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What Is Biotechnology?Biotechnology is technology based on biology, especially when used in agriculture, food science, and medicine. Of the many different definitions available, the one formulated by the UN Convention on Biological Diversity is one of the broadest: Biotechnology is any technological application that uses biological systems, living organisms, or derivatives thereof, to make or modify products or processes for specific use. One section of biotechnology is the directed use of organisms for the manufacture of organic products (examples include beer, milk-products, and skin). Naturally present bacteria are utilized by the mining industry in bioleaching. Biotechnology is also used to recycle, treat waste, clean up sites contaminated by industrial activities (bioremediation), and produce biological weapons. There are also applications of biotechnology that do not use living organisms. Examples are DNA microarrays used in genetics and radioactive tracers used in medicine. Modern biotechnology is often associated with the use of genetically altered microorganisms such as E. coli or yeast for the production of substances like insulin or antibiotics. It can also refer to transgenic animals or transgenic plants, such as Bt corn. Genetically altered Mammalian cells, such as Chinese Hamster ovarian cells, are also widely used to manufacture pharmaceuticals. Another promising new biotechnology application is the development of plant-made pharmaceuticals. There are number of jargon terms for sub-fields of biotechnology. Red biotechnology is biotechnology applied to medical processes. An example would include an organism designed to produce an antibiotic, or engineering genetic cures to diseases through genomic manipulation. White biotechnology, also known as grey biotechnology, is biotechnology applied to industrial processes. An example would include an organism designed to produce a useful chemical. White biotechnology tends to consume less resources that traditional processes when used to produce industrial goods. Green biotechnology is biotechnology applied to agricultural processes. An example would include an organism designed to grow under specific environmental conditions or in the presence (or absence) of certain agricultural chemicals. Green biotechnology tends to produce more environmentally friendly solutions then traditional industrial agriculture. An example of this would include a plant engineered to express a pesticide, thereby eliminating the need for external application of pesticides. The term blue biotechnology has also been used to describe the marine and aquatic applications of biotechnology, but its use is relatively rare. Biotechnology timeline: 8000BC Collecting of seeds for replanting. Evidence that Babylonians, Egyptians and Romans used selective breeding (artificial selection) practices to improve livestock. 6000BC Brewing beer, fermenting wine, baking bread with help of yeast 4000BC Chinese made yoghurt and cheese with lactic-acid-producing bacteria 1500 Plant collecting around the world 1800 Nikolai I. Vavilov created comprehensive research on breeding animals 1880 Microorganisms discovered 1856 Gregor Mendel started recombinant plant genetics 1919 Karl Ereky, a Hungarian engineer, first used the word biotechnology 1975 Method for producing monoclonal antibody developed by Kohler and Milstein 1980 Modern biotech is characterized by recombinant DNA technology. The prokaryote model, E. coli, is used to produce insulin and other medicine, in human form. (About 5% of diabetics are allergic to animal insulins available before) 1992 FDA approves of the first GM food from Calgene: "flavor saver" tomato 2000 Completion of the Human Genome Project Industrial biotechnology (also known as white biotechnology) is the practice of using cells to generate industrially-useful products. The Economist speculated (as cited in the Economist article listed in the "References" section) industrial biotechnology might significantly impact the chemical industry. The Economist also suggested it might enable economies to become less dependent on fossil fuels. Diversa is an example of a company that specializes in industrial biotechnology. Bioremediation can be defined as any process that uses microorganisms or their enzymes to return the environment altered by contaminants to its original condition. Bioremediation may be employed in order to attack specific contaminants, such as chlorinated pesticides that are degraded by bacteria, or a more general approach may be taken, such as oil spills that are broken down using multiple techniques including the addition of fertilizer to facilitate the decomposition of crude oil by bacteria. Not all contaminants are readily treated through the use of bioremediation; for example, heavy metals such as cadmium and lead are not readily absorbed or captured by organisms. The integration of metals such as mercury into the food chain may make things worse as organisms bioaccumulate these metals. However, there are a number of advantages to bioremediation, which may be employed in areas which cannot be reached easily without excavation. For example, hydrocarbon spills (or more specific: gasoline) may contaminate groundwater well below the surface of the ground; injecting the right organisms, in conjunction with oxygen-forming compounds, may significantly reduce concentrations after a period of time. This is much less expensive than excavation followed by burial elsewhere or incineration, and reduces or eliminates the need for pumping and treatment, which is a common practice at sites where hydrocarbons have contaminated groundwater. Generally, bioremediation technologies can be classified as in situ or ex situ. In situ bioremediation involves treating the contaminated material at the site while ex situ involves the removal of the contaminated material to be treated elsewhere. Some examples of bioremediation technologies are bioventing, land farming, bioreactor, composting, bioaugmentation and biostimulation. A bioreactor is a vessel in which is carried out a chemical process which involves organisms or biochemically active substances derived from such organisms. Bioreactors are commonly cylindrical, ranging in size from some liter to cube meters,and are often made of stainless steel. Bioreactor design Bioreactor design is quite a complex engineering task. Under optimum conditions the microorganisms or cells will reproduce at an astounding rate. The vessel's environmental conditions like gas (i.e., air, oxygen, nitrogen, carbon dioxide) flowrates, temperature, pH and dissolved oxygen levels, and agitation speed need to be closely monitored and controlled. One bioreactor manufacturer, Broadley-James Corporation, uses vessels, sensors, controllers, and a control system, digitally networked together for their bioreactor system. Fouling can harm the overall sterility and efficiency of the bioreactor, especially the heat exchangers. To avoid it the bioreactor must be easily cleanable and must be as smooth as possible (therefore the round shape). Heat exchange is needed to maintain the bioprocess at a constant temperature. Biological fermentation is a major source of heat, therefore in most cases bioreactors need water refrigeration. They can be refrigerated with an external jacket or, for very large vessels, with internal coils. Optimal oxygen transfer is perhaps the most difficult task to accomplish. Oxygen is poorly soluble in water -and even less in fermentation broths- and is relatively scarce in air (20.8%). Oxygen transfer is usually helped by agitation, that is also needed to mix nutrients and to keep the fermentation homogeneous. There are however limits to the speed of agitation, due both to high power consumption (that's proportional to the cube of the speed) and the damage to organisms due to excessive tip speed. Compost is the decomposed remnants of organic materials (those with plant and animal origins). Compost is used in gardening and agriculture, mixed in with the soil. It improves soil structure, increases the amount of organic matter, and provides nutrients. Biochem Biophys Res Commun, 1999 Aug 2, 261(2), 238 - 41Protein expression in liposomes; Oberholzer T et al.; Compartmentalization is one of the key steps in the evolution of cellular structures and, so far, only few attempts have been made to model this kind of "compartmentalized chemistry" using liposomes . The present work shows that even such complex reactions as the ribosomal synthesis of polypeptides can be carried out in liposomes . A method is described for incorporating into 1-palmitoyl-2-oleoyl-sn-3-phosphocholine (POPC) liposomes the ribosomal complex together with the other components necessary for protein expression . Synthesis of poly(Phe) in the liposomes is monitored by trichloroacetic acid of the (14)C-labelled products . Control experiments carried out in the absence of one of the ribosomal subunits show by contrast no significant polypeptide expression . This methodology opens up the possibility of using liposomes as minimal cell bioreactors with growing degree of synthetic complexity, which may be relevant for the field of origin of life as well as for biotechnological applications . Biodegradation, 1999 Feb, 10(1), 63 - 73 Anaerobic biodegradability of phthalic acid isomers and related compounds; Kleerebezem R et al.; All three phthalic acid isomers (ortho, meta and para benzene dicarboxylic acid) are produced in massive amounts, and used in the chemical industry as plasticizers or for the production of polyester . Wastestreams generated during the production of phthalate isomers generally contain high concentrations of aromatic acids . To study the potential biodegradability of these primarily anthropogenic compounds in anaerobic bioreactors, biodegradability studies were performed . Compounds tested were benzoate, ortho-phthalate, isophthalate, terephthalate, dimethyl phthalate, dimethyl terephthalate, para-toluate and para-xylene . Seed materials tested were two types of granular sludge and digested sewage sludge . It was found that all phthalate isomers and their corresponding dimethyl-esters, could be completely mineralized by all seed materials studied . Lag phases required for 50% degradation of these compounds, ranged from 17 to 156 days . The observed degradation curves could be explained by growth of an initially small amount of organisms in the inoculum with the specific ability to degrade one phthalate isomer . The observed order in the length of the lag phases for the phthalate isomers is: phthalate < terephthalate < isophthalate . This order appears to be related to the environmental abundancy of the different phthalate isomers . The initial step in the degradation pathway of both dimethyl phthalate esters was hydrolysis of the ester sidechain, resulting in the formation of the corresponding mono-methyl-phthalate isomer and phthalate isomer . The rate limiting step in mineralization of both dimethyl phthalate and dimethyl terephthalate was found to be fermentation of the phthalate isomer . Para-toluate was degraded only by digested sewage sludge after a lag phase of 425 days . The observed degradation rates of this compound were very low . No mineralization of para-xylene was observed . In general, the differences in the lag phases between different seed materials were relatively small . These results indicate that the time needed for the start-up of anaerobic bioreactors treating wastewaters containing phthalic acid isomers, depends little on the microbial composition of the seed material applied, but may take several months. Mol Reprod Dev, 1999 Sep, 54(1), 17 - 23 Analysis of control elements for position-independent expression of human alpha-lactalbumin YAC; Fujiwara Y et al.; A major problem in the production of transgenic animal bioreactors using microinjections is the low production rate of high-expressing transgenic animals due to the position effect . We previously reported that transgenic rats carrying the 210 kb yeast artificial chromosome (YAC) including the human alpha-lactalbumin gene express the transgene in a position-independent manner . The 210 kb YAC was thought to have all the elements necessary for position-independent expression . In this paper, we constructed fragmented YAC clones and a cosmid clone, and produced transgenic rats to analyze these elements . Transgenic rats with both the 50 kb upstream and downstream regions of the alpha-lactalbumin gene had position-independent expression . Transgenic rats with the 20 kb upstream and downstream regions, however, had position-dependent expression . Therefore, all the elements necessary for position-independent expression are thought to be located in the 50 kb upstream to 50 kb downstream region of the alpha-lactalbumin gene . Furthermore, we replaced the human alpha-lactalbumin promoter with the bovine alphaS1-casein promoter in the 210 kb YAC and produced transgenic rats . Position-dependent expression was observed . The elements required for position-independent expression of the bovine alphaS1-casein gene are different from those required for the human alpha-lactalbumin gene, despite the fact that the two genes have the same tissue and developmental specificity . Appl Microbiol Biotechnol, 1999 Jun, 51(6), 760 - 4 High-density Escherichia coli cultures for continuous L(-)-carnitine production; Obon JM et al.; The use of a biological procedure for L-carnitine production as an alternative to chemical methods must be accompanied by an efficient and highly productive reaction system . Continuous L-carnitine production from crotonobetaine was studied in a cell-recycle reactor with Escherichia coli O44 K74 as biocatalyst . This bioreactor, running under the optimum medium composition (25 mM fumarate, 5 g/l peptone), was able to reach a high cell density (26 g dry weight/l) and therefore to obtain high productivity values (6.2 g L-carnitine l-1 h-1) . This process showed its feasibility for industrial L-carnitine production . In addition, resting cells maintained in continuous operation, with crotonobetaine as the only medium component, kept their biocatalytic capacity for 4 days, but the biotransformation capacity decreased progressively when this particular method of cultivation was used. Ann N Y Acad Sci, 1999 Jun 18, 875, 405 - 11 Bioreactor development for tissue-engineered