Background of the Invention Methods for decontamination, neutralization and removal of chemicals, such as organophosphorous and organosulfur (OP refers to both) compounds, herbicides and insecticides, are known in the art. However, the compositions and devices utilized in the prior art methods have undesirable properties, such as corrosiveness, flammability, toxicity, difficulty in making and storing, and limited shelf-life.

For example, DS2, a standard decontamination agent, comprises 70% diethylenetriamine, 28% ethylene glycol monomethyl ether, and 2% NaOH by weight.

Although DS2 is effective, it is corrosive upon exposure to air. DS2 and any matter resulting from its use is classified and regulated as hazardous material. After an application, the DS2 must stand for 30 minutes before rinsing the treated area with water. Additionally, DS2 comprises a teratogen.

Some decontamination methods employ hypochlorite formulations which are corrosive and toxic and injure humans and sensitive tissues such as eyes. Other methods comprise incinerating the contaminated material and utilizing carbon filters to absorb the residual chemicals. Yet other methods utilize polymer beads or microemulsions which absorb the chemical and must be rinsed away. These methods are inherently dangerous, expensive and generate hazardous waste. Furthermore, as many of these compositions and compounds utilized degrade upon exposure to water and carbon dioxide, these compositions and compounds must be used the same day they are made.

Some in vivo methods employ cholinesterases in the presence of nucleophilic oximes to detoxify OP compounds. This enzyme bioscavenger approach is effective against a variety of OP compounds in rodents and nonhuman primates. For example, pretreatment of rhesus monkeys with fetal bovine serum acetylcholinesterase (FBS-AChE) or horse serum butyrylcholinesterase (Eq-BChE) confers protection against up to 5 LDSO of soman, a highly toxic OP nerve agent. Although, the use of an enzyme as a single pretreatment drug for OP toxicity is sufficient to provide complete protection to an individual subject, a relatively large (stoichiometric) amount of the enzyme is required to neutralize the OP compound in vivo.

Therefore, OP/enzyme stoichiometry is increased by combining enzyme pretreatment with oxime reactivation so that the catalytic activity of OP inhibited FBS-AChE is rapidly and continuously restored, and the OP compound is detoxified.

Clearly, a need for better methods and devices for neutralizing, detoxifying, decontaminating and cleaning materials, equipment and personnel exposed to OP compounds exists.

Recently, OP detoxifying compounds, devices and methods thereof, which allow the safe, effective and convenient detoxification of highly toxic compounds not possible by the prior art, have been developed. These environmentally friendly compounds, devices and methods are disclosed hereinbelow.

Summary of the Invention The present invention provides materials, compositions, kits and methods for neutralizing, detoxifying or decontaminating equipment and/or personnel exposed to OP compounds.

In one embodiment, the invention relates to a material comprising a mixture of enzymes and substrates for the removal, decontamination and neutralization of OP compounds including those directed against humans. The mixture of enzymes utilized comprises cholinesterases (ChEs) and/or OP hydrolases and reactivators, such as oximes which includes mono-disquarternary oximes. The material may comprise a flexible or rigid porous support.

The porous support may be a polyurethane matrix or equivalent.

For example, the porous support may be a flexible sponge-like substance or like material, wherein the enzymes are secured by immobilization. Depending on the polyurethane prepolymer or substrate utilized, porous supports of varying degrees of flexibility and porosity may be obtained. The porous support may be formed into various shapes, sizes and densities, depending on need and the shape of the mold. For example, the porous support may be formed into a typical household sponge or a towelette. The preferred dimensions of the sponge are 1"x 2"x 8"to 2"x 4"x 8". The preferred dimensions of the towelette are 4"x 4"x 0.25" to 4"x 4"x 0.03125" to 14"x 14"x 0.0625". However, during large-scale synthesis, the dimensions of the initial immobilized enzyme product might be large. For example, approximately 4 feet by 8 feet rolls could be produced and sized as appropriate and described above. The sponge-like support would be preferable for use on surfaces, including natural, synthetic and biological surfaces such as equipment, laboratory hardware, devices, skin and other delicate membranes, where decontamination of a rough or irregular surface is desired or where the prior art decontamination materials are incompatible with human tissue.

