Search PubMed⌕ Search

SEARCH · Search PubMed

Results for “Bioreactors”

Search indexed PubMed citations on genomics, clinical trials, systematic reviews and public health. Explore titles, authors and supplied subject terms, then open the PubMed record.

Quote a phrase for an exact phrase match. Source license links do not imply unrestricted reuse.

At least 253 records · Page 14Linked to original sources
PubMed1999

Large-scale production of natural cytokines during activation and expansion of human T lymphocytes in hollow fiber bioreactor cultures.

We studied the large-scale production of a variety of natural cytokines during the activation and expansion of human T lymphocytes in a hollow fiber bioreactor culture system. Peripheral blood mononuclear cells (PBMC) were activated using phytohemagglutinin plus recombinant interleukin-2 (IL-2). Phytohemagglutinin was either present in the hollow fiber bioreactor during the entire 15-16-day culture period or only during the 20-h preactivation of the PBMC in culture bags. The expanding T lymphocytes were mainly CD3+,8+ and exerted maximal natural, activated, bispecific monoclonal antibody-redirected and lectin-dependent cytolytic activities between days 9 and 13 of culture. IL-1 and IL-4 were only produced in low amounts. IL-8 and lymphotoxin were primarily produced during the first week of culture. Harvest of the hollow fiber bioreactor culture supernatant at the time of peak cytokine concentration would have yielded per 10(8) PBMC input between 3.7 and 4.9 micrograms of IL-8 (at days 2 or 3), and between 0.02 and 0.5 microgram of lymphotoxin (at days 6 or 7). Tumor necrosis factor-alpha and IL-6 were produced during the entire culture period of 15 or 16 days: per 10(8) PBMC input, between 0.1 and 0.4 microgram of tumor necrosis factor-alpha (at days 2 or 3) and between 0.03 and 0.5 microgram of IL-6 (at days 15 or 16). Production of interferon-gamma and granulocyte-macrophage colony-stimulating factor started from initiation of cultures onwards to reach peak levels at the end of the 15- or 16-day culture period, yielding at that time between 2.1 and 17.7 micrograms/ml of interferon-gamma and between 0.4 and 4.2 micrograms of granulocyte-macrophage colony-stimulating factor per 10(8) PBMC input. The production of tumor necrosis factor-alpha, IL-6, interferon-gamma, and granulocyte-macrophage colony-stimulating factor was proportional to the extent of lymphocyte multiplication. These results demonstrate the usefulness of hollow fiber bioreactor cultures to produce natural cytokines during the activation and expansion of predominantly CD3+,8+ T lymphocytes.

Bioreactors↗
PubMed2006

Identification and quantification of uncultivated Proteobacteria associated with pyrene degradation in a bioreactor treating PAH-contaminated soil.

Uncultivated bacteria associated with the degradation of pyrene in a bioreactor treating soil contaminated with polycyclic aromatic hydrocarbons (PAH) were identified by DNA-based stable-isotope probing (SIP) and quantified by real-time quantitative PCR. Most of the 16S rRNA gene sequences recovered from (13)C-enriched DNA fractions clustered phylogenetically within three separate groups of beta- and gamma-Proteobacteria unassociated with described genera and were designated "Pyrene Groups 1, 2 and 3". One recovered sequence was associated with the Sphingomonas genus. Pyrene Groups 1 and 3 were present in very low numbers in the bioreactor but represented 75% and 7%, respectively, of the sequences recovered from 16S rRNA gene clone libraries constructed from (13)C-enriched DNA. In a parallel time-course incubation with unlabelled pyrene, there was between a 2- and 4-order-of-magnitude increase in the abundance of 16S rRNA genes from Pyrene groups 1 and 3 and from targeted Sphingomonas spp. over a 10 day incubation. Sequences from Pyrene Group 2 were 11% of the SIP clone libraries but accounted for 14% of the total bacterial 16S rRNA genes in the bioreactor community. However, the abundance of this group did not increase significantly in response to pyrene disappearance. These data indicate that the primary pyrene degraders in the bioreactor were uncultivated, low-abundance beta- and gamma-Proteobacteria not previously associated with pyrene degradation.