cartilage; Wu F et al.; The development of tissue engineered cartilage is emerging as a potential treatment for the repair of cartilage defects . By seeding chondrocytes onto poly-glycolic acid (PGA) biodegradable scaffolds within a convective-flow bioreactor, the synthesis of tissue-engineered articular cartilage has been recently demonstrated . The ability to cultivate and manipulate this cell-polymer construct to possess specific dimensions, as well as biochemical and biomechanical properties is critical for potential application as an in vivo therapy of damaged articular surfaces . Bioreactor design requirements for stages from research to development to commercialization are discussed . Advantages and limitations to various bioreactor designs are critiqued . These studies illustrate the ability to synthesize tissue-engineered cartilage under convective-flow conditions for potential human tissue repair. Ann N Y Acad Sci, 1999 Jun 18, 875, 386 - 97 Computer controlled bioreactor for large-scale production of cultured skin grafts; Prenosil JE et al.; KERATOR--an automated membrane bioreactor--was developed to produce Autologous Wound Dressing (AWD) at significantly reduced cost and time of transplantation down to two weeks time . At the same time, the risk of human error is largely eliminated . The computer-controlled reactor is modular, allowing the production of up to 0.5 m2 AWD at one time . A special feature of the reactor is a hydrophilic polymeric support membrane on which the human keratinocytes attach and proliferate . Recently developed serum-free medium is used to culture keratinocytes as a monolayer without a feeder layer of murine fibroblasts . The use of composite skin grafts consisting of a subconfluent keratinocyte layer on a polymeric support film is a very promising method for skin transplantation owing to the high activity of non-differentiated keratinocyte cells and reduction of the time needed to prepare the skin grafts . A microscopic video system with image analysis was developed for on-line monitoring of the cell growth and morphology in the KERATOR . The computer uses the obtained information to control medium change and to predict the end of cultivation. Ann N Y Acad Sci, 1999 Jun 18, 875, 364 - 8 Cultivation and characterization of a new immortalized human hepatocyte cell line, HepZ, for use in an artificial liver support system; Werner A et al.; The new human hepatocyte cell line HepZ was investigated with regard to use it for a mass cell cultivation . The cells were originally derived from a human liver biopsy and immortalized through lipofectamine-mediated transfection of albumin-promotor-regulated antisense constructions against the negative controlling cell cycle proteins Rb and p53 (pAlb asRb, pAIb asp53) . Furthermore, plasmids including genes coding for the cellular transcription factor E2F and D1 cyclin (pCMV E2F, pSV2neo D1) were cotransfected to overcome the G1-restriction point . Cell cultivation was performed in a 2-liter bioreactor with a working volume of 1 liter . With CultiSpher G microcarriers used in a concentration of 3 g/l a maximal density of 7.1 x 10(6) cells/ml was achieved in a cultivation period of 20 days . The cells exhibited a maximal specific growth rate of 1.0 per day in the first 4 days . After 9 days of cultivation the stationary growth phase was reached with an average cell density of 5.5 x 10(6) cells/ml . The viability status of the culture was determined indirectly by measuring of the lactate dehydrogenase activity (LDH) at 37 degrees C . During the growth phase the activity rose slightly up to a value of 200 U/l . The cells were flat after first attachment on the gelatine microcarriers and spherical after growing into the three-dimensional inner matrix--both of which characteristics were verified by scanning electron microscopy (SEM) and transmission electron microscopy (TEM) . The liver-specific cytochrome P450 activity was challenged with a pulse of 7 micrograms/ml lidocaine at a cell density of 4.5 x 10(6) cells/ml . After an induction period of 3 days with 50 micrograms/ml of phenobarbital, 26 ng/ml MEGX were generated within one day compared to 5 ng/ml without induction . The new cell line HepZ has proven to retain liver-specific qualities and to be appropriate for mass cell cultivation for bioartificial devices. Ann N Y Acad Sci, 1999 Jun 18, 875, 326 - 39 Bioreactors for hybrid liver support: historical aspects and novel designs; Busse B et al.; A novel bioreactor construction has been designed for the utilization of hepatocytes and sinusoidal endothelial cells . The reactor is based on capillaries for hepatocyte aggregate immobilization . Three separate capillary membrane systems, each permitting a different function are woven in order to create a three dimensional network . Cells are perfused via independent capillary membrane compartments . Decentralized oxygen supply and carbon dioxide removal with low gradients are possible . The use of identical parallel units to supply hepatocytes facilitates scale up . In vitro studies demonstrate long-term external metabolic function in primary isolated hepatocytes within bioreactors . These systems are capable of supporting essential liver functions . Animal experiments have verified the possibility of scaling-up the bioreactors for clinical treatment . However, since there is no reliable animal model for investigation of the treatment of acute liver failure, the promising results obtained from these studies have limited relevance . The small number of clinical studies performed so far is not sufficient to reach conclusions about improvements in the therapy of acute liver failure . Although important progress has been made in the development of these systems, various hepatocyte culture models and bioreactor constructions are being discussed in the literature, which indicates competition in this field of medical research . An overview, which emphasizes the development of hepatocyte culture models for bioreactors, subsequent in vitro studies, animal studies, and clinical application, is also provided. Ann N Y Acad Sci, 1999 Jun 18, 875, 310 - 25 Overview of extracorporeal liver support systems and clinical results; McLaughlin BE et al.; Patients with acute liver failure (ALF) continue to have an almost 50% mortality rate despite improvements associated with the use of orthotopic liver transplantation (OLT) . Numerous ex vivo methods have been developed in attempts to improve patient survival . These methods can be divided into three groups: detoxification (e.g., dialysis, charcoal adsorption, plasma exchange), which only provides excretory function; ex vivo liver perfusion (e.g., whole organ or tissue perfusion), which provides some metabolic function; and bioartificial or cell-based systems, which combine elements of the first two methods . Clinical trials have shown minimal efficacy of the various detoxification methods in terms of ALF patient survival, while the relative success of OLT has shown the importance of providing metabolic as well as excretory functions . Attempts to provide those additional functions with ex vivo tissue perfusion have been fraught with complications such as clotting and acute tissue rejection, leading to the conceptual development of cell-based bioreactor systems . A number of these bioartificial systems have been clinically evaluated, and the preliminary patient survival rates have encouraged further work in this area. Arch Otolaryngol Head Neck Surg, 2001 May, 127(5), 525 - 8 Bacterial colonization of endotracheal tubes in intubated neonates; Friedland DR et al.; OBJECTIVE: To obtain in vivo bacterial colonization profiles on endotracheal tubes at different sites in the neonatal airway in an attempt to better characterize one potential element of chondritis . DESIGN: A case series in which cultures were obtained from calculated segments of 33 endotracheal tubes immediately following extubation . This allowed for sampling at specific levels of the airway corresponding to the trachea, the subglottis, and the oropharynx . Data collected included gender, race, duration of intubation, use of antibiotic therapy, comorbidities, gestational age at birth and extubation, crown-rump length, weight, radiographic distance from tube tip to carina, and culture results . SETTING: Newborn intensive care unit at a tertiary care medical center . PATIENTS: Twenty-nine neonates intubated for longer than 24 hours (range, 24 hours to 15 days) . MAIN OUTCOME MEASURES: Bacterial and fungal cultures obtained from 3 endotracheal tube segments for each extubation . RESULTS: A statistically significant difference (P < .05) was found in colonization rates between patients intubated for less than 4 days and those intubated for longer periods . No significant difference was noted in bacterial profile between the 3 sites . CONCLUSIONS: Data demonstrate that bacterial colonization of an indwelling object in the neonatal airway increases with the duration of intubation . Furthermore, 4 days seems to represent a critical period in the formation of such colonization (possibly in the form of a biofilm) . These bacteria may contribute to the chondritis known to precede the development of subglottic stenosis . Further studies are indicated to suggest ways to interrupt this process and reduce the incidence of airway injury. Antimicrob Agents Chemother, 2001 Jun, 45(6), 1761 - 70 Multidrug efflux pumps: expression patterns and contribution to antibiotic resistance in Pseudomonas aeruginosa biofilms; De Kievit TR et al.; Pseudomonas aeruginosa biofilms are intrinsically resistant to antimicrobial chemotherapies . At present, very little is known about the physiological changes that occur during the transition from the planktonic to biofilm mode of growth . The resistance of P . aeruginosa biofilms to numerous antimicrobial agents that are substrates subject to active efflux from planktonic cells suggests that efflux pumps may substantially contribute to the innate resistance of biofilms . In this study, we investigated the expression of genes associated with two multidrug resistance (MDR) efflux pumps, MexAB-OprM and MexCD-OprJ, throughout the course of biofilm development . Using fusions to gfp, we were able to analyze spatial and temporal expression of mexA and mexC in the developing biofilm . Remarkably, expression of mexAB-oprM and mexCD-oprJ was not upregulated but rather decreased over time in the developing biofilm . Northern blot analysis confirmed that these pumps were not hyperexpressed in the biofilm . Furthermore, spatial differences in mexAB-oprM and mexCD-oprJ expression were observed, with maximal activity occurring at the biofilm substratum . Using a series of MDR mutants, we assessed the contribution of the MexAB-OprM, MexCD-OprJ, MexEF-OprN, and MexXY efflux pumps to P . aeruginosa biofilm resistance . These analyses led to the surprising discovery that the four characterized efflux pumps do not play a role in the antibiotic-resistant phenotype of P . aeruginosa biofilms. Biomaterials, 2001 May, 22(10), 1035 - 47 Long-term stability of grafted polyethylene glycol surfaces for use with microstamped substrates in neuronal cell culture; Branch DW et al.; Crucial to long-term stability of neuronal micropatterns is functional retention of the underlying substratum while exposed to cell culture conditions . We report on the ability of covalently bound PEG films in long-term cell culture to continually retard protein adhesion and cell growth . PDMS microstamps were used to create poly-d-lysine (PDL) substrates permissive to cell attachment and growth, and polyethylene glycol (PEG) substrates were used to minimize protein and cell adhesion . Film thickness was measured using null ellipsometry and atomic force microscopy (AFM) . Organosilane film structure was examined using Fourier transform infrared (FT-IR) spectroscopy . Long-term film stability in cell culture conditions was tested by immersion in 0.1 M sodium phosphate buffer pH 7.4 for up to one month . Null ellipsometry and water contact measurements indicated that organosilane films were stable up to one month, whereas the PEG film thickness declined rapidly after day 25 . Hippocampal cells plated at 200 cells/mm2 on uniform PEG substrates gave a steady increase in biofilm thickness on PEG films throughout the culture, possibly from proteins of neuronal origin . We found that all the layers in the cross-linking procedure were stable in cell culture conditions, with the exception of PEG, which degraded after day 25. J Clin Periodontol, 2001 Jun, 28(6), 569 - 75 Infection-mediated early-onset periodontal disease in P/E-selectin-deficient mice; Niederman R et al.; BACKGROUND: Retrospective and correlation studies suggest that early-onset periodontal disease may be due to a deficiency in phagocyte function, a pathogenic oral biofilm, and/or dysregulated gingival cytokine expression . Increased susceptibility to periodontal disease is therefore thought to result from multiple risk factors . METHODS: We tested this hypothesis prospectively using P/E-selectin adhesion molecule deficient mice that mimic the human syndrome leukocyte adhesion deficiency II . RESULTS: Our studies demonstrate that, in comparison to wild type animals, P/E-/- mice exhibit: spontaneous, early onset alveolar bone loss which is significant by 6 weeks of age; a 10-fold elevation in bacterial colonization of their oral cavities; and elevated gingival tissue levels of the bone resorptive cytokine IL-1alpha . Alveolar bone loss is completely prevented by prophylactic antibiotic therapy . CONCLUSIONS: These experiments provide the first prospective evidence for the multiple risk factor hypothesis of periodontal disease, and validate the first animal model for early onset periodontitis in which both the microbiota and host response can be systematically manipulated . P/E-/- animals should be useful in testing the virulence of putative periodontal pathogens, in determining the role of host resistance factors in periodontitis, in exploring the proposed relationship(s) between infection mediated alveolar bone loss and systemic health disorders, and exploring their genetic relationships. J Clin Periodontol, 2001 May, 28(5), 411 - 8 The effect of systemic antibiotics in the treatment of patients with recurrent periodontitis; Serino G et al.; BACKGROUND: Subjects with periodontal disease exist who either (i) respond poorly to initial mechanical therapy ("refractory" periodontitis) or (ii) fail to adopt adequate self-performed plaque control techniques and hence develop recurrent disease ("recurrent" periodontitis) at multiple sites during the supportive treatment phase (SPT) . Various systemic antibiotic regimens have been tried as adjuncts to the mechanical (re-) treatment of such "difficult to treat"-patients . While most studies indicated a positive outcome of the adjunctive therapy, some clinical investigators reported that this additional measure provided little or no benefit . AIM: The aim of the present investigation was to study the more long term effect of adjunctive antibiotic therapy in the re-treatment of patients with a well defined history of recurrent periodontitis . MATERIAL AND METHODS: 17 subjects with recurrent advanced periodontal disease were, following a baseline examination, subjected to non-surgical therapy including the use of systemic antibiotics (amoxicillin and metronidazole) . They were placed in a careful SPT program and re-examined after 1, 3 and 5 years . The examinations included both clinical and microbiological assessments . RESULTS: It was demonstrated that in subjects with advanced and recurrent periodontitis, re-treatment including (i) comprehensive scaling and root planing (SRP), (ii) systemic administration of antibiotics and (iii) meticulous supragingival plaque control by both mechanical and chemical means established periodontal conditions that in the short term (3 years) and in the majority of subjects could be properly maintained by traditional SPT measures . Between 3 and 5 years, however, only 5 of the 17 subjects exhibited stable periodontal attachment levels . CONCLUSIONS: Some deep pockets and furcations were most likely inadequately instrumented during the active treatment phase . Microorganisms residing in biofilms left in such locations were probably not sufficiently affected by the 2 weeks of adjunctive antibiotic therapy . It is suggested that removal of certain subgingival deposits, therefore, may require surgical intervention. Infect Immun, 2001 Jun, 69(6), 4079 - 85 Anaerobic conditions induce expression of polysaccharide intercellular adhesin in Staphylococcus aureus and Staphylococcus epidermidis; Cramton SE et al.; Products of the intercellular adhesion (ica) operon in Staphylococcus aureus and Staphylococcus epidermidis synthesize a linear beta-1,6-linked glucosaminylglycan . This extracellular polysaccharide mediates bacterial cell-cell adhesion and is required for biofilm formation, which is thought to increase the virulence of both pathogens in association with prosthetic biomedical implants . The environmental signal(s) that triggers ica gene product and polysaccharide expression is unknown . Here we demonstrate that anaerobic in vitro growth conditions lead to increased polysaccharide expression in both S . aureus and S . epidermidis, although the regulation is less stringent in S . epidermidis . Anaerobiosis also dramatically stimulates ica-specific mRNA expression in ica- and polysaccharide-positive strains of both S . aureus and S . epidermidis . These data suggest a mechanism whereby ica gene expression and polysaccharide production may act as a virulence factor in an anaerobic environment in vivo. J Food Prot, 2001 May, 64(5), 652 - 8 Decontamination of lettuce using acidic electrolyzed water; Koseki S et al.; The disinfectant effect of acidic electrolyzed water (AcEW), ozonated water, and sodium hypochlorite (NaOCl) solution on lettuce was examined . AcEW (pH 2.6; oxidation reduction potential, 1140 mV; 30 ppm of available chlorine) and NaOCl solution (150 ppm of available chlorine) reduced viable aerobes in lettuce by 2 log CFU/g within 10 min . For lettuce washed in alkaline electrolyzed water (AIEW) for 1 min and then disinfected in AcEW for 1 min, viable aerobes were reduced by 2 log CFU/g . On the other hand, ozonated water containing 5 ppm of ozone reduced viable aerobes in lettuce 1.5 log CFU/g within 10 min . It was discovered that AcEW showed a higher disinfectant effect than did ozonated water significantly at P < 0.05 . It was confirmed by swabbing test that AcEW, ozonated water, and NaOCI solution removed aerobic bacteria, coliform bacteria, molds, and yeasts on the surface of lettuce . Therefore, residual microorganisms after the decontamination of lettuce were either in the inside of the cellular tissue, such as the stomata, or making biofilm on the surface of lettuce . Biofilms were observed by a scanning electron microscope on the surface of the lettuce treated with AcEW . Moreover, it was shown that the spores of bacteria on the surface were not removed by any treatment in this study . However, it was also observed that the surface structure of lettuce was not damaged by any treatment in this study . Thus, the use of AcEW for decontamination of fresh lettuce was suggested to be an effective means of controlling microorganisms. Environ Sci Technol, 2001 Mar 15, 35(6), 1118 - 26 Methyl tert-butyl ether biodegradation by indigenous aquifer microorganisms under natural and artificial oxic conditions; Landmeyer JE et al.; Microbial communities indigenous to a shallow groundwater system near Beaufort, SC, degraded milligram per liter concentrations of methyl tert-butyl ether (MTBE) under natural and artificial oxic conditions . Significant MTBE biodegradation was observed where anoxic, MTBE-contaminated groundwater discharged to a concrete-lined ditch . In the anoxic groundwater adjacent to the ditch, concentrations of MTBE were > 1 mg/L . Where groundwater discharge occurs, dissolved oxygen (DO) concentrations beneath the ditch exceeded 1.0 mg/Lto a depth of 1.5 m, and MTBE concentrations decreased to <1 microg/L prior to discharge . MTBE mass flux calculations indicate that 96% of MTBE mass loss occurs in the relatively small oxic zone prior to discharge . Samples of a natural microbial biofilm present in the oxic zone beneath the ditch completely degraded {U-14C}MTBE to {14C}CO2 in laboratory liquid culture studies, with no accumulation of intermediate compounds . Upgradient of the ditch in the anoxic, MTBE- and BTEX-contaminated aquifer, addition of a soluble oxygen release compound resulted in oxic conditions and rapid MTBE biodegradation by indigenous microorganisms . In an observation well located closest to the oxygen addition area, DO concentrations increased from 0.4 to 12 mg/L in <60 days and MTBE concentrations decreased from 20 to 3 mg/L . In the same time period at a downgradient observation well, DO increased from <0.2 to 2 mg/L and MTBE concentrations decreased from 30 to <5 mg/L . These results indicate that microorganisms indigenous to the groundwater system at this site can degrade milligram per liter concentrations of MTBE under natural and artificial oxic conditions. Crit Rev Oral Biol Med, 2001, 12(2), 179 - 85 Immunodominant antigens in periodontal disease: a real or illusive concept? Podmore M, Ebersole JL, Kinane DF. The humoral arm of the immune system provides protection from many medically significant pathogens . The antigenic epitopes of the pathogens which induce these responses, and the subsequent characteristics of the host response, have been extensively documented in the medical literature, and in many cases have resulted in the development and implementation of effective vaccines or diagnostic tests . There is a substantial body of literature on the humoral immune response in periodontal disease, which is targeted at micro-organisms present within periodontal pockets . However, the significance and specificity of the immune response in periodontal disease have proved difficult to elucidate, due to the large number of potential pathogens in the plaque biofilm and the apparent commensal nature of many of these opportunistic pathogens . This review addresses our current knowledge of the approaches and strategies which have been used to elucidate and examine the concept of immunodominant antigens in medical infections and, more recently, periodontal disease . An identification/understanding of the immunodominant antigens would be informative with respect to: (i) the relative importance of the implicated pathogens, (ii) new approaches to immunological diagnosis, (iii) specific bacterial virulence determinants, (iv) natural protective responses, and (v) the selection of potential vaccine candidate antigens . We conclude that immunodominance of antigens in periodontal disease may be relevant to our understanding of periodontal disease pathogenesis, but due to the complexity and diversity of the 'pathogenic microbial ecology', it is currently an enigmatic topic requiring a multidisciplinary approach linking clinical, microbiological, and immunological investigations . We also conclude, after assessing the literature available on the topic of immunodominance, that it is a term that, if used, must be clearly defined and understood, since it is often used loosely, leading to a general misinterpretation by readers of oral and medical literature. Water Res, 2001 Jun, 35(8), 2029 - 37 Clogging of a limestone fracture by stimulating groundwater microbes; Ross N et al.; Biological clogging is promoted in aquifers either to contain or to remediate groundwater . In this study, an apparatus able to detect small changes in hydraulic conductivity (K) was developed to measure the clogging of a single fracture in limestone, following microbial stimulation . The fracture had a 2.5 mm2 section and was 50 cm long . Prior to the inoculation of the limestone, the sequencing of representative clones from 16S rRNA genes isolated from groundwater, showed significant affiliation with Cytophaga spp., Arcobacter spp . and Rhizobium spp . These bacteria are known to secrete extracellular polymeric substances and form biofilms . When nutrients were added to the inoculated limestone, a decrease in K occurred after 8 days, reaching 0.8% of its initial value after 22 days (Kfi = 340 cm min-1) . This study showed that a stimulation of indigenous microbes from groundwater effectively clogged a macrofracture in limestone, suggesting the potential application of biobarriers in fractured rock aquifers. Int J Antimicrob Agents, 2001 May, 17(5), 351 - 6 Airway biofilm disease; Kobayashi H; This paper describes the formation of biofilm, its characteristics, its effect on the host cells and treatment of the condition . The airway biofilm diseases are known to be intractable and persistent; also, auto-immune factors play a role in the development of the symptoms . The characteristic of airway biofilm diseases is of a harmful auto-immune reaction occurring along with the symptoms which are different from the simple acute infection interaction between microorganism and host in an acute airway infection. Trends Microbiol, 2001 May, 9(5), 222 - 7 The biofilm matrix--an immobilized but dynamic microbial environment; Sutherland IW; The biofilm matrix is a dynamic environment in which the component microbial cells appear to reach homeostasis and are optimally organized to make use of all available nutrients . The major matrix components are microbial cells, polysaccharides and water, together with excreted cellular products . The matrix therefore shows great microheterogeneity, within which numerous microenvironments can exist . Although exopolysaccharides provide the matrix framework, a wide range of enzyme activities can be found within the biofilm, some of which will greatly affect structural integrity and stability. J Colloid Interface Sci, 2001 May 1, 237(1), 54 - 61 Atomic Force Microscopy Study of the Adhesion of Saccharomyces cerevisiae; Bowen WR et al.; An atomic force microscope (AFM) has been used to quantify directly the adhesion of metabolically active Saccharomyces cerevisiae cells at a hydrophilic mica surface, a mica surface with a hydrophobic coating, and a protein-coated mica surface in an aqueous environment . The measurements used "cell probes" constructed by immobilizing a single cell at the apex of a tipless AFM cantilever . Adhesion was quantified from force-distance data for the retraction of the cell from the surface . The data indicated stretching and sequential bond-breaking as the cell probe was retracted from all of the surfaces . Detailed studies were made for physiologically active cells, which were shown to have different adhesion properties to glutaraldehyde-treated cells . Greatest cell adhesion was measured at the hydrophobic surface . Prior adsorption of a bovine serum albumin protein layer at the hydrophilic surface did not significantly affect cell adhesion . Changes in yeast surface hydrophobicity and zeta-potential with yeast cell age were correlated with differences in adhesion . Cells from the stationary phase adhered most strongly to a mica surface . Time of surface contact was demonstrated to be important . Both the force needed to detach a cell from a hydrophilic mica surface and the length of the adhesive interaction increased after 5 min contact . The AFM cell probe technique gives unique insights into primary colonization events in biofilm formation . It will continue to aid both fundamental studies and the assessment of new procedures that are designed to lower cell adhesion at surfaces relevant to biotechnology, medicine, and dentistry Cornea, 2001 May, 20(4), 362 - 5 The detection of bacteria and bacterial biofilms in punctal plug holes; Sugita J et al.; PURPOSE: An investigation into bacterial biofilm formation on and in punctal plugs . METHODS: The study involved 21 patients with severe dry eye whose puncta were occluded by the use of punctal plugs . Of these, 15 had Sjogren's syndrome, 3 had non-Sjogren's syndrome, 2 had Stevens-Johnson syndrome, and 1 had graft-versus-host disease . From 17 of the 21 subjects, 18 samples of material were extracted from the holes of the punctal plugs (16 unilateral and 1 bilateral) and were subjected to enrichment culture . Nineteen punctal plugs were removed and processed for electron microscopy: 15 by scanning electron microscopy, and 4 by transmission electron microscopy . RESULTS: Positive cultures were found in 8 of 18 (44%) samples of the material extracted from the holes of punctal plugs . In six of these eight cases (75%) the cultured bacterial species was Staphylococcus epidermidis, whereas in the other two cases (25%) it was S . aureus . In 8 of the 15 punctal plugs examined