For example, the materials may be used to clean and decontaminate wounds as it is non-toxic and the immobilized enzymes will not leach into a wound. Therefore, the sponges could be used to decontaminate civilians contaminated by a terrorist attack at a public event.

If an object and/or area to be neutralized or decontaminated comprises cracks, crevices, porous or uneven surfaces, a foam-like support is suitable. Application of small quantities may be done with a spray-bottle or spray can with an appropriate nozzle. Further, foam may be selected so that it can be dispensed into the opening of sensitive equipment or an orifice of a subject, such as the ear canal. If a large area is contaminated, an apparatus that dispenses a large quantity of foam may be utilized.

The foam-like support may dissipate after a period of time like shaving cream or it may cure into a stable and flexible sponge-like support. The dissipating foam may be applied on living subjects. The foam, which cures, may be applied around an object and contain the contamination within the foam. Once the foam cures, the object may be handled and moved without further exposure to the hazardous chemical.

When necessary, the material may also comprise a rigid and porous support. The rigid material can be ground into a powder and added to lotions, soaps and other liquids for application. Likewise, the flexible material, supra, may be appropriately treated to render it suitable for use in lotions, soaps and other liquids.

The material may also be in the form of a filter for neutralizing, detoxifying or decontaminating gases such as air. Additionally, the material may be in a form suitable for use as clothing or linings of clothing. Furthermore, the material may be used to decontaminate water by placing the material in water and then removing it from the water.

In another embodiment, the material can be color-coded according to the specific substance it may neutralize, detoxify or decontaminate. The color or color scheme could be selected to indicate enzymatic concentration, activity and/or remaining shelf-life or range thereof.

As disclosed herein, one of ordinary skill in the art will appreciate the various materials and their uses as contemplated by the inventors. All of these forms may be appropriately combined with carbon for further absorption of OP compounds. The carbon may be embedded or incorporated within the porous support of the material or the carbon may be a layer, filter or other to be used in conjunction with the material. Additionally, a slow release form, such as a dry capsule, pellet, liposome or other, of a reactivating compound and OP reacting compounds such as certain oximes like HI-6 and mono-bisquaternary oximes such as pralidoxime chloride (2-PAM) may be embedded or incorporated within the porous support of the material.

A preferred embodiment of the invention comprises a material wherein AChE and/or BChE are simultaneously immobilized with OP hydrolases on or within the porous support during synthesis of the material. Preferably, the enzymes are immobilized through covalent linkages. The enzymes may be of prokaryotic or eukaryotic origin. The enzymes may be contained within the cell or cell free. The enzymes may be of recombinant origin. Other enzymes capable of hydrolyzing hazardous chemicals such as OP compounds may be employed, for example laccase. Additionally, other OP hydrolyzing enzymes would ensure rapid and complete destruction of any toxic intermediate (for example, phosphoryloximes) that might be generated during the decontaminaiton process. Likewise, enzymes such as triesterase may be used for the decontamination of pesticides in a similar manner as herein described. Preferred enzymes are those that may be reactivated.

The materials of the invention may be placed in containers to complete decontamination the OP compounds on the materials.

In another embodiment, the invention relates to the process of making a material, for the removal, decontamination or neutralization of hazardous chemicals such as OP compounds, comprising a mixture of enzymes immobilized on a porous support. In this embodiment, a mixture of enzymes and a prepolymer are gently and evenly mixed together with minimal degradation of the biotype component so that the resulting immobilized enzyme may effectively decontaminate, neutralize or detoxify an amount of an OP compound. The device utilized folds the components into one another. This is a low shear process. During synthesis of the material by prior art methods, for example a mixing drill, the enzymes utilized are subjected to fluid forces or shear stress. Use of a device that gently folds the components into one another greatly reduces these fluid forces or shear stress, and is the preferred device for enzymes, specifically enzymes that are sensitive to the high shear forces of the drill mixing device. Additionally use of additives such as surface-acting polymers, e. g. P-65, or low concentrations of glycerol protects against enzyme denaturation induced by shear forces, and modifies the final properties of the sponge to obtain the desired porosity and absorbent qualities.

