Dermal toxicity, dermal irritation, and delayed contact sensitization evaluation of oil body linked oleosin-hEGF microgel emulsion via transdermal drug delivery for wound healing.

Objective: The expression of therapeutic proteins in plant oil body bioreactors has attracted much attention. But its safety is not yet clear. This article determines the risk of safety after using the drug. Methods: The oil body-linked oleosin-hEGF microgel emulsion (OBEME) was prepared by mixing the xanthan gum with suitable concentrations in an appropriate proportion. Skin irritation and sensitization reaction were investigated in rats and guinea pigs using OBEME as test article.Results: The OBEME did not produce dermal erythema/eschar or oedema responses. The dermal subacute and subchronic toxicity of OBEME were evaluated in accordance with OECD guidelines. Compared with the control group, the basic physical signs, such as weight, feed, drinking, excretion, and behaviour of experimental animals, were not abnormal. In addition, no abnormality was found in haematological parameters, biochemical indexes, relative organ weight, and histopathological observation of organs, and there was no significant difference compared with normal saline treatment group. Therefore, we conclude that OBEME has no toxic effects and is safe and reliable to be used for topical application.

Histological Method to Study the Effect of Shear Stress on Cell Proliferation and Tissue Morphology in a Bioreactor.

Background: Tissue engineering represents a promising approach for the production of bone substitutes. The use of perfusion bioreactors for the culture of bone-forming cells on a three-dimensional porous scaffold resolves mass transport limitations and provides mechanical stimuli. Despite the recent and important development of bioreactors for tissue engineering, the underlying mechanisms leading to the production of bone substitutes remain poorly understood. Methods: In order to study cell proliferation in a perfusion bioreactor, we propose a simplified experimental set-up using an impermeable scaffold model made of 2 mm diameter glass beads on which mechanosensitive cells, NIH-3T3 fibroblasts are cultured for up to 3 weeks under 10 mL/min culture medium flow. A methodology combining histological procedure, image analysis and analytical calculations allows the description and quantification of cell proliferation and tissue production in relation to the mean wall shear stress within the bioreactor. Results: Results show a massive expansion of the cell phase after 3 weeks in bioreactor compared to static control. A scenario of cell proliferation within the three-dimensional bioreactor porosity over the 3 weeks of culture is proposed pointing out the essential role of the contact points between adjacent beads. Calculations indicate that the mean wall shear stress experienced by the cells changes with culture time, from about 50 mPa at the beginning of the experiment to about 100 mPa after 3 weeks. Conclusion: We anticipate that our results will help the development and calibration of predictive models, which rely on estimates and morphological description of cell proliferation under shear stress.

Produção de mudas de carobinha (Jacaranda decurrens Cham. ) em sistema de imersão temporária com biorreatores do tipo R.I.T.A. / "Carobinha" seedling production in a temporary immersion system with R.I.T.A. bioreactors

O objetivo deste trabalho foi averiguar a melhor densidade de explantes e o melhor tipo de sistema de cultivo visando desenvolver um protocolo de micropropagação de baixo custo para a Carobinha. Foram realizados experimentos de multiplicação in vitro com quatro tipos de frascos: R.I.T.A. (50 explantes/frasco), erlenmayer, (50 explantes/frasco), potes tipo maionese (6 explantes/frasco) e cubetas (1 explante/frasco). O co-cultivo de explantes, tanto em meio sólido quanto em meio líquido (R.I.T.A.), promoveu maiores taxas de explantes com brotação e de sobrevivência. O sistema de imersão temporária proporcionou melhores índices de desenvolvimento, brotação, sobrevivência e altura dos explantes. Concluímos que biorreatores podem ser utilizados eficientemente para a micropropagação de carobinha.

The aim of this study was to identify the best explant density and the best cultivation system with the goal of developing a micropropagation protocol of low cost for "carobinha" (Jacaranda decurrens CHAM.). Experiments of in vitro multiplication were carried out using four flask types: R.I.T.A. (50 explants/flask), Erlenmeyer (50 explants/flask), mayonnaise pots (6 explants/flask) and cuvettes (1 explant/flask). The co-cultivation of explants, in both solid and liquid medium (R.I.T.A.), led explants to show higher sprouting and survival rates. The temporary immersion system provided better rates of development, sprouting, survival and height of explants. We concluded that bioreactors may be efficiently used for the micropropagation of "carobinha".

