WATER PURIFICATION PROCESS AND APPARATUS EMPLOYING POLYPYRROLIDONE

Abstract: A process and an apparatus (10) for purifying water containing pathogens wherein a halogen selected from the group consisting of bromine or iodine is added to the water to be purified in a first treatment compartment in a quantity sufficient to purify the water and wherein the halogen is removed from the treated water, and wherein the water containing the halogen is brought into contact with polypyrrolidone (15) in a second treatment compartment for a period of time which is sufficient to form a complex of halogen an polypyrrolidone.

Description: This invention relates to a process for purifying water containing pathogens wherein a halogen selected from the group consisting of bromine or iodine is added to the water to be purified in a first treatment compartment in a quantity sufficient to purify the water and wherein the halogen is removed from the treated water. More specifically, the invention relates to methods and apparatus for the stepwise treatment of water for human or animal consumption preferably using iodine and the removal of the iodine to levels below that detectable by human taste or smell. It has long been known that elemental iodine posseses bactericidal, viricidal and cysticidal properties and that because of this biocidal action, it is ideal for use as a water purifying agent. U.S. Patent No. 3,408,295 discloses a method of purifying water for drinking purposes utilizing elemental iodine. However, it is also known that the use of iodine in the purification or drinking water is not widely used because, although sterile, the water has an objectionable odor, color and taste due to the iodine present. As a practical matter, the use of iodine to provide sterilized or purified drinking water is used only in emergency situations or where there is no other alternative available. To meet the requirements of potable water which also has acceptable taste, the iodine remaining after the treatment must be removed. U.S. Patent No. 4,367,149 discloses a method of removing this elemental iodine by the reaction of sodium or potassium thiosulfate. However, although the iodine is removed, there is left in its place other inorganic salts such as sodium iodide. Furthermore, unless the exact stoichiometric amount of thiosulfate is used, either some iodine or the excess thiosulfate will be present. Other chemical methods for removal of the elemental iodine from the treated water have been proposed. What is needed is a complexing agent, harmless to humans, which will act as a scavenging agent removing all the iodine but leaving nothing in its place. It is therefore a primary object of this invention to provide process or an apparatus using a complexing agent which will quickly and completely remove traces of iodine after its biocidal action has rendered the water safe for human and animal consumption. It is further an object of this invention to provide a simple and economical method or an apparatus for purifying and sterilizing water employing iodine or bromine which results in potable water which contains none of the characteristic taste or color of the elemental halogen employed as the biocidal agent. It is another object of this invention to provide a method or an apparatus in which the material employed to remove the halogen biocidal agent can be reactivated and reused repeatedly without loss in effectiveness. The primary object of the invention is realized in that the water containing the halogen is brought into contact with polypyrrolidone in a second compartment for a period of time which is sufficient to form a complex of halogen and polypyrrolidone. The polypyrrolidone enables to remove traces of the iodine in water. It is disclosed in the Canadian Patent No. 1,119,748, that polypyrrolidone also known as nylon 4, very readily forms a complex with iodine. It has been found that this tendency to form a complex with iodine is so strong that it acts effectively as a scavenger for iodine. Even very small amounts of iodine may be removed quickly and completely from an aqueous solution of iodine by contact with nylon 4 whereby the nylon 4 forms a complex with the iodine. The nylon 4 itself develops a pale yellow color while the solution which contained the dissolved iodine is rendered completly colorless. This result was surprising since it had previously been thought that an excess of iodine in the solution was necessary in order to drive the reaction toward the formation of the complex. The nylon 4 is preferably in a form having a maximum surface area available for complexing the iodine - e.g., tubing knit from a textured yarn is preferable over that knit from flat yarn. It has been found that amorphous or unoriented yarn is more effective than drawn yarn. Waste yarn formed when "spinning on the floor" while waiting for conditions in an extruder to stabilize is particularly useful. Nylon 4 "pulp" or fibrids are also useful. The invention