Preparation of I5-polyiodide disinfectant resins

Abstract: A method is provided for strong base anion exchange resins containing high concentrations of pen­ taiodide (I₅⁻). The resins are prepared from highly concentrated solutions of I₅⁻ and I₃⁻ ions. The exchanged ions, such as chloride (Cl⁻), are washed out of the resin after completion of the exchange reaction with the polyiodide ion mixture. The resulting product is a stable resin of predetermined I₅⁻ content, which is highly effective as a disinfectant for water, acting against water-borne bacteria, virus, and Giardia .

Description: The field of this invention is polyhalide anion exchange resins which provide halogen for disinfection of water. More particularly, the field of the invention is polyiodide quaternary ammonium anion exchange resin disinfectants. Triiodide (I₃⁻) anion exchange resins for disinfecting water are described in Taylor, et al. Appl. Microbiol. (1970), 20:720-722, United States Patents 3,817,860 and 3,923,675, and Fina and Lambert, "Proceedings, Second World Congress, International Water Resources Association", Vol. II, pp. 53-59, New Delhi, 1975. The disinfectant resins were prepared by contacting an anion exchange resin in chloride or sulfate form with a sodium or potassium triiodide solution. Typical concentrations of the triiodide ion were around one molar, and the contacting was carried out at room temperatures. The cited patents also describe alternative procedures. In one procedure (Patent 3,817,860, column 5, line 74, and column 6, line 5), the anion exchange resin, such as a quaternary ammonium resin, is first converted from the chloride or sulfate form to an iodide form by being contacted with a potassium iodide solution. The resin is then contacted with a triiodide solution or with elemental iodine (Patent 3,923,665, column 3, lines 62-69). Methods for preparing quaternary ammonium anion exchange resin triiodide disinfectants were reviewed by Hatch, et al., Ind. Eng. Chem. Prod. Res. Dev. (1980), 19:259-263. If quaternary ammonium anion exchange resins as supplied by the manufacturer contain unconverted tertiary amine groups, they can be remethylated by reaction with methyl iodide or dimethyl sulfate. However, most strong base anion exchange resins are supplied in substantially fully methylated form. A fully quaternarized resin, for example, can provide more stable triiodide disinfectants. In one of the methods described ("Method A"), enough aqueous triiodide ion to the resin was used to convert 97% of the anion sites. The triiodide solution was prepared with the stoichiometric amounts of potassium iodide and iodine, which were dissolved "in a near-minimum amount of water". The solution was stirred with the resin beads for 24 hours to complete the conversion. No heating is described so it can be assumed these procedures were all carried out at room temperature. Pentaiodide quaternary ammonium resins and their properties were described by Lambert, et al. in Ind. Eng. Chem. Prod. Res. Dev. (1980) 19:256-258. An I₅⁻ resin was prepared from an I₃⁻ resin by dissolving iodine in heated water and passing the water through the resin by a continuous recycle procedure. The I₃⁻ resin used as a starting material was prepared by a previously disclosed procedure in which an aqueous solution of triiodide is applied to the resin. It was found that at the recommended recycle temperature of about 60°C, the I₅⁻ resin could be produced in as little as 10 hours, but only on a small scale. This reference also described the preparation of an I₇⁻ resin from the I₅⁻ resin by a similar recycle procedure. United States Patent 4,238,477 discloses a procedure for preparing polyiodide quaternary ammonium anion exchange resins similar to that described in-Lambert, et al. (1980), cited above. The patent states that the procedure can be used to prepare I₃⁻, I₅⁻, I₇⁻ or mixed polyiodide resins. Mixed polyiodide resins are also described in United States Patents 4,187,183 and 4,190,529, a mixed polyhalide resin is disclosed in United States Patent 4,420,590. The mixed polyiodide resins disclosed in Patents 4,187,183 and 4,190,529 contained both I₃⁻ and I₅⁻ groups. From 40 to 80% of the exchange sites were I₃ and from 1 to 30% were I₅ groups. The method of this preparation was similar to that described in Hatch, et al. (1980), cited above. Resin beads were placed in a container and covered with a minimum volume of water. A separate container of crystalline iodine and potassium or other water-soluble iodized salts was solubilized in just enough water to dissolve the reactants (col. 2, lines 35-36). After the reactants had completely dissolved, the solution was added to the water containing the resin, mixed therewith for sufficient time to complete adsorption of the polyiodide