide) (PLGA 75:25) microparticles containing ovalbumin (OVA) as a model protein were fabricated by double-emulsion (w/o/w) method. The microparticles were incubated at 37 degrees C and 250 rpm in PBS buffer (pH 7.4) over a 100-day period. The in vitro polymer erosion, transient protein distribution profiles and protein release behaviors were investigated. Protein release profiles were determined via spectrophotometry using a BCA assay for the solution. Transmission electron microscopy (TEM) images were obtained for the OVA-loaded microparticles before and during degradation (0 day, 30 days and 60 days), and the corresponding 3-D constructions were developed. From the 3-D constructions, the overall protein distribution of the entire microparticle was vividly reflected. Pixel number analysis of the TEM images was used to quantify transient protein distribution. The transient protein release obtained from the TEM analysis was in good agreement with the BCA analysis. This technique provides an additional tool in helping develop polymer matrices for tunable delivery vehicles in vaccination and other drug delivery scenarios.

Mathematical modeling of myoglobin facilitated transport of oxygen in devices containing myoglobin-expressing cells.

Low pO(2) is perhaps the most significant factor in artificial pancreas failure. In these environments, not only is the beta cell production of insulin reduced, but the cell death rate is also significantly higher. Mathematical models are developed to test the feasibility of facilitated oxygen transport in enhancing O(2) flux to genetically engineered cells in a bioartificial device such as a pancreas. For this device, it is proposed that beta cells be genetically engineered to express myoglobin throughout the cell. In addition, the significance of including myoglobin throughout the alginate matrix present to provide immuno-protection for the transplanted cells is considered. The mathematical analysis predicts that myoglobin facilitated oxygen transport has the potential of increasing the oxygen concentration at the centre of a cluster of cells (islet) with an effective radius of 100 microm by 50%. These theoretical models for myoglobin facilitated oxygen transport with homogeneous Michaelis-Menten consumption also indicate that including myoglobin in the alginate gel would beneficially improve the flux of oxygen to the transplanted cells.

A generalized free-solvent model for the osmotic pressure of multi-component solutions containing protein-protein interactions.

The free-solvent model has been shown to have excellent predictability of the osmotic pressure for single and binary non-interactive proteins in aqueous solutions. Here the free-solvent model is extended to be more generalized by including the contributions of intra- and inter-protein interactions to the osmotic pressure of a solution in the form of homo- and hetero-multimers. The solute-solvent interactions are considered to be unique for each homo- and hetero-multimer in solution. The effect of the various generalized free-solvent model parameters on the osmotic pressure are examined for a single protein solution with a homo-dimer, a binary protein solution with no protein-protein interactions, and a binary protein solution with a hetero-dimer. Finally, the limitations associated with the generalized free-solvent model are discussed.

Interpretation of negative second virial coefficients from non-attractive protein solution osmotic pressure data: an alternate perspective.

A negative second virial coefficient has long been a predictor of potential protein crystallization and salting out. However, the assumption that this is due to attractive solute-solute interactions remains a source of debate. Here we reexamine the second virial coefficient from protein osmometry in terms of the free-solvent model. The free-solvent model has been shown to provide excellent predictions of the osmotic pressure of concentrated and crowded environments for aqueous protein solutions in moderate ionic strengths. The free-solvent model relies on two critical parameters, hydration and ion binding, both which can be determined independently of osmotic pressure data. Herein, the free-solvent model is mathematically represented as a virial expansion model and the second virial coefficient is expressed in terms of solute-solvent interactions, namely hydration and ion binding. Hydration and ion binding values are then used to estimate the second virial coefficient at various protein concentrations for three model proteins ovalbumin (OVA), bovine serum albumin (BSA), and hen egg lysozyme (HEL) in various monovalent salt aqueous solutions. The results show that the conditions for obtaining a negative second virial coefficient emerge when the ionic strength of the influenced region of the protein is higher than that of the bulk. This analysis suggests a plausible explanation as to why proteins are more favorable for salting out or crystallization when the solution is represented by a negative second virial coefficient.

Engineering excellence in breakthrough biomedical technologies: bioengineering at the University of California, Riverside.

The Department of Bioengineering at the University of California, Riverside (UCR), was established in 2006 and is the youngest department in the Bourns College of Engineering. It is an interdisciplinary research engine that builds strength from highly recognized experts in biochemistry, biophysics, biology, and engineering, focusing on common critical themes. The range of faculty research interests is notable for its diversity, from the basic cell biology through cell function to the physiology of the whole organism, each directed at breakthroughs in biomedical devices for measurement and therapy. The department forges future leaders in bioengineering, mirroring the field in being energetic, interdisciplinary, and fast moving at the frontiers of biomedical discoveries. Our educational programs combine a solid foundation in bio logical sciences and engineering, diverse communication skills, and training in the most advanced quantitative bioengineering research. Bioengineering at UCR also includes the Bioengineering Interdepartmental Graduate (BIG) program. With its slogan Start-Grow-Be-BIG, it is already recognized for its many accomplishments, including being third in the nation in 2011 for bioengineering students receiving National Science Foundation graduate research fellowships as well as being one of the most ethnically inclusive programs in the nation.