In a preferred process of making the material, a two chamber apparatus is utilized. See Figure 11 A and B. One chamber contains a mixture of enzymes and the other chamber contains the prepolymer. The mixture of enzymes and the prepolymer are simultaneously extruded at a 1: 1 ratio and mixed. Preferably, the mixture of enzymes and the prepolymer are rapidly and evenly extruded through a static mixing stator which gently and evenly mixes the enzymes and prepolymer. A preferred low shear device is a double chamber syringe and a static mixing stator typically used to mix viscous polyurethanes or epoxy glues. The size of the apparatus may vary depending on need. It may be pocketsize for use in the field by soldiers. Alternatively, the apparatus may be suitable for large-scale production and/or decontamination of a large objects or area. The low shear mixing device more than doubles the resultant AChE or BChE immobilized enzyme activity when compared to an identical mixture prepared with the high shear device.

The invention further relates to various materials, methods and devices for reactivating the enzymatic activity of the material. These materials, methods and devices will allow a person to use the decontamination material of the invention for several separate uses and/or for a single and continuous use, which would normally require several decontamination materials but for reactivation of the enzymatic activity of the immobilized enzymes.

Additionally, these materials, methods and devices allow for complete decontamination and/or neutralization of excess OP compounds absorbed by the porous support but did not react with the immobilized enzymes. These methods and reactivation materials employ substrates and/or oximes, to reactivate the catalytic activity of the OP inhibited and immobilized enzymes.

The invention further relates to various materials and additives that are added to the embodiment to aid in the removal and decontamination of organophosphate from surfaces such as cracks, crevices, porous or uneven surfaces such as clothes and biological surfaces that readily absorb the organophosphates or pesticides such as skin. The additives are used in conjunction with the sponge material and may be incorporated within the porous support of the material. The additives may be in a dry or liquid form, and may be organophosphate solubilizing compounds such as triacetin or tetraglyme, or oximes, which both aid in decontaminating and reactivating enzymes.

Another embodiment of the invention relates to a variety of kits. Along with the sponge containing a plurality of enzymes needed for the decontamination of organophosphorous and/or sulfur compounds the kit may include materials which would facilitate or be deemed necessary for the decontamination process. Kits may also include polymeric materials and enzymes if the foam is transient in nature, e. g. the prepolymer, a stable enzyme mixture and a low shear apparatus for making an organophosphorous and/or organosulfur decontamination foam. The kits may contain items to facilitate the use of the device, e. g. instructions, containers, test tubes, etc.

Description of the Drawings This invention is further understood by reference to the drawings wherein: Fig. 1A illustrates the modeled surfaces of acetylcholinesterase, butyrycholinesterase and phosphotriesterase.

Figure 1B illustrates the modeled surface of laccase.

Fig. 2 shows a cured material.

Fig. 3 schematically illustrates the specific reaction of the enzymes with prepolymer and the product polyurethane crosslinked ChE.

Fig. 4 shows the linear correlation between the amount of BChE added during synthesis of the material and the amount of BChE in the final material.

Fig. 5 shows the increasing amounts of BSA added during synthesis to a constant amount of AChE and TDI polymer.

Fig. 6 A and B illustrates that the materials maintained enzymatic stability for more than 12 months at 25° and 45°C and 3 years at 4°C for AChE (A) and BChE (B).

Fig. 7 shows that the material maintained enzymatic activity after consecutive washes.

Fig. 8 shows a substrate concentration dependent curve for soluble and polyurethane coupledAChE.

Fig. 9 illustrates the pH range of soluble and immobilized AChE.

Fig. 10 shows the relative activities of co-immobilized ChEs and OPHs.

Figs. 11A and B shows a version of a manual mixing gun and a disposable mixing stator.

Fig. 12 illustrates how oximes reactivate alkylphosphorylated ChE.

Fig. 13 A illustrates the enzyme activity of immobilized FBS-AChE. Fig. 13 B illustrates the enzyme activity of immobilized Eq-BChE.