ions on the exchange sites of the resin, for example, from 24 to 72 hours. No molalities or molarities are specified with respect to the reaction solution, and there is no disclosure of heating the reaction solution. Presumably, therefore, all steps of the method were carried out at room temperature. Triiodide and pentaiodide resins function as broad spectrum bacteriacides against both Gram-positive and Gram-negative bacteria in water, and also against RNA and DNA viruses: Lambert, et al. (1980), cited above; and Fina, et al., Appl. Environ. Microbiol. (1982) 44:1370-1373. It has also been reported the pentaiodide or mixed polyiodide resins are effective as disinfectants against water-borne cysts of Giardia muris . and Giardia lamblia . Marchin, et al., Appl. Envron. Microbiol. (1983), 46:965-969. Despite the great potential for I₃⁻, I₅⁻ and mixed polyiodide anion exchange resins for bacterial, viricidal, and Giardia disinfection of drinking water, these resins have thus far received only limited use. The available methods of producing polyiodide resins have not been adaptable to large scale economical production. The continuous cycle procedure using dilute solutions of iodine in warm water as described in United States Patent 4,238,477 and Lambert, et al. (1980), cited above, have been limited to small scale production. The method is labor intensive and time consuming. For producing a mixed polyiodide resin a two-stage procedure is required in which the I₃⁻ resin is first produced and then partially converted to include I₅⁻ sites. Specially designed equipment is required for use in cycling a large volume of water at 50-60°C for as long as three to four days to produce the mixed resin. Even with careful preparation by this method, a resin of defined characteristics cannot be reliably produced. For example, When a mixed resin containing I₃⁻ and I₅⁻ groups in preselected proportions is desired, the resulting product will contain a variable amount of I₇⁻ groups. This invention provides a direct method for preparing a polyiodide strong base anion exchange resin disinfectant containing a high concentration of I₅⁻ exchange sites, comprising the steps of: (a) contacting granules of a strong base anion exchange resin in chloride (Cl⁻) form with an aqueous treating solution containing I₅⁻ ions and I₃⁻ ions and (b) washing said resin with an aqueous wash to remove exchanged Cl⁻ ions therefrom, characterized in that the combined concentration of said I₅⁻ and I₃⁻ ions is at least 8 molal, at least 40% thereof being I₅⁻ and that contacting is carried out at a temperature of from 30 to 60°C so that at least 70% of the anion exchange sites of the resin have exchanged Cl⁻ for I₃⁻ or I₅⁻. Particular embodiments of the invention are set out in the dependent claims. The mole ratio of I₅⁻ to I₃⁻ can vary from 40% I₅⁻ with 60% I₃⁻ to 100% I₅⁻ with 0% I₃⁻. In preferred embodiments, the mole ratio of I₅⁻ to I₃⁻ is from 50 to 90% I₅⁻ to 50 to 10% I₃⁻. Especially effective disinfectant resins are prepared when the treating solution contains from 60 to 80% I₅⁻ to 40 to 20% I₃⁻. The treating solution is prepared by dissolving alkali metal iodide salt in a limited volume of water. For example, from 8 to 10 gram moles of potassium iodide can be dissolved per liter of water to produce 8 to 10 molal solutions of I⁻. Preparing such high concentrations requires heating of the solution, especially since the dissolving of the solid alkali metal iodide is endothermic. Typical temperatures are in the range from 40 to 50°C. After the iodide solution has been prepared at the required elevated temperature and molality, granular (solid) iodine (I₂) is added. As the I₂ dissolves, it forms the I₃⁻ and I₅⁻ ions by reacting with the I⁻ ion. This reaction is endothermic, so heat must be added to maintain the temperature. The amount of iodine added is carefully controlled according to a predetermined calculation so that substantially all of the I⁻ is converted to either the I₃⁻ or I₅⁻ forms without leaving either undissolved iodine or unreacted iodine in solution. For the contacting, the resin granules can be in a moist, swollen condition, but they preferably are substantially free of external water, Which can dilute the treating solution. The contacting is carried out on a batch basis with incremental addition of the resin granules. Typically, the contacting proceeds to completion so that the resin contains exchanged I₅⁻ and I₃⁻ in the same proportions as the treating solution. The process of this invention has many advantages. No special equipment is required, the contacting being carried out in an ordinary covered vessel equipped for gentle stirring. The process can be scaled up, since the size of the batch of resin to be treated is limited only by the physical size of