POROUS POLYMERIC BIOSUPPORTS AND THEIR USE IN THE BIOTREATMENT OF AQUEOUS WASTE STREAMS

Abstract: Porous biosupports for the support of microorganisms which are used in the biotreatment of an aqueous waste stream comprising a polymeric material and, optionally, fiber reinforcement, adsorbent material and/or inorganic filler wherein the biosupport has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to readily colonize within the pores, a process for preparing same, and processes for biodegrading an aqueous waste stream containing organic contaminants utilizing the porous biosupports.

Description: POROUS POLYMERIC BIOSUPPORTS AND THEIR USE IN THE BIOTREATMENT OF AQUEOUS WASTE STREAMS This invention relates to porous polymeric biosupports. particularly porous nylon biosupports In one aspect, this invention relates to use of porous polymeric biosupports in processes for biodegradation of aqueous waste streams containing organic contaminants In another aspect, this invention relates to use of porous polymeric biosupports in packed bed and fluidized bed reactors for biotreatment of aqueous waste streams In a further aspect, this invention relates to the process for preparing the porous polymeric biosupports Commercial utilization of immobilized bacteria technology (IBT) for cost-effective biological treatment of chemical wastes has been increasing IBT utilizes highly selected, chemical- degrading bacteria in bioreactors designed to provide optimal conditions for microbial activity In IBT. biosupports are hosts for the bacteria which degrade toxic or polluting chemicals in waste streams into environmentally harmless products This is usually done by flowing the waste stream through a reactor vessel containing the bacteria on a biosupport media Chemical degrading bacteria immobilized in bioreactors have been shown to achieve exceptional performance for the biotreatment of chemical industry wastes Use of IBT in fluidized bed reactors (FBRs) and packed bed reactors (PBRs) achieve high rates of chemical removal, tolerate harsh conditions, survive dormancy, tolerate surge loadings, and produce lower levels of biological solids than conventional waste treatment technologies The biosupports which are typically used in commercial scale bioreactors are predominantly sand, granular activated carbon (GAC) particles and porous inorganic particles such as diatomaceous earth, alumina oxide and sintered glass Although these biosupports. also known as biocamers. are commercially available and have been well-proven as supports for chemical-degrading bacteπa. they all have some disadvantages The GAC and inorganic biosupports are expensive and experience attrition of 5-20 % per year In addition, the removal of excess biomass from these biosupports is problematic since their high density and fragility make vigorous back-flushing or mechanical biomass separation difficult Sand is affordable and non-fragile, but requires a significantly longer period of time for microbial colonization (slower startup) and lacks the advantage of chemical adsoφtion as a supplementary removal mechanism. In addition, microorganisms on sand are more prone to performance failure and slow recovery after physical or chemical upsets Lodaya et al (U.S. Patent No. 5.403.487) has disclosed the use of microporous synthetic resinous materials, including nylon, as biosupports for use in treating aqueous waste streams in aerated packed bed reactors. The microporous synthetic resinous materials of Lodaya et al have a density less than the density of water, i.e. float in the reactor, and therefore require a screen to hold the resin particles in place. The density of the microporous synthetic resinous materials of Lodaya et ai creates the significant problem of not being able to handle biofouiing and biomass control in the packed bed reactor. The packed bed reactor of Lodaya et al also requires use of a recycle stream. In addition, the microporous synthetic resinous materials of Lodaya et al cannot be used in fluidized bed reactors because they float. A biosupport material which solves the problems ofthe commercially available biosuppoπs and of materials such as those disclosed in Lodaya et al would be highly desirable. It has now been found that the porous polymeric biosuppoπs of the invention solve the above-described problems. Specifically, the porous polymeric biosupports ofthe invention have the following advantages: ( 1 ) high porosity permitting rapid and heavy colonization by inoculated bacteria. (2) large pore sizes and open structure promoting higher levels of microorganism growth inside the biosupport and resulting in greater tolerance to upsets, less biomass loss during fluidization and higher overall performance. (3) high physical strength eliminating attrition. (4) inert to most chemicals and waste streams, (5) density slightly greater than the density of water eliminating the problems of Lodaya et al and permitting simple, cost- effective fluidization by air injection to control biomass in PBRs. (6) high rigidity providing good abrasion of excess biomass during fluidization. (7) chemical biodegradation rates equal to or exceeding commercially available biosupports. and (8) production process allowing flexibility in size, density, porosity and composition of the biosupports. The porous polymeric biosupports of the invention also have the advantage of utilizing waste polymer or recycle polymer as feedstock. This utilization of waste or recycle polymer is an environmentally friendly process resulting in waste recycling and reduction. It is an object ofthe invention to provide a porous polymeric biosupport having a density greater than the density of water and open pores of sufficient diameter to enable microorganisms to readily colonize within the pores. It is a further object ofthe invention to provide a porous polymeric biosupport which is essentially free from attrition during operation of a fluidized bed or packed bed bioreactor. It is yet a further object of the invention to provide a porous polymeric biosupport which is relatively inexpensive. It is still a further object of the invention to provide a porous polymeric biosupport to which can be incoφorated an adsorbent material for use as a supplementary removal -> mechanism to enhance biodegradation and maintain a high quality effluent, and fiber reinforcement for improved strength. According to the invention, a porous biosupport for the support of microorganisms which is used in the biotreatment of an aqueous waste stream is provided which comprises a polymeric material comprising a thermoplastic polymer and. optionally, fiber reinforcement, adsorbent material and/or inorganic filler, wherein the biosupport has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores. Further according to the invention, a process for biodegrading an aqueous waste stream containing organic contaminants is provided which comprises inoculating a bed of particles ofthe biosupport of the invention with an inoculum of a culture of microorganisms capable of biodegrading the organic contaminants and contacting the aqueous waste stream containing organic contaminants with the microorganisms on the biosupport for a sufficient time to degrade the organic contaminants. In one embodiment ofthe invention, the process is conducted in a packed bed reactor. In another embodiment of the invention, the process is conducted in a fluidized bed reactor. Still further according to the invention, a process for preparing the porous biosupport ofthe invention is provided which comprises extruding in a non-vented extruder a composition comprising a polymeric material comprising nylon and. optionally, fiber reinforcement and/or adsorbent material, wherein the composition being extruded has a moisture content of about 0. 1 - about 7 wt. %. and pelletizing the extrudate from the extruder. Fig. 1 is a plot of the incremental pore volume ( measured as incremental intrusion of mercury into pores of specific pore sizes at various pressures during mercury intrusion porosimetry analysis) versus pore diameter for porous nylon biosupport R533 of the invention (designated by solid squares) compared to two conventional biosuppoπs. i.e. diatomaceous eaπh beads (designated by solid triangles) and activated coconut carbon (designated by open squares). Each data point represents the pore volume for pores ranging in size from the plotted value down to the next lower plotted value. Fig. 2 is a plot ofthe biodegradation of p-nitrophenol at high chemical loading by Pseudomonas sp. PNP1 on R533 porous nylon biosuppoπ in a PBR. Fig. 3 is a plot of the biodegradation of p-nitrophenol at high flow rates by Pseudomonas sp. PNP1 on R533 porous nylon biosuppoπ in a 3.5 inch (8.9 cm ) inside diameter PBR. Fig. 4 is a plot of the biodegradation of p-nitrophenol at high flow rates by Pseudomonas sp. PNP1 on R533 porous nylon biosuppoπ in a 2.125 inch (5.4 cm) inside diameter PBR. Fig 5 A and 5B are longitudinal surface views of the R533 porous nylon biosuppoπ at two different magnifications Fig. 6A and 6B are longitudinal cross section views ofthe R533 porous nylon biosuppoπ at two different magnifications Fig 7 is an end view of the R533 porous nylon biosuppoπ A first embodiment of the invention relates to a porous biosuppoπ for the suppoπ of microorganisms for the biotreatment of an aqueous waste stream containing organic contaminants comprising (a) 40 - 100 wt % of a polymeric mateπal comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer. ethylene-vinyl alcohol copolymer, polysulfone, polyolefin. