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Applied and Environmental Microbiology, December 2004, p. 7404-7412, Vol. 70, No. 12
0099-2240/04/$08.00+0 DOI: 10.1128/AEM.70.12.7404-7412.2004
Copyright © 2004, American Society for Microbiology. All Rights Reserved.
Department of Chemical Engineering,1 Department of Chemistry, University of California at Berkeley,3 The Glenn T. Seaborg Center,2 Synthetic Biology Department, Lawrence Berkeley National Laboratory, Berkeley, California4
Received 26 February 2004/ Accepted 16 August 2004
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With respect to the biological precipitation of metals, both metal sulfides (12, 57, 58, 60) and metal phosphates (4, 33, 45) have been investigated due to their low solubilities. While some work has been done to produce sulfide aerobically (57), its production is generally an anaerobic process, limiting its applicability. The release of phosphate via the hydrolysis of an organic phosphate has been shown to be an effective method for the precipitation of metals on cell membranes. Macaskie and Dean (30) isolated a cadmium-resistant strain of Citrobacter that precipitated numerous metals, such as uranyl ion, as metal phosphates through the use of a membrane-bound acid phosphatase (26, 31, 32). Using glycerol-2-phosphate as a phosphate source, the organism cleaved phosphate from the source in the periplasmic space, leaving it to bind with metals that had been complexed in solution. Complexation was required, as the acid phosphatase was sensitive to the presence of free metal in solution (43). The insoluble metal phosphates precipitated on the surface of the cell.
Polyphosphate, a phosphate polymer with chain lengths of two to a few hundred, has been implicated in metal tolerance and removal in many microorganisms (1, 42, 49). Polyphosphate is reversibly and processively synthesized by polyphosphate kinase (PPK) with the addition of a phosphate from a high-energy phosphoryl donor, such as ATP, and irreversibly and processively hydrolyzed by exopolyphosphatase (PPX) (22). While heavy metal resistance has been reported to be correlated with intracellular polyphosphate levels, work with genetically engineered Escherichia coli indicates that the ability to turn over polyphosphate reserves was more important for metal resistance than simply the ability to accumulate polyphosphate: E. coli harboring multiple copies of the genes for PPK (ppk) and PPX (ppx) was able to tolerate increased concentrations of heavy metals, such as cadmium, whereas E. coli engineered with only ppk (so that it accumulated significant amounts of polyphosphate) had little more tolerance to heavy metals than polyphosphate-free strains (20). Furthermore, when ppk and ppx were overexpressed under the control of independently inducible promoters in an E. coli ppk-ppx deletion mutant, this organism accumulated large amounts of polyphosphate when ppk only was induced and then degraded polyphosphate and released phosphate into the medium when ppx was induced, simulating the release of phosphate seen in the metal-binding Citrobacter sp. We suspected that the phosphate generated by polyphosphate hydrolysis and secreted from the cell precipitated heavy metals on the outside of the cell, thereby reducing their toxicity, and that this mechanism could be used to remove metal and actinides from aqueous waste streams. Due to E. coli's intolerance of uranyl, this engineered organism could not be used to examine polyphosphate metabolism and biological uranyl removal.
Two examples of the use of polyphosphate cycling organisms, which were isolated from wastewater treatment processes, for heavy metal precipitation have been reported in the literature. The use of Acinetobacter johnsonii, isolated from an enhanced biological phosphorus removal (EBPR) reactor, was effective in removing lanthanum from solution (4, 5). In EBPR, biomass is cycled between an aerobic phase, in which phosphate is accumulated and stored as polyphosphate inside cells, and an anaerobic phase, in which phosphate is released from the microorganisms. While Acinetobacter is not believed to be the major phosphate cycling organism in the EBPR process, it does accumulate and degrade polyphosphate in aerobiosis and anaerobiosis, respectively. Approximately 0.5 g (dry cell weight) of Acinetobacter/liter was able to remove up to 0.3 mM lanthanum from solution through polyphosphate cycling. A full EBPR consortium, isolated from a wastewater treatment plant and subsequently enriched for its ability to cycle phosphate, was able to remove over 98% of a 1.5 mM solution of uranyl nitrate, with reported loading of over 0.5 g of uranium/g of dry-cell weight (45).