Novel in situ normal streaming potential device for characterizing electrostatic properties of confluent cells.

The characteristics of transport across confluent cell monolayers may often be attributed to its electrostatic properties. While tangential streaming potential is often used to quantify these electrostatic properties, this method is not effective for transport normal to the apical cell surface where the charge properties along the basolateral sides may be important (i.e., confluent cells with leaky tight junctions). In addition, even when cells have a uniform charge distribution, the shear stress generated by the conventional tangential flow device may dislodge cells from their confluent state. Here we introduce a novel streaming potential measurement device to characterize the normal electrostatic properties of confluent cells. The streaming potential device encompasses a 24 mm cell-seeded Transwell(®) with two AgCl electrodes on either side of the cell-seeded Transwell. Phosphate buffered saline is pressurized transversal to the Transwell and the resultant pressure gradient induces a potential difference. Confluent monolayers of HEK and EA926 cells are used as examples. The corresponding zeta potential of the cell-membrane configuration is calculated using the Helmholtz-Smoluchowski equation and the zeta potential of the confluent cell layer is deconvolved from the overall measurements. For these test models, the zeta potential is consistent with that determined using a commercial dispersed-cell device. This novel streaming potential device provides a simple, easy, and cost-effective methodology to determine the normal zeta potential of confluent cells cultured on Transwell systems while keeping the cells intact. Furthermore, its versatility allows periodic measurements of properties of the same cell culture during transient studies.

Theoretical prediction of induction period from transient pore evolvement in polyester-based microparticles.

A model was developed and compared to experimental results for prediction of the induction period during drug delivery from various compositions of biodegradable copolymer PLGA microparticles. The uniqueness of this model is that it considers transient pore evolvement and uses the kinetic parameters of polymer degradation, which are independent of experimental measurements of microparticle erosion, in its analysis. Delivery data from PLGA microparticles (50:50, 75:25, and 85:15) releasing ovalbumin (OVA, 46 kDa) and bovine serum albumin (BSA, 66 kDa) were determined and used as the model systems. Experimental measurements were carried out from 85 to 150 days depending on the PLGA characteristics. The predicted induction periods were approximately 45, 70, and 105 days for the release of both OVA and BSA from 50:50, 75:25, and 85:15 PLGA microparticles, respectively. Overall, these values were in very good agreement with experimentally estimated results.

Determining design and scale-up parameters for degradation of atrazine with suspended Pseudomonas sp. ADP in aqueous bioreactors.

This work investigated the kinetic parameters of atrazine mineralization by suspended cells of Pseudomonas sp. ADP in both shake flasks and spherical stirred tank batch reactors (SSTR). The degradation of atrazine and growth of Pseudomonas sp. ADP were studied. Experiments were performed at different temperatures and stirring speeds in both reactors at varying initial concentrations of atrazine. Cell growth and atrazine concentration were monitored over time, and a Monod model with one limiting substrate was used to characterize the kinetic behavior. Temperature, stirring speed, and reactor type were all found to significantly affect the regressed Monod parameters. At 27 degrees C and 200 rpm, for the shaker flask experiments, mu max and Ks were determined to be 0.14 (+/-0.01) h-1 and 1.88 (+/-1.80) mg/L, respectively. At 37 degrees C, mu max and Ks increased to 0.25 (+/-0.05) h-1 and 9.59 (+/-6.55) mg/L, respectively. As expected, stirrer speed was also found to significantly alter the kinetic parameters. At 27 degrees C and 125 rpm, mu max and Ks were 0.04 (+/-0.002) h-1 and 3.72 (+/-1.05) mg/L, respectively, whereas at 37 degrees C and 125 rpm, mu max and Ks were 0.07 (+/-0.008) h-1 and 1.65 (+/-2.06) mg/L. In the SSTR the kinetic parameters mu max and Ks at room temperature were determined to be 0.12 (+/-0.009) h-1 and 2.18 (+/-0.47) mg/L, respectively. Although the mu max values for both types of reactors were similar, the shaker flask experiments resulted in considerable error. Error analysis on calculated values of Ks were found to impact estimates in atrazine concentration by as much as two orders of magnitude, depending on the reactor design, illustrating the importance of these factors in reactor scale-up.