by scanning electron microscopy and in the material extracted from 1 plug that was examined by transmission electron microscopy, there was clear evidence of bacterial colonization . CONCLUSION: Careful observation of patients with punctal plugs is important . If material accumulates in or on a punctal plug, it may contain bacteria and may form a bacterial biofilm . In these cases, replacement of the plug, clearing of the hole, or an alternative treatment should be considered. Water Res, 2001 May, 35(7), 1730 - 8 The formation of malodorous dimethyl oligosulphides in treated groundwater: the role of biofilms and potential precursors; Franzmann PD et al.; Water distributed from the Wanneroo Groundwater Treatment Plant intermittently contains dimethyl trisulphide (DMTS) . The compound is responsible for a "swampy odour" in the water . DMTS production from potential precursors was insignificant in the absence of biofilms when compared with DMTS production from precursors in the presence of biofilms in a biofilm reactor . Greatest dimethyl disulphide (DMDS) and DMTS production (> 3000 ng L-1 DMTS) occurred in the reactors when supplied with methane thio-containing compounds, such as methionine, S-methyl cysteine and methyl-3-(methylmercapto)-propionate . Abiotic DMTS production from oligosulphides also occurred through the addition of the methylating agents, methyl iodide or methyl-p-toluene sulphonate . Significant DMTS production also occurred with Wanneroo water that contained added omega-thio-containing compounds such as cysteine (1400 ng L-1 DMTS), and 3-mercaptopropionate (210 ng L-1) . Biomethylation, a ubiquitous response by microorganisms for the detoxification of toxic compounds, generated DMDS/TS from biofilm oligosulphides . Biofilms exposed to the toxic compounds selenate or 2,4,6-trichlorophenol methylated oligosulphides in addition to the toxins . Sodium sulphide also stimulated DMTS production . Easily Biodegradable Dissolved Organic Carbon (BDOC) probably contributed indirectly to DMTS production by the biofilms, although whether this was a result of its stimulation of greater microbial activity or consumption of oxygen, or both, remains unresolved . Stagnation of water in the biofilm reactors also increased DMTS production, which was concomitant with depletion of oxygen concentrations in the bulk water . Many processes, such as degradation of methane thio-containing compounds, methylation of sulphides and oligosulphides, and changes in contributions of different metabolic pathways upon depletion of oxygen concentrations upon water stagnation, probably contribute simultaneously to "swampy odour" production in the distribution system. J Periodontol, 2001 Mar, 72(3), 401 - 10 Evaluation of ultrasonic scaling unit waterline contamination after use of chlorine dioxide mouthrinse lavage; Wirthlin MR et al.; BACKGROUND: An infection control problem in dental operatories which is not fully controlled is waterline contamination by heterotrophic mesophilic bacteria . These bacteria are present in water supplies as a planktonic phase and adhere to the lumen of tubings as a biofilm comprised of their external cell surface glycocalyx and by production of extracellular carbohydrate polymers . The adherent film is most difficult to remove . The accumulated planktonic phase can be reduced significantly by flushing water from the lines before use in patient treatment, but will return when the equipment is idle through the accumulation of more planktonic phase and by slough of the biofilm surface-adsorbed phase not yet enmeshed in the carbohydrate matrix . Chlorine dioxide has antimicrobial activity against many bacteria, spores, and viruses . It is used in water supply treatment as a disinfectant and slime preventive and has an advantage over chlorine in that carcinogenic trihalomethanes are not generated . METHODS: This study compared use of phosphate buffer-stabilized chlorine dioxide (0.1%) mouthrinse as a lavage in ultrasonic dental scaler units with the use of tap water as a control . Sterile water flushed through the units onto heterotrophic plate count (HPC) sampler plates was cultured 7 days at room temperature and colonies were counted at 12x . One test and one control unit were used for biopsy of internal tubing and scanning electron microscopy imaging . RESULTS: The HPC counts, in colony forming units (CFU)/ml, were reduced 3- to 5-fold by flushing tap water through the units, but they returned after units were idle overnight . When phosphate-buffered chlorine dioxide mouthrinse was used as a lavage, CFU/ml were reduced 12- to 20-fold . Holding chlorine dioxide in waterlines overnight reduced recurrent buildup compared to water (P <0.05) . Scanning electron microscopy images indicated a significant reduction of biofilm coverage by chlorine dioxide as compared to water (P<0.001) . CONCLUSIONS: Phosphate-buffered chlorine dioxide mouthrinse was effective in these short-term trials for control of waterline contamination in ultrasonic dental scaling units . It should prove as useful in dental professional waterline applications as it has in industrial uses for biofilm control. J Periodontol, 2001 Mar, 72(3), 393 - 400 Dental unit waterline contamination and its possible implications during periodontal surgery; Putnins EE et al.; BACKGROUND: Dental unit waterline contamination has become a concern to clinical dentistry . This concern arises from the fact that bacteria sloughed from established biofilms in dental unit waterlines increase heterotrophic bacteria counts in water exiting these units . METHODS: Scanning microscopy and bacterial viability staining were used to examine the sessile and planktonic biofilm present in dental unit waterlines and water samples, respectively . In addition, the limulus amebocyte assay was used to measure the lipopolysaccharide (LPS) levels in water samples . RESULTS: All dental unit waterlines were coated with a well-established biofilm made up of filamentous and bacillus-like microorganisms . Water samples collected from these dental units contained high numbers of individual bacteria and bacterial aggregates . A viability staining technique identified significantly more bacteria in water than could be cultured, and 64% of the total bacterial population stained as nonvital . Since the bacterial load (viable and nonviable) was high, we examined the LPS in dental unit water samples . The mean LPS levels in water collected from high-speed and air/water lines in use were 480 and 1,008 endotoxin units (EU)/ml . This was significantly higher than the mean level of 66 EU/ml found in water samples collected from adjacent clinic sinks . The LPS level at the start of the day (2,560 EU/ml) was reduced by 70% with 1 minute of flushing (800 EU/ml) . Flushing times of 5 and 10 minutes were not able to reduce LPS levels to zero . CONCLUSION: The presence of high heterotrophic bacterial counts, sloughing biofilm, and high LPS levels are discussed in relation to patient risk and periodontal wound healing biology. J Calif Dent Assoc, 2000 Mar, 28(3), 185 - 93 Responsible use of antimicrobials in periodontics; Jorgensen MG et al.; New products and treatment modalities for the management of periodontal disease continue to offer the clinician a large number of choices, many of which involve antimicrobials . Specific pathogenic bacteria play a central role in the etiology and pathogenesis of destructive periodontal disease . Under suitable conditions, periodontal pathogens colonize the subgingival environment and are incorporated into a tenacious biofilm . Successful prevention and treatment of periodontitis is contingent upon effective control of the periodontopathic bacteria . This is accomplished by professional treatment of diseased periodontal sites and patient-performed plaque control . Attention to community factors, such as water contamination and bacterial transmission among family members, facilitates preventive measures and early treatment for the entire family . Subgingival mechanical debridement, with or without surgery, constitutes the basic means of disrupting the subgingival biofilm and controlling pathogens . Appropriate antimicrobial agents that can be administered systemically (antibiotics) or via local delivery (povidone-iodine) may enhance eradication or marked suppression of subgingival pathogens . Microbiological testing may aid the clinician in the selection of the most effective antimicrobial agent or combination of agents . Understanding the benefits and limitations of antibiotics and antiseptics will optimize their usefulness in combating periodontal infections. J Mass Dent Soc, 2000 Autumn, 49(3), 10 - 3 Quantifiable risk in dentistry--a letter to the profession; Neiburger EJ; Recent attention to certain worries such as the AIDS "epidemic," biofilms in dental unit water lines, and hepatitis C have resulted in unbalanced and often inappropriate action by dentists and public health authorities . These actions include exaggerating, underestimating, and ignoring risks in the dental environment . To be effective and responsible practitioners, we must recognize reality and proportion, concentrate resources on the greatest problems, and seek dependable epidemiology . Infection control issues are an important application for this form of evidence-based science. Microbiology, 2001 May, 147(Pt 5), 1383 - 91 Assessment of GFP fluorescence in cells of Streptococcus gordonii under conditions of low pH and low oxygen concentration; Hansen MC et al.; Use of green fluorescent protein (GFP) as a molecular reporter is restricted by several environmental factors, such as its requirement for oxygen in the development of the fluorophore, and its poor fluorescence at low pH . There are conflicting data on these limitations, however, and systematic studies to assess the importance of these factors for growing bacterial cultures are lacking . In the present study, homogeneous expression of the gfpmut3* gene directed by a synthetic constitutive lactococcal promoter was demonstrated in batch cultures and in biofilms of Streptococcus gordonii DL1 . A lower limit of oxygen concentration for maturation of the GFP fluorophore was determined: fluorescence was emitted at 0.1 p.p.m . dissolved oxygen (in conventionally prepared anaerobic media lacking reducing agents), whereas no fluorescence was detected in the presence of 0.025 p.p.m . dissolved oxygen (obtained by addition of L-cysteine as reducing agent) . When an anaerobically grown (non-fluorescent) >50 microm thick biofilm was shifted to aerobic conditions, fluorescence could be detected within 4 min, reaching a maximum over the next 16 min . It was not possible to detect any fluorescence gradients (lateral or vertical) within the >50 microm thick biofilm, and fluorescence development after the shift to aerobic conditions occurred throughout the biofilm (even at the substratum) . This suggests that oxygen gradients, which might result in reduced GFP fluorescence, did not exist in the >50 microm thick biofilm of this organism . Production of lactic acid and the subsequent acidification in batch cultures of S . gordonii DL1 led to a decrease in fluorescence intensity . However, severe pH reduction was prevented when the bacterium was grown as a biofilm in a flowcell, and a homogeneous distribution of a strong fluorescence signal was observed . These findings show that GFP can be applied to studies of oxygen-tolerant anaerobic bacteria, that densely packed, flowcell-grown biofilms of S . gordonii do not develop oxygen gradients inhibitory to GFP fluorescence development, and that the often transient nature of GFP fluorescence in acid-producing bacteria can be overcome in flowcells, probably by the elimination of metabolic by-product accumulation. Appl Environ Microbiol, 2001 May, 67(5), 2319 - 25 Shewanella putrefaciens adhesion and biofilm formation on food processing surfaces; Bagge D et al.; Laboratory model systems were developed for studying Shewanella putrefaciens adhesion and biofilm formation under batch and flow conditions . S . putrefaciens plays a major role in food spoilage and may cause microbially induced corrosion on steel surfaces . S . putrefaciens bacteria suspended in buffer adhered readily to stainless steel surfaces . Maximum numbers of adherent bacteria per square centimeter were reached in 8 h at 25 degrees C and reflected the cell density in suspension . Numbers of adhering bacteria from a suspension containing 10(8) CFU/ml were much lower in a laminar flow system (modified Robbins device) (reaching 10(2) CFU/cm(2)) than in a batch system (reaching 10(7) CFU/cm(2)), and maximum numbers were reached after 24 h . When nutrients were supplied, S . putrefaciens grew in biofilms with layers of bacteria . The rate of biofilm formation and the thickness of the film were not dependent on the availability of carbohydrate (lactate or glucose) or on iron starvation . The number of S . putrefaciens bacteria on the surface was partly influenced by the presence of other bacteria (Pseudomonas fluorescens) which reduced the numbers of S . putrefaciens bacteria in the biofilm . Numbers of bacteria on the surface must be quantified to evaluate the influence of environmental factors on adhesion and biofilm formation . We used a combination of fluorescence microscopy (4',6'-diamidino-2-phenylindole staining and in situ hybridization, for mixed-culture studies), ultrasonic removal of bacteria from surfaces, and indirect conductometry and found this combination sufficient to quantify bacteria on surfaces. Water Res, 2001 Apr, 35(6), 1624 - 6 Helicobacter sp . recovered from drinking water biofilm sampled from a water distribution system; Park SR et al.; Workers examining the transmission route(s) and reservoir(s) of infection for Helicobacter pylori have postulated several environmental reservoirs for the organism, including water . Such work has, to date, concentrated on the bulk liquid in drinking water systems rather than on biofilms . Previous investigations by the authors have suggested biofilms in water distribution systems are a possible reservoir of infection . This current study comprised of an analysis of a section of cast iron mains distribution pipe removed from an urban environment in the north-east of Scotland during routine maintenance work . Immediately upon removal of the pipe section, the interior lumen was swabbed to remove the biofilm layer . Subsequent analysis for the presence of Helicobacter DNA using a nested PCR approach produced a positive result . This data provides the first evidence for the existence of Helicobacter in biofilms found in water distribution systems anywhere in the world. Water Res, 2001 Apr, 35(6), 1379 - 86 Methane microprofiles in a sewage biofilm determined with a microscale biosensor; Damgaard LR et al.; Microprofiles of the methane concentration in a 3.5-mm-thick sewage outlet biofilm were measured at high spatial and temporal resolution using a microscale biosensor for methane . In the freshly collected biofilm, methane was building up to a concentration of 175 mumol l-1 at 3 mm depth with a total methanogenesis of 0.14 mumol m-2 s-1, as compared to an aerobic respiration (including methane oxidation) of 0.80 mumol m-2 s-1 . A model biofilm was established by homogenisation of an in situ biofilm and 12 days of incubation with surplus sodium acetate . The homogenised biofilm was able to maintain 50% of the methanogenic activity in the absence of external electron donor . Oxygen had only a minor effect on the methane production, but aerobic respiration consumed a substantial part of the produced methane and was thus an important control on methane export from the biofilm . A concentration of 2 mmol l-1 nitrate was shown to inhibit methanogenesis only in the upper layer of the biofilm, whereas a further addition of 2 mmol l-1 sulphate inhibited methanogenesis in the entire biofilm . The study demonstrated the power of the methane microsensor in the study of microhabitats with concurrent production and consumption of methane. J Clin Pediatr Dent, 2000 Spring, 24(3), 237 - 43 Effects of three different infant dentifrices on biofilms and oral microorganisms; Modesto A et al.; The purpose of this work was to evaluate the effects of infant dentifrices: A--with lactoperoxidase, glucose oxidase and lactoferrin; B--with 1100 ppm of NaF and sodium lauryl sulfate; C--with extract of calendula . The dentifrices were test on biofilms formed in vitro from saliva and dental plaque of infants, using reference strains A . viscosus (ATCC 43146); C . albicans (ATCC 51501); L . casei (ATCC 4646); S . mitis (ATCC 49456); S . mutans (ATCC 25175); S . oralis (ATCC 35037); S . sanguis (ATCC 10586); S . sobrinus (ATCC 27609) and isolated clinically microorganisms C . albicans, S . mitis, S . mutans, S . oralis, S . sanguis, S . sobrinus and Lactobacillus sp . Twenty infants were chosen, who were beginning treatment at the Infants Clinic of the Pediatric Dentistry Department, Federal University of Rio de Janeiro . A pool of unstimulated saliva and a pool of dental plaque were collected from which biofilms were produced . Supernatants from each dentifrice were prepared and concentrated and diluted solutions of the dentifrices and a control sterile diluent were tested against the biofilms produced, for 1 and 3 minutes, and against the microorganisms . The results were statistically analyzed by the ANOVA and Tukey Test . After the exposure of the biofilms produced both from saliva and from dental plaque, to the dentifrice B concentrated and 1/2, for 1 and 3 minutes, the viable microorganisms count (CFU/ml), compared to the controls, was significantly reduced (p < 0.05) . However, exposure to the dentifrices A and C concentrated and dentifrice B 1/4 and 1/8, for 1 and 3 minutes, was not significantly lethal to the biofilms . The dentifrices A and C, either concentrated or diluted (1/2 to 1/128) and the dentifrice B in the dilutions 1/16 to 1/128 did not have an antimicrobial effect on any microorganism evaluated . For all the microorganisms evaluated, the dentifrice B concentrated and in the 1/2 dilution showed a significant antimicrobial effect, when compared with the control (p < 0.05). FEMS Microbiol Lett, 2001 Apr 13, 197(2), 151 - 7 Characterization and expression of secA in Mycobacterium avium; Limia A et al.; Mycobacterium avium is both a pathogen that infects several hosts such as humans, pigs, and birds, as well as a microorganism that is encountered in environmental sources (soil and water) . Protein secretion by the bacterium is likely to influence its ability to overcome adverse and competitive conditions both within or outside the host . Using a combination of cloning and information available in the databank, we characterized the secA gene from M . avium, encoding for a major preprotein translocase subunit associated with the secretion system of prokaryotics . In addition, we cloned the secA promoter sequence in a reporter construct upstream of a promoterless gfp . It was determined that the secA of M . avium shares large homology with the secA of Mycobacterium tuberculosis but not with secA of Mycobacterium leprae . secA expression was determined to be greater at logarithmic growth phase although it was also expressed at low levels during the stationary phase . secA expression was also observed when the bacteria were incubated in water as well as within human monocyte-derived macrophages and in conditions that are associated with biofilm formation . Future evaluation of the sec pathway in M . avium might provide important information about secreted proteins that are required for survival in different environments. Ann N Y Acad Sci, 1999 Jun 18, 875, 84 - 104 Physico-chemical and mass transfer considerations in microencapsulation; Goosen MF; To gain better insight into mass transfer problems in encapsulated cell systems requires a combination of experimental investigations and mathematical modeling . Specific mass transfer studies are reviewed including oxygen transfer in immobilized animal cell culture bioreactors, modeling of polymer droplet formation and encapsulated animal cell growth, and growth of somatic tissue encapsulated in alginate using electrostatics . Special emphasis is given to electrostatic droplet generation for cell immobilization. Can J Microbiol, 1999 Mar, 45(3), 235 - 41 Removal of phenolic compounds from a petrochemical effluent with a methanogenic consortium; Charest A et al.; A methanogenic consortium was used to degrade phenol and ortho- (o-) cresol from a specific effluent of a petrochemical refinery . This effluent did not meet the local environmental regulations for phenolic compounds (178 mg/L), oils and greases (61 mg/L), ammoniacal nitrogen (75 mg/L) or sulfides (3.2 mg/L) . The consortium, which degrades phenol via its carboxylation to benzoic acid, was progressively adapted to the effluent . Despite the very high effluent toxicity (EC50 of 2% with Microtox), the adapted consortium degraded 97% of 156 mg/L phenol in the supplemented effluent after 13 days in batch cultures (serum bottle) . The addition of proteose peptone to the effluent is essential for phenol degradation . o-cresol was also transformed but not meta- or para-cresols . A continuous flow fixed-film anaerobic bioreactor was developed with the consortium . Treating the effluent with the bioreactor reduced phenol and phenolic compounds concentrations by 97 and 83%, respectively, for a hydraulic residence time of 6 h . This treatment also reduced by about half the effluent toxicity . Oils and greases and ammoniacal nitrogen were not affected . Similar microbiological forms were observed in serum bottles and in the bioreactors with or without the petrochemical effluent . These results indicate that this methanogenic consortium can treat efficiently the phenolic compounds in this specific petrochemical effluent. J Immunother, 1999 Jul, 22(4), 299 - 307 Large-scale production of natural cytokines during activation and expansion of human T lymphocytes in hollow fiber bioreactor cultures; Lamers CH et al.; 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. Biotechnol Bioeng, 1999 Sep 5, 64(5), 580 - 9 Cardiac tissue engineering: cell seeding, cultivation parameters, and tissue construct characterization; Carrier RL et al.; Cardiac tissue engineering has been motivated by the need to create functional tissue equivalents for scientific studies and cardiac tissue repair . We previously demonstrated that contractile cardiac cell-polymer constructs can be cultivated using isolated cells, 3-dimensional scaffolds, and bioreactors . In the present work, we examined the effects of (1) cell source (neonatal rat or embryonic chick), (2) initial cell seeding density, (3) cell seeding vessel, and (4) tissue culture vessel on the structure and composition of engineered cardiac muscle . Constructs seeded under well-mixed conditions with rat heart cells at a high initial density ((6-8) x 10(6) cells/polymer scaffold) maintained structural integrity and contained macroscopic contractile areas (approximately 20 mm(2)) . Seeding in rotating vessels (laminar flow) rather than mixed flasks (turbulent flow) resulted in 23% higher seeding efficiency and 20% less cell damage as assessed by medium lactate dehydrogenase levels (p < 0.05) . Advantages of culturing constructs under mixed rather than static conditions included the maintenance of metabolic parameters in physiological ranges, 2-4 times higher construct cellularity (p &le 0.0001), more aerobic cell metabolism, and a more physiological, elongated cell shape . Cultivations in rotating bioreactors, in which flow patterns are laminar and dynamic, yielded constructs with a more active, aerobic metabolism as compared to constructs cultured in mixed or static flasks . After 1-2 weeks of cultivation, tissue constructs expressed cardiac specific proteins and ultrastructural features and had approximately 2-6 times lower cellularity (p < 0.05) but similar metabolic activity per unit cell when compared to native cardiac tissue . Appl Biochem Biotechnol, 1999 Spring, 77-79, 455 - 71 Bioconversion of mixed solids waste to ethanol; Nguyen QA et al.; A mixed solids waste (MSW) feedstock, comprising construction lumber waste (35% oven-dry basis), almond tree prunings (20%), wheat straw (20%), office waste paper (12.5%), and newsprint (12.5%), was converted to ethanol via dilute-acid pretreatment followed by enzymatic hydrolysis and yeast fermentation . The MSW was pretreated with dilute sulfuric acid (0.4% w/w) at 210 degrees C for 3 min in a 4-L steam explosion reactor, then washed with water to recover the solubilized hemicellulose . The digestibility of water-washed, pretreated MSW was 90% in batch enzymatic hydrolysis at 66 FPU/g cellulose . Using an enzyme-recycle bioreactor system, greater than 90% cellulose hydrolysis was achieved at a net enzyme loading of about 10 FPU/g cellulose . Enzyme recycling using membrane filtration and a fed-batch fermentation technique is a promising option for significantly reducing the cost of enzyme in cellulose hydrolysis . The hexose sugars were readily fermentable using a Saccharomyces cerevisiae yeast strain that was adapted to the hydrolysate . Solid residue after enzyme digestion was subjected to various furnace experiments designed to assess the fouling and slagging characteristics . Results of these analyses suggest the residue to be of a low to moderate slagging and fouling type if burned by itself. Biotechnol Bioeng, 1999 Aug 20, 64(4), 459 - 77 Integrated two-liquid phase bioconversion and product-recovery processes for the oxidation of alkanes: process design and economic evaluation Mathys RG, Schmid A, Witholt B. Pseudomonas oleovorans and recombinant strains containing the alkane oxidation genes can produce alkane oxidation products in two-liquid phase bioreactor systems . In these bioprocesses the cells, which grow in the aqueous phase, oxidize apolar, non-water soluble substrates . The apolar products typically accumulate in the emulsified apolar phase . We have studied both the bioconversion systems and several downstream processing systems to separate and purify alkanols from these two-liquid phase media . Based on the information generated in these studies, we have now designed bioconversion and downstream processing systems for the production of 1-alkanols from n-alkanes on a 10 kiloton/yr scale, taking the conversion of n-octane to 1-octanol as a model system . Here, we describe overall designs of fed-batch and continuous-fermentation processes for the oxidation of octane to 1-octanol by Pseudomonas oleovorans, and we discuss the economics of these processes . In both systems the two-liquid phase system consists of an apolar phase with hexadecene as the apolar carrier solvent into which n-octane is dissolved, while the cells are present in the aqueous phase . In one system, multiple-batch fermentations are followed by continuous processing of the product from the separated apolar phase . The second system is based on alkane oxidation by continuously growing cultures, again followed by continuous processing of the product . Fewer fermentors were required and a higher space-time-yield was possible for production of 1-octanol in a continuous process . The overall performance of each of these two systems has been modeled with Aspen software . Investment and operating costs were estimated with input from equipment manufacturers and bulk-material suppliers . Based on this study, the production cost of 1-octanol is about 7 US$kg-1 when produced in the fed-batch process, and 8 US$kg-1 when produced continuously . The comparison of upstream and downstream capital costs and production costs showed significantly higher upstream costs for the fed-batch process and slightly higher upstream costs for continuous fermentation . The largest cost contribution was due to variable production costs, mainly resulting from media costs . The organisms used in these systems are P . putida alk+ recombinants which oxidize alkanes, but cannot oxidize the resulting alkanols further . Hence, such cells need a second carbon source, which in these systems is glucose . Although the continuous process is about 10% more expensive than the fed-batch process, improvements to reduce overall cost can be achieved more easily for continuous than for fed-batch fermentation by decreasing the dilution rate while maintaining near constant productivity . Improvements relevant to both processes can be achieved by increasing the biocatalyst performance, which results in improved overall efficiency, decreased capital investment, and hence, decreased production cost . Biotechnol Bioeng, 1999 Aug 20, 64(4), 452 - 8 Membrane sparger in bubble column, airlift, and combined membrane-ring sparger bioreactors Poulsen BR, Iversen JJ. The bubble