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S L Ong

Publications and source records attributed to S L Ong.

24 records · Page 2Linked to original sources

Toxicity assays to determine the start-up strategy for an anaerobic sequencing batch reactor (anSBR).

Addition of glucose as the co-substrate and the use of a water-based polymer to enhance granulation were studied with the aim of shortening the start-up period of an anSBR (anerobic sequencing batch reactor) for high-strength industrial wastewater treatment. An initial start-up feed composition consisting of 70% sucrose and 30% industrial wastewater was favorable to reduce the start-up time. Increase in the average particle size and reduction in settled supernatant turbidity was observed with increased water-based polymer addition up to a concentration of 0.1 m/L. Polymer dosages above 0.1 ml/L were undesirable as big and "flaky" flocs were formed which prevented the flocs from settling quickly. Addition of 0.005 ml/L to 0.1 ml/L polymer to the mixed liquor had no observable adverse effects on the anaerobic biomass metabolism. Instead, the addition of the polymer appeared to improve biogas production and had an overall positive effect on anSBR performance treating the industrial wastewater.

Bacteria, Anaerobic↗

Fermentation of starch for enhanced alkaline protease production by constructing an alkalophilic Bacillus pumilus strain.

A new engineering strain, Bacillus pumilus c172-14 (pBX 96), was obtained by introducing the pBX 96 plasmid, which carries the alpha-amylase amy gene, into the host strain of alkalophilic Bacillus pumilus c172 via transformation. The newly constructed strain was found to express the amy gene and could use starch instead of glucose or starch hydrolysate as carbon source for its fermentation of alkaline protease. The pBX 96 plasmid in the new host was found to be segregationally and structurally stable. The expression of amy gene did not affect the host strain's resistance to bacteriophages. Moreover, the level of alkaline protease was improved significantly compared with the parent strain. The constructed strain gave a maximum alkaline protease activity of 14,014 U/ml in shaking flask after 48 h cultivation when growing in a medium containing 6% corn meal, 4% soybean flour, 0.4% Na2HPO4, 0.03% KH2PO4, 0.02% MgCl2, 0.3% CaCl2, 0.25% Na2CO3, 0.1% glucose, and 20 microg/ml kanamycin (pH 7.0). The optimal pH value and temperature of the alkaline protease were 11.0 and 40 degrees C, respectively. This enzyme was stable over a pH range of 8-11. Its residual activity remained at 100% when treated under a temperature of less than 45 degrees C for 30 min. The corresponding residual activity reduced to 65% of its optimal value at 60 degrees C for 30 min. The alkaline protease was a kind of serine protease, which was demonstrated by the complete inactivation by PMSF (1 mM). This newly constructed strain will be useful in the alkaline protease industry.

Bacillus↗

Denitrifying phosphorus removal by anaerobic/anoxic sequencing batch reactor.

Denitrifying phosphorus removal was verified in a laboratory anaerobic/anoxic Sequencing Batch Reactor (A/A SBR) for a period of 18 months. The results obtained demonstrated the ability of the anaerobic/anoxic strategy to enrich the growth of denitrifying phosphorus bacteria (DPB) capable of taking up phosphate under anoxic conditions by using nitrate as the electron acceptor. Phosphorus removal efficiency ranging from 40-100% could be attained in an A/A SBR system. Simultaneous anoxic phosphate uptake and biological denitrification under anaerobic/anoxic condition occurred in this system. Batch tests showed, however, that simultaneous presence of carbon and nitrate would be detrimental to denitrifying phosphorus removal. Results of bacteria studies suggested that three denitrifying isolates had aerobic phosphorus removing ability.

Anaerobiosis↗

The effects of water reclamation technologies on biological stability of industrial water.