Evaluación de la transferencia de oxígeno en cultivos con lactococcus lactis empleando un sistema de fermentación con aireación externa / Evaluating oxygen transfer in a Lactococcus lactis cultures using an external aeration fermentation system (EAFS)

En fermentaciones aerobias el oxígeno, como aceptor terminal de electrones en el proceso de respiración, comúnmente se constituye en limitante debido entre otros factores al diseño del biorreactor (factores geométricos), a las condiciones de operación de los fermentadores (condiciones ambientales requeridas en el cultivo, potencia transferida al cultivo por el sistema de agitación, propiedades del medio líquido), demanda de oxígeno por parte del microorganismo, sistema de aireación (concentración de oxígeno en el gas, solubilidad del oxígeno). La limitación de oxígeno se refleja en la fermentación con Lactococcus lactis cepa IBUN 34.1, en que presenta una baja disponibilidad de oxígeno desde muy temprano en la fase exponencial del cultivo. Para superar estas limitaciones se diseñó y desarrolló un sistema de suministro de oxígeno de alta tasa de transferencia, consistente en un sistema de fermentación con aireación externa (SFAE), el cual es comparado en este trabajo con el sistema tradicional de fermentador agitado dotado con dos turbinas tipo Rushton y aireación por difusor interno. En este trabajo se evalúa la operación del SFAE, se seleccionan y estudian algunas variables operacionales y su efecto sobre la transferencia de oxígeno gas-líquido. Los resultados indican que las variables que tienen efecto significativo sobre el coeficiente volumétrico global de transferencia de masa kLa son la agitación y el flujo de medio de cultivo que circula por el aireador externo denominado flujo de recirculación. Los valores de kLa obtenidos indican que con el fermentador convencional con aireación interna el mayor valor de kLa alcanzado fue de 40,68 (h-1), en tanto que con el SFAE se alcanzaron valores de 63,18 (h-1).

In aerobic fermentations, oxygen as terminal electron acceptor in respiration process, is commonly a limiting due to factors like its low solubility in aqueous solutions, bioreactors’ geometric factors and operating characteristics, liquid media properties, oxygen concentration in gas supply, microorganisms’ characteristics, environmental culture conditions, power supply by agitation system, etc. Oxygen limitation is present in cultures using the IBUN 34.1 Lactococcus lactis strain where oxygen availability is low some minutes after the exponential phase starts. A high transfer rate oxygen supply system was thus designed to overcome such limitations; it consisted of an external aeration fermentation system (EAFS) which was compared in this work with a conventional agitated tank fermenter equipped with two Rushton turbines and internal diffuser aeration flute mechanism.This paper evaluates the EAFS; some operational variables were selected and studied as well as their effect on oxygen transfer. Our results showed that agitation and culture medium flow through the aerator (called external recirculation flow) were the variables having the main effect on overall volumetric mass transfer coefficient (kLa). The highest kLa value in the conventional bioreactor having internal aeration was 40.68 kLa (h-1), while the EAFS reached 90 (h-1).

Modeling shear-induced CHO cell damage in a rotary positive displacement pump.

Rotary lobe pumps are commonly used in the biotechnology industry for a variety of purposes. Shear damage to animal cells within the rotary lobe pump can adversely affect the product yield or purity during, for example, cell concentration via cross-flow filtration. In this research, CHO cells grown in 20-L bioreactors were fed to a rotary lobe pump in both single pass and recycle experiments were conducted at different RPMs and "slip" conditions. The results indicate that the slip flow rate more severely impacts the viability of the CHO cells than the pump RPM. A novel mathematical modeling approach is presented that predicts shear rates in all of the positive displacement pump's slip regions, and then predicts cell death vs. operating conditions. This model accounts for the complex flow situation that results from changes to RPM, backpressure and pump geometry (i.e., clearances).

Mechanical contributions to astrocyte adhesion using a novel in vitro model of catheter obstruction.

Drainage and diversion of cerebrospinal fluid (CSF) through shunt systems is the most common treatment for hydrocephalus, but complications due to tissue obstruction of the catheter occur in up to 61% of patients. Although shunt systems have undergone limited technological advancements to resist mammalian cell adhesion, there is a need to further reduce adhesion that can exacerbate obstruction. The high intrinsic variability in clinical studies and an inability to predict chronic adhesion of host cells in vitro while maintaining the environmental conditions observed in hydrocephalus have impeded progress. We designed the hydrocephalus shunt catheter bioreactor (HSCB) to measure inflammatory cell adhesion under experimentally manipulated conditions of CSF pressure, pulsation rate, and flow rates. For a 20-h period, astrocytes were perfused through the pulsatile flow system, and adhesion on silicone catheters was recorded. These results were compared with those obtained under static cell culture conditions. Astrocyte adhesion was significantly increased under conditions of increased flow rate (0.25 and 0.30 mL/min), and a trend toward increased adhesion was observed under conditions of elevated pressure and pulsation rate. Because the HSCB represents physiologic conditions more accurately than static cell culture, our results suggest that standard static cell culturing techniques are insufficient to model inflammatory cell adhesion on catheters used in the treatment of hydrocephalus and that changes to the ventricular microenvironment can alter the mechanisms of cellular adhesion. The HSCB represents a relevant test system and is an effective model system for the analysis of cellular adhesion and occlusion of shunt catheters.

