SYNERGISTICALLY STABILIZED MIXED FORM HALOGENATED AND/OR INTERHALOGENATED RESINS FOR DISINFECTING WATER

Abstract: Synergically stabilized mixed form halogenated and/or interhalogenated forms of the free-­ base polyvinyl-pyridine resin for disinfecting water. The resins may be employed in a single pass column or bed system to provide instantaneous disinfection of bacterially contaminated water.

Description: Background and Summary of the Invention The present invention relates to the on-contact, instantaneous disinfection of water, and more particularly to the use of synergically stabilized, mixed form halogenated and/or interhalogenated vinyl-pyridine resins for disinfecting water. Several techniques employing resins are known for killing bacteria in water. The usual method involves treating the water with resins that provide halogen residuals such as I₂, Br₂, and Cl₂ for disinfection. Several methods involve the use of polyhalide anion exchange resins. Still another water disinfecting technique involves the use of an anion exchange resin loaded with insoluble triiodide ions (I - / 3). The following patents show examples of these techniques: US-A-3,316,173; 3,425,790; 3,436,345; 3,462,363; 3,565,872; 3,817,860; 3,923,665; 4,187,183; 4,190,529; and 4,420,590. Resins in accordance with the techniques noted above have the potential for releasing halide and polyhalide ions and do not produce an optimum halogen-hypohalous acid mixture, and, as such, diminish their bactericidal efficiency. The resins of US-A-3,565,872, though not made from anion exchange resins, also have these disadvantages, as well as the disadvantage for the potential for promoting resin decomposition in aqueous media, such as with the Cl₂-, Br₂-, and the BrCl- forms. Further, none of the above anion exchange resins generate hypohalous acid when treating water high in total dissolved salts with the exception of the one disclosed in US-A-4,187,183 which releases only very low levels of hypoiodous acid (less than 0.22 mg/l HOI) under such circumstances. Hypoiodous acid is desirable since it is more bactericidal and more virucidal than iodine (I₂). Heretofore, significant levels of hypoiodous acid have had to be generated by either an iodinated anion exchange resin in combination with a scavenger system as in US-A-4,187,183 or by adding an extraneous oxidant such as a chloramine as in US-A-3,163,716 and US-A-3,161,588. The interhalogenated resins in US-A-3,565,872 produce hypohalous acids but not in an optimum disinfecting mixture with a corresponding halogen, e.g., I₂-HOI, Br₂-HOI, or Br₂-HOBr. Therefore, a resin which provides for single pass, on-contact instantaneous disinfection, releases an optimum mixture of disinfecting levels of halogen and hypohalous acid without halide and polyhalide release, and which provides for long term resin stability in aqueous medium would be a significant improvement in water treatment technology. Accordingly, it is an object of the present invention to provide synergistically stabilized, mixed form halogenated and/or interhalogenated polymeric, vinyl pyridine resins for single pass, on-contact instantaneous disinfection of water. It is another object to provide such resins as disinfectants capable of producing optimum disinfecting mixtures of halogen and hypohalous acid (e.g., HOBr or HOI through hydrolysis of the interhalogen, or through reaction of one halogen or interhalogen with another halogen) for universal disinfection against bacteria, viruses, and amoebic cysts. Still another object of the invention is to provide such resins for producing halide- and polyhalide-free effluents when treating water relatively high in salt content. Yet another object of the invention is to provide such resins that possess long term stability in an aqueous medium. In accordance with these objects, granular or bead form, polymeric vinylpyridine resins which have been cross-linked with divinylbenzene, divinylpyridine, or other conventional crosslinking agent and which contain the pyridyl functional group covalently bonded to the vinyl polymeric backbone by the pyridyl No. 2 or No. 4 carbon are treated with a mixture of halogens and/or interhalogens to provide a media for disinfection of bacterially contaminated water. With the present invention, depending on the degree of loading of halogens and/or interhalogens on the vinylpyridine resin, instantaneous, single-pass flow-through disinfection can be achieved and a residual halogen and hypohalous acid (HOBr or HOI) is produced. If the residual halogen and hypohalous acid are to be reduced or removed, a simple follow-up scavenger column or bed of activated carbon can be employed. The combined features of non-ionic complexation of the mixture of halogens and/or interhalogens with the pyridyl functional group and the hydrolysis of the interhalogens and/or reaction of one halogen or interhalogen with another halogen within the resin matrix precludes the ion exchange of halide ions (I⁻ and Br⁻) and polyhalide ions (I₃⁻, Br₃⁻, I₂Cl⁻, etc.) which