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral stvrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof, (b) 0 - 60 wt % of a fiber reinforcement, (c) 0 - 60 wt % of an adsorbent material, and (d) 0 - 40 wt % of an inorganic filler, wherein the sum ofthe amounts of fiber reinforcement, adsorbent material and inorganic filler in the biosuppoπ is 0 - 60 wt %. and the biosuppoπ has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores The preferred polymeπc materials for use in the biosuppoπ of the invention comprise a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer. polysulfone. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof because the polymers have specific gravities greater than 1 0 More preferred polymeric materials for use in the biosuppoπ ofthe invention comprise a polymer selected from the group consisting of nylon, thermoplastic polyester, and mixtures thereof because of the availability of recycle or waste material The most preferred polymer for use in the polymeric materials ofthe invention is nylon because of excellent results obtained therewith In addition to the polymer, the polymeric mateπal ofthe invention can also contain polymers other than those listed above and fillers, particularly inorganic fillers. When a polymer with a specific gravity less than 1.0, e.g a polyolefin, is used the polymeric material must contain other materials or the biosuppoπ must contain an adsorbent material, a fiber reinforcement and/or an inorganic filler such that the specific gravity of the polymeπc material is greater than 1 0 For example, if a polyolefin is used then either an additional polymer having a specific gravity greater than 1.0 or an adsorbent material, a fiber reinforcement and/or an inoreanic filler must also be used. Suitable nylon polymers for use in the biosuppoπ include any readily available type of nylon, paπicularly nylon 6, nylon 6.6. nylon 4.6. nylon 1 1. nylon 12. nylon 6.9. nylon 6.10 and blends or copolymers thereof. The currently preferred nylon polymers are nylon 6 and nylon 6,6 because of their cost and availability. Of paπicular interest for use in the biosuppoπs of the invention are waste nylon materials including, but not limited to. manufacturing wastes, off-spec product, and cuttings from the manufacture of nylon caφet. In addition, nylon for use in the invention can be derived from used nylon caφet which is obtained according to the process described in U.S. Patent No. 5.294,384. which is incoφorated by reference herein. The nylon derived from used caφet which is processed without separating the caφet into its component pans will also contain at least one polyolefin (derived from the backing), a styrene-butadiene rubber (SBR) (used as an adhesive) and. optionally, an inorganic filler. Nylon for use in the invention can also be derived from other recycled nylon products such as molded nylon objects which can be reprocessed. Such nylon products may contain fiber reinforcement and inorganic fillers. The use of waste or recycle nylon as the source of nylon in the biosuppoπs ofthe invention is an environmentally friendly utilization of waste material which would otherwise have to be disposed of, such as by landfill ing. Suitable thermoplastic polyesters for use in the biosuppoπ are readily available and include polymers described in the Encyclopedia of Polymer Science and Engineering, 2nd ed.. Vol. 12, pp. 1-75 and 217-256 ( 1988), which is incoφorated by reference herein. Paπicularly useful thermoplastic polyesters include polyethylene terephthalate (PET) and polybutylene terephthalate (PBT). In paπicular. waste or recycle PET and PBT. including material derived from used polyester caφet. are suitable sources of polyester material. The polyester derived from used caφet which is processed without separating the caφet into its component pans will also contain material derived from the backing, e.g. a polyolefin. an adhesive such as SBR and. optionally, an inorganic filler. The polyvinyl chloride for use in the biosuppoπ can be a homopolymer or it can be a copolymer of vinyl chloride and vinyl acetate which typically contains 85-97 % ofthe chloride monomer. The polyolefins for use in the biosuppon include homopolymers of ethylene and propylene, and copolymers of ethylene and propylene with another olefin, e.g. ethylene/propylene and ethylene/hexene copolymers. Used polypropylene caφet is a suitable source of polypropylene. The polypropylene derived from used caφet which is processed without separating the caφet into its component pans will also contain material derived from the backing, an adhesive such as SBR and, optionally, an inorganic filler. The polysulfones for use in the biosuppoπ are readily available and include polymers described in the Encvclopedia of Polvmer Science and Engineering. 2nd ed . Vol 13, pp. 196-21 1 (1988). which is incoφorated by reference herein The polysulfones for use in the biosuppoπs of the invention include polyethersulfones. The polycarbonates for use in the biosuppoπ are readily available and include polymers described in the Encvclopedia of Polvmer Science and Engineering. 2nd ed . Vol 1 1 , pp. 648-718 (1988), which is incoφorated by reference herein The polyimides for use in the biosuppoπ are readily available and include polymers descπbed in the Encvclopedia of Polvmer Science and Engineering. 2nd ed . Vol 12, pp. 364-383 ( 1988). which is incoφorated by reference herein The polyimides for use in the biosuppoπs of the invention include polyetheπmides The poiyetheretherketones for use in the biosuppoπ are readiK available and include polymers described in the Encvclopedia of Polvmer Science and Engineering, 2nd ed . Vol 12, pp 313- 320 ( 1988), which is incoφorated by reference herein Suitable polyphenylene sulfide for use in the biosuppoπ are readily available and include polymers descπbed in the Encvclopedia of Polvmer Science and Engineering, 2nd ed.. Vol 1 1 , pp 531- 557 (1988), which is incoφorated by reference herein The cellulose ester plastics for use in the biosuppoπ are readily available and include polymers descπbed in the Encvclopedia of Polvmer Science and Engineering. 2nd ed.. Vol 3. pp 181- 200 ( 1988). which is incoφorated by reference herein PanicularK useful cellulose ester plastics are cellulose acetate, cellulose acetate butvrate and cellulose acetate propionate The polyvinyl butyral mateπals for use in the biosuppoπ are commercially available and have a hydroxyl content expressed as percent poly (vinyl alcohol) of up to 20 % The ethylene-vinyl acetate and ethylene-vinyl alcohol copolymers for use in the biosuppoπs of the invention are commercially available Styrenic polymers, as used herein, include polystyrene, rubber-modified polystyrene or high impact polystyrene (HIPS), acrylonitπle-styrene copolymers (SAN), rubber-modified acrylonitπle- styrene copolymers (ABS). styrene-maleic anhydride copolymers (SMA), styrene-methyl methacrylate copolymers. and acrylate-styrene-acrylonitπle copolymers (ASA) The styrenic polymers for use in the biosuppoπ are readily available and include polymers descπbed in the Encvclopedia of Polvmer Science and Engineering, 2nd ά.. Vol 16, pp 62-97. and Vol 1, pp 388-426 and 452-464 (1988), which are incoφorated by reference herein. Suitable polyurethane materials for use in the biosuppoπ are commercially available and are rigid, thermoplastic materials that are capable of producing open-cell structures. Suitable inorganic fillers for use in the biosupports of the invention include carbonates such as calcium carbonate and barium carbonate, silicates such as clay (kaolin), calcium silicate, mica, talc and wollastonite. sulfates such as calcium sulfate and barium sulfate. and oxides such as silicon dioxide and titanium dioxide. The currently preferred fillers are calcium carbonate, calcium sulfate. kaolin, mica, talc and wollastonite. The amount of polymeric material present in the biosuppoπs of the invention is broadly 40 to 100 wt. % ofthe biosupport. The preferred biosupports of the invention contain 40 to about 80 wt. % polymeric material with the remainder being fiber reinforcement, adsorbent material and/or inorganic filler. It is more preferred that the biosupports of the invention contain at least some fiber reinforcement to improve the physical strength of the biosupport. It is currently preferred that the polymeric material consist essentially of nylon. If the polymeric material contains other components, the amount of nylon present is about 35 to about 95 wt. %, preferably about 40 to about 85 wi %. of the polymeric material. When the source of nylon is used caφet. which typically contains an inorganic filler in the SBR adhesive used, the polymeric material comprises 35 to 67 wt. % nylon. 8 to 21 wt. % polyolefin. 