In this work, a two-stage system is presented for the removal of heavy metals from aqueous streams. First, large amounts of polyphosphates were accumulated in Pseudomonas aeruginosa, which was chosen for its native metal tolerance and apparent ability to accumulate larger amounts of polyphosphates than many other organisms. The metal-binding effects shown with the Citrobacter sp. and the polyphosphate-accumulating organisms from EBPR were then mimicked via the degradation of large amounts of polyphosphate and the concomitant release of phosphate from the cell. Phosphate was therefore available to bind and precipitate uranyl out of solution in a manner similar to that shown with the Citrobacter sp., while doing so in a manner that requires neither an organic phosphate source nor the presence of a chelation system nor, in fact, the existence of a live cell.
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Molecular biological methods.
The genes encoding PPK and PPX in P. aeruginosa were identified (16, 62); the sequence for the ppk-ppx gene cluster was obtained from GenBank. PCR amplification of ppk from the chromosome was performed with primers PAO1 M.2 (GGAAGCTTTGACCCCCTCGGGAAGATGAATG) and PAO1E.2 (GGAAGCTTGGCTACAGCCTCAACGTGCGGT); homologous regions are underlined. The resulting 2.2-kb PCR product was digested with HindIII and ligated into the HindIII site of the broad-host-range plasmid pMMB206 (37) behind the Ptac-lac promoter to make pNSR20.
Plasmids were transformed into E. coli by using electroporation with a Bio-Rad Gene Pulser electroporator at 1.8 kV. Plasmids were transformed into P. aeruginosa HN854 by triparental mating (46) by using E. coli DH5
as the donor strain, E. coli DH5
pRK2013 (9) as a helper strain, and streptomycin resistance in selection for P. aeruginosa HN854.
The ppk and ppx genes were knocked out of HN854 through a homologous deletion-insertion, thereby creating strain P. aeruginosa NSR1. The region containing both ppk and ppx (3' of ppk, but on the complementary strand) were PCR amplified with primers PAO1 M.2 and PPXUP3.S (GAGAGGTACCGCAGGATGGCGCAGTTTTC; the homologous region is underlined) and cloned into pUC19. The 2.1-kb region bound by PstI sites was excised and replaced with a tetracycline resistance cassette (8). This replacement removed 1.0 kb of the 2.2-kb ppk gene and 1.1 kb of the 1.3-kb ppx gene, both at the 3' ends of the genes. The ppk'-ppx' region was then subcloned into the suicide vector pEX100T (47) and transformed into P. aeruginosa HN854, where it was homologously recombined into the chromosome. The first and second crossover events were selected for with tetracycline resistance and sucrose tolerance, respectively. Presence of the construct in the chromosome was confirmed by PCR.
PCR was performed by using an Extend High Fidelity system (Boehringer Mannheim). Oligonucleotides were purchased from Genemed Synthesis (South San Francisco, Calif.) and QIAGEN Operon (Alameda, Calif.).
Polyphosphate degradation in crude cell lysates.
P. aeruginosa culture samples of 1 ml were taken in stationary phase, harvested by centrifugation at 12,000 x g for 5 min, and resuspended in 50 mM Tris (pH 7.5)-10% sucrose to give a final OD600 of 20. The samples were frozen in liquid nitrogen and stored at 87°C prior to lysis. The samples were thawed on ice, and 50 µl of cells was combined with 50 µl of lysis buffer containing 50 mM Tris (pH 7.5), 10% sucrose, 300 mM NaCl, 90 mM EDTA, and 3 mg of lysozyme/ml. The resulting mixture was incubated on ice for 1 h. Samples were subjected to repeated freeze-thaw cycles, alternating between liquid nitrogen and 37°C, followed by sonication twice at approximately 100 W for 4 s at 4°C with a Branson Sonifier (Branson Ultrasonics Corp., Danbury, Conn.) fitted with a microtip. The samples were then frozen in liquid nitrogen and stored at 87°C prior to the assays.