column and the two internal loop airlift reactors (riser/downcomer area ratios of 0.11 and 0.58) characterized in this study were equipped with a rubber membrane sparger, which produced small bubbles, giving high mass transfer coefficients . The low mixing intensity in the bubble column was increased by an order of magnitude in the airlift reactors . We designed a novel aeration and mixing system by adding a ring sparger to the membrane sparger in the bubble column and maintained the advantages of both airlift configuration (good mixing properties) and bubble column configuration (efficient aeration, without any internal constructions) . The combined membrane-ring sparger system has unique features with respect to the efficiency of utilization of substrate gasses and energy . Model experiments showed that the small bubbles from the membrane sparger do not coalesce with the large bubbles from the ring sparger . If different gases were added through the two spargers it was possible to transfer a hazardous or expensive gas quantitatively to the liquid through the membrane sparger (dual sparging mode) . In the combined membrane-ring sparger system the energy input for mixing and mass transfer is divided . Therefore, the energy consumption can be minimized if the flow distribution of air through the membrane and ring sparger is controlled by the oxygen demand and the inhomogeneity of the culture, respectively (split sparging mode) . The dual sparging mode was used for mass production of the alga Rhodomonas sp . as the first step in aquatic food chains . Avoiding mechanical parts removes an important risk of malfunction, and a continuous culture could be maintained for more than 8 months . Biotechnol Bioeng, 1999 Jul 5, 64(1), 14 - 26 Characterization of bimodal cell death of insect cells in a rotating-wall vessel and shaker flask Cowger NL, O'Connor KC, Hammond TG, Lacks DJ, Navar GL. In previous publications, we reported the benefits of a high-aspect rotating-wall vessel (HARV) over conventional bioreactors for insect-cell cultivation in terms of reduced medium requirements and enhanced longevity . To more fully understand the effects that HARV cultivation has on longevity, the present study characterizes the mode and kinetics of Spodoptera frugiperda cell death in this quiescent environment relative to a shaker-flask control . Data from flow cytometry and fluorescence microscopy show a greater accumulation of apoptotic cells in the HARV culture, by a factor of at least 2 at the end of the cultivation period . We present a kinetic model of growth and bimodal cell death . The model is unique for including both apoptosis and necrosis, and further, transition steps within the two pathways . Kinetic constants reveal that total cell death is reduced in the HARV and the accumulation of apoptotic cells in this vessel results from reduced depletion by lysis and secondary necrosis . The ratio of early apoptotic to necrotic cell formation is found independent of cultivation conditions . In the model, apoptosis is only well represented by an integral term, which may indicate its dependence on accumulation of some factor over time; in contrast, necrosis is adequately represented with a first-order term . Cell-cycle analysis shows the percent of tetraploid cells gradually decreases during cultivation in both vessels . For example, between 90% and 70% viability, tetraploid cells in the HARV drop from 43 +/- 1% to 24 +/- 4% . The data suggests the tetraploid phase as the likely origin for apoptosis in our cultures . Possible mechanisms for these changes in bimodal cell death are discussed, including hydrodynamic forces, cell-cell interactions, waste accumulation, and mass transport . These studies may benefit insect-cell cultivation by increasing our understanding of cell death in culture and providing a means for further enhancing culture longevity . Biotechnol Bioeng, 1999 Jun 5, 63(5), 601 - 11 Epoxidation of 1,7-octadiene by pseudomonas oleovorans in a membrane bioreactor Doig SD, Boam AT, Livingston AG, Stuckey DC. A growing cell culture of Pseudomonas oleovorans was used to biotransform 1,7-octadiene to 1,2-epoxy-7,8-octene in a continuous-flow bioreactor with an external membrane module . A dense silicone rubber membrane was used to contact an organic phase, containing both the reactant (1,7-octadiene) and the growth substrate (heptane), with an aqueous biomedium phase containing the biocatalyst . Heptane and octadiene delivery to the aqueous phase, and epoxide extraction into the solvent, occurred by diffusion across the dense membrane under a concentration-driving force . In addition, a liquid feed of heptane and octadiene was pumped directly into the bioreactor to increase the rate of delivery of these compounds to the aqueous phase . In this system 1,2-epoxy-7,8-octene accumulated in a pure solvent phase, thus, product recovery problems associated with emulsion formation were avoided . Furthermore, no phase breakthrough of either liquid across the membrane was observed . In this system, the highest volumetric productivity obtained was 30 U.L-1, and this was achieved at a dilution rate of 0.07 h-1, 70 m2 . m-3 of membrane area, and a steady-state biomass concentration of 2 . 5 g.L-1 . The system was stable for over 1250 h . Decreasing the dilution rate led to an increased biomass concentration, however, the specific activity was significantly reduced, and therefore, an optimal dilution rate was determined at 0.055 h-1 . Biotechnol Bioeng, 1999 Jun 5, 63(5), 593 - 600 Studies on the respiration rate of free and immobilized cells of cephalosporium acremonium in cephalosporin C production Araujo ML, Giordano RC, Hokka CO. Bioprocesses using filamentous fungi immobilized in inert supports present many advantages when compared to conventional free cell processes . However, assessment of the real advantages of the unconventional process demands a rigorous study of the limitations to diffusional mass transfer of the reagents, especially concerning oxygen . In this work, a comparative study was carried out on the cephalosporin C production process in defined medium containing glucose and sucrose as main carbon and energy sources, by free and immobilized cells of Cephalosporium acremonium ATCC 48272 in calcium alginate gel beads containing alumina . The effective diffusivity of oxygen through the gel beads and the effectiveness factors related to the respiration rate of the microorganism were determined experimentally . By applying Monod kinetics, the respiration kinetics parameters were experimentally determined in independent experiments in a complete production medium . The effectiveness factor experimental values presented good agreement with the theoretical values of the approximated zero-order effectiveness factor, considering the dead core model . Furthermore, experimental results obtained with immobilized cells in a 1.7-L tower bioreactor were compared with those obtained in 5-L conventional fermentor with free cells . It could be concluded that it is possible to attain rather high production rates working with relatively large diameter gel beads (ca . 2.5 mm) and sucrose consumption-based productivity was remarkably higher with immobilized cells, i.e., 0.33 gCPC/kg sucrose/h against 0.24 gCPC/kg sucrose/h in the aerated stirred tank bioreactor process . Biotechnol Bioeng, 1999 Aug 20, 64(4), 401 - 17 Incorporation of ammonium into intracellular UDP-activated N-acetylhexosamines and into carbohydrate structures in glycoproteins; Valley U et al.; The negative effects of ammonia on animal cells, especially in vitro cultures, are well known, but the mechanism of how ammonia inhibits cell growth and influences the glycosylation of proteins is not completely understood . We investigated the ammonium action on the synthesis of the intracellular UDP-N-acetylhexos- amines (UDPGNAc), which are precursors of glycosylation as well as on N-linked oligosaccharides of a recombinant human IL-2 mutant variant model glycoprotein expressed in BHK-21 cells under defined and controlled culture conditions in a continuously perfused bioreactor . The examinations were based on our previous observations that increased ammonia concentrations in the medium lead to the intracellular formation and accumulation of UDPGNAc (Ryll et al., 1994) . The kinetics of formation of the UDPGNAc pool after adding ammonia and its reconstitution to normal conditions are shown . To study the pathway leading to the intracellular increase of UDPGNAc, the uptake and incorporation of 15NH4+ was confirmed by the detection of 15N in UDP-N-acetylglucosamine (UDP-GlcNAc) . UDP-GlcNAc was purified using high pH anion-exchange chromatography with pulsed amperometric detection and analyzed by GC/MS . The proportion of UDP-GlcNAc containing 15N was approximately 60% and corresponds quantitatively to the increased intracellular concentration of UDP-GlcNAc . In order to confirm the direct influence of ammonia on protein glycosylation, the human IL-2 mutant glycoprotein variant IL-Mu6, bearing a novel N-glycosylation site, has been produced under defined protein-free medium conditions in the presence of 15NH4Cl . IL-Mu6 glycoprotein was purified and N-glycans released were analyzed by matrix-assisted laser desorption ionization time of flight mass spectroscopy . Maximally 60-80% of N-acetylated sugars in N-glycan structures contained 15N indicating that ammonium is used as a building block during synthesis of the carbohydrate structures expressed from in vitro cultivated mammalian cells . Biotechnol Bioeng, 1999 Aug 5, 64(3), 357 - 67 Monitoring of intracellular ribonucleotide pools is a powerful tool in the development and characterization of mammalian cell culture processes; Grammatikos SI et al.; Efficient cell culture process development for the industrial production of recombinant therapeutics is characterized by constraints which pertain to issues such as costs, competitiveness and the meeting of project timelines . These constraints require tools which can help the developer learn as much as possible as quickly as possible about the cell at hand and identify features of a particular culture which are amenable to improvement . Current on- and off-line monitoring parameters, however useful, provide only late indications (cell concentration, viability) and circumstantial evidence (lactate, ammonia, etc.) with regard to the physiologic status of cells at the time of sampling . The relative intracellular content of purine to pyrimidine nucleotide triphosphates as well as the ratio of UTP to UDP-N-acetylhexosamines have been previously described as sensitive indicators of a cell's metabolic status, growth potential, and overall physiological condition . The sensitivity of such nucleotide ratios and their usefulness in commercially relevant process development and characterization were tested at Boehringer Ingelheim Pharma KG in a large number of fermentations (>80) with a variety of culture modes, cells, and products in scales up to 10,000 litres . Monitoring of these intracellular parameters allows a timely and reliable assessment of cell state and growth potential, which is possible neither by classical cell number and viability measurements nor by a variety of fermentation data typically monitored . The view inside the cell afforded by nucleotide monitoring enables prediction of the behavior of a culture up to 2 days before any hint of physiological changes is given by cell number and viability estimation . In this paper, data relating the growth behavior of CHO and hybridoma cell lines to their nucleotide pools are shown . Two very different processes for the production of recombinant tPA in 10,000-litre bioreactors are compared and characterized with respect to their nucleotide profiles . Examples from industrial process development cases in which intracellular nucleotide information is used to advantage are also presented and discussed . Biotechnol Bioeng, 1999 Jul 20, 64(2), 194 - 9 Efficient coupled transcription/translation from PCR template by a hollow-fiber membrane bioreactor; Nakano H et al.; A novel bioreactor using a hollow-fiber membrane was developed for the coupled transcription/translation system using T7 RNA polymerase and Escherichia coli S30 extract . The large surface area per the reaction volume of the reactor assured rapid mass transfers of substrates into the reaction mixture and of wastes out from it across the membrane by their molecular diffusion . The flux was large enough to maintain nucleotide concentrations for more than 3 h, which increased the protein synthesis greatly . In addition, the T7 terminator sequence downstream from the reporter genes was found to increase the synthesized protein significantly, especially when the product of polymerase chain reaction (PCR) was used as a template . Implementation of this finding and use of the bioreactor developed multiplied the productivity of protein by the in vitro direct expression from PCR template . Biotechnol Bioeng, 1999 Jun 5, 63(5), 618 - 24 Regional heparinization via simultaneous separation and reaction in a novel Taylor-Couette flow device; Ameer GA et al.; The development of a safe and efficient bioreactor design has remained a challenge for the clinical application of immobilized enzymes . Specifically, the use of immobilized heparinase I has been the target of many studies to make heparin anticoagulation therapy safer for the critically ill patient with kidney failure or heart disease . We have investigated the use of Taylor-Couette flow for a novel type of bioreactor . In a previous study, we showed that the fluidization of agarose immobilized heparinase within Taylor vortices in whole blood can lead to extensive blood damage in the form of cell depletion and hemolysis . Based on these findings, we designed and developed a reactor, referred to as vortex-flow plasmapheretic reactor (VFPR), that incorporated plasmapheresis and fluidization of the agarose in the reactive compartment, separate from the whole-blood path . In the present study, immobilized heparinase I was tested as a means of achieving regional heparinization of a closed circuit . This is a method in which heparin is infused into the extracorporeal circuit predialyzer and neutralized postdialyzer . Saline studies were performed with an immobilized heparinase I-packed bed and with the VFPR . An in vitro feasibility study was performed with