5 to 29 wt. % SBR and 10 to 40 wt. % inorganic filler. The fiber reinforcement for use in the biosupports of the invention are fibers selected from the group consisting of glass, carbon, aramid. fiber-forming inorganic material selected from alumina, silica, boron, boron nitride, boron carbide, silicon carbide or alumino-silicate. and mixtures thereof. The currently preferred fiber reinforcement is glass fiber or carbon fiber due to cost, performance and availability, with glass fiber being most preferred. The preferred form of the fiber reinforcement is chopped fibers. The adsorbent material for use in the biosuppoπs of the invention are selected from the group consisting of carbon (including charcoal, activated carbon, graphite and carbon black), ion exchange resins, zeolites and mixtures thereof. The currently preferred adsorbent material is carbon, specifically charcoal or activated carbon. The amount of fiber reinforcement present in the biosuppoπs of the invention is broadly 0 to 60 wt. % of the biosuppoπ, preferably about 5 to about 50 wt. %. and most preferably about 15 to about 40 wt. %. The amount of adsorbent material present in the biosuppoπs of the invention is broadly 0 to 60 wt. % ofthe biosuppoπ. preferably about 2 to about 50 wt. %. and more preferably about 3 to about 30 wt. %. The amount of inorganic filler present in the biosuppons of the invention is broadly 0 to 40 wt. % of the biosuppoπ, preferably about 5 to about 30 wt. %. and more preferably about 10 to about 25 wt. %. The total amount of fiber reinforcement, adsorbent material and inorganic filler in the biosuppoπs of the invention shall not exceed 60 wt. %. The polymeric material of the biosuppoπs ofthe invention can further comprise a polymeric additive material wherein the additive material contains one or more of fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the primary polymeric material of the biosupport. Examples of plastic or rubber materials which can be present in the polymeric additive material but which are not suitable as the primary polymeric material ofthe biosupport include polybutadiene and rubbery copolymers thereof, e.g. styrene-butadiene rubber (SBR). acrylic polymers, polyphenylene oxide-based resins (PPO). and fiberglass reinforced plastics, paπicularly material recycled from automobiles, which contain, for example, crosslinked polyesters. A paπicularly suitable source of a rubbery polymeric additive is recycled used tires. Used tires contain, in addition to a rubber material such as SBR, materials including carbon black, fiber reinforcement, and polyester fibers. The polymeric additive material optionally contains other additives such as antioxidants, stabilizers, coupling agents, etc. which are not classified as fiber reinforcement, adsorbent material or inorganic fillers. The percentage of plastic or rubber material present in the polymeric additive will determine the level of polymer additive which can be incoφorated into the biosuppoπ. The upper limit of the amount of polymeric additive is that amount above which will cause problems in production of the biosuppoπ and will depend on the specific plastic or rubber material and its rheological and other peπinent propeπies. Generally, the upper limit will be that amount in which the amount of plastic or rubber material plus the amount of any additives other than fiber reinforcement, adsorbent material and inorganic filler present is up to about 30 wt. %. preferably up to about 15 wt. %. and more preferably about 10 wt. % ofthe biosupport. Acrylic polymers, as used herein, include poly(methylmethacryiate), rubber-modified poly(methylmethacrylate). poly(methylacrylate), poly(ethylacrylate). poly(butylacrylate) and poly(ethylmethacrylate). Polyphenylene oxide-based resins, paπicularly blends of polyphenylene oxide with impact polystyrene, such as HIPS, are readily available. The polymeric materials or polymeric additive materials utilized in the biosuppoπs of the invention cannot contain an amount of any stabilizer, antioxidant. etc. which when incoφorated in the biosuppoπ would prevent the biosuppoπ from being innoculated or from supponing microorganisms when used in immobilized bioreactors. The biosuppoπs ofthe invention are substantially open-cell materials, i.e. having open pores, and have a specific gravity greater than the specific gravity of water. The specific gravity ofthe biosuppoπ has to be great enough that inoculated biosuppoπ particles are not buoyant in the immobilized bacteria bioreactor during normal operation or during aeration or fluidization used for biomass control. Preferably, the specific gravity ofthe biosupports of the invention is greater than 1.1. The specific gravity ofthe biosupport can be readily controlled by varying the composition ofthe biosuppoπ. i.e. the type and amount of polymeric material, fiber reinforcement and adsorbent material, and the process conditions under which the biosuppoπs are extruded, e.g. concentration of water or foaming agent. The specific gravity of the biosuppoπs of the invention enable the biosupports to be utilized in both fluidized bed and packed bed reactors. In FBRs. the specific gravity of the biosupport panicles enables the biosupport particles to be fluidized during operation. In PBRs. the specific gravity of the biosupport particles enables the biosupport particles to be sufficiently mixed for biomass control in the reactor using air injection. The specific gravity ofthe biosupports of the invention is controlled such that the specific gravity is less than the specific gravity at which it is no longer practical to fluidize or sufficiently mix a bed of the biosupport particles. It is currently preferred that the specific gravity of the biosupport particles is below about 3. more preferably below about 2. The biosupports of the invention have pores of sufficient diameter to enable microorganisms to colonize within the pores. Typical microorganisms have a diameter or thickness of 0.5 - 5 μm. such as about I - 2 μm. and a length of 2 - 4 μm. Therefore, biosupports having pore sizes larger than the size of the microorganisms are particularly useful. Generally, microorganisms require a pore diameter of at least 4 μm to have access to the pore. The biosupports of the invention were analyzed to determine pore sizes using mercury intrusion porosimetry and scanning electron microscopy. Mercury intrusion porosimetry is used to determine pore sizes in the range of 1 μm to about 390 μm. Scanning electron microscopy is used to qualitatively determine pore sizes of greater than 390 μm. It is clear from analyzing the micrographs (see Example 6) that the biosupports of the invention can be produced with external pore sizes, i.e. pore openings, of up to 700 μm and internal openings of up to 3.9 mm in length. The biosupports of the invention are particularly useful because they have external pores within the range of 1 μm to about 700 μm, preferably within the range of 1 μm to about 420 μm. and internal openings typically of up to about 800 to about 1200 μm in length. As the range of pore sizes is used herein. the biosuppoπs ofthe invention can have pores that are smaller than 1 μm and larger than those set forth above. For pore sizes between 1 μm and 390 μm. the biosupports ofthe invention have a median pore diameter (based on volume) of at least about 40 μm. preferably at least about 50 μm, and most preferably at least about 70 μm. The actual median pore diameter of the biosupports ofthe invention will typically be larger due to the number of pores of diameter greater than 390 μm. The biosupports of the invention can also be characterized via the cumulative pore volume and cumulative pore area. The cumulative pore volume or pore volume (for pore sizes greater than about 1 μm and up to 390 μm) of the biosupport particles is preferably at least 0.2. more preferably at least about 0.3. and even more preferably about 0.3 to about 1.0. mL/g biosupport. The cumulative pore area or pore area (for pore sizes greater than about 1 μm and up to 390 μm) of the biosupport particles is preferably at least 0.025. more preferably at least 0.03. m " /g biosupport. As with the pore diameter, the actual cumulative pore volume and cumulative pore area will typically be larger due to the number of pores of diameter greater than 390 μm. A second embodiment ofthe invention relates to a process for biodegrading an aqueous waste stream containing organic contaminants comprising inoculating a bed of particles of a biosupport with an inoculum of a culture of microorganisms capable of aerobically biodegrading the organic contaminants, and contacting the aqueous waste stream containing organic contaminants with the microorganisms on the biosupport for a sufficient time to degrade the organic contaminants: wherein the biosupport is as defined above. The biodegradation process can be conducted in any suitable immobilized bacteria bioreactor. particularly a fluidized bed or packed bed reactor. Suitable immobilized bacteria bioreactors also include in-situ biotreatment zones useful in m-situ bioremediation processes. An example of such an tn-sttu bioremediation process is described in U.S. Patent No. 5.398.756. which is incoφorated herein by reference. The biodegradation can be conducted aerobically or anaerobically depending on the specific organic contaminants and the microorganisms selected. It is currently preferred that the process be conducted aerobically due to applicability of aerobic biodegradation to a wide variety of organic contaminants. A third embodiment of the invention relates to a process for treatment of an aqueous waste stream containing