Fig. 14 represents inhibition of foam-immobilized FBS-AChE by DFP and reactivation by HI-6.

Fig. 15 represents inhibition of foam-immobilized Eq-BChE by DFP and reactivation by TMB4.

Fig. 16 shows restoration of the original sponge activity with HI-6.

Fig. 17 (A, B and C) shows the protection afforded by sponge with various additives, i. e. tetraglyme (A), HI-6 (B) and 2-PAM (C).

Fig. 18 shows the capacity of the resulting carbon sponge for binding methylene blue.

Detailed Description of the Invention Enzymes have been incorporated in hypo-based urethane foam during polymer synthesis. See U. S. Patent No. 4,342,834. Hypoprepolymer is synthesized from a reaction of polyether (or polyester) polyol with isocyanates in the presence of cross-linking agents. See Havens, P. L., et al., Ind Eng Chem Res (1993) 32: 2254-2258; U. S. Patent No. 4,137,200; LeJeune, K. E., et al., Biotechnology and Bioengineering (1999) 20 ; 62 (6): 659-665. Synthesis is initiated by bringing water molecules into contact with isocyanate groups present within the polyurethane prepolymer.

A two-step procedure occurs from this point. Isocyanates react with water to form an unstable carbonic acid, which in turn degrades to an amine yielding C02 that gives the porous support lift and enables it to rise. The amines readily react with isocyanate groups, leading to production of urea type linkages. Since the enzyme contains multiple functional groups, such as amines and hydroxyls that can react with isocyanates, the enzyme becomes an integral part of the porous support during synthesis. Significant quantities of enzyme can link to the porous support without disrupting the progress of polymer synthesis. The reaction occurring during the polymer synthesis is shown below.

1. C02Evolution: 2. Urea Linkage: 3. Amine Group Enzyme Immobilization: 4. Hydroxyl Group Enzyme Immobilization: The following list of enzymes and chemicals are examples of those suitable for use in the instant invention: Acetylcholinesterase (AChE); Butyrylcholinesterase (BChE); Pseudocholinesterase; Organophosphate hydrolases (OPH) ; Phosphotriesterase; Pseudomonas diminua bacterial OPH (paraoxonase); Laccases; Organophosphate acid anhydrase (OPAA) Pralidoxime chloride (2-PAM); 7-(methoxyphosphinyloxy)-1-methylquinolium(methoxyphosphinyl oxy)-1-methylquinolium iodide (MEPQ); Diisopropyl fluorophosphate (DFP); Acetylthiocholine iodide (ATC); S-butyrylthiocholine iodide (BTC); 5,5'-dithio-bis (2-nitrobenzoic acid) (DTNB); N, N'-trimethylene bis (pyridinium-4-aldoxime) dibromide (TMB4); and 1- (2-hydroxyiminomethyl-1-pyridinium)-1- (4-carboxyaminopyridinium)-dimethylether hydrochloride (HI-6).

The following examples are intended to illustrate but not to limit the invention.

Example 1 Determination of Possible Enzyme Interference As polyether prepolymer derived from tolyl diisocyanate (TDI), reacts most favorably with free aliphatic amines such as lysine and arginine present on the surface of the ChEs (or any protein) to become a permanent cross-linked part of the material, computer aided molecular modeling of the enzymes was performed to highlight the available amino groups on the surface of each enzyme, and to determine whether the coupling of these groups to a porous support would interfere with enzymatic function. This may be performed on every enzyme for which its crystal structure is known, or enzymes which may be modeled by homology.

Figure 1 A illustrates the modeled surfaces of acetylcholinesterase, butyrycholinesterase and phosphotriesterase and shows the lysine and arginine residues on the surface of the ChEs which are available for coupling to the prepolymer. This was generated by Insight II, molecular modeling software, by Biosym Technologies. Based on the molecular modeling, there are at least one lysine and 29 arginine water-accessible residues on the surface of FBS-AChE to couple to the porous support, while 26 lysine and 26 arginine residues were modeled for equine-BChE. The majority of the lysine and arginine residues were found on the backside of the ChEs, and only a few are found on the side of the enzyme where the catalytic site gorge is located. The rim and the catalytic site gorge opening of both AChE and BChE appeared to be essentially devoid of lysine and arginine. Therefore, coupling these enzymes to the porous support should have minimal effect on the entrance of substrate, inhibitors such as OPs, or reactivators such as oximes which includes mono-disquarternary oximes, release of products of catalysis to and from the active site, and the kinetic rates of the enzymes.