the VFPR using human blood . The VFPR achieved heparin conversions of 44 +/- 0.5% and 34 +/- 2% in saline and blood, respectively . In addition, the VFPR caused no blood damage . We report a novel method to achieve fluidization which depended on secondary, circumferencial flow, and was independent of the primary flow through the device . Compost is a common name for humus, which is the result of the decomposition of organic matter. Decomposition is performed primarily by microbes, although larger creatures such as worms and ants contribute to the process. Decomposition occurs naturally in all but the most hostile environments, such as buried in landfills or in extremely arid deserts, which prevent the microbes and other decomposers from thriving. Composting is the controlled decomposition of organic matter. Rather than allowing nature to take its slow course, a composter provides an optimal environment in which decomposers can thrive. To encourage the most active microbes, the compost pile needs the proper mix of the following ingredients: Carbon Nitrogen Oxygen (air) Water. Decomposition happens even in the absence of some of these ingredients, but not nearly as quickly and not nearly as pleasantly (for example, the plastic bag of vegetables in your refrigerator is decomposed by microbes, but the absence of air encourages anaerobic microbes that produce disagreeable odors). All guidelines for building compost piles have the goal of creating the proper environment for a decomposing ecosystem. The ecosystem in a compost pile is a microcosm of larger ecosystems. The correct environment must be maintained for a healthy and vigorous community of decomposers. In addition to the decomposers that work directly on the organic content of the pile, compost piles provide habitat for those that prey upon direct decomposers. Their waste also becomes part of the process. The most effective decomposers are bacteria and other microorganisms. Also important are fungi, molds, protozoa, and actinomycetes--which is something between a fungus and a mold and is often seen as white filaments in decomposing organic matter. At a macroscopic level, earthworms, ants, snails, slugs, millipedes, sow bugs, springtails, and others work on consuming and breaking down the organic matter. Centipedes and other predators feed upon these decomposers. Compost ingredients The goal in a compost pile is to provide a healthy environment--and nutrition--for the rapid decomposers, the bacteria. The most rapid composting occurs with the ideal ratio--by dry chemical weight--of carbon to nitrogen, from 25-to-1 to 30-to-1. In other words, the ingredients placed in the pile should contain 30 times as much carbon as nitrogen. For example, grass clippings average about 19-to-1 and dry autumn leaves average about 55-to-1. Mixing equal parts by volume approximates the ideal range. Commercial-grade composting operations pay strict attention to this ratio. For backyard composters, however, the charts of carbon and nitrogen ratios in various ingredients and the calculations required to get the ideal mixture can be intimidating, so many rules of thumb exist to guide composters in approximating this mixture. High-carbon sources provide the cellulose needed by the composting bacteria for conversion to sugars and heat. High-nitrogen sources provide the most concentrated protein, which allow the compost bacteria to thrive. Some ingredients with higher carbon content: Dry, straw-type material, such as cereal straws Autumn leaves Sawdust and wood chips Some paper and cardboard (such as corrugated cardboard or newsprint with soy-based inks) Some ingredients with higher nitrogen content: Wilted green material (usually crop residues, or plants mowed for the purpose) Animal manures (vegetarians, not meat-eaters) Grass clippings Fruit and vegetable trimmings, skins, and waste Poultry manure provides lots of nitrogen but little carbon. Horse manure provides both. Sheep and cattle manure don't drive the compost heap to as high a temperature as poultry or horse manure, so the heap takes longer to produce the finished product. In an attempt to judge the proper mix of materials, different rules of thumb are available. Some prefer to add one basket full of nitrogen source followed by one basket of carbon source. Mixing the materials as they are added increases the rate of decomposition, but some people prefer to place the materials in alternating layers, approximately 15 cm (6 inches) thick, to help estimate the quantities. Keeping carbon and nitrogen sources separated in the pile can slow down the process but decomposition will occur in any event. Composting techniques There are two primary methods of aerobic composting: Active (or hot) composting, which allows the most effective decomposing bacteria to thrive, kills most pathogens and seeds, and rapidly produces usable compost Passive (or cold) composting, which lets nature take its course in a more leisurely manner and leaves many pathogens and seeds dormant in the pile Most commercial and industrial composting operations use active composting techniques. This ensures a higher quality product and produces results in the shortest time (SEE compost windrow turner). Home composters use a range of techniques varying from extremely passive composting (throw everything in a pile in a corner and leave it alone for a year or two) to extremely active (monitoring the temperature, turning the pile regularly, and adjusting the ingredients over time) and combinations of both. Some composters use mineral powders to absorb smells, although a well-maintained pile seldom has bad odors. Microbes and heating the pile An effective compost pile is kept about as damp as a well wrung-out sponge. This provides the moisture that all life needs to survive; in a compost pile, it provides an environment in which microbes can begin to do their work. Bacteria and other microorganisms fall into a variety of groups in terms of what their ideal temperature is and how much heat they generate as they do their work. Mesophilic bacteria enjoy midrange temperatures, from about 20 to 40 °C (70 to 110 °F). As they decompose the organic matter, they generate heat, and the inner part of a compost pile heats up the most. The heap should be about 1 m (3 ft) wide, 1 m (3 ft) tall, and as long as is practicable – the advantage to making the heap at least 1 m³ (1 yd³) is that it provides suitable insulating mass to allow a good heat build-up as the material decays. The ideal temperature range hovers around 60 °C (140 °F), which kills most pathogens and weed seeds and also provides a suitable environment for thermophilic (heat-loving) bacteria, which are the fastest acting decomposers. The centre of the heap should get quite warm, possibly hot enough to burn a bare hand. If this fails to happen, common reasons include the following: The heap is too wet, thus excluding the oxygen required by the compost bacteria The heap is too dry, so that the bacteria do not have the moisture needed to survive and reproduce There is insufficient protein (nitrogen rich material) The solution is to add material, if necessary, and/or to turn the pile to aerate it. Depending on how quickly the compost is required, the heap can be turned one or more times to bring the outer layers to the inside of the heap and vice versa, as well as to aerate the mixture. Adding water at this time keeps the pile as damp as a wrung-out sponge. One guideline is to turn the pile when the high temperature has begun to drop, indicating that the food source for the fastest-acting bacteria (in the center of the pile) has been largely consumed. After the temperature stops rising after the pile has been turned, there is no further advantage in turning the pile. When all the material has become barely recognisable from the original ingredients, turning into dark brown or nearly black crumbly matter, it's ready to use. Some practitioners like to leave the compost to mature further for up to a year as this seems to make the benefits of compost last longer. Other ingredients Some like to put special materials and activators into their compost. A light dusting of agricultural lime (not on the animal manure layers) can curb excessive acidity that can slow down the fermentation. Seaweed meal can provide a ready source of trace elements. Finely pulverised rock dust can also provide needed minerals, but watch out for rock dust that consists mostly of clay. The animal manure part of compost source materials can be collected by composting toilets (in this case, human feces). However, such compost is usually not used as a fertilizer for plants that are directly edible (e.g., salad crops) but should instead be used on trees, bush fruits or else on the ornamental garden. Bioaugmentation refers to the introduction of a group of natural microbial strain or a genetically engineered variant so as to achive bioremediation. Usually the step involves studying the indigenous varieties present in the location. If the indigenous variety do not have the metabolic machinery that can do the remediation process, exogenous varieties with such sophisticated pathways are introduced. Remediation is the removal of pollution or contaminants from land (including sediments in waterways) for the general protection of the environment or, quite commonly, from a brownfield site so that it can be reused. The reuse of brownfield sites is part of the urban consolidation movement and allows the regeneration of decaying former industrial areas, sometimes for industry, but often for high density housing, particulalry in areas of scenic beauty (along Harbours and rivers) and close to the CBD of a city or major transport infrastructure such as railway stations. Remediation is generally subject to an array of legislation, and is based on assessments of health and ecological risks where there are no legislated standards or where standards are advisory (often called preliminary remediation goals (PRG)s). Remediation in terms of new media, is the representation of one medium in another. (Jay David Bolter and Richard Grusin 1999). Remediation standards In the USA the most comprehensive set of PRG's is from the EPA Region 9, although the Canadian EPA also has a comprehensive spreadsheet of PRG's. There is also a set of standard used in Europe commonly called the Dutch standards. The EU is rapidly moving towards European wide standards, although most of the industrialised nations in Europe have their own standards at present Site assessment Once a site is suspected of being seriously contaminated there is a need to assess it. The historical use of the site and the materials used and produced on site will guide the assessment strategy and nature of sampling and chemical testing to be done. Often nearby sites owned by the same company or which are nearby and have been reclaimed, levelled or filled are also contaminated even where the current land use seems innocuous. For example, the car park may have been levelled by using contaminated waste in the fill. It is also important to consider off site contamination or nearby sites often through decades of emissions to soil, water, and air. Ceiling dust, topsoil, surface and groundwater of nearby properties should be tested both before and after the remediation. This is a controversial step as: No one wants to have to pay for the clean up of the site; If nearby properties are found to be contaminated it may have to be noted on their property title, potentially affecting saleability or value; No one wants to pay for the cost of assessment. Often corporations which do voluntary testing of their sites are protected from the reports to environmental agencies becoming public under Freedom of Information Acts, however a Freedom Of Information inquiry will often produce other documents that are not protected or will produce references to the reports. Funding remediation In the US there has been a mechanism for taxing polluting industries to form a Superfund to remediate abandoned sites, or to litigate to force corporations to remediate their contaminated sites. Other countries have other mechanisms and commonly sites are rezoned to "higher" uses such as high density housing, to give the land a higher value so that after deducting clean up costs there is still an incentive for a developer to purchase the land, clean it up, redevelop it and sell it on, often as apartments (home units). Remediation technologies Remediation technologies are many and varied. The best source of information is probably http://www.clu-in.org/ Some technologies are controversial, particularly anything involving relative low temperature incineration because of the risks of dioxins released in the atmosphere through the exhaust gases. For this reason remediation proponents often use terminolgy like thermal oxidiser and direct thermal desorption to minimise the risk of the community thinking about incineration risks. However, controlled, high temperature incineration with filtering of exhaust gases should not pose any risks. The treatment of environmental problems through biological means is known as bioremediation and the specific use of plants is known as phytoremediation. Community consultation and information In preparation for any significant remediation there should be extensive community consultation. The proponent should both present information to and seek information from the community. The proponent needs to know about "sensitive" (future) uses like childcare, schools, hospitals, and playgrounds as well as community concerns and interests information. Consultation should be open, on a group basis so that each member of the community is informed about issues they may not have individually thought about. An independent chairperson acceptable to both the proponent and the community should be engaged (at proponent expense if a fee is required). Minutes of meetings including questions asked and the answers to them and copies of presentations by the proponent should be available both on the internet and at a local library (even a school library) or community centre. Incremental health risk Incremental Health Risk is the increased risk that a receptor (normally a human being living nearby) will face from (the lack of) a remediation project. The use of incremental health risk is based on cancer and non-cancer effects such as reproductive abnormalities and often involves value judgements