Post-treatment of a submerged anaerobic membrane bioreactor (SAMBR) saline effluent using powdered activated carbon (PAC).

Powdered activated carbon (PAC) was added to an effluent from a submerged anaerobic membrane bioreactor (SAMBR) treating saline wastewater as a post-treatment method. The adsorption of contaminants was carried out and key Freundlich isotherm parameters were evaluated. The results showed a reduction in dissolved organic carbon (DOC) in the effluent of over 80% after treatment with 1.7gPAC/L. The composition of the effluent was determined by the use of size exclusion chromatography (SEC) and by GC-MS analysis. Most of the components of the effluent had a MW less than 1 kDa, and these were the hardest to eliminate by PAC adsorption. m-Aminophenylacetylene, cyclohexane 1,2,4 trimethyl and cholestan 3-one were found in the effluent, but could be removed by PAC adsorption. Finally, different methods for using PAC, with or without biomass, revealed that aerobic biomass enhanced the adsorption process resulting in higher DOC removals.

Performance of membrane bioreactor (MBR) system with sludge Fenton oxidation process for minimization of excess sludge production.

The study reports the minimization of excess sludge produced in the membrane bioreactor (MBR) coupled with a sludge Fenton oxidation (oxidation using H(2)O(2) with an iron catalyst) process. Total experimental period was divided into two stages. At the first stage, a series of batch studies were carried out to elucidate the parameters governing the activated sludge disintegration. It was found that Fenton oxidation can disrupt the cell walls and cause the release of plasm from the cells, thus increasing the content of soluble organics and soluble nitrogen in the solution. At the following stage, two MBRs with and without the Fenton process were operated to evaluate the influence of sludge Fenton oxidation on the sludge yield and water quality. It was demonstrated that the incorporation of Fenton process can significantly reduce sludge production, as evidenced from the decrease in the value of the average sludge yield from 0.15 to 0.006 g MLSS/g COD. The water quality of effluent in both systems was maintained at a satisfactory level. Furthermore, it was revealed that the MBR system with the sludge Fenton oxidation process showed relatively better performance for TN removal than that without it.

Changes in characteristics of soluble microbial products in membrane bioreactors associated with different solid retention times: Relation to membrane fouling.

A membrane bioreactor (MBR) is a promising wastewater treatment technology, but there is a need for efficient control of membrane fouling, which increases operational and maintenance costs. Soluble microbial products (SMP) have been reported to act as major foulants in the operation of MBRs used for wastewater treatment. In this study, SMP in MBRs operated with different sludge retention times (SRTs) were investigated by means of various analytical techniques and their relations to the evolution of membrane fouling were considered. Bench-scale filtration experiments were carried out in a laboratory with synthetic wastewater to eliminate fluctuations that would occur with the use of real wastewater and that would lead to fluctuations in compositions of SMP. Three identical submerged MBRs were operated for about 50 days under the same conditions except for SRT (17, 51 and 102 days). Accumulation of SMP in the MBRs estimated by conventional analytical methods (i.e., the phenol-sulfuric acid method and the Lowry method) was significant in the cases of short SRTs. However, the degrees of membrane fouling in the MBRs were not directly related to the concentrations of SMP in the reactors estimated by the conventional analytical methods. Non-conventional analytical methods such as excitation-emission matrix (EEM) fluorescence spectroscopy revealed that characteristics of SMP in the three reactors considerably differed depending on SRT. Foulants were extracted from the fouled membranes at the end of the operation and were compared with SMP in each MBR. It was clearly shown that characteristics of the foulants were different depending on SRT, and similarities between SMP and the extracted foulants were recognized in each MBR on the basis of results of EEM measurements. However, such similarities were not found on the basis of results obtained by using the conventional methods for analysis of SMP. The results of this study suggest that the use of conventional methods for analysis of SMP is not appropriate for investigation of membrane fouling in MBRs.

Prevalence of porcine endogenous retrovirus in Chinese pig breeds and in patients treated with a porcine liver cell-based bioreactor.

