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Electronic Journal of Biotechnology

versión On-line ISSN 0717-3458

Electron. J. Biotechnol. v.11 n.4 Valparaíso oct. 2008

 

 

Microbial Biotechnology

Electronic Journal of Biotechnology ISSN: 0717-3458 Vol. 11 No. 4, Issue of October 15, 2008
© 2008 by Pontificia Universidad Católica de Valparaíso -- Chile Received June 5, 2007 / Accepted September 27, 2007
DOI: 10.2225/vol11-issue4-fulltext-1 How to reference this article
TECHNICAL NOTE

Equipment design for biosorption studies with microorganisms

Thomas E. Jensen
Department of Biological Sciences
Lehman College
City University of New York
250 Bedford Park Boulevard West, Bronx
NY 10468, USA
Tel: 718 960 8235
Fax: 718 960 8236
E-mail: dolores.vitanza@lehman.cuny.edu

Mary C. Crang
Trauma Unit
Loyola University Medical Center
2160 S. First Ave., Maywood
IL 60153, USA
Tel: 708 327 3717
Fax: 708 327 2818
E-mail: mhitt@lumc.edu

Richard F.E. Crang*
Department of Plant Biology
University of Illinois at Urbana-Champaign
505 S. Goodwin Ave., Urbana
IL 61801, USA
Tel: 217 333 0616
Fax: 217 244 7246
E-mail: r-crang@life.uiuc.edu

*Corresponding author

Financial support: This work was funded in part by a grant from the Research Foundation of the City University of New York and NIH SCORE grant #5S06GM008225-22.

Keywords: bead maker, biosorption, flow-cell, sodium alginate.

Abbreviations:

ICP: Inductively Coupled Plasma

Abstract   Reprint (PDF)
Abstract
Article
References

Two laboratory devices have been designed for experimental use in biosorption studies involving the uptake and controlled release of elements from encapsulated living cells of microorganisms. The first device is an alginate bead maker capable of producing uniform (1.5 mm diameter) sodium alginate beads with encapsulated microorganisms. The second device is a flow-cell that can subject the encapsulated microorganisms to changing fluids, streaming gaseous microaerophyllic conditions, and which also allows for samples of fluid and beads to be extracted at any time during changing experimental conditions. Both devices are novel and simple in their design, and enable improved accuracy and precise handling of encapsulated specimens with minimal labour and expenditure.

Article
Article
Materials and Methods

  • Alginate bead-maker
  • Flow-cell
  • System use and construction
    Results and Discussion
    Acknowledgments
    Figure 1
    Figure 2
    Figure 3
    Figure 4
    Figure 5
    References
  • Following the early success of Murashige and Skoog (1962) in obtaining tobacco tissue culture growth, researchers have utilized a variety of technical approaches in the encapsulation of individual or clusters of living cells (Bashan, 1986), and their experimental handling for the uptake and release of varied compounds, as well as heavy metals (Wilde and Benemann, 1993). Many research efforts have aimed at producing biological cells in an “immobile” form through the process of embedding living cells in sodium alginate beads, which are porous enough for the exchange of various fluid substances that are life supporting as well as experimental in nature. The production of uniform size and composition alginate beads has been employed for some time by multiple researchers for a variety of purposes including the encapsulation of: bacteria (Lee and Heo, 2000), pancreatic and other mammalian cells (Heald et al. 1994), hemoglobin (Huguet et al. 1994), a variety of algae and cyanobacteria (Gonzalez and Bashan, 2000) as well as plant microshoots (Previati et al. 2005) and somatic plant embryos.

    Some of these applications require beads of a specific size in order to accommodate larger specimens, but most utilize a standard of approximately 1-1.5 mm diameter beads. In most protocols, exuding droplets of sodium alginate into a calcium chloride (CaCl2) solution solidifies the alginate and produces beads. Many factors determine the size and hardness of the beads including: the size of the pores through which the sodium alginate is exuded, the concentration of the sodium alginate as well as that of the CaCl2, the length of time in which the exuded beads remain within the calcium chloride solution, and physical or electrostatic forces that may be used to drive the extrusion of the beads (Serp et al. 2000; Klokk and Melvik, 2002).