Radiolabeled polyphosphate was prepared in 50 mM HEPES (pH 7.2), 40 mM (NH4)2SO4, 4 mM MgCl2, 1 mM ATP, 8 mM phosphoenolpyruvate, 2 U of pyruvate kinase/ml, and 15 µCi of
-labeled ATP/ml. Purified PPK was added to the mixture, and the reaction was run at 37°C for 45 min. Radiolabeled polyphosphate was extracted from the reaction mixture by binding and eluting from Glassmilk (silica glass; Bio 101) (2).
Radiolabeled polyphosphate degradation experiments were performed with 50 mM HEPES (pH 7.2)-40 mM (NH4)2SO4-4 mM MgCl2 supplemented with ATP, ADP, AMP, glucose, glucose-1-phosphate, or potassium phosphate (at 20 mM) or with glycogen (at 20 mg/ml), all at pH 7.2. Approximately 200 µmol of radiolabeled polyphosphate (in phosphate equivalents)/liter and 20 µl of crude cell lysate per ml of reaction mixture were added. The reaction was run at 37°C for 1 h. Samples of the reaction mixtures (2 µl) were spotted onto cellulose-polyethyleneimine thin-layer chromatography plates and developed in a solution of 1 M formic acid and 0.4 M LiCl. Plates were imaged with a PhosphorImager (Molecular Dynamics). The intensities of the polyphosphate spots (at the origins) were recorded by using IPLab Gel software, and pseudo-first order polyphosphate decay constants were estimated from these data.
Controlled polyphosphate accumulation and degradation and uranyl-binding experiments.
Cells were grown under phosphate starvation conditions in minimal medium for 24 h. At the end of the 24-h period, excess phosphate and IPTG (isopropyl-ß-D-thiogalactopyranoside; 1 mM) were added, and cells were incubated for an additional 24 h. At the end of the incubation period, cells were centrifuged at 10,000 x g for 10 min, washed with a 0.5 M NaCl solution, and then centrifuged again. In polyphosphate-degradation experiments, cells were suspended in 40 mM MOPS (pH 7.2). In metal-binding experiments, cells were suspended in a 1 mM uranyl nitrate solution at pH 4, below the solubility limit of U(VI) (50, 13).
Assays of uranyl, polyphosphate, and phosphate.
Uranyl concentration was assayed by using the Arsenazo III reagent (11). A sample of 20 µl was added to 50 µl of Arsenazo reagent (60 mg/ml) and 450 µl of 0.5 M HCl. The absorbance at a wavelength of 652 nm was recorded. Concentrations were calculated by comparing to a standard curve.
Polyphosphate was measured using one of two assays. In the absence of heavy metals, polyphosphate was measured by binding polyphosphate to Glassmilk (2). In the presence of uranyl, this assay does not work, due to the interference of uranyl with the binding of polyphosphate to Glassmilk. In this case, polyphosphates were precipitated selectively from cell lysates (48), hydrolyzed with 0.1 M HCl at 95°C for 1 h, and analyzed for phosphate.
Phosphate concentration was measured with a Calcium/Phosphorus Measurement Kit (Sigma). A fixed-volume sample was added to 500 µl of aluminum molybdate reagent. The absorbance at a wavelength of 340 nm was measured and compared to a set of similar-volume standards.
Electron microscopy and energy-dispersive X-ray spectroscopy (EDXS).
One-milliliter samples were fixed in a 2% glutaraldehyde solution at 4°C for 12 h and then with a 1% osmium tetroxide solution for 2 h. Samples were dehydrated with a series of 5-min acetone washes of increasing concentrations. Samples were infiltrated with an epoxy resin and left to harden overnight. Samples were sectioned by using an MT-6000 microtome, placed on 100 mesh carbon-coated copper grids, and analyzed by a JEOL transmission electron microscope.