Base Sequence↗
PubMed2005

Morphology and kinetics studies on cephalosporin C production by Cephalosporium acremonium M25 in a 30-l bioreactor using a mixture of inocula.

AIMS: In this study, the relationship between morphology and cephalosporin C (CPC) production in a 30-l bioreactor culture of Cephalosporium acremonium M25 using a 3:7 seed mixture was investigated. In addition, the kinetic model was established and applied. METHODS AND RESULTS: CPC production was performed in a 30-l bioreactor using a 3:7 seed mixture. It was recognized that a 3:7 seed mixture was able to reduce lag phase and enhance CPC production. The maximum CPC production and cell mass were 1.96 and 81.5 g l-1 respectively. Through a morphology study by observation using image analysis, it was concluded that changes of morphological features predicted the progressive production of CPC and that a morphology study could be useful in monitoring the CPC fermentation by C. acremonium M25. In the kinetics study, a kinetic model of CPC fermentation was developed and applied. The proposed model could adequately describe the fermentation of C. acremonium M25 in a 30-l bioreactor. CONCLUSIONS: CPC productivity was improved by using a 3:7 seed mixture in a 30-1 bioreactor. The changes in morphological features showed a very similar tendency with CPC production. A kinetic model of CPC fermentation was successfully established. SIGNIFICANCE AND IMPACT OF THE STUDY: The results of the present study suggest that the use of a 3:7 seed mixture inocula has considerable possibilities for improving CPC productivity if applied to industrial scale fermentations. Through morphology and kinetics study, the kinetic model to describe the morphological differentiation and CPC production by C. acremonium M25 was established.

Acremonium↗
PubMed2005

Hepatocyte function in a radial-flow bioreactor using a perfluorocarbon oxygen carrier.

UNLABELLED: The aims of this study were, first, to indicate the metabolic activity of hepatocytes in a radial-flow polyurethane foam matrix bioreactor relative to monocultures, and second, to evaluate the effect on the hepatocytes of including a synthetic perfluorocarbon (PFC) oxygen carrier to the recirculating medium. The efficient O2-carrying ability of PFCs may be beneficial to bioreactors employed in stressed cellular environments. Thus, they may also be useful in the treatment of an acute liver failure patient with a bioartificial liver support system (BALSS). Data on the function of three-dimensional (3-D) hepatocyte cultures exposed to emulsified PFCs are lacking. RESULTS: the metabolic functions of the 3-D hepatocyte cultures were improved relative to monocultures. Three-dimensional cultures with and without PFC behaved similarly, and no adverse effects could be detected when PFC was included in the recirculating medium. The addition of PFC significantly improved lidocaine clearance possibly due to the presence of higher O2 tension in the medium. Imaging indicated that large aggregates formed and that seeding had followed flow through the matrix. Simulations indicated first, that the cell numbers used in this study had been insufficient to challenge the bioreactor O2 supply explaining the similarity in performance of the 3-D cultures, and second, that the benefit of adding PFC would be more pronounced at the cell densities likely to be used in a BALSS bioreactor.

Animals↗
PubMed2006

Construction of functional soft tissues from premodulated smooth muscle cells using a bioreactor system.