will now be described in more details and with reference to figure 1 which gives a partial cross-section view of an embodiment of the invention for the apparatus for purification of water. It will be clear that the invention is not limited to the illustrated embodiment and that several modifications are possible. In the purification of water to obtain potable drinking water, iodine is introduced into the impure water by any method, e.g., the method disclosed in U.S. Patent No. 3,408,295 or in U.S. Patent No. 4,367,149, or by contracting the water with a nylon 4-iodine complex disclosed in Canadian Patent No. 1,119,748. Sufficient time is allowed for the iodine to destroy the microbial organisms present and then, in order to make the water potable, it is contacted with nylon 4 in a form which provides maximum surface area. Within a short time the water becomes colorless, all the iodine present having transferred to the nylon 4 where it is retained in the form of a complex. In this system where the nylon 4 is in considerable excess and the iodine concentration is very low, the equilibrium is virtually 100% in the form of the complex. If, on the other hand, a more heavily "loaded" nylon 4-iodine complex (say 5% iodine) is added to water, some of the iodine will leave the complex establishing an equilibrium where some of the iodine is in the water. This provides a means of introducing controlled amounts of iodine into the water. This purification system may be used to make small portions of potable drinking water in the field or adapted to a larger scale continuous purification process. In the case of larger scale purification systems it may be desirable to rejuvenate the nylon 4 sequestering agent. This is conveniently accomplished by contacting the nylon 4 containing complexed iodine with a solution of sodium bisulfite or sodium thiosulfate. The iodine will be completely removed leaving white nylon 4. The nylon 4 is then rinsed with water to remove the sodium bisulfite or sodium thiosulfate reaction products. The nylon 4 is then ready for reuse. Alternatively, the nylon 4 sequestering agent may be immersed in boiling water for a few minutes after which all the iodine will have been removed and the nylon 4 is ready for reuse. As mentioned above, it is desirable to use a form of nylon 4 which provides maximum surface area. For this reason, nylon 4 in staple form is better than, for example, untexturized knit tubing. The staple also packs well in a column. The ideal nylon 4 material is either a mat or staple form made from textured undrawn yarn. The unoriented fiber absorbs iodine more rapidly and the texturizing provides more surface area. This material also packs better in the column. It may be advantageous to wash the nylon 4 in whatever form it is used in hot water containing a detergent followed by rinsing to remove any finish or low molecular weight material which may be present. Where a complex of nylon 4 and iodine is employed to introduce iodine into the water to be purified, the complexed material should be washed before being contacted with the water in order to remove any excess iodine. The temperature of the water to be treated is not critical, but the temperature is desirably in the range from 0° to 40°C, and preferably in the range of 10° to 25°C. Figure 1 is a schematic representation of one embodiment of an apparatus for use in the practice of the process of this invention. Treatment chamber 10 is adapted to maintain complexed material 17 in a first treatment compartment and untreated nylon 4 material 15 in a second treatment compartment, and both in position within the flow path of the liquid to be treated. Chamber 10 may be a section of pipe fabricated from metal, opaque or transparent plastic, or from glass, which is provided with inlet 12 and outlet 14 to permit passage of the liquid. In order to facilitate installation of the complexed material, chamber 10 can be provided with a removable fluid-tight cap 16 at its upstream end and coupling 20 which permits separation of the chamber into two parts above the region in which the nylon 4 is retained. Perforated retainers 18 and 22 are securely fit within the interior of chamber 10 and are adapted to maintain the complexed material and nylon 4, respectively, in position and to permit free flow of the liquid through the chamber. Liquid inlet conduit 24 and outlet conduit 26 are adapted to fit in a fluid-tight seal with chamber inlet 12 and outlet 14, respectively. In the embodiment of Figure 1, pump 28 is adapted to fit with oulet conduct 26 to facilitate and control the rate of flow of the liquid through the treatment chamber 10, and thereby control the contact time of the liquid with the complexed material 17 and the untreated nylon 4 material 15. As will be apparent to one familiar with the art, pump 28 can be positioned upstream of chamber 10 on conduit 24, or the entire system can be gravity fed, with a valve or other restriction means