organic contaminants comprising passing the aqueous waste stream through a packed bed reactor, the packed bed reactor containing a packed bed of biosupport particles supporting microorganisms capable of biodegrading the organic contaminants, by a process in which the aqueous waste stream is oxygenated by introducing oxygen into the feed end of the packed bed reactor, thereby to subject the organic contaminants in the oxygenated aqueous waste stream to aerobic biodegradation and to produce a purified aqueous effluent: wherein the biosupport is as defined above. The process can be conducted in conventional immobilized bacteria packed bed reactors which are well known to those skilled in the art. such as the one described in Heitkamp et al. "Biodegradation of p-Nitrophenol in an Aqueous Waste Stream by Immobilized Bacteria " , Appl. Environ. Microbiol., October 1990. pp. 2967-2973. which is incoφorated by reference herein. A fourth embodiment of the invention relates to a process for treatment of an aqueous waste stream containing organic contaminants comprising passing the aqueous waste stream through a fluidized bed reactor, the fluidized bed reactor including a recycle line and containing a fluidized bed of biosupport particles supporting microorganisms capable of biodegrading the organic contaminants, by a process in which the feed to the fluidized bed reactor is oxygenated, thereb to subject the organic contaminants in the oxygenated feed to aerobic biodegradation and to produce a purified aqueous effluent, wherein the feed to the fluidized bed reactor comprises a recycle stream of a poπion of the effluent and the aqueous waste stream and the feed is oxygenated by dissolving oxygen in the recycle stream, the aqueous waste stream or the feed to the fluidized bed reactor at a point external to the fluidized bed: wherein the biosuppoπ is as defined above. The process can be conducted in conventional immobilized bacteria fluidized bed reactors which are well known to those skilled in the an. such as the one described in Edwards et al. "Laboratory-scale evaluation of aerobic fluidized reactors for the biotreatment of a synthetic, high- strength chemical industry waste stream " . Water Environ. Res.. Vol. 66. No. I . pp. 70-83 (January/February 1994) and U.S. Patent No. 5.540.840 which issued July 30. 1996. both of which are incoφorated by reference herein. A fifth embodiment of the invention relates to a process for preparing the porous biosuppoπ of the invention comprising extruding in a non-vented extruder a composition comprising: (a) 40 - 100 wt. % of a polymeric material comprising nylon. (b) 0 - 60 wt. % of a fiber reinforcement. (c) 0 - 60 wt. % of an adsorbent material, and (d) 0 - 40 wt. % of an inorganic filler, the sum ofthe amounts of fiber reinforcement, adsorbent material and inorganic filler in the biosuppoπ is 0 - 60 wt. %. in the presence of about 0.2 to about 5 wt. % (based on the weight of the total composition) of water, a foaming agent or mixtures thereof, and pelletizing the extrudate from the extruder: wherein the biosupport has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores. Water and/or the foaming agent present in the composition being extruded is broadly about 0 1 to about 7. preferably about 0 1 to about 5. more preferably about 0 1 to about 2. and most preferably about 0 2 to about 1 , wt % based on the weight of the total composition being extruded The compound present in the composition being extruded which causes foaming and results in formation of the porous biosupport is water, a foaming agent or a mixture of water and a foaming agent Water and/or foaming agent added to the composition being extruded is selected to achieve the desired porosity and pore size distribution for the biosupport being produced and will depend on the particular polymeπc mateπal being extruded The selection of water and/or foaming agent to achieve the desired amount of vapor production or foaming in the extruder will be readily apparent to those of ordinary skill in the art The currently preferred mateπal for use in production of the porous biosupports of the invention is water due to its effectiveness and economics Foaming agents, or blowing agents, are converted to gas during processing, i e extrusion, and the gas thus evolved creates the porous structure in the biosupport This structure is influenced by the type and amount of foaming agent selected, the type of gas evolved and its solubility .the method of compounding/extrusion used, temperatures and pressures involved in processing, and the melt viscosity of the mateπal being extruded In the extrusion process for preparing the porous biosuppoπs of the invention, water functions as a foaming agent Examples of suitable foaming agents include, but are not limited to. fluorinated aliphatic hydrocarbons such as chlorofluorocarbons. 1.1-azobιsformamιde (ABFA), p.p -oxybιs(benzenesulfon l hydrazide) (OBSH). p-toluene sulfony I semicarbazide (TSSC). tπhydrazine triazine (THT). 5- phenyltetrazole (5-PT). sodium bicarbonate and mixtures thereol The composition to be extruded is prepared by mixing or blending the composition in any conventional polymer compounding blender The temperature and pressure used in the extruder will depend on the pamcular material being extruded and will be readily apparent to those of ordinary skill in the art In addition, the type and size of extruder used will be readily apparent to those of ordinary skill m the art A single screw extruder is currently preferred The biosupport pellets produced can have any size and shape such as will allow them to be randomly packed in a packed bed reactor or fluidized in a fluidized bed reactor The cross-section ofthe biosupport pellets w ill have the shape of the particular die used during extrusion, e.g circular. rectangular, square, etc The length of the biosupport pellets is determined by how the extrudate is cut or chopped The biosupport pellets preferably have an effective diameter and or length such that the pellets have a desired size of greater than a No 10 Sιeve (U S A Sieve Seπes-ASTM E-l 1-70, 2 0 mm), preferably greater than a No. 7 Sieve (U.S. A. Sieve Series-ASTM E- l 1-70, 2.8 mm). The maximum size ofthe biosupport pellets is that size which is no longer capable of being adequately fluidized or mixed in a bioreactor or which have a particle surface area to pore area ratio such that the pores are ineffective in enhancing the biodegradation in the bioreactor. A typical shape for the biosupports of the invention is cylindrical. For example, a typical extruded porous biosupport ofthe invention will have a cylindrical shape with a diameter of about 0.25 - about 1.3 cm, preferably about 0.25 - about 0.6 cm. and a length of about 0.6 cm - about 1.3 cm. EXAMPLES The chemicals used in the examples are as follows. p-Nitrophenol (PNP) having a purity >99% was obtained from Aldrich Chemical Co. (Milwaukee. WI). Standard plate count (SPC) agar and plating agar was obtained from Difco Laboratories (Detroit. MI). Yeast extract was obtained from Sigma Chemical Company (St. Louis. MO). Trypticase Soy Agar was obtained from Becton Dickinson and Company (Cockeysville. MD). Inorganic chemicals were purchased from Fisher Scientific (Fair Lawn, NJ). Nylon was obtained from Monsanto Company. Diatomaceous earth (type R635) was obtained from the Manville Company. Activated coconut carbon was obtained from Charcoal Filtration Co. (Ingiewood. CA). PNP concentrations were determined spectrophotometrically by measuring optical absorbance at 414 nm. A linear relationship was observed between PNP absorbance and concentrations of PNP ranging from 0.5 to 35 mg/L. The pH of samples and standards was adjusted to above 8.0 using identical volumes of concentrated sodium hydroxide (2.5 N) in order to assure complete chromophore formation by the PNP. The absorbance of samples and standards was measured in 96-well microtiter plates using a Titertek Multiskan MCC/340 automatic plate reader (Flow Laboratories. Mclean. VA). Effluent samples were collected with a pipette from each column and filtered through a 0.45 μm Acrodisc 25 syringe filter (Gelman Sciences. Ann Arbor. MI) prior to chemical analysis. Porosity analyses were conducted as follows. Pore size distribution for the porous biosuppoπs was determined by mercury intrusion porosimetry. Samples were placed into a penetrometer test cell which was then evacuated and filled with mercury. The diameter of the pores was calculated from the pressure required to force mercury into the porous biosuppoπ panicles. This pore diameter calculation assumes a circular cross-section for the pores. The samples were analyzed over the full instrument range, 0.46 psia (390 μm diameter) to 60.000 psia (30 Angstrom diameter). Scanning electron micrographs were used to determine the presence of pore sizes greater than 390 μm. Samples for scanning electron microscopy (SEM) were rinsed in a buffered solution (0.1 M sodium cacodylate, pH=7.4). fixed in 2% glutaraldehyde and stored in a refrigerator until analyzed. The fixed samples were warmed to room temperature, rinsed in the sodium cacodylate buffer solution and fixed in buffered 2% osmium tetroxide for one hour The samples were then rinsed in the sodium cacodylate buffer solution, dehydrated using an ethanol seπes (50%. 70%. 