Process of preparing homogeneous resin-polyiodide disinfectants

Claim 2

The process of preparing a homogeneous resin-polyiodide disinfectant containing a pre-determined quantity of a selected polyiodide or mixture of polyiodides, comprising: (a) converting strong base anion exchange resin beads to the iodide(I - ) form, the equivalent exchange capacity of the combining sites of the resin being known, said iodide resin beads being contained in a reactor; (b) selecting the equivalent amount of crystalline iodine for reaction with the I - of the resin to produce the desired polyiodide disinfectant, said iodine being contained in a dissolver separate from said reactor; (c) circulating water in a recycling stream arranged to contact sequentially said iodine in said dissolver and said resin beads in said reactor, said circulating water gradually dissolving said iodine and carrying it as I 2 in a substantially saturated solution to said resin beads for absorption thereby, said water being free of halide ions; and (d) continuing said circulation until substantially all of said amount of crystalline iodine has been dissolved by said water and until substantially all of said I 2 has been absorbed by said resin beads.

Claim 3

The process of claim 1 in which said resin is a quaternary ammonium resin.

Claim 4

The process of claim 1 or claim 2 in which said water is maintained at a non-boiling temperature of not lower than 40° C.

Claim 5

The process of claim 1 or claim 2 in which said water is maintained at a temperature of from 60° to 95° C.

Claim 6

The process of claim 1 in which said equivalent of iodine is the amount required to convert all of the I - of said resin to triiodide (I 3 - ).

Claim 7

The process of claim 1 or claim 2 in which the equivalent amount of said iodine is the amount required to convert all of the I - of said resin to penta-iodide (I 5 - ).

Claim 8

The process of claim 1 in which said equivalent amount of iodine is the amount required to convert the I - of said resin to a mixture of triiodide (I 3 - ) and penta-iodide (I 5 - ).

Claim 9

The process of claim 1 in which said resin beads are contacted with said water in a bed of said beads which is fluidized by the flow of said water therethrough, said reactor being a fluidized bed reactor.

Claim 10

The process of preparing a homogeneous resin-triiodide disinfectant containing a pre-determined quantity of triiodide (I 3 - ), comprising: (a) converting quaternary ammonium anion exchange resin beads to the iodide (I - ) form, the equivalent exchange capacity of the combining sites of the resin being known, said resin beads being contained in a reactor; (b) selecting the equivalent amount of crystalline iodine for reaction with the I - of the resin on a stoichiometric basis to convert the quaternary ammonium sites to triiodide, said iodine being contained in a dissolver separate from said reactor; (c) circulating water in recycling stream arranged to contact said iodine in said dissolver and said resin beads in said reactor, said circulating water gradually dissolving said iodine and carrying it as I 2 in a substantially saturated solution to said resin beads for absorption thereby, said water being maintained at a non-boiling temperature of not lower than 40° C. and being free of halide ions; and (d) continuing said circulation until substantially all of said amount of crystalline iodine has been dissolved by said water and until substantially all of said I 2 has been absorbed by said resin beads.

Claim 11

The process of preparing a homogeneous resin-triiodide disinfectant containing a pre-determined quantity of triiodide (I 3 - ), comprising: (a) converting quaternary ammonium anion exchange resin beads to the iodide (I - ) form, the equivalent exchange capacity of the combining sites of the resin being known, said resin beads being contained in a reactor; (b) selecting the equivalent amount of crystalline iodine for reaction with the I - of the resin on a stoichiometric basis to convert the quaternary ammonium sites to triiodide, said iodine being contained in a dissolver separate from said reactor; (c) circulating water in recycling stream arranged to contact said iodine in said dissolver and said resin beads in said reactor, said circulating water gradually dissolving said iodine and carrying it as I 2 in a substantially saturated solution to said resin beads for absorption thereby, said water being maintained at a non-boiling temperature of not lower than 40° C. and being free of halide ions; and (d) continuing said circulation until substantially all of said amount of crystalline iodine has been dissolved by said water and until substantially all of said I 2 has been absorbed by said resin beads.

Claim 12

The process of claim 9 in which said resin beads are contacted with said water in a bed of said beads which is fluidized by the flow of said water therethrough, said reactor being a fluidized bed reactor.

Claim 13

The process of claim 9 or claim 10 in which said water is maintained at a temperature of from 60° to 95° C.

Claim 14

The process of preparing a homogeneous resin-penta-iodide disinfectant, comprising: (a) converting quaternary ammonium anion exchange resin beads to the iodide (I - ) form, the equivalent exchange capacity of the combining sites of the resin being known, said iodide resin beads being contained in a reactor; (b) selecting the equivalent amount of crystalline iodine for reaction with the I - of the resin on a stoichiometric basis to produce the penta-iodide disinfectant, said iodine being contained in a dissolver separate from said reactor; (c) circulating water in a recycling stream arranged to contact sequentially said iodine in said dissolver and said resin beads in said reactor, said circulating water gradually dissolving said iodine and carrying it as I 2 in a substantially saturated solution to said resin beads for absorption thereby, said water being maintained at a non-boiling temperature of not lower than 40° C. and being free of halide ions; and (d) continuing said circulation until substantially all of said amount of crystalline iodine has been dissolved by said water and until substantially all of said I 2 has been absorbed by said resin beads.

Claim 15

The process of preparing a homogeneous resin-penta-iodide disinfectant, comprising: (a) converting quaternary ammonium anion exchange resin beads to the iodide (I - ) form, the equivalent exchange capacity of the combining sites of the resin being known, said iodide resin beads being contained in a reactor; (b) selecting the equivalent amount of crystalline iodine for reaction with the I - of the resin on a stoichiometric basis to produce the penta-iodide disinfectant, said iodine being contained in a dissolver separate from said reactor; (c) circulating water in a recycling stream arranged to contact sequentially said iodine in said dissolver and said resin beads in said reactor, said circulating water gradually dissolving said iodine and carrying it as I 2 in a substantially saturated solution to said resin beads for absorption thereby, said water being maintained at a non-boiling temperature of not lower than 40° C. and being free of halide ions; and (d) continuing said circulation until substantially all of said amount of crystalline iodine has been dissolved by said water and until substantially all of said I 2 has been absorbed by said resin beads.

Claim 16

The process of claim 12 in which said resin beads are contacted with said water in a bed of said beads which is fluidized by the flow of said water therethrough, said reactor being a fluidized bed reactor.

Claim 17

The process of claim 12 in which said water is maintained at a temperature of from 60° to 95° C.