Similarly, a model of the surface of laccase (Figure 1 B) is shown with available residues to couple covalently to the prepolymer.

Example 2 Synthesis of an Enzyme Bound Polyurethane Material A typical synthesis of the material comprises mixing enzymes in phosphate buffer containing 1 % (final concentration) surfactant with prepolymer. Polyether prepolymer derived from tolyl diisocyanate (TDI), Hypol prepolymer TDI 3000 (Hampshire Chemical, Lexington, MA), and Pluronic P-65 surfactant (BASF Specialty Chemicals, Parsippany, NJ) were used.

The 2-phase system is mixed and placed into a suitable mold and left to cure. Figure 2 shows a cured material which comprises a sponge-like support.

Figure 3 schematically illustrates the specific reaction of the enzymes with prepolymer.

Synthesis begins when H20 molecules react with the isocyanate groups present within the polyurethane prepolymer. Isocyanate reacts with the water to form an unstable carbonic acid, which degrades to an amine yielding CO2. The C02 causes the polymer to rise and become porous, and simultaneously the amines readily react with the isocyanate groups leading to urea linkages. While the amino groups are the preferred reaction site between the enzyme (s) and the prepolymer, hydroxyl (OH) groups are also available to interact within the reaction buffer, e. g. H20 and on the enzyme (s).

Since the ChE contains amines that are on the surface and available to react with the isocyanate groups, they can become an integral part of the polyurethane support during synthesis. There is no significant entrapment of the enzyme in the material as found with cyclodextrins, or physical adsorption of the enzymes, as observed with activated carbon. The inclusion of a surfactant such as Pluronic P-65 at about 1% final concentration controls the final structure and absorption potential of the material.

To create a material comprising a porous polyurethane support, approximately 30 mL of 50 mM phosphate buffer, pH 8.0, containing P-65 surfactant buffer, was placed in a 600 mL plastic beaker. 3 to 5 mL of either purified FBS-AChE (7500 units) or purified Eq-BChE (5000 units) was added, followed by approximately 40 gm of Hypo 3000 prepolymer (tolyl diisocyanate). The two-phase system was mixed and the material was allowed to expand for 10 min, extruded from the container. The material was washed thoroughly with 50 mM phosphate buffer, pH 8.0, dried and stored in a zippered bag at 4°C for future use.

Example 3 Characteristics of Svnthesized Material Approximately 20-90% of the enzymes were covalently linked to the porous support through free amino-or hydroxyl groups. This was determined by the presence of enzyme in first and second washes of the material.

Since the enzymes can be attached at multiple points, they become a part of the cross- linked polymer support. The cross-linked polymer support imparts considerable stability to the bound enzymes. A large quantity of enzyme can be incorporated into a small polyurethane support, thereby rendering the cross-linked polymer support a highly effective material for decontamination.

A. Enzymatic Activity.

Five samples of materials containing FBS-AChE and five samples of materials containing Eq-BChE, ranging in weight from 1 to 40 mg, were suspended in 2.8 mL of 50 mM phosphate buffer, pH 8.0, and assayed using the method of Ellman. See Ellman, G. L., et al., (1961) Biochem Pharmacol. 7: 88-95. A linear correlation was found between the weight of the sponge and enzyme activity for both FBS-AChE and Eq-BChE immobilizations. See Figs.

13A and B. The linear correlation between the weight of the material and enzyme activity indicates a uniform immobilization of AChE or BChE throughout the material.

The material was washed with either 50 mM phosphate buffer, distilled water, or 10 mM ammonium bicarbonate without affecting substrate hydrolysis. Therefore, the mixing of prepolymer, surfactant, and enzyme in situ at 22°C yields a useful and effective material retaining about 50% of the original activity of soluble ChE.