80%. 90%. 95% and 100%) and critical point dried using liquid carbon dioxide. The dried samples were placed onto Al SEM mounts with double stick tape and coated with Au/Pd using the Polaron E5100 Coating Unit for electron beam conductivity The SEM analyses and micrographs were obtained using a JEOL 840 scanning electron microscope Example 1 The following porous biosuppoπs have been prepared according to the process ofthe invention A porous biosuppoπ designated R533 was prepared b\ blending a composition containing 67 wt % nylon 6.6 (Vydyne®21 of Monsanto Company) and 33 wt % chopped glass fibers ( 1/8 2 (0.32 cm) length. Certa teed 93B Fiberglass) using a twin-shell cone blender The nylon had a moisture content of 0 3 - 0 5 wt %. i e contained 0 3 - 0 5 wt % water The blend was compounded using a 1 5 : (3 8 cm) diameter. 24/1 L/D non-vented extruder at a temperature of about 285 °C (extruder barrel temperatures were set on a decreasing profile of 295-280 °C) The extrudate was quenched in a water bath and pelletized A porous biosuppoπ designated 740FG was prepared according to the method used to prepare biosuppoπ R533 except the nylon was a nylon 6.6 crumb containing finish oils and the extruder was a 1 5- (3 8 cm) diameter. 24/1 L/D non-vented single screw extruder The nylon 6.6 crumb was produced by chopping nylon 6.6 fibers (Monsanto Company) into 1/16 - 1/8 inch (0 16 - 0 32 cm) lengths and passing through a Pallman densifier (Plas-Aglomerator) In this process, the nylon fibers were fused together via frictional heat and passed through a die to obtain the final crumb product A porous biosuppoπ designated 744FG was prepared according to the method used to prepare biosuppoπ 740FG except the nylon was a ny lon 6.6 crumb ithout finish oils Biosuppoπs R533, 740FG and 744FG were analyzed using mercury intrusion porosimetry to determine pore size distribution In addition, the consolidated bulk density of the biosuppoπs was determined The results are set foπh in Table I In addition, a 12 2 (30 5 cm) packed bed of biosupport R533 submerged in water was completely fluidized by air injection into the bottom of a 3 5 2 (8 9 cm) ID column indicating that periodic fluidization to remove excess microbial biomass could be done with air injection as opposed to more expensive and difficult hydraulic mixing and back-flushing Table I Cumulative Cumulative Mean Pore Bulk Pore Volume Pore Area Pore Dia a Range 3 Density BIOSUDDOΠ mL/ε m-/g um um lb/ft 3 R533 0 5 0.036 83.5 3-390 20.2 740 FG 0.38 0.030 72.2 2-390 22. 744 FG 0.29 0.030 59 1 1 -390 24. a As determined by mercury intrusion porosimetry where maximum pore size measurable is 390 μm. Example 2 The following additional porous biosuppoπs have been prepared according to the process of the invention. A porous biosupport designated R400G was prepared by blending calcined clay (Englehard Coφ.. Satintone #5) and a nylon 6/6.6 random copolymer (Monsanto Company. 10.5 wt. % nylon 6 and 89.5 wt. % nylon 6,6). This blend was compounded by high intensity mixing in a Farrel Continuous Mixer. This mineral reinforced product was then blended ith chopped glass fibers (described in Example 1 ) using a twin-shell cone blender (63.5 wi. % nylon. 20 wt % clay and 16.5 wi. % glass fiber). The nylon contained 0 9 wt % water. The blend was compounded using a l .5 ; (3.8 cm). 24/1 IJD non-vented single screw extruder at a temperature of 285 °C The extrudate was quenched in a water bath and pelletized. A porous biosupport designated R400G-01 was prepared according to the method used for biosupport R400G except the composition also contained 0.2 wt % carbon black (the carbon black was charged by adding 0 6 wi % of a prepared carbon black concentrate containing 34 wi % Cabot XC-72 carbon black in nylon 6 obtained from Custom Resins Incoφorated (CRJ ) A 12 2 (30.5 cm) packed bed of porous biosupports R400G and R400G-01 were each submerged in water in the bottom of a 3.5 : (8 9 cm) ID column and fluidization with air attempted. Neither the R400G bed nor the R400G-01 bed was fluidized or mixed at the air injection rate which completely mixed the R533 biosupport Low magnification light microscopy ofthe samples indicated that while R400G and R400G-01 were porous. R533 was more porous than either R400G or R400G-01. It is expected that R400G and R400G-01 could be fluidized at a higher air injection rate than that used for R533. Example 3 The following additional porous biosupports containing fiber reinforcement and adsorbent material were prepared according to the process of the invention A porous biosuppoπ designated T-4198 was prepared from nylon 6.6 crumb (Example 1 ) and 3 wi % carbon black with 25 wt % glass fiber reinforcement. A blend of 25 wt % chopped glass fiber ( l/8 2 (0.32 cm) length). 8 9 wt % carbon black concentrate ( 34 wt % carbon black in nylon 6; same concentrate as described in Example 2). and 66 l wt . % nylon 6.6 crumb was prepared using a drum tumble blender The nylon had a water content of 0.5 - 1.0 wt %. The blend was compounded using a l 5 2 (3 8 cm) diameter. 24/1 L/D non-vented single screw extruder at a temperature of 285 °C The extrudate was quenched in a water bath and pelletized A porous biosuppoπ designated T-4202 was prepared from the carbon black concentrate with 25 wt % chopped glass fibers for reinforcement to yield 25 5 wt % carbon black in the final product A blend of 75 wt % carbon black concentrate ( 34 wt % carbon black in nylon 6. same concentrate as described in Example 2) and 25 wt. % chopped glass fiber ( l/8 2 (0.32 cm) length) was prepared using a rwin-shell cone blender The concentrate had a water content of 0 5 - l 0 wt % The blend was compounded using a I 5 : (3 8 cm) diameter. 24/1 L'D non-vented single screw extruder at a temperature of 285 °C. The extrudate was quenched in a water bath and pelletized Example 4 This example shows a comparison between porous nylon biosuppoπ R533 of the invention and two commercial biosuppoπs which are commonly used as suppoπs for immobilized bacteria in bioreactors. i.e. R635 diatomaceous eaπh beads from Manville Company and activated coconut carbon from Charcoal Filtration Co.. Mercury intrusion porosimetry analyses were conducted on each sample The R533 biosuppoπ had a mean pore diameter of 83.5 μm while the R635 diatomaceous eaπh and activated coconut carbon biosuppoπs had mean pore diameters of 12.9 μm and 0 1 13 μm. respectively Incremental intrusion (measured in μL of pore volume per gram of biosuppoπ) was plotted vs pore diameter for the three samples (Fig 1 ) Fig 1 clearly shows the significant differences between the R533 porous biosuppoπ of the invention and the R635 diatomaceous eaπh and activated coconut carbon biosuppons The R533 biosupport contains a significantly greater number of pores with pore diameter greater than 50 μm indicating that the porous biosupports of the invention should result in faster startup after inoculation and higher overall performance for chemical biodegradation In addition, the open porosity ofthe porous biosupports of the invention should result in better penetration of chemical and oxygen into the interior ofthe particle resulting in higher overall levels of microbial activity in comparison to the conventional biosupports which have limited diffusion of chemical or oxygen. Example 5 This example demonstrates the effectiveness of R533 porous nylon pellets as a biosupport for Pseudomonas sp PNP1 in the biodegradation of PNP in a packed bed bioreactor. A Pseudomonas sp. strain PNP1 that had been isolated from municipal sludge (see Heitkamp et al. "Biodegradation of p-Nitrophenol in an Aqueous Waste Stream by Immobilized Bacteria", Appl. Environ. Microbiol., October 1990, pp. 2967-2973) was used as inoculum for the biosupports in these experiments. This Pseudomonas sp. is able to completely degrade PNP as a sole source of carbon and energy. A synthetic PNP waste stream (pH 7.8) consisting of half strength inorganic mineral salts (L- salts) containing PNP concentrations ranging from 100 to 1400 mg/L was pumped though the immobilized bacteria columns to determine the performance of immobilized bacteria for degrading PNP. The bench-scale PBRs in this study were 3.5 inch (8.9 cm) inside diameter x 24 inch (61 cm) long x 0.2 inch (0.5 cm) wall plexiglass columns. The columns used in the high-flow studies were 2.125 inch (5.4 cm) inside diameter x 24 inch (61 cm) long x 0.2 inch (0.5 cm ) wall plexiglass tubes. The bottom of each column was sealed by a rubber stopper and a wire screen located 2.5 inches above the base supported a 12 inch bed depth of biosupport in each column. An air stone was inserted through the rubber stopper at the base to provide continuous aeration of each column and air was introduced at a flow rate of 750 cc min for the 3.5 inch (8.9 cm) column and 300 cc/min for the 2.125 inch (5.4 cm) column. This aeration maintained oxygen saturation of liquid throughout the length of each column during the length of the experiment. The synthetic PNP waste stream was pumped into each column through a stainless steel tube located 1 inch (2.54 cm) above the bottom of the biosupport bed. The effluent from each column was discharged from a liquid headspace via a drain line positioned 2 inches (5.1 cm) above the top of the biosupport bed. The R533 porous nylon biosupport was inoculated with a moderately turbid culture of Pseudomonas sp. strain PNP1 grown in half-strength L-salts containing 100 mg/L PNP. The L-salts were prepared according to Leadbetter. E.R. and Foster. J.W.. "Studies on some methane utilizing bacteria " . Arch. Mikrobiol.. 