replacing pump 28 to control the rate of flow of liquid through the chamber. Preferably there is a continuous flow of liquid through the chamber so that a continuous pyrifying process can occur. In the operation of the apparatus illustrated in the embodiment of figure 1, the water or other liquid to be treated enters chamber 10 through inlet conduit 24 and contacts a mass of complexed material 17. In a preferred embodiment the complexed material is in the form of yarn or fibers which comprise a non-woven structure through which the liquid will uniformly pass without channelling. During the liquid's contact with the complex of iodine and nylon 4, a predetermined amount of iodine passes into the liquid and functions as a biocide to eliminate bacteria contamination or other organisms which are present. The iodine containing liquid then passes through a similar mass of yarn or non-woven fiber of nylon 4, during which contact, the free iodine complexes with the nylon 4 and is removed from the liquid. The treated liquid discharged from conduit 26 is free of bacterial contamination and contains no iodine which is detectable by taste or odor. For convenience, the complex of nylon 4 and iodine is referred to in these examples as "complexed material". A complex of iodine with nylon 4 knit tubing was prepared as follows. Nylon 4 tubing, 68 grams, was soaked in several liters of water containing a few drops of liquid detergent for 2-3 minutes. Excess detergent solution was squeezed out of the tubing. An iodine solution was prepared by dissolving 56 grams of potassium iodide in approximately 100 ml. tap water followed by the addition of 28 grams of iodine crystals. When all of the iodine had dissolved the solution was diluted to 1400 ml. The wetted undrawn yarn was immersed in the iodine solution, with stirring, for approximately 5 minutes and then removed from the iodine solution, immersed in cold tap water, and rinsed twenty times to remove excess iodine. The treated yarn was hung to druy overnight. The dry complexed material was brown in color and contained approximately 10% iodine. The amount of iodine complexed with the nylon 4 material can be varied by adjusting the concentration of the iodine solution and the time during which the nylon 4 is in contact with the solution. Complexed material containing from 1% to 20% of iodine based on the weight of the nylon 4 material can be prepared for use in the invention, and complexed material containing from 5% to 15% of iodine are particularly suitable. In several of the examples which followed a glass column fitted with a filter at its base was employed. The glass filter has a sufficient pore size so that water flow through the apparatus is not unduly restricted. The filter column used in the examples was sterilized by exposure to ethanol overnight and between repacking of the column. Tubing used for sample collection was also sterilized with ethanol. The column and tubing were rinsed three times with sterile water prior to packing the column with the complexed material. The waste water sample was collected from a municipal sewage treatment facility located at Bethlehem, Pennsylvania, and stored at 4°C prior to use. The waste water sample consisted of treated, clarified, unchlorinated municpal waste water, with a pH of 5-6. Ten milliliter samples for coliform bacterial analysis were collected in duplicate. Samples were stored at 4°C and were analyzed and showed the presence of Gram negative lactose-germenting bacilli (coliform) and Gram positive staphylococci, streptococci and enterococci by enumeration of colony forming units/ml on MacConkey agar and Columbia Colinstin Naladixic Acid agar, respectively. Colorimetric assays for iodine in aqueous solutions were employed having a lower level of detection of 2 micrograms per millilter ("2µg/ml"). Example 1 A saturated solution of elemental iodine was prepared by adding a sufficient quantity of elemental iodine crystals to one liter of water at room temperature so that undissolved crystals remained after allowing the mixture to stand for a few hours. The liquid was then decanted from the crystals. 50 grams of suitably washed knit tubing made or 100% drawn nylon 4 yarn was immersed in the saturated aqueous iodine solution and within 5 minutes the water was colorless, all the iodine having complexed with the nylon 4. No trace of the characteristic odor or taste of iodine remained in the treated water, and there were no pathogens present. Example 2 A saturated solution of iodine in water was prepared as described in Example 1 and the solution decanted from the crystals. The solution was divided into 2 parts of 500 ml each. To one part was added 5 grams of knit tubing made from drawn yarn and to the other part was added 5 grams of a bundle of undrawn yarn. The iodine was removed from solution more rapidly (150 seconds) when the undrawn yarn was used. The drawn yarn in the form of knit tubing required twice as long (300 minutes) to remove