the equipment, and the ability of the operator to manipulate it. It is desirable to carry out the contacting in a closed vessel, since at the elevated temperatures used there is a tendency for some of the iodine to be vaporized from the solution. Regardless of the size of the batch being treated, the entire reaction and conversion of the resin can be completed in a few hours. In preferred embodiments, substantially all of the exchange sites of the resin are I₅⁻ or I₃⁻ and the I₅⁻ sites predominate, for example, as indicated above, from 60 to 80% of the sites may be I₅⁻ and 40 to 20% I₃⁻. This assures the resin will be highly effective as a disinfectant for bacteria, virus and Giardia . The demand release of the disinfecting iodine species will be primarily from the I₅⁻ sites, since the extra I₂ on these sites is more readily released than the I₂ associated with the I₃⁻ sites. Also the stability of the resin is protected by the I₃⁻ sites, since I₂ released from the I₅⁻ sites can recombine with the I₃⁻ site to reform I₅⁻ sites. DETAILED DESCRIPTION The method of this invention can be practiced with any strong base anion exchange resin. Such resins are commercially available in the form of granules or "beads" prepared for ion exchange use, and are typically provided in the chloride or sulfate form. For the purpose of this invention the resin is preferably obtained in the chloride form. If necessary, however, it can be converted to the chloride form by ion exchange. Commercially available quaternary ammonium anion exchange resins which can be used in practicing the present invention include Rexyn 201 (Fisher Scientific Co.), Amberlite IRA-400 and Amberlite IRA-401 SI Rohm & Haas Company), Ionac ASB-1 (Ionac Company), Dowex I and Dowex 21K (Dow Chemical Co.), and Duolite A-101D and A-109 (Diamond Shamrock Chemical Co.). These resins all have quaternary ammonium ion exchange groups, and are supplied in the salt form, usually as the chloride or sulfate, and are in the form of porous granules or "beads" of various mesh sizes. Other strong base anion exchange resins can be employed, such as tertiary sulfonium resins, quaternary phosphonium resins, and alkyl pyridinium resins. (See United States Patent 3,817,860, col. 3, lines 12-29; and Fina and Lambert (1975), pages 53-54.) For purpose of the present invention, it is preferred that the resin contain substantially all of the exchange sites in the form of quaternary groups. The resins identified above are supplied in that form. However, if required, the resin can be treated with a methylating agent. This procedure has been referred to as "resin remethylation". It is described in United States Patent 4,238,477 and Hatch, et al. (1980), cited above. The preferred strong base quaternary ammonium anion exchange resins are styrene resins having polystyrene backbone with the anion exchange sites connected to the backbone through phenylmethyl chains. As described in Hatch, et al. (1980), cited above, the presence of a phenyl group contiguous to the basic nitrogen group assists in stabilizing the resin after conversion to the polyiodide form. In the key step of the process of this invention, granules of the quaternary anion exchange resin in chloride (Cl⁻) form are contacted with an aqueous solution containing a highly concentrated mixture of I₃⁻ and I₅⁻ ions. An elevated temperature is used such as a temperature at least within the range from 30 to 60°C. The combined concentration of the I₃⁻ and I₅⁻ ions should be at least equal to 8 molal. Preferably, at least 70% of the anion exchange sites of the resin are exchanged from Cl⁻ for I₅⁻ or I₃⁻. The required amount of I₅⁻ and I₃⁻ ions in the contacting solution are calculated so as to be stoichiometrically sufficient to obtain the desired conversion. After the reaction is completed, the resin granules and residual liquid will contain a high concentration of chloride (Cl⁻) ions. The chloride can be removed by washing the granules with water. Stable polyiodide resins are thereby produced with predetermined proportions of I₅⁻ and I₃⁻. Predetermined proportions of I₅⁻ and I₃⁻ sites on completion of the reaction are illustrated in Tables I and II. As illustrated by Tables I and II, the polyiodide resins may contain on a mole ratio basis from 50 to 75% of I₅⁻ and from 25 to 50% I₃⁻. In preferred ratios, the I₅⁻ is present in a substantially higher proportion than the I₃⁻. On a mole ratio basis, the resin preferably contains from 65 to 75% I₅⁻ sites and from 25 to 35% I₃⁻ sites. In an optimized formulation (Product A of Tables I and II), about 70% of the sites are I₅⁻ and about 30% are I₃⁻. To achieve these ratios in the resin, the treating solution will contain a minimum of 1.5 moles of I₂ per mole of I⁻ to 2 moles of I₂ per mole of I⁻, corresponding