about the acceptable projected rate of increase in cancer. In some jursdictions this is 1 in a million, but in other jurisdictions it is 1 in 100,000. A relatively small incremental health risk from a single project is not of much comfort if the area already has a relatively high health risk from other operations like incinerators or other emissions, or if there are other projects at the same time causing a greater cumulative risk or an unacceptably high total risk. An analogy often used by remediators is to compare the risk of the remediation on nearby residents to the risks of death through car accidents or tobacco smoking. Emissions standards Standards are set for the levels of dust, noise, odour, emissions to air and groundwater, and discharge to sewer or waterways of all chemicals of concern or chemicals likely to be produced during the remediation by processing of the contaminants. These are compared against both natural background levels in the area and standards for areas zoned as nearby areas are zoned and against standards used in other recent remediations. Just because the emission is emanating from an area zoned industrial doesn't mean that in a nearby residential area there should be permitted any exceedences of the appropriate residential standards. Monitoring for compliance against each standards is critical to ensure that exceedences are detected and reported both to authorities and the local community. Enforcement is necessary to ensure that continued or significant breeches result in fines or even a jail sentence for the remediator. Penalties must be significant as otherwise fines are treated as a normal expense of doing business. It must be cheaper to comply than have continuous breeeches. Transport and emergency safety assessment Assessment should be made of the risks of operations, transporting contaminated material, disposal of waste which may be contaminated including workers clothes, and a formal emergency response plan should be developed. Every worker and visitor entering the site should have a safety induction tailored to their involvement with the site. Impacts of funding remediation The rezoning is often resisted by local communities and local government because of the adverse impacts on the local amenity of the remediation and the new development. The main impacts during remediation are noise, dust, odour and incremental health risk. Then there is the noise dust and traffic of developments. Then there is the impact on local traffic, schools, playing fields, and other public facilities of the often vastly increased local population. Example of a major remediation project For an example of a complete rezoning by a state government over the opposition of local government and local communities of former chemical plants to fund remediation to allow for redevelopment for high density residential, retail and office development in Australia see http://rhodesnsw.org In this case the proposed rezoning, remediation and redevelopment has a wealth of material available through the internet from: list of sources of publicly available material, most accessible through the internet and from http://rhodesnsw.org: Numerous investigations and reports by Australian and International consultants For the former Union Carbide site, a previous remediation by excavation and containment in a clay capped sarcophagus, separated from the Bay by a bentonite wall. A Parliamentary Inquiry by the Upper House of the Parliament of New South Wales, a state of Australia; Two Commissions of Inquiry, one for each of the major dioxin contaminated sites, both contaminated by the operations of Union Carbide; Resolutions by the relevant local government bodies (originally Concord council and after the Municipality of Concord was merged with Drummoyne Council to form the City of Canada Bay, by that Council); Campaigns by local residents' groups, Greenpeace Australia, Nature Conservation Council of NSW, and Inner West (of Sydney branch of the) Greens published submissions by Planning NSW and Environmental Protection Agency of NSW; Comprehensive Environmental Impact studies published in digital format and available on CD from Planning NSW. This rezoning, remediation and redevelopment of land contaminated by Union Carbide, ICI and others also involves the remediation of a strip of dioxin contaminated sediments in Homebush Bay, New South Wales. The Homebush Bay area was home to the main events of the Sydney 2000 Summer Olympics. The sediments were dealt with in the Commission of Inquiry into the Lednez site formerly owned by Union Carbide, but not to the satisfaction of local community activists. The remediation of Homebush Bay is important because of its impact on the food chain which extends through benthos not only to local protected and threatened species of birds, but also to JAMBA and CAMBA protected species and species which use other RAMSAR protected wetlands. Ultimately human health is impacted through the food chain. Homebush Bay has a complete fishing ban, there is a commercial fin fishing ban west of the Gladesville Bridge, and based on submissions of the remediator and NSW Waterways and EPA the complete fishing ban ought be extended to the whole of the Parramatta River west of Homebush Bay and at least as far East as the Ryde Traffic Bridge. Phytoremediation is the technical term used to describe the treatment of environmental problems through the use of plants. Certain plants are able to extract hazardous substances such as arsenic, lead and uranium from soil and water. One example is alpine pennycress, a plant which naturally accumulates high levels of cadmium and zinc from the environment. Alpine pennycress is therefore known as a hyperaccumulator of these metals, which in unnaturally high levels would be poisionous to many plants. Another example of a hyperaccumulator is the brake fern. This fern extracts arsenic from the soil at a much greater rate than other plants. This has been done successfully in clinical trials, particularly in the case of Ashanti DeSilva, a girl who had a defective gene that was responsible for the immune system enzyme ADA. Thus she was prone to infections. Scientists took out her white blood cells and used a delivery system to inject a functional ADA gene into the cells. These were injected back into Ashanti's arm. a, f. Now she takes only a small "backup" dose of what would have been a battery of preventive medicines for maintaining her healthy state. This arsenic is stored in the fern's leaves at as much as 200 times that present in the soil, thus enabling effective and practical clean-up programs. Sunflowers were also used to clean up uranium near Chernobyl. Breeding programs and genetic engineering are powerful methods for enhancing natural tendencies of plant, or for introducing these tendencies into alternative types of plant which might be more suitable for the environmental conditions. The range of biological treatments for environmental problems, as described by the term phytoremediation, actually consists of several specific processes: Phytoextraction - Uptake of substances from the environment, with storage in the plant (phytoaccumulation). Phytostabilisation - Reducing the movement or transfer of substances in the environment. For example, limiting the leaching of substances contaminating soil. Phytostimulation - Enhancement of microbial activity for the degradation of contaminants, typically around plant roots. Phytotransformation - Uptake of substances from the environment, with degradation occurring within the plant (phytodegradation). Phytovolatilization - Removal of substances from the soil or water with release into the air, possibly after degradation. Rhizofiltration - The removal of toxic metals from ground water. Bioleaching is the extraction of specific metals from their ores through the use of bacteria. Bioleaching is a new technique used by the mining industry to extract minerals such as gold and copper from their ores. Traditional extractions involve many expensive steps such as roasting and smelting, which requires sufficient concentrations of elements in ores. Low concentrations are not a problem for bacteria because they simply ignore the waste which surrounds the metals, attaining extraction yields of over 90% in some cases. These microorganisms actually gain energy by breaking down minerals into their constituent elements. The company simply collects the ions out of solution after the bacteria have finished. Some advantages associated with bioleaching are: economical: bioleaching is generally simpler and therefore cheaper to operate and maintain than traditional processes, since fewer specialists are needed to operate complex chemical plants. environmental: The process is more environmentally friendly than traditional extraction methods. For the company this can translate into profit, since the necessary limiting of sulfur dioxide emissions during smelting is expensive. Less landscape damage occurs, since the bacteria involved grow naturally, and the mine and surrounding area can be left relatively untouched. As the bacteria breed in the conditions of the mine, they are easily cultivated and recycled. Some disadvantages associated with bioleaching are: not economical: the bacterial leaching process is very slow compared to smelting. This brings in less profit as well as introducing a significant delay in cash flow for new plants. not environmental: Toxic chemicals are sometimes produced in the process. Sulfuric acid and H+ ions formed can leak into the ground and surface water turning it acidic, causing environmental damage. Heavy ions such as iron, zinc, and arsenic leak during acid mine drainage. When the pH of this solution rises, as a result of dilution by fresh water, these ions precipitate, forming "Yellow Boy" pollution. For these reasons, setup of bioleaching must be carefully planned, since the process can lead to biosafety failure. f, i, a. Currently it is more economical to smelt copper ore rather than to use bioleaching, since the concentration of copper in its ore is generally quite high. The profit obtained from the speed and yield of smelting justifies its cost. However, the concentration of gold in its ore is generally very low. The cheaper cost of bacterial leaching in this case outweighs the time it takes to extract the metal. Bacteria (singular, bacterium) are a major group of living organisms. They are microscopic and mostly unicellular, with a relatively simple cell structure lacking a cell nucleus, cytoskeleton, and organelles such as mitochondria and chloroplasts. Such organisms are called prokaryotes, in contrast to organisms with more complex cells, called eukaryotes. The term bacteria has variously applied to all prokaryotes or to a major group of them, depending on ideas about their relationships. abundant of all organisms. They are ubiquitous in soil, water, and as symbionts of other organisms. Many pathogens, including those responsible for many if not most non-hereditary diseases, are bacteria. Most are minute, usually only 0.5-5.0 μm in size, though one type may reach 0.3 mm in diameter (Thiomargarita). They generally have cell walls, like plant and fungal cells, but with a very different composition (peptidoglycans). Many move around using flagella, which are different in structure from the flagella of other groups. The first bacteria were observed by Antony van Leeuwenhoek in 1683 using a single-lens microscope of his own design. The name bacterium was introduced much later, by Ehrenberg in 1828, derived from the Greek word βακτηριον meaning "small stick". Louis Pasteur (1822-1895) and Robert Koch (1843-1910) described the role of bacteria as conveyors and causes of disease or pathogens. Originally the bacteria were considered microscopic fungi (called Schizomycetes), except for the photosynthetic cyanobacteria, which were considered a group of algae (called Cyanophyta or blue-green algae). It was only with the study of detailed cell structure that it was realized they formed a fundamental group, separate from the other organisms. In 1956 Copeland gave them their own kingdom Mychota, later renamed Monera, Prokaryota, or Bacteria. During the 1960s the concept was refined and bacteria (now including cyanobacteria) were recognized as one of two major divisions of the living world, together with the eukaryotes. Eukaryotes were generally believed to have evolved from bacteria, later from assemblies of bacteria. The advent of molecular systematics challenged this view. In 1977, Woese divided the prokaryotes into two groups based on 16S rRNA sequences, called the kingdoms Eubacteria and Archaebacteria. He argued that each of these and the eukaryotes all evolved separately and in 1990 emphasized this by promoting them to domains, which were renamed the Bacteria, Archaea, and Eucarya. This redefinition has generally been accepted by molecular biologists but criticized by some others, who maintain that he over-emphasized a few genetic differences and that both archaebacteria and eukaryotes probably developed from within the eubacteria. Reproduction Bacteria reproduce only asexually, not sexually. Specifically they reproduce by binary fission, or simple cell division. During this process, one cell divides into two daughter cells with the development of a transverse cell wall. However, independent of sexual reproduction, genetic variations can occur within individual cells through recombinant events such as mutation (random genetic change within a cell's own genetic code). Similar to more complex organisms, bacteria also have mechanisms for exchanging genetic material. Although not equivalent to sexual reproduction, the end result is that a bacterium contains a combination of traits from two different parental cells. Three different modes of exchange have thus far been identified in bacteria: transformation (the transfer of naked DNA from one bacterial cell to another in solution, this can include dead bacteria), transduction (the transfer of viral, bacterial, or both bacterial and viral DNA from one cell to another via bacteriophage) and; bacterial conjugation (the transfer of DNA from one bacterial cell to another via a special protein structure called a conjugation pilus). Bacteria, having acquired DNA from any of these events, can then undergo fission and pass the recombined genome to new progeny cells. Many bacteria harbor plasmids that contain extrac |