A modified Assimilable Organic Carbon (AOC) procedure was adopted in conjunction with Heterotrophic Plate Count (HPC) method to assess the effect of Single Effect Distillation (SED) and Reverse Osmosis (RO) lab-scale systems on the biological stability of industrial water. Industrial water was collected from a local Industrial Water Works, pre-treated with alum coagulation and cartridge filtration, before being subjected to advanced water treatment. The results obtained in this study indicated that AOCs in the SED product water were in the range of 70-80 micrograms acetate-C/L, while those in the RO product water ranged from 30-40 micrograms acetate-C/L in the 15-min permeate to 55-65 micrograms acetate-C/L in the 3-hr permeate. The above findings suggested that product water of both systems were potentially biologically unstable and would likely lead to bacteria regrowth during its distribution and storage. Removal efficiencies of lab-scale RO and SED systems on AOC were as high as 90%, dependent on the concentration of AOC-NOX in the industrial water. The RO system had much higher organic removal efficiencies in terms of AOC and DOC than the SED system. Organics removed from both feed waters were found to be concentrated in the brine water and rejected water in SED and RO systems respectively.

Conservation of Natural Resources↗

Hormonal effects on the immunocytochemical location of 3',5'-cyclic adenosine monophosphate-dependent protein kinase in rat tissues.

Homogeneous preparations of type I and type II regulatory subunits (RI and RII, respectively) of cAMP-dependent protein kinase (cAMP kinase) were utilized as antigens to obtain isozyme specific antisera. Injections of pure catalytic subunit (C) from the type I isozyme resulted in antisera that reacted with C subunit obtained from either isozyme type. Cross-reactivity of the antisera raised against isolated subunits of the kinase was assessed by immunodiffusion analysis and by measuring the cAMP binding and phosphotransferase activities of the subunits after immunoprecipitation. These antisera were used to localize subunits of type I and type II cAMP kinases in rat skeletal muscle, liver, and adrenal by using indirect immunofluorescence and immunoperoxidase techniques. Specificity of the immunofluorescence was shown by absorption of the antisera with pure homologous antigens. In skeletal muscle, both R and C subunits of the type I and type II cAMP kinases were localized in the area of the sarcoplasmic reticulum and in periodic crossbands. Specific fluorescence for these components was observed in both isotropic and anisotropic band regions of the sarcomere. Densitometric determinations of immunoperoxidase staining revealed a larger amount of RI, RII, and C subunits in the isotropic band than in the anisotropic band regions. In liver, C, RI, and RII subunits were distributed both in cytoplasmic and nuclear areas and along plasma membranes of hepatocytes; however, there were qualitative differences observed among these various subcellular sites. With each antiserum, fluorescence was blocked by prior absorption with homologous antigen. After treatment of rats with glucagon, dramatic changes in the relative distribution patterns of C and RII were noted in the nucleus. In the adrenal gland, RI, RII, and C subunits were localized in both cytoplasmic and nuclear areas, and an apparent redistribution of these subunits occurred after treatment of (dexamethasone-suppressed) rats with ACTH. The application of this immunocytochemical approach provides a tool for examining and monitoring the subcellular distribution of these components of cAMP kinase in biological systems.

Adrenal Glands↗

Monitoring of bacterial morphology for controlling filamentous overgrowth in an ultracompact biofilm reactor.

This research was part of a study of filamentous growth and control in an ultracompact biofilm reactor (UCBR). Morphologies of biofilm and filamentous bacteria in the UCBR were investigated. Ethanol was used as a substrate and sodium hypochlorite was applied as a toxicant to control filamentous growth. The results indicated that factors such as chemical oxygen demand, surface loading rate, pH, and dissolved oxygen could initiate filamentous overgrowth in the UCBR. Different biofilm and filamentous morphologies in the UCBR were observed under different operational conditions. Chlorination was an effective approach to control filamentous growth during and after biofilm formation. Proper chlorine dosing had no effect on biofilm, but killed filaments. Overdose of chlorine damaged biofilm and caused adverse effects such as low treatment efficiency, media clogging and washout, and biofilm color change in the reactor. Frequent monitoring of the morphologies of filaments and biofilm was needed during chlorination to prevent chlorine overdose.

Bacteria↗