Artificial smooth muscle tissues should be constructed with well-differentiated and aligned smooth muscle cells (SMCs) for proper functioning. In a previous study, we produced cell/scaffold hybrids composed of consistently aligned SMCs in a contractile state using cyclic mechanical strain. In this study, the preconditioned hybrids were organized as functional smooth muscle constructs, which had a high cellular density, using a bioreactor system. We determined that the alignment and contractile phenotype of the initially generated SMCs would be retained after a 7-day culture period in a bioreactor. Mechanical properties of the smooth muscle constructs were measured and compared with those of native smooth muscle tissues and acellular scaffolds. The constructs had a denser cell concentration than the preconditioned hybrids, although they were not fully filled with cells. The premodulated cell alignment and contractile phenotype were retained after culture in a bioreactor. The 7-day-cultured constructs had similar allowed stress levels to native tissues while their stiffness was much lower, suggesting that they had malleable and durable characteristics. These results suggest that functional smooth muscle tissues with mechanical stability can be produced using premodulated SMCs and a bioreactor system.

Actins↗
PubMed2002

Bioreactors and bioprocessing for tissue engineering.

Bioreactor design in tissue engineering is complex, and at the early stages of its development. Design of biologically effective, yet scalable, devices requires intimate collaboration between engineers and biologists to ensure that all aspects are considered fully. Growth conditions, harvesting time, scale-up, storage, and sterility issues all need to be considered and incorporated into the design of bioreactors. Each tissue-engineered product will likely require individualized bioreactor design. However, without a comprehensive understanding of each of these components, bioreactor design and tissue growth to manufacture product will remain at a relatively rudimentary and limited level. Increased fundamental understanding of the issues can have a dramatic impact on the ability to generate tissue-engineered product safely, economically, and in the numbers that are required to fully address the patient populations in need.

Animals↗
PubMed2003

Why and how membrane bioreactors with unsteady filtration conditions can improve the efficiency of biological processes.

A membrane bioreactor (MBR), an association of a bioreactor with a crossflow filtration unit, enables continuous processes with total cell retention within the reactor to be realized. Provided that high dilution rates can be applied and that inhibition processes are avoided, very high biomass concentrations can be reached, thereby improving the volumetric productivities. These membrane bioreactors have been successfully applied to various microbial bioconversion, such as alcoholic fermentation, solvents, organic acid production, starters, and wastewater treatment. On the basis of the biological reaction characteristics and bibliographic results, the potentialities and bottlenecks of this methodology are discussed. Depending on the application, it is shown how the performance of the membrane bioreactor can be enhanced by acting either on the biological reaction achievement, by controlling the balance between cell growth and death, or on the dilution rate, by increasing the permeate flux through the filtration unit. This discussion is based on results obtained in specific biological treatments applied to polluted liquid and gas.

Bioreactors↗
PubMed2003

Bioreactors for cardiovascular cell and tissue growth: a review.

Heart disease is a major cause of death in the Western world. In the past three decades there has been a number of improvements in artificial devices and surgical techniques for cardiovascular disease; however, there is still a need for novel devices, especially for those individuals who cannot receive conventional therapy. The major disadvantage of current artificial devices lies in the fact that they cannot grow, remodel, or repair in vivo. Tissue engineering offers the possibility of developing a biological substitute material in vitro with the inherent mechanical, chemical, biological, and morphological properties required in vivo, on an individual patient basis. In order to develop a true biological cardiovascular device a dynamic physiological environment needs to be created. One approach that employs the use of a simulated biological environment is a bioreactor in which the in vivo biomechanical and biochemical conditions are created in vitro for functional tissue development. A review of the current state of the art bioreactors for the generation of tissue engineered cardiovascular devices is presented in this study. The effect of the simulated physiological environment of the bioreactor on tissue development is examined with respect to the materials properties of vascular grafts, heart valves, and cardiac muscles developed in these bioreactors.

Animals↗
PubMed2002

ALEX (artificial liver for extracorporeal xenoassistance): a new bioreactor containing a porcine autologous biomatrix as hepatocyte support. Preliminary results in an ex vivo experimental model.