Energy-dispersive X-ray spectroscopy was performed by using a JEOL 200CX microscope with two Kevex EDX detectors coupled to a computer running Emispec analytical software. Elemental analysis was performed by the comparison of uranium m-peaks at 3.16 keV and phosphorus k-peaks at 2.01 keV. Lack of microscope drift during the EDX scan was confirmed after the scan by reacquiring the image and observing the location of the path of material eliminated by the scan.
Time-resolved laser-induced fluorescence spectroscopy (TRLFS).
To excite U(VI), a pulsed Nd-YAG laser (GCR-3; Spectra Physics) operating at a wavelength of 355 nm was used. The wavelength of 355 nm is achieved by third harmonic generation of the 1,064-nm emission of the Nd-YAG laser with two KD*P crystals. The laser was operated at a pulse energy of about 1 mJ. Laser energy was monitored by a calibrated energy meter (1812C; Newport) placed in the reflex of the laser beam from a quartz plate placed in the beam at a 45° angle to the beam axis. The laser beam then passes through a rectangular quartz cuvette with a 3-ml volume containing the samples. The fluorescence emission, perpendicular to the laser beam axis, is focused by a lens system onto the entrance slit of a spectrograph (Spectra Pro 500i; Acton Research). The spectrograph provides three gratings. For our experiments, a grating with 300 lines per mm and a spectral resolution of 0.2 nm was used. The fluorescence emission was detected by an intensified gated charge-coupled device camera system (PI-Max; Princeton Instruments). A combined camera controller and a pulser and timing generator (ST-133; Princeton Instruments) can set a variable time delay and time gate, respectively, to the laser pulse for the measurements. A delay time of 2 µs after the lamp trigger signal of the laser was found to be optimal to discriminate light scattering. The gate width was set to 1 µs. One hundred spectra were accumulated for every measurement. All functions of the spectrograph, controller, pulser, timing generator, and charge-coupled device camera, as well as the data collection, were controlled with a personal computer by using the program Winspec 2.4 (Princeton Instruments).
Prior to analysis by TRLFS, biomass samples were centrifuged, washed in 50 mM potassium nitrate, centrifuged again, and suspended in 50 mM potassium nitrate to remove any remaining uranyl from solution. The final pH after the wash and suspension is roughly 4.5. Therefore, all comparisons were made to solutions which were also at pH 4.5.
Phosphate release in irradiated cells.
Cells were grown as described above to accumulate polyphosphate. Cells were then washed, suspended in 50 mM MOPS (pH 7.4), and exposed to 35 Gy/h from Co-60 (1.2 and 1.1 MeV gamma rays) source while being shaken. The dose rate was measured by using a Fricke dosimeter at the same distance from the Co source as the samples. Control samples were shaken in the same room behind a lead-shielded 2-ft concrete wall. The samples remained at the same temperature, approximately 25°C. Samples were taken intermittently and soluble phosphate was measured.
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Polyphosphate accumulation in P. aeruginosa HN854 overexpressing ppk was significant, resulting in a 100-fold increase in polyphosphate levels compared to those for wild-type cells (no overexpression of ppk) and a nearly 10,000-fold increase compared to those for the ppk-ppx knockout strain (NSR1) (Fig. 1). Deletion of chromosomal ppk and ppx did not affect the final polyphosphate content of cells overexpressing ppk. P. aeruginosa was able to accumulate approximately three times the polyphosphate compared to a similarly engineered E. coli strain (55). Phosphate starvation of the cells prior to induction resulted in a twofold increase in polyphosphate content over cells that were similarly engineered but not phosphate starved, likely attributed to an increase in active phosphate import into the cell.
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FIG. 1. Polyphosphate accumulation in P. aeruginosa HN854. Cells were grown to an OD of 0.3 and then induced for ppk overexpression. Filled squares: initially phosphate starved, ppk overexpressed. Filled circles: phosphate rich, ppk overexpressed. Empty squares: initially phosphate starved, control (no ppx overexpressed). Empty circles: phosphate rich, control. Cells overexpressing ppk accumulated 100-fold more polyphosphate (PolyP) than control cells. Phosphate starvation conditions prior to induction resulted in a faster accumulation of polyphosphate and a higher end content of polyphosphate. l, liter.