B. Protein Loading Capacity.

The material has a significantly higher loading capacity for ChEs such as BChE or AChE. The final activity of the BChE immobilized in the material could be increased by adding larger quantities of enzyme during synthesis. See Fig. 4. When nonspecific protein (bovine serum albumin, BSA) was added to a constant amount of purified AChE, there was no reduction in ChE activity. See Fig. 5. Thus, higher potency materials may be synthesized with additional proteins, enzymes and other ChEs. Additionally, materials effective against a diverse array of OP compounds may be readily synthesized by with combinations of multiple enzymes or a plurality of enzymes.

C. Enzymatic Stability.

As illustrated by Figure 6, the immobilized ChE and OP hydrolase maintained enzymatic stability for more than 12 months at 25°C and 45°C, respectively. If the material is frozen in liquid nitrogen, most of the original activity remains. TDI imparts remarkable stability to the immobilized ChE; about 50% of the original activity of the immobilized AChE and 20% of the activity of the immobilized BChE remained after 16 hours at 80°C, conditions under which the soluble enzymes would exhibit no activity. The ChE materials can be exhaustively dried under vacuum at 22°C and then rehydrated without loss of enzyme activity.

When AChE or BChE materials were exhaustively washed and assayed for activity, the wash and assay cycle repeated more than twenty times over three days, no decrease in activity occurred. See Fig. 7. This indicates that the material may be used repeatedly.

These results also demonstrate that the ChEs are covalently cross-linked in the porous support and that the ChEs will not leach out to skin, water, or equipment. Therefore, once the immobilized enzymes bind an OP compound the OP is removed from the surface requiring decontamination.

D. Kinetic Constants.

The number of active sites of either the immobilized or soluble ChEs was determined by titration with the organophosphorous compound MEPQ, 7- (methylethoxyphosphinyloxy)- 1-methylquinolinium iodide. The bimolecular rate constants for the inhibition of AChE material and BChE material and the respective soluble enzymes by MEPQ at 25°C showed that there was no significant difference between the soluble and covalently bound enzymes.

Table 1. Time-Dependent Inhibition of ChEs by MEPQ <BR> <BR> <BR> <BR> <BR> ChE Bimolecular rate constant<BR> <BR> <BR> Form (M min) i SD FBS-AChE soluble 1.59#0.52x108 coupled to sponge 1.00#0.28x108 Equine-BChE soluble 4.15 0.78 x 10 coupled to sponge 4.21 2.00 x 10 See Table 1. These results demonstrate that the immobilized and soluble forms of ChEs interact with the OP compounds similarly. Therefore, enzymatic activity assays which are generally available and known in the art may be used.

An initial rates method using a modified Ellman's assay was used to determine the parameters Km, eoh t and kcaJKm for immobilized and soluble AChE and BChE. The number of active sites of either the coupled or soluble ChEs was determined by titration with MEPQ. As shown in Table 2 and Figure 8 for AChE, the Km values for the immobilized ChEs were about 10-fold greater than the corresponding soluble enzymes, and the k,,,, values were less dramatically affected. The combined effects on affinity for substrate and kcar resulted in approximately a 20 to 50-fold decrease in acylation (kcaJKm) Interestingly, while soluble BChE lacked substrate inhibition, immobilized BChE yielded substrate inhibition. These results suggest that covalent binding of surface residues of ChEs to the porous support changed some properties of the active site region of the bound enzymes directly or indirectly. Table 2. Kinetic parameters for soluble and polyurethane coupled ChEs. Substrate Km Ks"Kvt Kct Enzyme Form inhibition (mM) (mM) B (mini') (M''mini') FBS-AChE Soluble yes 0. 119 18-2. 8 x 105 2. 5 x 109 immobilized yes 1. 090 22-5. 9 x 104 5. 4 x 10' Equine-BChE Soluble no 0. 127 1. 5 1. 8 3. 1 x 104 2. 4 x 108 immobilized yes 1 200 16 - 1.8x104 1.5x107 Generally, immobilized cholinesterases or OP hydrolyzing enzymes exhibit between the same to 10 fold greater Km values than the corresponding soluble enzymes. In addition to the cholinesterases, OPH (derived from Pseudomonas diminuta, figure 19A) shows about a 10- fold increase in Km because a shift to the right is also observed in the immobilized (sponge) form when determined using the substrate paraoxon. On the other hand, OPAA (derived from Alteromonas, Figure 19B), shows little change in Km for the substrate paraoxon.