Long-term maintenance of viability and expression of differentiated hepatocyte function is crucial for bioartificial liver support. We developed a new bioreactor design (ALEX), associated with a new extracellular autologous hepatocyte biomatrix (Porcine Autologous Biomatrix - PBM) support. To test this new bioreactor, we compared it to a standard BAL (BioArtificial Liver) cartridge in a ex vivo model using human plasma added to bilirubin, ammonium and lidocaine. A pathology study was performed on both bioreactors. The results suggest that ALEX allows a maximal contact between the perfusing plasma and the liver cells and a proper hepatocyte support by a cell-to-matrix attachment. ALEX is a suitable cell support bioreactor, guaranteeing long-term maintenance of the metabolic activity of hepatocytes when compared to a standard BAL cartridge.

Ammonia↗
PubMed2004

Three-dimensional bioreactor cultures: a useful dynamic model for the study of cellular interactions.

The ex vivo expansion of hematopoietic cells is a developing area with emphasis on bioreactor systems for amelioration of culture conditions. A rational design of bioreactors, especially those allowing microgravity, could permit the production of stem cells and will offer new approaches for studying the mechanisms of proliferation, differentiation, and signal transduction of cultured cells. The efficacy of two commercially available bioreactors (rotating-vessel miniPERM and static INTEGRA CL 350) to support long-term bone marrow cell cultures (LTBMCC) and three-dimensional growth of Hodgkin's lymphoma HD-MY-Z cells was investigated. In the miniPERM system, the growth of LTBMCC spheroids (containing 30-40 cells) was obtained. An essentially higher content of hematopoietic precursor cells (colony-forming units-granulocyte macrophage) was registered in the rotating-vessel system. In this bioreactor, a growth of large HD-MY-Z spheroids (containing 100-200 cells) was achieved. The composed mathematical models of the physicomechanical behavior of spheroids enabled the evaluation of the revolution frequency increase schedule. The differential equations took into account all inertial effects caused by the production module rotation movement as well as those caused by the relative movement of the spheroid in the fluid. The models aimed at the optimization of the rotation frequency increase schedule for different types of cells to reduce shear stress, augment productivity, and tolerate the growth of large spheroids. The models were numerically tested using MATLAB-SIMULINK software, and the trajectories of prestained HD-MY-Z spheroids were filmed. The coincidence of the theoretical and experimental trajectories was sufficient.

Animals↗
PubMed2002

Cytoskeletal and functional changes in bioreactor assembled thyroid tissue organoids exposed to gamma radiation.

Fischer rat thyroid cells were grown under low-shear stress in a bioreactor to a stage of organization composed of integrated follicles resembling small thyroid glands prior to exposure to 3 Gray-gamma radiation. Bioreactor tissues and controls (both irradiated and non-irradiated) were harvested at 24, 48, 96 and 144 hours post-exposure. Tissue samples were fixed and fluorescently labeled for actin and microtubules. Tissues were assessed for changes in cytoskeletal components induced by radiation and quantified by laser scanning cytometry. ELISA's were used to quantify transforming growth factor-beta and thyroxin released from cells to the culture supernatant. Tissue architecture was disrupted by exposure to radiation with the structural organization of actin and loss of follicular content the most obviously affected. With time post-irradiation the actin appeared disordered and the levels of fluorescence associated with filamentous-actin and microtubules cycled in the tissue analogs, but not in the flask-grown cultures. Active transforming growth factor-beta was higher in supernatants from the irradiated bioreactor tissue. Thyroxin release paralleled cell survival in the bioreactors and control cultures. Thus, the engineered tissue responses to radiation differed from those of conventional tissue culture making it a potentially better mimic of the in vivo situation.

Animals↗
PubMed1999

Closed water recirculating system for fish rearing equipped with bioreactor capable of simultaneous nitrification and denitrification.