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A P. aeruginosa ppk-ppx deletion mutant (NSR1) showed that polyphosphate degradation was independent of exopolyphosphatase (encoded by ppx) and was induced via carbon starvation (Fig. 2). In the mutant, the addition of any carbon source to the medium halted all polyphosphate degradation, while the parent strain (HN854) maintained a slow release in the presence of a carbon source, attributed to the native activity of PPX.
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FIG. 2. Effect of carbon on phosphate release from (a) P. aeruginosa HN854 and (b) the P. aeruginosa ppk-ppx deletion mutant (NSR1). Cells were filled with polyphosphate and resuspended in 40 mM MOPS (pH 7.2) with and without a carbon source (glycerol). Filled squares: glycerol fed. Open circles: no carbon addition. Phosphate release from cells was significantly faster for cells that were carbon starved.
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FIG. 3. Polyphosphate degradation in crude cell lysates of HN854. Radiolabeled polyphosphate was added to crude cell lysate, and polyphosphate degradation was monitored after the addition of various supplements. All supplements were added to a final concentration of 20 mM, except for glycogen, which was added to a final concentration of 20 mg/ml. Water was added to the control sample to mimic the dilution effect of the addition of a supplement.
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Additionally, polyphosphate degradation in vitro was not dependent on the conditions from which the cell lysate was prepared. That is, lysates taken from cells prior to resuspension in carbon-free medium degraded polyphosphate at the same rate as those taken postresuspension, indicating that the production of enzymes required to degrade polyphosphate are not induced by carbon starvation, but rather that they may be allosterically regulated by energy-related molecules in the cell, as is the regulation of E. coli glycogen phosphorylase by AMP (7).
Uranyl precipitation by P. aeruginosa releasing phosphate from polyphosphate.
Noting that efficient phosphate release had been achieved simply by suspending the cells into carbon-free medium, uranyl removal from solution via precipitation was attempted. Cells that had been induced for polyphosphate accumulation as before were suspended to an OD600 of 1.5 and challenged with a 1 mM uranyl nitrate solution (Fig. 4). A significant amount of the removed uranyl (20%) was apparently sorbed to the cell. An additional 60% was removed from solution upon the degradation of polyphosphate and subsequent release of phosphate from the polyphosphate-filled cells. The resulting cells accumulated over 40% of their dry cell weight as uranyl. More densely resuspended cultures were able to completely remove uranyl from solution. In order to confirm the presence of the metal on the cell, samples were passed through a 0.22-µm-pore-size filter. While cells are too large to pass through the pores, uranyl phosphate crystals formed in solution are small enough to pass through and remain in solution. In the presence of cells secreting phosphate due to polyphosphate degradation, nearly all of the uranyl remained with the cells, indicating that the uranyl removed from solution was cell associated. In control experiments under identical conditions with no cells but with inorganic phosphate added to the medium, no uranyl was removed from solution by filtration, indicating the need for cells. In addition, in control experiments under identical conditions but with no cells and in solutions around pH 4.5, no uranyl was removed from solution, indicating that uranyl did not precipitate as a hydroxide complex (13, 50). These filtration experiments also highlight the distinct advantages that precipitation in or on the cell membrane has over purely chemical precipitation, as cell attachment allows faster settling over the fine precipitate formed chemically. Furthermore, the resulting metal-loaded biomass is less bulky than precipitates formed with the addition of chemical flocculants traditionally used to aid precipitation and settling.
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FIG. 4. Polyphosphate degradation (a) and concomitant uranyl removal from solution (b). Polyphosphate (PolyP) and control samples were resuspended in 1 mM uranyl nitrate. As a result of polyphosphate degradation and phosphate release, additional uranyl (550 µM) was removed from solution. L, liter.
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FIG. 5. Transmission electron micrographs of uranyl-challenged HN854 8 h after resuspension. (a) Polyphosphate-packed, uranyl-challenged cells. (b) Control uranyl-challenged cells. (c) Polyphosphate-packed control cells. (d) Polyphosphate-free control cells. Note the dark, electron-dense membranes in panel A, which are not observed in any of the control samples. The electron-dense regions inside cells as well as the completely electron-free regions are polyphosphate granules.