can occur in the previous state of the art disinfecting resins when they are challenged with water containing a high level of total dissolved salts. Minimizing the halide and polyhalide content of the effluent water provides for more potent disinfecting action and for a more physiologically acceptable potable water as pointing out in US-A-4,420,590. The problem of excess halide (greater than 5-10 mg/l) and polyhalide exchange from resins when treating water high in total dissolved salts can occur with resins prepared in accordance with the previous state of the art such as those resins in US-A-3,565,872; 3,187,806; and 4,187,183. This problem is eliminated and does not occur with resins prepared in accordance with the present invention. Because of the non-ionic complexation in the present invention, no iodide or bromide salt (e.g., KI or KBr) is needed in the preparation, thereby maximizing the disinfection efficiency of the total halogens and interhalogens. For example, in the Br - / 3, form of polyhalide resin such as in US-A-3,462,363, one-third of the halogen is wasted just to provide for binding the negatively charged tribromide ion (Br - / 3), to the positively charged anion exchange resin. Resins prepared in accordance with the present invention may be employed for swimming pool disinfection, emergency water disinfection kits, and small scale drinking water treatment systems with appropriate scavenging systems, as well as other applications where water disinfection is desired. The unique features of this invention solve problems apparently not recognized in the prior art. These unique features are not characterized by the vinylpyridine-based polymers alone, but by their mixed form halogen and/or interhalogen molecular addition reaction products which, heretofore, have never been prepared and tested. Neither have the on-contact, bactericidal action and heretofore unknown synergistic stability of the mixed form resins been demonstrated; nor has their ability to produce effluents containing optimum mixtures of halogen and hypohalous acid been demonstrated. The synergistic stability of the mixed form resins, though not fully understood, is believed to be due to an inherent reduction-oxidation buffering phenomenon or "redox" equilibria occurring within the resin matrix and is believed to occur to some degree in all of the mixed form resins. Similar redox equilibria is defined by Light (T. S. Light, Anal. Chem. , 44 , 1038 (1972)) and examples are given by Lambert et al. ( Anal. Chem. , 47 , 915 (1975)) and Black and Whittle ( J-AWWA , 59 , 607 (1967)). The disclosures of the prior art, including US-A-3,565,872, fail to provide any teachings of the present invention, and the advantages of the present invention as described above are, as a whole, believed to be unobvious and of a surprising and unexpected nature to one skilled in the art. Description of the Preferred Embodiment In accordance with the present invention, a free base, vinyl polymeric resin (granular or bead-form) which has been crosslinked with divinylbenzene, divinylpyridine, or other conventional crosslinking agent and which contains the pyridyl functional group covalently bonded to the vinyl polymeric backbone by the pyridyl number 2 or number 4 carbon is reacted with a mixture of halogens and/or interhalogens to provide a media for on-contact, instantaneous single-pass disinfection of bacterially contaminated water. Instantaneous disinfection is accomplished within the resin bed because of the relatively high concentration of halogen and hypohalous acid (HOBr or HOI) at the surface of the granules or beads. If desired, the residual halogen and hypohalous acid can be reduced or removed by a simple follow-up scavenger column or bed of activated carbon. The preparation of the free base, crosslinked virgin material (poly-2- and poly-4-vinylpyridine) is described in US-A-2,739,948 and follows below: Poly-2-vinylpyridine, Crosslinked Crosslinked copolymers of 2-vinylpyridine are made in bead form by suspension polymerization in a pressure-tight autoclave by the following procedure. To the autoclave are added (parts are given in parts by weight): 0.18 part benzoyl peroxide- dissolved in vinylpyridine 0.05 part tert.-butyl perbensoate dissolved in vinylpyridine 90 parts 2-vinylpyridine 10 parts divinylbenzene (or 2,4-divinylpyridine, prepared as in 2,739,948) 200 parts distilled water 3 parts hydroxy apatite (sub-micronic particle size) 0.03 parts sodium oleate The autoclave is then closed and agitated by a rocking mechanism while the autoclave is immersed in a controlled-temperature bath at 90°C for about 7 hours and then at 113°-115°C for about 3 hours. The resultant copolymer beads are washed with dilute hydrochloric acid to remove any suspension agent, then with dilute sodium hydroxide to remove adsorbed hydrochloric acid, then with water, and subsequently dried at 70°C for about two hours. Poly-4-vinylpyridine, Crosslinked Follow the procedure above for poly-2-vinylpyridine but substitute