30:9\ 1 18 ( 1958). The purity of this culture was checked by selective plating on L-salts agar containing PNP. plating on standard plate count (SPC) agar and by direct examination with light microscopy. The porous nylon biosuppoπ was inoculated by recycled pumping of a 1 liter turbid culture of Pseudomonas sp. strain PNP1 at 1 ml/min through the PBR bed for 24 hours with continuous aeration. Once microbial degradation of PNP was observed in the PBR. synthetic wastes were pumped continuously through the PBR. Metered liquid pumps from FMI coφoration (Model RHSY, Oyster Bay, NY) were used to feed synthetic wastes into the PBR at calibrated flow rates throughout the study. Chemical loading to the columns was increased by raising the concentration of PNP in the feedstock to approximately 1,400 mg L and increasing the feed rate to 2 mi/min. In the second phase of testing, the concentration of PNP was maintained at approximately 66 mg L. but the flow rates were increased until continuous breakthrough of PNP was observed in the PBR effluent. The biodegradation of PNP by Pseudomonas sp. PNP1 immobilized on R533 porous nylon pellets in the 3.5 inch (9.8 cm) PBR at increasing chemical loadings is shown in Fig. 2. The chemical loading of PNP (mg/h) into the PBR was raised by first increasing the concentration of PNP in the synthetic media from 400 mg/L to 1200 mg L during the first 7 days of the experiment. Fuπher increases in PNP loading were accomplished by step-wise increases in the feed flow rate from 3 ml/min up to 10 ml/min during days 15-25. Since significant levels of microbial biomass were observed on the porous nylon biosuppoπ during the second week of operation, the packed bed was fluidized by vigorous air injection on day 19. This fluidization caused the release of the excess biomass into the PBR effluent and resulted in very little observable excess biomass in the PBR after fluidization. Therefore, the packed bed was fluidized approximately every other day throughout the remainder ofthe experiment to prevent liquid channeling or the loss of reactor volume due to accumulation of excess biomass in the PBR. The biodegradation of PNP by immobilized bacteria in the PBR showed a pattem of 15-25% breakthrough of undegraded PNP within 24 h after each step increase in chemical loading. Characteristically, the PBR would regain a high rate of PNP biodegradation within the next 24-48 hours. Presumably, this recovery resulted from fuπher growth of bacteria into the biosuppoπ in the PBR in response to each increase in chemical loading. However, consistent breakthrough of undegraded PNP was observed in the PBR effluent after day 33 when PNP loading was increased shaφly from 657 mg/hr to 787 mg hr. The removal of PNP dropped initially to 86% and recovered to 91 -96% removal over the next 10 days (days 35-44) as PNP loading averaged 736 mg hr. The performance of the PBR unexpectedly dropped to 74-77% removal on days 46-47. Since chemical loading had not increased in this time frame, the PBR did not contain excess biomass and no operational problems were evident, it was presumed that the immobilized bacteria were stressed by a lack of micronutrients or trace elements due to long exposure to synthetic feed containing only inorganic macronutrients and PNP. The addition of 5 mg L of yeast extract, a common source of micronutrients and trace elements, restored performance. Throughout the remainder ofthe experiment the synthetic feed was supplemented with 5- 10 mg/L of yeast extract to eliminate micronutrient limitation as an experimental variable. The PBR averaged 91% PNP removal during the eleven day period from days 52-62 when PNP loading averaged 707 mg/hr and 95.3% PNP removal from days 74-96 (22 days) when PNP loading averaged 532 mg/hr. The performance of bacteria immobilized on R533 porous nylon pellets were also evaluated for high-flow applications. The concentration of PNP in the synthetic feed was dropped to approximately 40 mg/L and the flow was increased stepwise through the PBR until consistent breakthrough of undegraded PNP was observed in the effluent (Fig. 3). However, flow rates as high as 40 ml/min failed to result in any detectable discharge of undegraded PNP. Since higher flow rates were impractical in the laboratory due to the high volume of feed required, a poπion ofthe porous nylon was transferred from the 3.5 inch (8.9 cm) inside diameter column to a column having a 2.125 inch (5.4 cm) inside diameter. This significantly lowered the volume of the PBR resulting in shoπer hydraulic residence times for the same flows tested in the larger column. The smaller PBR maintained near complete PNP removal at flow rates of 10. 20. 25 and 30 mls/min. but dropped to 51-69% removal at 40 ml/min on days 1 19-122 (Fig. 4) Table II shows a summary of the maximum chemical degradation rates for high chemical concentration and high liquid flow applications of Pseudomonas sp PNPl immobilized on porous nylon R533 biosuppoπ in the PBR. In both cases, the Pseudomonas sp PNPl immobilized on porous nylon R533 biosuppoπ removed >90 % of the PNP Table II Maximum Chemical Degradation Rates for Pseudomonas sp. PNPl immobilized on porous nylon R533 biosupport in the PBR Mean PNP a Hydraulic PNP PNP COD Concentration Residence Removal Removed Removed (me/L Time (mm) (%) (Ib/fV/dav) (lb/ft 3 /dav 40 12 >99 0.18 0.32 1200 130 90+ 0.37 0.66 p-Nitrophenol in synthetic L-salts medium. A sample of the biofilm from the biosuppoπ bed in the PBR at the conclusion ofthe chemical loading study was plated onto petri dishes containing SPC media and 2% agar. Bacterial isolates were selected from the SPC plates based upon observed differences in pigmentation, colony moφhology. cellular moφhology and gram reaction. The isolates were transferred to agar plates containing 100 mg L PNP. Isolates capable of degrading PNP were determined by observing clearing of the yellow PNP surrounding the colony The isolated bacteria were incubated for 24 hours on Trypticase Soy Agar prior to identification using a VITEK AMS microbial identification system (McDonnel Douglas Inc., St. Louis. MO) Cellular moφhology and gram stain were determined with an Axioskop light microscope (Zeiss. Federal Republic of Germany) One major bacterial moφhotype was isolated from the R533 porous nylon biosuppoπ at the conclusion of these experiments. This microorganism was identified as a Pseudomonas sp. by the VITEK AMS microbial identification system and was presumed to be the Pseudomonas sp. PNPl originally inoculated onto the porous nylon biosuppon. Example 6 The R533 porous nylon biosuppoπ produced according to the process ofthe invention was analyzed for the presence of macropores using scanning electron microscopy Micrographs ofthe R533 porous nylon biosuppon were taken in three views: longitudinal surface (Fig. 5), longitudinal cross section (Fig. 6). and end view (Fig. 7). The longitudinal surface view at 15 x magnification (Fig. 5A) shows the rough fibrous characteristics of the surface of the extruded porous nylon biosuppoπ. The surface structure appears rough and irregular in texture and numerous large openings provide for microbial penetration, attachment and growth. The longitudinal surface at 70 x magnification (Fig. 5B) more clearly shows the large openings in the surface of the fibrous polymer biosuppoπ. It is noteworthy that some large openings, ranging in size from 20-700 μM. are seen to extend from the longtidunal surface down into the interior ofthe porous biosuppon thus providing ready intemal access to inoculated bacteria. The longitudinal cross sectional view at 15 x magnification (Fig. 6A) shows that extremely large pore openings exist throughout the inside of the biosuppoπ running in parallel to the direction of extrusion It is notewoπhy that many of these cavities are 800- 1200 μM in length and some are as long as 3.9 mm. These cavities allow the existence of large populations of chemical-degrading bacteria within the biosuppoπ. Fuπhermore. the open structured matrix ofthe biosuppoπ eliminates growth limitations due to slow diffusion of nutrients or chemical into the biosuppoπ. The longitudinal cross section view at 50 x magnification (Fig. 6B) more clearly shows the size and shape of these large internal cavities The diameters of these long cavities range from 30-690 μM with most having a diameter of 95-295 μM. The end-view at 70 x magnification (Fig. 7) shows that the long cavities running through the porous biosuppon (as seen in Fig. 6A and 6B) exist as open channels and are accessed through openings in the cut end of he biosuppon. These openings are numerous across the end of the biosuppon and have diameters ranging from 40-415 μM providing ready access to inoculated bacteria. It is clear from these scanning electron microscopy analyses that the porous nylon biosuppoπ contains a high number of very large pore openings. Fuπhermore. these pore openings occur throughout the interior of the biosuppoπ and are accessible to microorganisms by openings through both the sides and cut ends ofthe biosuppon.