    Herein, we report on the design of two laboratory devices that provide reliable and reproducible results for a variety of experimental purposes involving the production and experimental use of encapsulated organisms as in the biosorption of cations and heavy metals. First, it is important to have a device that will produce uniform size beads of sodium alginate into which cells are encapsulated. As with most methods, we utilize extrusion of the alginate containing living cells into an external gelation fluid. Following this, a reaction vessel, hereafter referred to as a flow-cell, may be utilized with a means of introducing fluids that can bathe a mass of experimental alginate beads, as well as to subject them to different levels of oxygenation. We describe a relatively simple but unique design of these two laboratory devices, their operational features and some potential research applications. Both devices are designed to be autoclaved as needed.

    Materials and Methods

    Alginate bead-maker

    We have designed a bead-maker that is simple and relatively inexpensive in construction, capable of working with small (approx. 30 ml) volumes of liquid alginate containing cellular suspensions, and giving reproducible results. The assembled unit is shown in Figure 1 and stands approx. 40 cm high with a basal circumference of approx. 12.5 cm. It is comprised of three Pyrex® glass components separated by O-rings and a porous aluminium grid, and held together by two horseshoe clamps. Figure 2 shows the individual components in an exploded view that allows for better distinguishing their features. Figure 3 illustrates a pair of aluminium disks showing both surfaces in which A = top and B = bottom surface. The depression wells each have an approx. 1 mm diameter opening with a bevelled edge after that as described by de-Bashan et al. (2003).

    Flow-cell

    The flow-cell is a multi-piece Pyrex® glass compartment in which alginate beads with encapsulated cells are contained in a bath of nutrients or other fluids, and in which the air quality can be modified as desired through the introduction of other gasses as desired for experimental purposes. As shown in Figure 4a, the uppermost piece of the flow-cell has a standard hose connector for the attachment of a feeder line of solutions (gravity fed) that may be used in the experimental processes. It is connected to the main central unit using an O-ring and a standard horseshoe clamp with three tightening screws. This central unit also possesses a sidearm with a Teflon® shutoff valve, and a female fitting for the attachment of a standard Leur-loc® syringe that enables the extraction of samples from the specimen chamber during operations. The central unit, in turn, is connected to a lower assembly by means of another standard horseshoe clamp and with another O-ring. The lower unit possesses a Teflon® shutoff valve and a hose connector for the attachment of another plastic hose line that may be used for releasing solutions, or for the introduction of an upwards flow of dry N2 gas through the experimental chamber. When the lower valve is closed, the volume capacity of the entire flow-cell unit assembly is 300 ml. Figure 4b illustrates an expanded view of selected parts of the flow-cell assembly.

    An optional adaptor has been designed to fit into the central unit prior to its assembly that restricts the total internal volume capacity of the flow-cell to 50 ml (Figure 5). It is comprised of a Pyrex® glass cylinder sealed at both ends, and with a slotted base unit that allows for the non-obstructive flow of fluids and beads. Clearly, insert adaptors of other sizes can be fabricated by glassblowing with minimal cost and effort, making the flow-cell more versatile in working with experimental materials contained in varied volumes.

    System use and construction

    Beads containing varied encapsulated substances or living cells are collected in a bath of calcium chloride solution and, typically within 30 min, are washed free of the CaCl2 solution in distilled water (3x) for 10 min each with gentle stirring. The beads are then transferred to the flow-cell containing an experimental medium that may be stationary, flowing, gas charged or with continuous changeable solutions as dictated by experimental protocol.

    Construction of all glassware components was fabricated at: O’Brien Glassblowing, 750 Railroad, P.O. Box 495, Monticello, IL 61856, USA. The aluminium filter plates for both the alginate bead-maker and the flow-cell were made at: IFab Precision Prototyping, 1821 S. Oak St., Champaign, IL 61820, USA.