an equimolar quantity of 4-vinylpyridine monomer for the 2-vinylpyridine monomer. Also, poly-2- and poly-4-vinylpyridine (crosslinked) may be obtained from Reilly Tar & Chemical Corp., identified as LX-101 and R-8050, respectively. The resin complexes of the present invention are comprised of the molecular addition reaction products formed from the reaction of the polymerized, free base pyridyl functional groups with a combination or mixture (two or more) of halogens (I₂ and Br₂) and/or interhalogens (ICl, IBr, and BrCl) such that all or a fraction of the pyridyl functional groups are complexed. The reaction or complexation of the polymerized free base pyridine resin (poly-4-vinylpyridine) and a mixture of a halogen (I₂) and interhalogen (ICl) may be illustrated by the following equation: General Preparation Procedure The first step in preparing the complexed resin of the present invention is to calculate the equivalent weight of halogens and/or interhalogens needed to give the desired form and loading on the resin for a given weight of the dry virgin resin material. Then, add the appropriate mixture of halogens and/or interhalogens to a corrosion-proof vessel containing a compatible solvent such as methyl alcohol. When using bromine chloride (BrCl), a non-oxidizable solvent such as methylene chloride (CH₂Cl₂) or chloroform (CHCl₃) should be used. Allow for complete dissolution to occur, then add the dry resin directly to the alcohol solution. Continuous mixing of the resin slurry is preferred to provide a more homogeneous product, but occasional mixing every 3-5 minutes for approximately 1 hour will suffice. Allow the slurry to stand overnight. The next day pour off or suction filter off the excess methanol. Rinse the resin either batch-wise or by a flow-through column method with 5-10 bed volumes of water. The following are some examples of synergistically stabilized, mixed form complexes of the present invention. These examples serve to illustrate various methods of practicing the invention and are not intended as limitations to the scope of the invention. The specific amounts described in these examples can be scaled up to provide larger quantities as desired or changed to provide any degree of or combination of loading on the resin. EXAMPLE I For 18.74 g of dry virgin resin material (poly-4-vinylpyridine, crosslinked or P4VP) (8.8 meq/g ), add 12.56 g of I₂ and 8.03 g of iodine monochloride (ICl) to approximately 100 ml of methyl alcohol. After the I₂ and ICl are dissolved, add the resin and mix, let stand overnight, and rinse as described in the general procedure above. For this resin 30% of the available pyridyl sites are complexed with I₂ and 30% with ICl. EXAMPLE II For 17.31 g of virgin P4VP, add 19.33g of I₂ and 2.43 g of bromine (Br₂) to approximately 100 ml of methyl alcohol. After the I₂ and Br₂ are dissolved, add the dry resin material, mix, let stand, and rinse as above. For this resin 50% of the pyridyl sites are complexed with I₂ and 10% with Br₂. EXAMPLE III Follow the same procedure for EXAMPLE II except substitute 2.47 g of ICl for the Br₂. This resin is comprised of 50% I₂ and 10% ICl (as per cent available pyridyl functional sites). EXAMPLE IV For 17.31 g of virgin P4VP, add 12.17 g of Br₂ and 1.76 g of bromine chloride (BrCl) in approximately 100 ml of chloroform (CHCl₃). After the Br₂ and BrCl are dissolved in the CHCl₃, add the dry resin material, mix, let stand, and rinse as above. This resin is comprised of 50% Br₂ and 10% BrCl ( as per cent available pyridyl functional sites). EXAMPLE V Follow the same procedure for EXAMPLE IV except substitute 15.75 g of iodine monobromide (IBr) for the Br₂. This resin is comprised of 50% IBr and 10% BrCl (as per cent available pyridyl functional sites). EXAMPLE VI For 6.68 g of the dry virgin poly-2-vinylpyridine (crosslinked) resin (8.5 meq/g ), add 7.21 g of I₂ and 0.92 g of ICl to approximately 100 ml of methyl alcohol. After the I₂ and ICl are dissolved, add the resin, mix, let stand, and rinse as above. This resin is comprised of 50% of I₂ and 10% ICl (as per cent available pyridyl sites). EXAMPLE VII Follow the same procedure for EXAMPLE VI except substitute 0.91 g of Br₂ for the ICl. This resin is comprised of 50% I₂ and 10% Br₂ (as per cent available pyridyl sites). EXAMPLE VIII For 34.62 g of dry virgin P4VP, add 15.46 g of I₂ and 4.87 g of Br₂ to approximately 100 ml of methyl alcohol. After the I₂ and Br₂ are dissolved, add the dry resin material, mix, let stand, and rinse as above. This resin is comprised of 20% I₂ and 10% Br₂ (as percent available pyridyl sites). EXAMPLE IV Follow the same procedure for EXAMPLE VIII, except use 11.6 g of I₂ and 7.3 g of Br₂. This resin is comprised of 15% I₂ and 15% Br₂ (as percent available pyridyl sites). Table I shows the effluent composition of some of the previous state-of-the-art iodinated resins compared to the present invention's mixed form halogenated and/or interhalogenated resins upon treatment with three different feed waters. All of the