Claims: CLAIMS: 1. A composition for the biotreatment of an aqueous waste stream comprising microorganisms colonized within the pores of a porous biosuppoπ. said biosuppoπ comprising: (a) 40 - 100 wt. % of a polymeric material comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer, ethylene-vinyl alcohol copolymer, polysulfone. polyolefin. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof; (b) 0 - 60 wt. % of a fiber reinforcement: (c) 0 - 60 wt. % of an adsorbent material: and (d) 0 - 40 wt. % of an inorganic filler. wherein the sum of the amounts of fiber reinforcement, adsorbent material and inorganic filler in said biosuppoπ is 0 - 60 wt. %. and wherein said biosuppoπ has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores. 2. The composition of claim 1 wherein the pores of said biosuppoπ have a diameter in the range of 1 μm to about 700 μm. 3. The composition of claim 2 wherein said pores have a median diameter (based on volume) of at least about 40 μm for pore sizes in the range of 1 μm to 390 μm. '4. The composition of claim 3 wherein said pores have a volume of at least about 0.2 mlJg for pore sizes in the range of 1 μm to 390 μm. 5. The composition of claim I wherein said polymeric material comprises a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer, polysulfone. polyvinyl chloride, polycarbonate, polyimide, polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral, styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. The composition of claim 5 wherein said polymeric material comprises nylon. 7. The composition of claim 1 comprising about 5 to about 50 wt. % of a fiber reinforcement. 8. The composition of claim 7 comprising about 15 to about 40 wt. % of a fiber reinforcement. 9. The composition of claim 7 comprising about 2 to about 50 wt. % of an adsorbent material. 10. The composition of claim 1 comprising 40 to about 80 wt % of said polymeric material. 1 1. The composition of claim 7 comprising about 5 to about 30 wt. % of an inorganic filler. 12. The composition of claim 6 wherein said polymeric material fuπher comprises material selected from the group consisting of polyolefin. styrene-butadiene rubber, an inorganic filler and mixtures thereof. 13. The composition of claim 6 wherein said nylon is selected from the group consisting of nylon 6, nylon 6.6, nylon 4.6, nylon 1 1 , nylon 12. nylon 6.9, nylon 6.10. and blends or copolymers thereof. 14. The composition of claim 1 1 wherein said polymeric mateπal contains about 35 to about 95 wt % nylon. 15. The composition of claim 1 wherein said polymeric material consists essentially of nylon. 16. The composition of claim I wherein said fiber reinforcement is fibers selected from the group consisting of glass, carbon, aramid. fiber-forming inorganic material selected from alumina, silica, wollastonite. boron, boron nitride, boron carbide, silicon carbide or alumino-silicate. and mixtures thereof. 17. The composition of claim 16 wherein said fiber reinforcement is chopped fibers. 18. The composition of claim 16 wherein said fiber reinforcement is glass fiber or carbon fiber. 19 The composition of claim 1 wherein said adsorbent material is selected from the group consisting of carbon, ion exchange resins, zeolites and mixtures thereof 20 The composition of claim 19 wherein said adsorbent material is charcoal or activated carbon 21 A process for biodegrading an aqueous waste stream containing organic contaminants comprising inoculating a bed of panicles of a biosuppoπ with an inoculum of a culture of microorganisms capable of biodegrading said organic contaminants, and contacting said aqueous waste stream containing organic contaminants with the microorganisms on said biosuppoπ for a sufficient time to degrade said organic contaminants, wherein said biosuppoπ comprises (a) 40 - 100 wt % of a polymeπc material comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer. ethylene-vinyl alcohol copolymer. polysulfone, polyolefin. polyviny l chloride, polycarbonate, polyimide. polyetheretherketone. polyphenylene sulfide. cellulose ester plastics, polyvinyl burvral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. (b) 0 - 60 wt % of a fiber reinforcement. (c) 0 - 60 wt % of an adsorbent material, and (d) 0 - 40 wt % of an inorganic filler. wherein the sum of the amounts of fiber reinforcement, adsorbent material and inorganic filler in said biosuppoπ is 0 - 60 wt %. and wherein said biosuppoπ has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores 22 The process of Claim 1 wherein said biosuppoπ has pores hav ing a diameter in the range of 1 μm to about 700 μm 23 The process of Claim 22 wherein said biosuppoπ has pores having a median pore diameter (based on volume) of at least about 40 μm for pore sizes in the range of 1 μm to 390 μm 24 The process of Claim 23 wherein said biosuppoπ has pores having a pore volume of at least about 0 2 mL/g for pore sizes in the range of 1 μm to 390 μm 25 The process of Claim 21 wherein said polymeric material comprises a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer, polysulfone. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. 26. The process of Claim 25 wherein said polymeric material comprises nylon. 27. The process of Claim 21 wherein said biosuppoπ comprises about 5 to about 50 wt. % of a fiber reinforcement. 28. The process of Claim 27 wherein said biosuppoπ comprises about 2 to about 50 wt. % of an adsorbent material. 29. The process of Claim 27 comprising about 5 to about 30 wt % of an inorganic filler 30. The process of Claim 26 wherein said polymeric material in said biosuppoπ fuπher comprises material selected from the group consisting of polyolefin. styrene-butadiene rubber, an inorganic filler and mixtures thereof. 31. The process of Claim 30 wherein said polymeric material contains about 35 to about 95 wt. % nylon. 32. The process of Claim 21 wherein said polymeric material of said biosuppoπ consists essentially of nylon. 33. The process of Claim 26 wherein said nylon in said biosuppoπ is selected from the group consisting of nylon 6. nylon 6.6. nylon 4.6. nylon 1 1 , nylon 12. nylon 6.9, nylon 6.10, and blends or copolymers thereof. 34. A process for treatment of an aqueous waste stream containing organic contaminants comprising passing said aqueous waste stream through a packed bed reactor, the packed bed reactor containing a packed bed of biosuppoπ panicles suppoπing microorganisms capable of biodegrading said organic contaminants, by a process in which the aqueous waste stream is oxygenated by introducing oxygen into the feed end of the packed bed reactor, thereby to subject said organic contaminants in the oxygenated aqueous waste stream to aerobic biodegradation and to produce a purified aqueous effluent: wherein said biosuppoπ comprises: (a) 40 - 100 wt. % of a polymeric material comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer, ethylene-vinyl alcohol copolymer. polysulfone, polyolefin. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof: (b) 0 - 60 wt. % of a fiber reinforcement; (c) 0 - 60 wt. % of an adsorbent material: and (d) 0 - 40 wt. % of an inorganic filler, wherein the sum of the amounts of fiber reinforcement, adsorbent material and inorganic filler in said biosupport is 0 - 60 wt. %. and wherein said biosupport has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores. 35. The process of Claim 34 wherein said biosupport has pores having a diameter in the range of 1 μm to about 700 μm. 36. The process of Claim 35 wherein said biosupport has pores having a median pore diameter (based on volume) of at least about 40 μm for pore sizes in the range of 1 μm to 390 μm. 37. The process of Claim 35 wherein said biosupport has pores having a pore volume of at least about 0.2 mlJg for pore sizes in the range of 1 μm to 390 μm. 38. The process of Claim 34 wherein said polymeric material comprises a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer. polysulfone. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone. polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. 39. The process of Claim 38 wherein said polymeric material comprises nylon. 40. The process of Claim 34 wherein said biosupport comprises about 5 to about 50 wt. % of a fiber reinforcement. 41. The process of Claim 40 wherein said biosupport comprises about 2 to about 50 wt. % of an adsorbent material. 42. The process of Claim 40 comprising about 5 to about 30 wt. % of an inorganic filler. 43. The process of Claim 39 wherein said polymeric material in said biosupport further comprises material selected from the group consisting of polyolefin. styrene-butadiene rubber, an inorganic filler and mixtures thereof. 44. The process of Claim 43 wherein said polymeric material contains about 35 to about 95 wt. % nylon. 45. The process of Claim 34 wherein said polymeric material of said biosupport consists essentially of nylon. 46. The process of Claim 39 wherein said nylon in said biosupport is selected from the group consisting of nylon 6, nylon 6,6, nylon 4.6. nylon 1 1, nylon 12. nylon 6.9, nylon 6.10. and blends or copolymers thereof. 