the iodine. Example 3 The procedure of Example 1 was followed, except that bromine water was substituted for the aqueous iodine solution. The nylon 4 tubing completely decolorized the bromine water within 5 minutes. Example 4 This example demonstrates the release of iodine from complexed material The process employed the steps of the filtration of sterile water through the complexed material, supported by the glass column described above, followed by quantitative analysis of iodine in the liquid effluent from the column. A pump was connected to the column in order to draw the water through it and vary the flow rate through the complexed material and nylon 4. Iodine was readily released from the complexed material upon the addition of water at room temperature. At a flow rate of 450 ml/min a concentration of iodine of 260 µg/ml was found to be present. Comparative Example 5 Sterile water and then waste water were filtered through untreated nylon 4 packed in the glass column described above followed by quantitative analysis for viable bacteria in the filtered water. Analysis of waste water samples collected at flow rates of 120 ml/min and 500 ml/min all showed Gram negative bacteria in a concentration of about 2 or 3 x 10³ CFU/ml, and Gram negative bacteria in a concentration of about 1 x 10² CFU/ml. No bacteria were found in the sterile water samples. Example 6 Waste water was sequentially filtered through complexed material and nylon 4 packed in the glass column described above, followed by quantitative analysis for viable bacteria and iodine in the liquid effluent from the column. A total of 16 liters of waste water was collected and analyzed. As the waste water passed through the column it was observed that iodine rapidly moved down the nylon 4 sample in the column. After 16 liters passed through the column, the iodine colored the top portion of the nylon 4 sample brown while the bottom portion was only a faint yellow. Samples were collected after 1 liter, 4 liters, 6 liters, 8 liters and 16 liters. Nylon 4 and the complexed material were used in a ratio 2:1, specifically 100gm:50gm. This ratio can be adjusted to prevent the excess leaching of iodine from the complexed material into the treated water and its passage through the nylon 4. Iodine was effectively removed by nylon 4 from the effluent which had first passed through the complexed material as shown by the presence of only 2 µg/ml of iodine in the effluent in all samples. In addition, all samples showed the complete absence of the Gram positive and Gram negative bacteria tested for. Example 7 A sample or unoriented nylon 4 yarn having a high surface area especially adapted for removing traces of iodine from water was made as follows : Filaments of nylon 4 were taken as they emerged from an extruder and collected on a tube in a take-up machine without the application of any finish, or alternatively, simply with the application of water. This undrawn yarn was then texturized, or crimped, and cut into short lengths to form a staple material which, unlike conventional staple, was unoriented. This material packs well in a glass column or filter cartridge with a minimum of voids. Being amorphous it complexes with iodine more rapidly and completely than other forms of fibers. Example 8 With reference to Figure 1, a treatment chamber 10 is for example fabricated from two sections of threaded steel pipe three inches in diamter which are joined by threaded coupling 20. Perforated retainers 18 and 22 are fabricated from steel screening having a mesh opening of one-eighth inch and securely fitted within the sections of the chambers, as illustrated. Approximately 50 grams each of complexed material 17 and untreated nylon 4 material 15 in the form of undrawn yarn are compressed lightly to form pads which are placed on the upstream sides of the retainers 18 and 22, respectively. The sections are joined by coupling 20, and threaded closures 16 having central apertures are placed on the inlet and outlet ends of chamber 10. Inlet conduit 24 and outlet conduit 26 are secured to the closure at either end of the chamber. A source of waste water from a municipal sewage treatment plant is tested for the presence of bacterial contamination and found to contain coliform, staphilococci, streptococci and enterococci bacteria contamination. Waste water to be treated is admitted from a source (not shown), into the chamber via inlet conduit 24, and pump 28 is activated ; the flow rate is adjusted until a steady flow rate is observed. The treated effluent from outlet conduit is sampled and tested for the presence of bacterial contamination and iodine. Plate assays performed as described above are negative, indicating the absence of bacterial contamination of the types originally determined to be present in the liquid stream before treatment. Tests for free iodine are also negative indicating that no iodine was present at the sensitivity levels of the test, e.g., less than 2 µg/ml.