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FIG. 6. EDXS of metal-associated membrane. The results of a line scan through the cell membrane, as highlighted by the arrows on the micrograph. Closed circles, background. Closed squares, phosphorus. Open circles, uranium. The line on the graph corresponds to the small dot on the line in the micrograph. The phosphorus and uranium are colocated in a 1:1 stoichiometric ratio, suggesting the presence of uranyl phosphate (UO2HPO4).
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Changes in the inner sphere complexation of the uranyl cation can be easily monitored by changes in the fluorescence spectrum (Fig. 7). At pH 4.5, various hydrolysis products of uranyl [UO2OH+, (UO2)2(OH)22+, and (UO2)3(OH)5+] are dominant (19, 21, 39), having been formed by complexation with hydroxyl anions. Samples from polyphosphate-packed cells shortly after uranyl challenge and polyphosphate-lacking cells challenged with uranyl showed similar spectra. These spectra closely resemble those of uranyl hydroxide species at the relevant pH. This finding implies that upon resuspension in uranyl, hydroxides on the surface of the cell sorb the metal.
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FIG. 7. Time-resolved laser fluorescence spectra of uranyl bound to P. aeruginosa. Polyphosphate-filled cells were resuspended in 1 mM uranyl nitrate, and samples were subsequently taken for TRLFS analysis. Uranyl appears to sorb to cells as a uranyl hydroxide species and then, as phosphate is secreted from the cell, is precipitated to the surface of the cell as uranyl phosphate. d, days.
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Since the polyphosphate degradation machinery apparently exists constantly within the cell, a live cell may not be necessary for the release of phosphate and the subsequent removal of metals from solution. Thus, it may be possible to remove radionuclide from solution in situations where the resulting radiation would quickly kill cells. To test this hypothesis, engineered P. aeruginosa was subjected to lethal doses of irradiation from a 60Co source in a buffered medium, and phosphate secretion was monitored (Fig. 8). Little difference in phosphate release between irradiated and nonirradiated cells was observed. It should be noted that since polyphosphate is stable under the levels of radiation used, phosphate release was due solely to enzymatic degradation of internal phosphate stores. This finding indicates that live cellsthat is, cells that are actively synthesizing new proteinare not required for the degradation of polyphosphate and subsequent precipitation of metal phosphates, increasing the possible applicability of such a technology.
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FIG. 8. Phosphate secretion in irradiated P. aeruginosa. Cells were filled with polyphosphate and resuspended in MOPS-buffered medium and shaken at 25°C. Closed squares: exposed to 60 Gy/h from a 60Co source. Open circles: nonirradiated samples. Exposure to lethal doses of radiation did not affect phosphate release, implying that the enzymes responsible for the degradation of polyphosphate were present in the cell prior to suspension. L, liter.
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Unlike results with E. coli in previous works on engineering the polyphosphate metabolism (53-55), P. aeruginosa is able to survive and metabolize polyphosphate when exposed to relatively high levels of uranyl. Even in the presence of ionizing radiation, the enzymes present in P. aeruginosa were able to metabolize polyphosphate and remove uranyl from solution. This finding may be particularly important for concentrating uranyl in radioactive waste sites; dilute solutions of radioactive uranyl could be concentrated on the outside of polyphosphate-engineered cells or even natural cells whose polyphosphate metabolism could be controlled by changes in environmental conditions.
This report is not the first documentation of uranyl phosphate immobilization on the outside of the cell. It has been shown that metals and actinides can be precipitated on the Citrobacter cell wall by phosphate starving the cells and adding organophosphates and chelating agents (15, 27-29, 31-33, 36). A membrane-bound acid phosphatase hydrolyzes the organophosphate, releasing orthophosphate, which precipitates metal phosphate complexes. Because organophosphates and chelating agents can be expensive to add to wastewater, and the ability to degrade organophosphates in the presence of metal does not appear to be universal, another biological source for phosphate might be more practical; one such source is polyphosphate. While the addition of chemical inducers to uranyl-contaminated wastewater to induce polyphosphate synthesis and degradation in the engineered strain would also be expensive, promoters that respond to oxygen or carbon deprivation may be realistic and economical alternatives to chemically inducible promoters.