AIM: To determine the prevalence of porcine endogenous retrovirus (PERV) in various pig breeds raised in China including Chinese experimental mini-pigs by PERV-reverse transcriptase (PERV-RT enzyme). Moreover, the potential for infection of PERV was investigated in patients treated with a bioreactor based on porcine liver cells (n = 3). METHODS: Pig serum, liver and muscle cell-free supernatants were collected from various Chinese pig breeds. Porcine hepatocytes were isolated with a two-step perfusion method. Three patients with acute or chronic liver failure were treated with a bioartificial liver support system (BALSS) for 8-12 h and serum samples were collected from the patients before, immediately after and 30 d after treatment. RESULTS: The activities of PERV-RT enzyme in pig liver and muscle cell-free supernatants were higher than in normal human controls. PERV-TR enzyme activity did not increase in patients before and after 1 mo of treatment. PERV-RT activities were not significantly different when compared with pre-treatment group (1.544+/-0.155576), the post-treatment groups (1.501+/-0.053507, 1.461+/-0.033808 and 1.6006667+/-0.01963 for 0, 14 and 30 d post-treatment, respectively, P>0.05), and normal control group (1.440+/- 1.0641, P>0.05). RT enzyme activity in Chinese experimental mini-pigs was higher than in normal human control group (1.440+/-1.0641 U/mL, P<0.05), and not significantly different (P>0.05) when compared with the pig breeds except in the muscle supernatants. All the samples including muscle and liver cell supernatants from the Chinese mini-experimental pigs and the four domestic Chinese pig breeds contained PERVs. CONCLUSION: These results suggest that the risk of PERV infection through BALSS containing porcine liver cells without immunosuppressants may be quite low. Although there were PERVs in Chinese experimental mini-pigs and porcine liver cell culture suspensions, we did not find any evidence of persistent PERV infection in patients treated with this porcine hepatocyte-based bioartificial liver.

Bioartificial liver assist devices in support of patients with liver failure.

Bioartificial liver assist devices (BALs) offer an opportunity for critical care physicians and transplant surgeons to stabilize patients prior to orthotopic liver transplantation. Such devices may also act as a bridge to transplant, providing liver support to patients awaiting transplant, or as support for patients post living-related donor transplant. Four BAL devices that rely on hepatocytes cultured in hollow fiber membrane cartridges (Circe Biomedical HepatAssist(r), Vitagen ELADTM, Gerlach BELS, and Excorp Medical BLSS) are currently in various stages of clinical evaluation. Comparison of the four devices shows that several unique approaches based upon the same overall system architecture are possible. Preliminary results of the Excorp Medical BLSS Phase I safety evaluation at the University of Pittsburgh, after treating four patients (F, 41, acetominophen-induced, two support periods; M, 50, Wilson's disease, one support period; F, 53, acute alcoholic hepatitis, two support periods; F, 24, chemotherapy-induced, one support period, are presented. All patients presented with hypoglycemia and transient hypotension at the start of extracorporeal perfusion. Hypoglycemia was treated by IV dextrose and the transient hypotension responded positively to IV fluid bolus. Heparin anticoagulation was used only in the second patient. No serious or adverse events were noted in the four patients. Moderate Biochemical response to support was noted in all patients. More complete characterization of the safety of the BLSS requires completion of the Phase I safety evaluation.

Safe biotechnology 9: values in risk assessment for the environmental application of microorganisms. The Safety in Biotechnology Working Party of the European Federation of Biotechnology.

Risk assessment for the deliberate release of microorganisms into the environment is traditionally carried out on a case-by-case basis. In a similar approach to that used when assessing human pathogenicity, we propose an alternative approach by introducing risk classes to facilitate or complement this type of risk assessment. These consider several sets of scenarios that address the different values that need to be protected. Examples of this approach include risk-class definitions for soil fertility and biodiversity.

Developments toward large-scale bacterial bioprocesses in the presence of bulk amounts of organic solvents.

Many pseudomonads and other bacteria can grow on aliphatic and aromatic hydrocarbons that occur in the environment. We are examining the potential of such organisms as biocatalysts for the oxidation of a variety of substituted aliphatic and aromatic compounds. To attain a high production rate of oxidation products via such biotransformations, we have focused on two-liquid phase culture systems. In these systems, cells are grown in liquid media consisting of an aqueous phase containing water-soluble growth substrates and droplets of a water-immicible organic solvent containing bioconversion substrates and products. For industrial applications of such two-liquid phase processes, several questions remain. What are the maximum rates at which apolar compounds can be transferred from the apolar phase to cells growing in the aqueous phase, i.e., what are the maximum space-time yields attainable in two-liquid phase fermentations under practical conditions? What does an efficient downstream processing of two-liquid phase medium involve? What safety regimes should be considered in working with flammable organic solvents? Can elevated pressure be used to increase oxygen transfer? Based on answers to these questions, we have recently developed a high-pressure, explosion-proof bioreactor system with Bioengineering AG (Wald, Switzerland), which will be installed in our pilot plant and used to explore two-liquid phase bioconversions at a pilot scale.