    Results and Discussion

    Alginate beads for experimental purposes have commonly been made manually through expulsion from a needle-less syringe, one at a time, using a simple dropper method. While adequate in many circumstances, the technique is very rudimentary, time-consuming and prone to considerable variation in bead size and shape. One of the more effective devices for producing large quantities of beads has been through the use of a gravity-flow system that was designed by de-Bashan et al. (2003); however, the unit they originally conceived required up to 500 ml solution, and the early drops that were intended to form beads often developed in the form of elongated strings, as well as those of the final ones produced when the level of fluid became low. Only those beads formed during the mid-range of alginate flow were found to be uniform in size and shape. Also, it was often difficult to obtain enough microbiological specimen cultures to prepare adequately loaded beads for experimental use when dealing with volumes over 100 ml. The bead maker described herein has been designed with a capacity of 30 ml, which allows for uniform bead formation, and an alginate/specimen slurry can be easily refilled into the unit before the last beads have moved through the filter plate.

    Beads along with their experimental solution (e.g. growth medium) are then quickly loaded into the flow-cell chamber with the top unit removed, and then the devise is assembled with attachment of a hose to the top unit. Regulation of the valve on the lower unit allows for the continuous flow of fluids, or their retention. For continuous recycling purposes, the use of a peristaltic pump on the effluent hose line can reintroduce the solutions to the flow-cell through the upper unit fitting.

    In our experimental procedures, we have introduced different solutions into the flow-cell assembly that (among other protocols) provide exposure of encapsulated cells in beads to phosphorus and, subsequently, to selected heavy metals. Samples of beads can be extracted from the flow-cell at any time during operations using a 10 ml syringe attached to the main body sidearm. Samples that are prepared for microscopy can then be quickly injected under the surface of fixative solutions or into cryogenic media, allowing virtually no exposure of the specimens to air. As a consequence, structural organization and native cellular composition are kept to a minimum of alteration. The biosorption of phosphates (as an example) along with heavy metals, and their release under microaerophyllic conditions (by means of upwards flowing gaseous N2 through the medium for a designated period of time), can be determined through the use of techniques such as ICP, energy-dispersive X-ray microanalysis and spectrophotometric procedures, as well as the examination of specimens through the use of varied types of microscopy.

    We have employed the use of the equipment described in this paper in evaluating the ability of the cyanobacterium, Plectonema boryanum, to sequester lead in inorganic polyphosphate bodies and to release the lead and phosphorus under microaerophyllic conditions. Details of this work are to be separately reported. High titers of P. boryanum were prepared in a phosphorus-rich medium and, after reaching stationary phase, were gently blended with a 5% sodium alginate solution until a uniform mixture was established. Beads, 1.5 mm in diameter were collected and suspended in a CaCl2 solution for 30 min, and then washed 3x in distilled water as described above. Approx. 30 ml of beads were then transferred to a flow-cell within a nutrient medium that lacked phosphorus. The flow-cell was recirculated with the medium for 18 hrs after which the medium with phosphorus was reintroduced along with 0.1 mg/l PbCl2 for a period of 1 hr. Within 5 min, samples of beads with P. boryanum extracted from the flow-cell showed evidence of inorganic polyphosphate body formation. By 1 hr, the polyphosphate bodies containing Pb were numerous and ranged up to 1.0 µm in diameter. The beads were then washed with a phosphorus-rich medium and subjected to microaerophyllic conditions by using an upwards dry nitrogen gas bubbling in the flow-cell for up to 24 hrs. Samples collected during this time were analyzed with ICP for the amount of phosphorus and lead per mg of beads. A 44% reduction in the amount of phosphorus and a 27% reduction in the amount of lead per mg of beads was recorded by the end of 24 hrs. Additional studies are being conducted on the ability of P. boryanum to sequester and release other metals using the devices described in this report.

    In our opinion the two pieces of equipment described in this paper offer a simple, economical and reliable means for conducting a variety of biological, biochemical and pharmaceutical research procedures involving studies on the encapsulation of biochemical, microbiological and/or cultured cellular components and their experimental use in biosorption and other applications.

    In our opinion the two pieces of equipment described in this paper offer a simple, economical and reliable means for conducting a variety of biological, biochemical and pharmaceutical research procedures involving studies on the encapsulation of biochemical, microbiological and/or cultured cellular components and their experimental use in biosorption and other applications.

    Acknowledgments

    We wish to thank the technical assistance of M. Baxter, J. Goldberg and J. Hagan-Brown for testing the utilization of the equipment described in this paper.

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