Alternatives to genetically modified organisms are organisms that naturally accumulate polyphosphate, such as those found in wastewater treatment plants designed to biologically remove phosphate (34, 35). These organisms synthesize polyphosphate under aerobic conditions and degrade it under anaerobic conditions. Indeed, we have recently shown that wastewater sludge enriched for organisms that accumulate and degrade polyphosphate can remove uranyl from solution (45). Others have shown the ability for a single isolate from EBPR to accumulate metals through phosphate cycling (4, 5). Unfortunately, the specific organism responsible for polyphosphate metabolism in wastewater has neither been isolated nor characterized. While much work has been done in the analysis of Acinetobacter as the polyphosphate-accumulating organism, recent studies have shown that it represents a small proportion of the EBPR consortium. Here, we have shown that a single organism can be engineered to accumulate and degrade polyphosphate and subsequently immobilize uranyl phosphate on the outside of the cell. The use of a genetically engineered microorganism in conjunction with electron microscopy, EDXS, and TRLFS allowed us to examine the mechanism of uranyl association with the cell and subsequent precipitation on the outside of the cell.
Interestingly, polyphosphate degradation was largely independent of ppx expression and dependent on carbon starvation. In vitro enzyme assays using cell lysates indicated that polyphosphate degradation was tied to degradation of glycogen. Unfortunately, the link between polyphosphate and glycogen metabolism could not be confirmed in vivo because of the inability to delete the glycogen phosphorylase gene, indicating that the gene may be essential for cell viability.
Recently, a second polyphosphate kinase (PPK2) in P. aeruginosa and several other bacteria was discovered (17, 63). PPK2 can synthesize polyphosphate by using both ATP and GTP but prefers to use GDP to degrade polyphosphate, whereas PPK1 prefers to use ATP for synthesis and ADP for degradation. In addition, the reverse PPK2-catalyzed reaction rate is 75-fold higher than the forward reaction rate, whereas the reverse PPK1-catalyzed reaction rate is one-fourth of the forward reaction rate. The combination of the in vitro reaction results presented here and the kinetics of the PPK1- and PPK2-catalyzed reactions implicated PPK2 in the in vivo polyphosphate degradation observed here. A possible link between polyphosphate and glycogen metabolisms is alginate biosynthesis. Alginate synthesis is induced during starvation and requires both mannose-1-phosphate and GTP (6). Polyphosphate may supply the GTP (via PPK2) and glycogen may supply the mannose-1-phosphate (e.g., via glycogen phosphorylase to form glucose-1-phosphate, phosphoglucomutase, and phosphoglucose isomerase to form fructose-6-phosphate and via mannose-6-phosphate isomerase and phosphomannomutase to form mannose-1-phosphate). However, neither the regulation of PPK2 activity nor its connection to glycogen degradation and carbon starvation is known.
Regardless of the mechanism of polyphosphate degradation, we have demonstrated that controlled polyphosphate metabolism can be used to sequester large quantities of phosphate in the form of intracellular polyphosphate, degrade the polyphosphate, secrete the resulting phosphate from the cell, and precipitate uranyl phosphate on the cell wall. Furthermore, we demonstrated that uranyl ion initially sorbs to the cell, most likely to hydroxyls on the outside of the cell, and then forms a uranyl phosphate complex when polyphosphate is degraded and phosphate is secreted from the cell. The initial sorption to the cell may be critical for uranyl removal from solution. If there were no sorption to the cell, phosphate secreted from the cell could form a complex with the uranyl in solution rather than on the cell wall. These fine uranyl phosphate complexes do not settle well and are too small to be filtered, making uranyl removal difficult or impossible. Precipitation of uranyl phosphate on the cell wall is an efficient method for uranyl removal from solution, as uranyl phosphate-plated cells are easily separated from the medium by filtration or settling.
We thank the NABIR program of the Department of Energy for funding.
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