Five crucian carp, Carassius auratus langsdorfiicarps had been reared in a closed water recirculating system. The system was equipped with the compact bioreactor using the plate gels capable of both nitrification and denitrification in a single unit. Ammonia and nitrite concentrations in the rearing water had been maintained below 0.05 mg-N/L, and nitrate concentration also controlled between 2 and 8 mg-N/L with the bioreactor. As concerns nitrogen budget in the closed system, 95.0% of nitrogen income from feed was lost as nitrogen gas from the closed system. All fish was alive for 91 days without any unusual behavior. Thus, the bioreactor performed both nitrification and denitrification abilities enough to rear the five fish for 91 days. The bioreactor using the plate gels would be effective to simplify the closed system both physically and operationally, since it can remove the ammonia excreted from fish as nitrogen gas by a single step.

Ammonia↗
PubMed1996

Microencapsulated genetically engineered E. coli DH5 cells for plasma urea and ammonia removal based on: 1. Column bioreactor and 2. Oral administration in uremic rats.

We report a novel approach for plasma urea and ammonia removal using artificial cells microencapsulated genetically engineered bacteria E. coli DH5 cells. This has been evaluated for use in a column bioreactor for removing plasma urea and ammonia. It has also been evaluated in uremic rats for urea removal by oral administration. In 30 minutes, microencapsulated E. coli DH5 in a column bioreactor in-vitro lowered plasma urea to 10.47 +/- 3.45 mg/dl from 45.85 +/- 2.98 mg/dl and lowered plasma ammonia concentration to 46.00 +/- 4.00 microM from 679 +/- 32 microM/1. The efficiency of this bioreactor for plasma urea and ammonia removal is much higher than any other available methods. Initial plasma urea and ammonia concentration does not affect the plasma urea and ammonia removal efficiency of the column bioreactor. In in-vivo studies of oral administration to uremic rats, both free and encapsulated bacteria both lowered systemic urea from the initial 52.08 (S.D.2.37) mg/dl to 10.58 (S.D.0.85) mg/dl. Unlike free bacteria, microencapsulated bacteria was not retained in the intestine.

Administration, Oral↗
PubMedDate not supplied

[In vitro experimentation of a new model of radial flow bioreactor containing isolated hepatocytes].

Hepatocyte based artificial liver support systems are under investigation to support acute liver failure patients. The main purpose of such systems is to serve as a bridge to liver transplantation, or to promote spontaneous liver recovery. Limitation in mass-transfer capacity makes hollow-fiber bioreactors unsuited for long-term functioning of hybrid devices. We developed a novel radial-flow bioreactor in which the fluid perfuses the module from the center to the periphery, after having diffused through a space occupied by a three-dimensional structure filled with the hepatocytes. Five grams of freshly isolated porcine hepatocytes were seeded into uncoated, woven-non woven, hydrophilic polyester fabric, overlaid by two polyethersulfone membranes. Liver cells were perfused with 37 degrees C-warm, oxygenated, serum-free tissue culture medium, in which NH4Cl and Lidocaine were added at the final concentration of 1 mM and 60 micrograms/ml, respectively. Ammonium chloride removal, urea synthesis, monoethylglycinexylide (MEGX), pO2, pCO2, and pH were measured throughout the 14 day duration of the study. In a separate set of experiments, a scaled-up version of the radial flow bioreactor containing 150 grams of cells was perfused for 7 h with recirculating human plasma and MEGX production was monitored. During the 2 weeks of the study, an increasing production of urea was paralleled by constant ammonium removal. MEGX concentration after Lidocaine addition increased throughout the 14 days of perfusion with tissue culture medium, as well as after 7 hour perfusion with human plasma. Under transmission and scanning electron microscopy cells appeared attached to the polyester and one to each other, displaying ultrastructural features typical of functioning hepatocytes. Our study showed that liver cells were metabolically active when perfused into the radial-flow bioreactor. This configuration allowed close contact between media, or plasma, and cells at a physiological flow rate, by equalizing the concentration of the perfusing components, including O2, throughout the module. Our results suggest a potential use of this system for temporary extracorporeal liver support in acute hepatic failure patients.