Claims: A process for purifying water containing pathogens wherein a halogen selected from a group consisting of bromine or iodine is added to the water to be purified in a first treatment compartment in a quantity sufficient to purify the water and wherein the halogen is removed from the treated water, characterized in that the water containing the halogen is brought into contact with polypyrrolidone in a second treatment compartment for a period of time which is sufficient to form a complex of halogen and polypyrrolidone. A process as claimed in claim 1, characterized in that use is made of polypyrrolidone in a form having a high surface area to mass ratio. A process as claimed in claim 1, characterized in that the halogen is added to the water by contacting the water with a complex of iodine or bromine and polypyrrolidone. A process as claimed in anyone of claims 1 to 3, characterized in that said polypyrrolidone is washed in a solution of aqueous detergent prior to its contact with iodine. A process as claimed in anyone of claims 1 to 4, characterized in that the water is treated at a temperature in the range from 0° to 40°C. A process as claimed in claim 3, characterized in that the complex of polypyrrolidone and halogene containing from 8% to 12% iodine by weight based on the weight of polypyrrolidone is used. A process as claimed in anyone of claims 1 to 6, characterized in that the polypyrrolidone is regenerated by contact with a compound which decomplexes the halogen. A process as claimed in claim 7, characterized in that the compound is selected from the group consisting of sodium bisulfite and sodium thiosulfate. A process as claimed in claim 8, characterized in that the sodium thiosulfate and sodium bisulfite are in aqueous solution. A process as claimed in claim 8, characterized in that the polypyrrolidone is brought into contact with clean water for rinsing away the decomplexed halogen. Apparatus for water purification which comprises a treatment chamber having a water inlet and oulet opening, the chamber having a first treatment compartment adjacent the water inlet adapted to enable the addition of iodine to the water, said first treatment compartment containing a material which will introduce a halogen into the water, characterized in that said apparatus comprises a second treatment compartment adjacent the water outlet which contains polypyrrolidone in a form which is adapted to enable the uniform free flow of the treated water through the polypyrrolidone and formation of a complex of a halogen and polypyrrolidone to thereby remove the halogen from the water prior to its exit from the chamber. An apparatus as claimed in claim 11, characterized in that said material includes a complex of a halogen with polypyrrolidone in the first treatment compartment in a form adapted to enable the uniform free flow of the water through the complex of a halogen and polypyrrolidone to thereby add halogen to the water. An apparatus as claimed in claim 1 or 12, characterized in that it includes means for controlling the flow rate of the water through the treatment chamber. An apparatus as claimed in claim 13, characterized in that said means for controlling the flow rate comprises a pump. An apparatus as claimed in claim 13, characterized in that said means for controlling the flow rate comprises at least one valve. An apparatus as claimed in claim 15, characterized in that said treatment chamber is provided for receiving water by gravity feed through a conduit communicating with the inlet opening. An apparatus as claimed in claim 11 or 12, characterized in that said polypyrrolidone is in the form of a pad of textured undrawn yarn. An apparatus for treating an aqueous solution with halogen which comprises a conduit through which the solution is adapted to pass, the conduit having an inlet and an outlet. characterized in that the interior of the conduit contains polypyrrolidone material complexed with a halogen positioned between the inlet and the outlet. An apparatus as claimd in claim 18, characterized in the it includes means for controlling the flow rate of the aqueous solution through the polypyrrolidone material.

Inventors: BARNES, ARTHUR CONARD, BARNES, CARL EDMUND
Applicants: BARSON CORPORATION
Application year: 1989
Main classification: C02F1
IPC codes: C02F1