respectively to 50% I₅⁻ and 75% I₅⁻. For 65% I₅⁻ the treating solution will contain 1.65 moles of I₂ per mole of I⁻. The amount of conversion of the chloride sites of the resin is from 70 to 99%. For example, as illustrated by Table A, conversions up to 97% were obtained. Conversions of 90 to 99% are preferred, while conversions of 96 to 98% are believed to be optimum. Preferred contacting temperatures for the reactions are from 40 to 50°C, such as approximately 45°C. Preferred solution concentrations are from 8 to 10 molal based on the total combined content of the I₃⁻ and I₅⁻ ions. The optimized concentration on the same basis is about 9 molal. The treating solution is prepared by dissolving alkali metal iodide salt in ion-free water. Potassium iodide is the preferred salt, but sodium iodide can be used or other alkali metal iodide. The water is heated to the temperature to be used for the dissolving and is maintained at that temperature by adding additional heat as required during the dissolving which proceeds endothermically. The temperatures used may be the same as those to be employed for the contacting. Preferred temperatures are from 40 to 50°C, such as approximately 45°C. After the iodide solution has been formed, such as a potassium iodide solution as preferred, solid granular iodine is added with stirring of the solution. As the iodine dissolves, it forms the I₃⁻ and I₅⁻ ions, the initial dissolving forming primarily I₃⁻ ions and I₅⁻ ions being primarily formed after most of the I⁻ has been converted to the I₃⁻ form. It is desirable to avoid fully saturated conditions, that is, I⁻ saturation or saturation with I₃⁻ or I₅⁻. The objective is to dissolve all of the iodine required for the conversion, leaving no undissolved iodine. For this purpose a combination of temperature and molality is used which assures complete dissolving. For example, one optimized combination is a molality of about 9 based on the total I⁻ content of the solution, whether in the form of I⁻, I₃⁻, or I₅⁻, and a temperature of 45°C. The dissolving is preferably carried out in closed system, since some iodine may be evolved as a vapor. At temperatures of about 45°C, the amount of iodine lost through vaporization will increase. It is desired to employ temperatures which minimize such iodine loss while producing the high molality solutions required for the process. After the treating solution has been produced as described and the amount of resin to be converted has been determined from the exchange equivalent of the resin, the contacting reaction can proceed. The entire volume of the solution to be used for treating the quantity of resin can be placed in a reaction vessel. If all of the resin is added to the container at one time, even though the resin is stirred in the solution, some encrustation of iodine on the outer surfaces of the granules can occur. Also, reaction of the entire resin mass in the solution at one time can result in a less uniform product. It is therefore preferred to use incremental addition of portions of the resin batch. As each increment is added it is stirred until the resin is fully covered by the solution. The objective is to disperse the beads in the treating solution, and redissolve any iodine that may possibly have precipitated. The stirring of the granules should be carried out without rupturing or fragmenting the granules. Gentle stirring is therefore advisable. The amount of treating solution should be sufficient to completely cover the granules after the entire batch of granules has been added. Stated otherwise, the granules should be completely immersed in the solution throughout the conversion process. As the conversion progresses, granules become more dense by shrinking in size. The final size of the body of granules in the solution will therefore be of smaller volume than the original volume of the granules before treatment. After the resin has been completely reacted, the depleted solution is removed, for example, by drainage through a sieve retaining the granules. Then the granules are washed with water to completely remove exchanged chloride (Cl⁻) and unreacted material. The resin may be washed on a batch basis or washed in a column. The washing does not remove the triiodide or pentaiodide, which are stabilized on the basic nitrogen sites. The water used for the washing is preferably ion-free. The method of this invention in an optimized embodiment is illustrated by the following example. EXAMPLE To prepare Product A of Table I with 70% of the iodinated sites I₅⁻ sites and with 97% of the total sites iodinated), the following stepwise procedure can be used. 1. Measure appropriate wet volume of Chloride (Cl⁻) form of resin. (a) To determine the volume needed, see Calculation Procedures, step 1, as a guide. (b) Use the Cl⁻ form of a Type 1, approximately 8% divinylbenzene crosslinked, polystyrene, quaternary ammonium, strongly basic, anion exchange resin. (c) Be sure resin has had sufficient time to "soak". (d) Allow resin to settle in measuring container. Tapping and shaking of container may be needed to insure settling. (e) Add sufficient water to cover resin. Heat and maintain at 45°C until used in step 6. 