mixed form resins of the present invention shown in Table I were prepared in accordance with the methods described above. The following results disclose problems apparently not recognized in the prior art. Table I shows that for the three different feed waters illustrated therein each of the last three resins (X, Y, and Z) release halide ion (I⁻) and polyhalide ion (I - / 3,) with at least one of the waters. In contrast, none of the mixed form halogenated and/or interhalogenated resins release I⁻. Each of the mixed form halogenated and/or interhalogenated resins release both iodine (I₂) and hypoiodous acid (HOI) or bromine, hyopbromous acid (HOBr) and/or hypoiodous acid in near equal or significant levels. Also, samples of single-form resins according to US-A-3,565,872 (Cl₂-, Br₂-, and BrCl-forms) were prepared and were found to undergo severe resin decomposition within hours or weeks after preparation. After one year of standing in aqueous medium, these resins were incapable of releasing detectable levels (<0.01 mg/l) of halogen residual. In contrast, the mixed form resins prepared according to the present invention which contained Br₂ or BrCl (EXAMPLES II, V, and VII) exhibited no detectable resin decomposition and EXAMPLE IV (Br₂/BrCl-mixed form) exhibited only moderate degradation after one year in aqueous medium. These mixed form resins (EXAMPLES II, IV, V, and VII), after one year in aqueous medium still released disinfecting levels (≧0.50 mg/l) of halogen and/or hypohalous acid. This heretofore unknown synergistic stability demonstrated by EXAMPLES II, IV, V, and VII is but one of the unique advantages of the present invention over the prior art and is believed to occur to some degree in all of the mixed form resins. To further demonstrate the unobvious advantages of the present invention, the degree of resin degradation (swelling) and effluent composition of several resins are compared in Table II. Resins A and B were prepared according to US-A-3,565,872. Although resin A (15% I₂) does not exhibit degradation (no swelling), it has the disadvantage of releasing iodide (I⁻). Resin B (15% Br₂) exhibits significant swelling indicating resin degradation. However, EXAMPLES VIII and IX which are the mixed-form resins do not exhibit resin degradation and both release a mixture of iodine and hypoiodous acid (HOI)(also see Table I). Table III shows the on-contact, instantaneous disinfection efficiency of the various halogenated and/or interhalogenated vinylpyridine resins prepared in accordance with the present invention. Note particularly the poor disinfection efficiency of the untreated resin, i.e., the virgin granular crosslinked poly-4-vinylpyridine, as compared to the other resins in Table III. As illustrated in Tables I and III, EXAMPLES I and II are the preferred embodiments since both iodine (I₂) and hypoiodous acid (HOI) or iodine and bromine (Br₂) are produced in the effluent at a total active halogen level of approximately 8-10 mg/l. This level of iodine and/or bromine is adequate for essentially complete disinfection of moderately and heavily contaminated water. The molecular iodine (I₂) and bromine (Br₂) are most effective against amoebic cysts and the hypoiodous acid is desirable since it is more bactericidal and at least 40 times more virucidal than iodine. Not only is instantaneous, on-contact disinfection achieved with the mixed form resins, but halogen residuals are also produced to provide for protection against post-disinfection recontamination. If the final use of the treated water requires that the halogen and the hypohalous acid be removed, both may be effectively removed by employing an activated charcoal follow-up scavenger column or bed in the water treatment system. If a lower level of halogen and hypohalous acid are desired in the effluent, the resin can be prepared initially with a lower weight per cent of halogens and/or interhalogens.

Claims: A stable, mixed form halogenated and/or interhalogenated molecular addition reaction product of (a) polyvinylpyridine having the cyclic pyridyl functional ring group C₅H₅N crosslinked with divinylbenzene, within the range of about 2 % to about 25 % by weight based on the weight of vinylpyridine, and (b) a combination of two or more halogens and/or interhalogens selected from the group consisting of I₂/ICl, I₂/IBr, I₂/Br₂, I₂/BrCl, Br₂/BrCl, Br₂/ICl, Br₂/IBr, BrCl/ICl, BrCl/IBr, ICl/IBr, bonded to the nitrogen atom of the pyridyl functional group, so that at least about 10 % of the pyridyl functional groups are complexed by halogens and/or interhalogens, whereby no halogen and/or interhalogen is present in a molar ratio of less than 0,08 of the total absorbed halogens and/or interhalogens. The product of claim 1, wherein the polyvinylpyridine is poly-4-vinylpyridine. The product of claim 1 wherein the polyvinylpyridine is poly-2-vinylpyridine.

Inventors: HATCH, GARY L.
Applicants: AMETEK, INC. PLYMOUTH PRODUCTS DIVISION
Application year: 1986
Main classification: C02F1
IPC codes: A01N59, C08F8