Animals↗
PubMed2001

[Quinoline removal in fluidized-bed bioreactor using immobilized cells].

Burkholderia pickettii, capable of using quinoline as sole source of carbon, nitrogen and energy, was immobilized by an innovative PVA-H3BO3-gauze method. A fluidized-bed bioreactor, in which immobilized cells were added, was constructed to degrade quinoline in wastewater. When the initial concentrations of quinoline were 100, 350 and 500 mg/L, the bioreactor can remove it completely within 2.5, 6 and 12 hours respectively. A series of zero-order reaction equations were proposed to describe quinoline biodegradation process in this bioreactor kinetically. In continuous flow experiments, the performance of the bioreactor was investigated at different HRT (dilution rate) for different quinoline concentrations in wastewater and the tolerance against shock loading was determined by increasing quinoline concentration from 100 to 300 to 500 mg/L at HRT 4 hours.

Bioreactors↗
PubMed2001

Clinostats and bioreactors.

The environment created on Earth within a clinostat or Rotating Wall Vessel (RWV) bioreactor is often referred to as "simulated microgravity". Both devices utilize constant reorientation to effectively nullify cumulative sedimentation of particles. Neither, however, can fully reproduce the concurrent lack of structural deformation, displacement of intercellular components and/or reduced mass transfer in the extracellular fluid that occur in actual weightlessness. Parameters including density, viscosity, and even container geometry must each be considered to determine the overall gravity-dependent effects produced by either a clinostat or the RWV bioreactor; in addition, the intended application of these two devices differs considerably. A state of particle "motionlessness" relative to the surrounding bulk fluid, which is nearly analogous to the extracellular environment encountered under weightless conditions, can theoretically be achieved through clinorotation. The RWV bioreactor, on the other hand, while similarly maintaining cells in suspension as they continually "fall" through the medium under 1 g conditions, can also purposefully induce a perfusion of nutrients to and waste from the culture. A clinostat, therefore, is typically used in an attempt to reproduce the quiescent, unstirred fluid conditions achievable on orbit; while the RWV bioreactor ideally creates a low shear, but necessarily mixed, fluid environment that is optimized for suspension culture and tissue growth. Other techniques for exploring altered inertial environments, such as freefall, neutral buoyancy and electromagnetic levitation, can also provide unique insight into how gravity affects biological systems. Ultimately, all underlying biophysical principles thought to give rise to gravity-dependent physiological responses must be identified and thoroughly examined in order to accurately interpret data from flight experiments or ground-based microgravity analogs.

Acceleration↗
PubMed2003

Process enhancement in anaerobic bioreactor landfills.

The development of bioreactor landfills originated with the recognition that the sequential acid and methane fermentation phases of anaerobic waste stabilization could be accelerated by leachate recirculation. Original studies suggested the potential for such a change in design and management of landfills receiving both municipal and industrial solid wastes, followed by both pilot- and full-scale bioreactor landfill demonstrations. The enhancement of waste transformation within controlled bioreactor landfills is addressed in terms of the sequential phases of waste stabilization, temporal and spatial distribution of leachate and gas generation patterns, mechanisms of conversion, and proposed process and operational modifications. Selected results from investigations on bioreactor landfills include co-treatment of organic and inorganic constituents and the use of dedicated treatment zones.

Bacteria, Anaerobic↗
PubMed2004

[Bioreactors for animal cell culture and their mechanical environment].

Bioreactor is a key device during in vitro animal cell culture. It provides an appropriate growth environment for the cells, enabling them to proliferate and become the final bio-product. Since animal cells are different from microbial cells in morphology, culture skill needed, and mechanical stimulation needed, the traditional microbial bioreactors are not suitable for the large-scale animal cell culture any more, and many new bioreactors are developed. This paper reviews the bioreactors particularly designed for the animal cell culture, and addresses the mechanical loads on the cultured cells.

Animals↗