2. Measure appropriate amount of potassium iodide (KI) and place in reaction container. (a) To determine the weight needed, see Calculation Procedures, step 2, as a guide. 3. Add measured amount of heated distilled water to reaction container to dissolve KI. (a) To determine the volume needed to produce a 9.0 molal solution, see Calculation Procedures, step 3, as a guide. (b) The initial water temperature should be high enough that the temperature of the solution in the reaction container can be easily maintained at 45°C. If necessary, heat may be added. (c) The KI will not completely dissolve at this concentration unless the 45°C temperature is maintained. 4. To the 45°C KI solution, add the measured amount of iodine (I₂) needed for the desired triiodide (I₃) - pentaiodide (I₅) formulation. (a) To determine the weight needed, see Calculation Procedures, step 4, as a guide. (b) Measure the I₂ and then immediately add it to the KI solution. The I₂ cannot be measured ahead of time due to its volatility. (c) Use all appropriate precautions for handling volatile chemicals. (d) Be sure the I₂ does not adhere to the sides of the reaction container above the KI solution. Undissolved I₂ interferes with proper formation of the resin-I₅. 5. Prepare the triiodide-pentaiodide (I₃-I₅) solution by dissolving the I₂ in the KI solution with gentle agitation and heating of the reaction container (to maintain the 45°C). (a) Container should be sealed until the iodine is completely dissolved. (b) Heating will be necessary to maintain the temperature at 45°C, since the reaction is endothermic. (c) Agitate solution in a fashion that prevents splashing onto the sides of the container. (d) The iodine must be completely dissolved . Continue agitation and heating (limit 45°C) until there are no undissolved particles remaining. 6. Prepare the measured Cl⁻ form of resin (step 1) for addition to I₃⁻ and I₅⁻ solution. (a) Remove excess water above and surrounding the beads. Do this by either a drain in the bottom of the container or by inserting a tube to the bottom of the resin and removing the water by suction or siphon. In either case, use care not to remove any resin. (b) Proceed to step 7 without delay so that beads will remain moist and at 45°C. 7. Add the prepared and measured Cl⁻ form of resin (step 6) to the I₃⁻ - I₅⁻ solution. (a) Add the resin in increments to the solution. A scoop or similar device may be used. Be sure none of the resin adheres to the mouth or sides of the reaction container. (b) After each increment of resin is added, agitate the reaction container as before. This will disperse the beads, cover them with solution, and redissolve any I₂ that may have precipitated due to water added in the resin increment. (c) Do not add water along with the resin. If any water appears in the resin container, remove it as outlined in step 6a above, before continuing. 8. Allow the resulting polyiodide resin to stand at room temperature until adsorption is complete. (a) Observe the color of the supernatant. When the color no longer changes, the reaction is complete. (b) Occasional swirling of the polyiodide resin will speed up the adsorption. 9. Wash the polyiodide resin. (a) Remove (as in step 6a) and discard all the liquid above and surrounding the polyiodide resin. (b) Add a volume of distilled water equal to approximately double the volume of the polyiodide resin. Let stand for at least 15 minutes, swirling occasionally. (c) Repeat steps 9a and 9b testing each discarded wash for iodine residual, until the desired concentration is reached. CALCULATION PROCEDURES The information needed for the calculations is listed below (values used for the sample calculations are given in parentheses). A. Final volume of resin-I₅ desired (10 liters) B. Exchange capacity of resin, wet volume (1.4 eq/l) C. Desired % resin sites triiodinated (97%) D. Desired % I₃⁻ sites pentaiodinated (70%) E. Equivalent weight of Potassium Iodide (166.01 g/eq) F. Equivalent weight of Iodine (253.80 g/eq) G. Volume Cl¹ form of resin needed (see Step 1) H. Weight potassium iodide needed (see Step 2) Note: 1. Values for items A, C and D may be changed as desired to fit requirements. 2. Value for B varies for each resin and is supplied by the manufacturer. 3. E and F are constants. 4. Values for G and H will be calculated during steps 1 and 2 below. Sample Calculation Step 1. Volume Cl⁻ form of resin needed (compensate for 12.2% shrinkage) Formula: (A) ÷ (.878) = liters resin needed Example: (10 liters) ÷ (.878) = 11.390 liters Cl⁻ form of resin Step 2. Weight potassium iodide needed. Formula: (G·B·E·C) = grams potassium iodide needed Example: (11.390 l)(1.4 eq/1)(166.01 g/eq)(.97) = 2568 g KI Step 3. Volume water needed Formula: (H ÷ E) ÷ (9 mole/kg) = kilograms water needed Example: (2568 g ÷ 166.01 g/mole ÷ (9 mole/kg) = 1.719 kg water 1.719 kg water equal 1.719 liters Step 4. Weight iodine needed Formula: (G·B·F·C) + (G·B·F·C·D) = grams iodine needed Example: (11.390 1)(1.4 eq/1)(253.809 g/eq)(.97) = 3926 g I₂ (11.390 1)(1.4 eq/q)(253.809 g/eq)(.97)(.70) = 2748 g I₂ Total 6674 g I₂