E. pH of Soluble and Immobilized Enzymes.

The pH profiles of immobilized and soluble AChE are identical and the enzymes exhibit activity throughout the broad pH range of 7-8.5. See Fig. 9. Since the pH profiles of soluble cholinesterases and OP hydrolases have optimal activities in this same pH range, the materials may be optimized and diversified by employing a plurality of these multiple enzymes immobilized on or within a porous support.

Determined in 50 mM phosphate, pH 8 at 25°C using an initial rates method.

Calculated from Vmax and the active site concentration of ChE that was determined by MEPQ titration.

Values were calculated2 using modified Haldane equations, and the special case where b=0. The best fit between the two was determined using an F test, where significance was defined as p<0.05.

Example 4 Immobilization of a Pluralitv of Enzymes ChEs were co-immobilized with bacterial OP hydrolase (OPHB) and/or rabbit serum OP hydrolase (OPHR). There was no reduction in the enzymatic activities of AChE or BChE co-immobilized with OPH as compared to the enzymatic activities of each of these enzymes individually immobilized. See Fig. 10. Additionally, there was no reduction in the enzymatic activity of co-immobilized OPH. Therefore, a plurality of enzymes, which each enzyme differentially reacts with various OP compounds, may be selected and utilized in a material to create a decontamination material effective against a wide range of OP compounds.

Example 5 Rapid Mixing Synthesis By utilizing a method of syntheses modified from the adhesive industry (CPA, Greenville, RI 02828) shear forces which decrease enzymatic activity are reduced. See Fig.

11. In this method, the enzyme is not in an organic buffer as required in some immobilization techniques. This results in less air-induced shearing, thereby maintaining enzymatic activity.

This method is also simple to conduct, rapid and reproducible. The low shear mixing device more than doubles the resultant AChE and/or BChE immobilized enzyme activity when compared to an identical mixture prepared with the high shear device such as a mixing drill.

See Table 3. Table 3 Technique AChE Activity U/mg High shear mixing drill 0.100 Low shear 2-chamber device 0.270 Example 6 Inhibition of Immobilized FBS-BChE with DFP and Reactivation with HI-6 100 mg samples of immobilized FBS-AChE were incubated with varying concentrations of DFP in 2 mL of 50 mM phosphate buffer, pH 8.0, for 1 hour at 25°C. In parallel experiments, 1 mM HI-6 was added to the same amount of material and DFP.

Residual DFP in the samples was measured by adding a 0.5 mL aliquot of the reaction mixture to 0.5 mL of a fresh 1 U/mL solution of FB S-AChE, incubating for 1 hour, and assaying 10 us aliquots using the Ellman procedure. The results are shown in Figure 14.

The inhibition of FBS-AChE activity by DFP was proportional to the stoichiometric amount of DFP added to the foam suspended in buffer. The presence of 1 mM HI-6 nearly completely prevented enzyme inhibition by DFP. This indicates that immobilized FBS-AChE may be repeatedly reused after reactivating the enzyme with an oxime solution such as HI-6.

Figure 12 illustrates how oximes may reactivate alkylphosphorylated ChE activity.

Example 7 Inhibition of Immobilized Eq-BChE with DFP and Reactivation with TMB4 50 mg samples of immobilized Eq-BChE were incubated with varying concentrations of DFP in 2 mL of 50 mM phosphate buffer, pH 8.0, for 18 hours at 25°C. In parallel experiments, 1 mM TMB4 was added to the same amount of material and DFP. Residual DFP in the samples was determined by adding a 0.5 mL aliquot of the reaction mixture to 0.5 mL of a fresh 1 U/mL solution of Eq-BChE, incubating for 1 hour, and assaying 10 ul aliquots using the Ellman procedure.