47. A process for treatment of an aqueous waste stream containing organic contaminants comprising passing said aqueous waste stream through a fluidized bed reactor, said fluidized bed reactor including a recycle line and containing a fluidized bed of biosupport particles supporting microorganisms capable of biodegrading said organic contaminants, by a process in which the feed to said fluidized bed reactor is oxygenated, thereby to subject said organic contaminants in the oxygenated feed to aerobic biodegradation and to produce a purified aqueous effluent, wherein said feed to said fluidized bed reactor comprises a recycle stream of a poπion of said effluent and said aqueous waste stream and said feed is oxygenated by dissolving oxygen in said recycle stream, said aqueous waste stream or said feed to the fluidized bed reactor at a point extemal to the fluidized bed; wherein said biosuppoπ comprises: (a) 40 - 100 wt. % of a polymeric material comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer. ethylene-vinyl alcohol copolymer. polysulfone, polyolefin. polyvinyl chloride, polycarbonate, polyimide, polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof; (b) 0 - 60 wt. % of a fiber reinforcement: (c) 0 - 60 wt. % of an adsorbent material: and (d) 0 - 40 wt. % of an inorganic filler, wherein the sum of the amounts of fiber reinforcement, adsorbent material and inorganic filler in said biosuppoπ is 0 - 60 wt. %. and wherein said biosuppoπ has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize within the pores. 5 48. The process of Claim 47 wherein said biosuppoπ has pores having a diameter in the range of 1 μm to about 700 μm. 49 The process of Claim 48 wherein said biosuppoπ has pores having a median pore diameter (based on volume) of at least about 40 μm for pore sizes in the range of 1 μm to 390 μm. io 50. The process of Claim 49 wherein said biosuppoπ has pores having a pore volume of at least about 0.2 mL/g for pore sizes in the range of 1 μm to 390 μm. 51. The process of Claim 47 wherein said polymeric material comprises a polymer selected from is the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer. polysulfone. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone. polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. 20 52. The process of Claim 51 wherein said polymeric material comprises nylon. 53. The process of Claim 47 wherein said biosuppoπ comprises about 5 to about 50 wi % of a fiber reinforcement. 25 54 The process of Claim 53 wherein said biosuppoπ comprises about 2 to about 50 wt % of an adsorbent material. 55. The process of Claim 53 comprising about 5 to about 30 wt % of an inorganic filler. 0 56. The process of Claim 52 wherein said polymeric material in said biosuppoπ fuπher comprises material selected from the group consisting of polyolefin. styrene-butadiene rubber, an inorganic filler and mixtures thereof. 57. The process of Claim 56 wherein said polymeπc mateπal contains about 35 to about 95 wt. % 5 nylon. 58. The process of Claim 47 wherein said polymeric material of said biosuppoπ consists essentially of nylon. 59. The process of Claim 52 wherein said nylon in said biosuppoπ is selected from the group consisting of nylon 6. nylon 6.6. nylon 4.6. nylon 1 1 , nylon 12. nylon 6.9, nylon 6.10. and blends or copolymers thereof. 60. The process of Claim 47 wherein said organic contaminants are organic nitrogen compounds and said effluent contains water, ammonia and carbon dioxide. 61 A process for preparing a porous biosuppoπ comprising extruding in a non-vented extruder a composition comprising: (a) 40 - 100 wt. % of a polymeric material comprising a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl acetate copolymer. ethylene-vinyl alcohol copolymer, polysulfone. polyolefin. polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone, polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral. styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. (b) 0 - 60 wt % of a fiber reinforcement; (c) 0 - 60 wt % of an adsorbent material: and (d) 0 - 40 wt % of an inorganic filler. wherein the sum of the amounts of fiber reinforcement, adsorbent material and inorganic filler in said biosuppoπ is 0 - 60 wi. %. in the presence of about 0 1 to about 7 wt % of water, a foaming agent or mixtures thereof, and pellettzing the extrudate from said extruder. wherein said biosuppoπ has a specific gravity greater than the specific gravity of water and pores of sufficient diameter to enable microorganisms to colonize withm the pores 62. The process of Claim 61 wherein the amount of water, foaming agent or mixture thereof present is about 0.1 to about 5 wt. %. 63. The process of Claim 61 wherein said biosupport has pores having a diameter in the range of 1 μm to about 700 μm. 64. The process of Claim 63 wherein said biosupport has pores having a median pore diameter (based on volume) of at least about 40 μm for pore sizes in the range of 1 μm to 390 μm. 65. The process of Claim 64 wherein said biosupport has pores having a pore volume of at least about 0.2 mL/g for pore sizes in the range of 1 μm to 390 μm. 66. The process of Claim 61 wherein said polymeric material comprises a polymer selected from the group consisting of nylon, thermoplastic polyester, ethylene-vinyl alcohol copolymer. polysulfone, polyvinyl chloride, polycarbonate, polyimide. polyetheretherketone. polyphenylene sulfide. cellulose ester plastics, polyvinyl butyral, styrenic polymers, rigid, thermoplastic polyurethanes. and mixtures thereof. 67. The process of Claim 66 wherein said polymeric material comprises nylon. 68. The process of Claim 61 wherein said biosupport comprises about 5 to about 50 wt. % of a fiber reinforcement. 69. The process of Claim 68 wherein said biosupport comprises about 2 to about 50 wt. % of an adsorbent material. 70. The process of Claim 68 comprising about 5 to about 30 wt. % of an inorganic filler. 71. The process of Claim 67 wherein said polymeric material in said biosupport further comprises material selected from the group consisting of polyolefin. styrene-butadiene rubber, an inorganic filler and mixtures thereof. 72. The process of Claim 71 wherein said polymeric material contains about 35 to about 95 wt. % nylon. 73. The process of Claim 61 wherein said polymeric material of said biosupport consists essentially of nylon. 74. The process of Claim 67 wherein said nylon in said biosupport is selected from the group consisting of nylon 6. nylon 6.6. nylon 4.6, nylon 1 1. nylon 12. nylon 6,9, nylon 6.10. and blends or copolymers thereof. 75. The process of Claim 61 wherein said foaming agent is fluorinated aliphatic hydrocarbons. 1,1 - azobisformamide, p,p * -oxybis-(benzenesulfonyl hydrazide), p-toluene sulfonyl semicarbazide. trihydrazine triazine. 5-phenyltetrazole. sodium bicarbonate and mixtures thereof. 76. The process of Claim 61 wherein said composition is extruded in the presence of water. 77. The process of Claim 61 wherein said composition further comprises an amount of a polymeric additive material wherein said additive material contains one or more of said fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the polymeric material (a) of said composition and wherein the amount of said plastic or rubber material plus the amount of any additives other than said fiber reinforcement, adsorbent material and inorganic filler present in said composition is up to about 25 wt. %. 78. The biosupport of Claim 1 wherein said biosupport further comprises an amount of a polymeric additive material wherein said additive material contains one or more of said fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the polymeric material (a) of said biosupport and wherein the amount of said plastic or rubber material plus the amount of any additives other than said fiber reinforcement, adsorbent material and inorganic filler present in said biosupport is up to about 25 wt. %. 79. The process of Claim 21 wherein said biosuppoπ further comprises an amount of a polymeric additive material wherein said additive material contains one or more of said fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the polymeric material (a) of said biosuppoπ and wherein the amount of said plastic or rubber material plus the amount of any additives other than said fiber reinforcement, adsorbent material and inorganic filler present in said biosuppoπ is up to about 25 wt. %. 80. The process of Claim 34 wherein said biosupport further comprises an amount of a polymeric additive material wherein said additive material contains one or more of said fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the polymeric material (a) of said biosupport and wherein the amount of said plastic or rubber material plus the amount of any additives other than said fiber reinforcement, adsorbent material and inorganic filler present in said biosupport is up to about 25 wt. %. 81. The process of Claim 47 wherein said biosupport further comprises an amount of a polymeric additive material wherein said additive material contains one or more of said fiber reinforcement, adsorbent material, inorganic fillers, and polymeric material in addition to a plastic or rubber material not suitable as the polymeric material (a) of said biosupport and wherein the amount of said plastic or rubber material plus the amount of any additives other than said fiber reinforcement, adsorbent material and inorganic filler present in said biosupport is up to about 25 wt. %. 82. The process of claim 61 wherein the amount of water, foaming agent, or mixture thereof is about 0.1 to about 2 wt. %. 83. The process of claim 61 wherein the amount of water, foaming agent, or mixture thereof is about 0.2 to about 1 wt.%.

Inventors: HEITKAMP MICHAEL A, STOW GEORGE C, HEITKAMP, MICHAEL, A., STOW, GEORGE, C.
Applicants: HEITKAMP MICHAEL A, MONSANTO CO, STOW GEORGE C, HEITKAMP, MICHAEL, A., MONSANTO COMPANY, STOW, GEORGE, C.
Application year: 1996
Main classification: C12N11
IPC codes: C02F3, C12N11