Claims: A method for preparing a polyiodide strong base anion exchange resin disinfectant containing a high concentration of I₅⁻ exchange sites, comprising the steps of: (a) contacting granules of a strong base anion exchange resin in chloride (Cl⁻) form with an aqueous treating solution containing I₅⁻ ions and I₃⁻ ions and (b) washing said resin with an aqueous wash to remove exchanged Cl⁻ ions therefrom, characterized in that the combined concentration of said I₅⁻ and I₃⁻ ions is at least 8 molal, at least 40% thereof being I₅⁻ and that contacting is carried out at a temperature of from 30 to 60°C so that at least 70% of the anion exchange sites of the resin have exchanged Cl⁻ for I₃⁻ or I₅⁻. The method according to claim 1 characterized in that the I₃⁻ and I₅⁻ ions are present in a stoichiometric amount in relation to the amount of said resin granules so that 70 to 99% of the strong base anion sites are exchanged. The method according to claims 1 and 2 characterized in that the concentration of I₃⁻ and I₅⁻ ions is 8 to 10 molal and that the aqueous solution is essentially free of undissolved iodine. The method according to any of the previous claims, characterized in that contacting is carried out at a temperature of 40 to 50°C. The method according to any of the previous claims, characterized in that the resin is a quaternary ammonium resin. The method according to any of the previous claims, characterized in that the resin beads are formed of a styrene resin having quaternary ammonium sites linked to a styrene backbone by phenylmethyl chains. The method according to any of the previous claims, characterized in that 50 to 90% of the combined concentration of the I₅⁻ and I₃⁻ ions is I₅⁻ and that the aqueous solution contains I₅⁻ and I₃⁻ ions in such an amount in relation to the resin granules so that 70 to 99% of the anion sites are exchanged in the same I₅⁻ and I₃⁻ proportions as the treating solutions. The method according to any of the previous claims, characterized in that contacting is carried out at a temperature of about 45°C. The method according to any of the previous claims, characterized in that the aqueous solution has a combined concentration of I₅⁻ and I₃⁻ ions of 8.5 to 9.5 molal and that the solution is essentially free of undissolved iodine. The method according to any of the previous claims, characterized in that the aqueous solution has a combined concentration of I₅⁻ and I₃⁻ ions of substantially 9.0 molal and that it is essentially free of undissolved iodine. The method according to any of the previous claims, characterized in that the treating solution contains 60 to 80% I₅⁻ with 40 to 20% I₃⁻ and that contacting is carried out so that the resin contains I₅⁻ and I₃⁻ ions in essentially the same proportions as the treating solutions and that 90 to 99% of the resin sites are exchanged. The method according to any of the previous claims, characterized in that the aqueous solution is an aqueous solution of potassium iodide (KI) having an I⁻ concentration of 8 to 10 molar, that fractions of the total amount of the quaternary ammonium exchange resin are incrementally contacted with the treating solution so that at least 90% of the quaternary resin sites exchange Cl⁻ for I₅⁻ or I₃⁻ ions, and that all solutions have a temperature of 40 to 50°C. The method according to claim 12 characterized in that the treating solution contains from 60 to 80% I₅⁻ with 40 to 20% I₃⁻ ions and that contacting is carried out so that the resin contains I₅⁻ and I₃⁻ ions in essentially the same proportions as the treating solution. The method according to claims 12 and 13 characterized in that the treating solution contains a stoichiometric amount of I₅⁻ and I₃⁻ ions so that about 96 to 98% of the quaternary ammonium resin sites are exchanged for I₅⁻ and I₃⁻ ions.

Inventors: BRIDGES RONALD L, FINA LOUIS R, LAMBERT JACK L, BRIDGES, RONALD L., FINA, LOUIS R., LAMBERT, JACK L.
Applicants: UNIV KANSAS STATE, KANSAS STATE UNIVERSITY RESEARCH FOUNDATION
Application year: 1990
Main classification: B01J41
IPC codes: B01J41, A01N59, B01J47