TMB4 was used as a reactivator instead of HI-6, since TMB4 is a more efficient reactivator of inhibited Eq-BChE than is HI-6. These results are shown in Figure 15. As in Example 6, the foam-bound Eq-BChE may be repeatedly reused after reactivating the enzyme with an oxime solution such as TMB4.

Example 8 Inhibition of Immobilized AChE with the Organophosphate MEPO and Detoxification of the MEPQ and Reactivation of the Immobilized Enzyme in the presence of HI-6 50 mg samples of immobilized acetylcholinesterase were incubated with varying concentrations of MEPQ in 2 mL of 50 mM phosphate buffer, pH 8.0 at 25°C for 1 hr. In the absence of oxime HI-6, the sponge soaks up the MEPQ and is inactivated. Addition of HI-6 reactivates the sponge's activity, and the MEPQ is detoxified, and most of the original activity of the sponge returns. Only at very high ratios of organophosphate (1000-fold molar excess) is the process of binding, reactivation, and detoxification not complete. However, fresh HI-6 can restore most of the original activity once again. See Figure 16.

Example 9 Additives to the Sponge to Improve Decontamination of Soman (GD ! Contaminated Skin of Guinea pigs Sponges approximately 1'h x 2'/z x 1/4" (HxLxD) contained 9.0 mL of additive and a second sponge contained 4.5 mL of additive. Each guinea pig was wiped with the first sponge and then the second sponge after soman (GD) exposure. Survival of the guinea pigs was determined after 24 hours, and the protective ratio determined. The protective ratio is the ratio of the LD50 of the sponge containing an additive to the LD ; o of soman in the absence of sponge. Thus, the higher the LD50, then the higher the protective ratio and the more effective the sponge combination is for decontamination of guinea pig skin and protecting the animal from the organophosphate. The sponge was compared to the M291 kit (available from Truetech, Inc.), the currently used decontamination kit fielded by the US Army. As shown in the table, the sponges provide 4 to 5-fold better protection than the M291 kit.

Figure 17A shows the protection afforded by tetraglyme; Figure 17 B the protection afforded by HI-6, and Figure 17C the protection afforded by 2-PAM. The number on the top of each bar shows the number of guinea pigs evaluated at the indicated dose of soman (GD).

For reference, the LD5o of soman on guinea pigs without any effort to decontaminate is shown by the label"GP", while the protection offered by the M291 kit is shown by"M291". Other additives to the sponge such as triacetin also afforded some additional protection compared to the M291 kit. Additive to sponge LDSO Protective Ratio HI-6 (oxime, 50 mM) 79 8. 0 2-PAM (oxime, 50 mM) 76 7. 7 Tetraglyme (30%) 88 8. 9 Referencevalues M291 decon kit 17. 7 1. 8 Soman alone 9. 9 Example 10.

Activated Carbon Containing Sponge.

0.5-1 grams of activated carbon was added to about 4 mL of the prepolymer prior to mixing with acetylcholinesterase (5 mL of Electric eel, in 50 mM pH 8.0 phosphate buffer with 1% Pluronic P-65) to produce an acetylcholinesterase immobilized carbon sponge. The addition of carbon did not interfere with the immobilization of the enzyme, as shown in the table. The capacity of the resulting carbon sponge for binding methylene blue (an colorimetric indicator for activated carbon or resin) is illustrated in the Figure 18. Therefore, comparison of the sponge with activated carbon to the sponge lacking activated carbon demonstrates that it can bind about 2-fold more methylene blue at less than saturating concentrations.

Activities of Sponges and Activated Carbon Relative Activity (% control Relative Activity to Type of Sponge in absence of carbon) absorb methylene blue Electric eel AChE sponge 100 % 1X Electric eel AChE sponge 108% 2X with Activated Carbon Activated Carbon not in the --- 13X sponge Incorporation by Reference To the extent necessary to understand or complete the disclosure of the present invention, all publications, patents, and patent applications mentioned herein are expressly incorporated by reference therein to the same extent as though each were individually so incorporated.