A SEMIPERMEABLE MEMBRANE

Abstract: A membrane treating agent for rejuvenating and impro­ ving a rejection performance of a semipermeable mem­ brane, which contains an effective amount of a modified vinyl polymer having acetoxy groups and at least one group represented by the Formula (I) and/or (II): (1) -O--R-(-COOH) n (11) -O-R-(-COOH) n wherein R is a radical selected from the group consisting of aliphatic, aromatic and heterocyclic radicals having from 1 to 9 carbon atoms, and n is an integer from 1 to 3. Valuable modified vinyl polymers are obtained by reacting a partially saponified vinyl polymer with at least one carboxylic acid such as maleic acid, phthalic acid, succinic acid, butane tetracarboxylic acid and/or acid anhydrides or acid chlorides thereof.

Description: A MEMBRANE TREATING AGENT FOR REJUVENATING AND IMPROVING A SEMIPERMEABLE MEMBRANE This invention relates to a membrane treating agent for rejuvenating or regenerating and improving semipermeable membrane performance, especially for reverse osmosis and ultrafiltration membranes, to a membrane treated by the membrane treating agent and also to a treatment process using the membrane treating agent. In recent years, much. research and development has taken place in an effort to obtain an excellent semipermeable membrane which is useful for producing fresh or potable water from such sources as sea water or brackish water, for the treatment of polluted water, for the concentration of orange juice or milk and for the recovery of useful materials from such sources as metal plating sewage or electrodeposition painting sewage. This is desirable because such procedures are in need of no phase transition, no temperature change and use less energy than other purification methods. In general, the membrane performance of a reverse osmosis membrane is expressed in terms of both solvent permeability and solute rejection. Solvent permeability is the quantity of permeated solvent per unit period and unit area, generally in terms of m3/m2 day. Solute rejection (%) is calculated as follows: Solute Rejection (%) EMI1.1 wherein CO is the concentration of solute in the feed solution and C is the concentration of solute in the permeated. solution. At the present time, semipermeable membranes produced for reverse osmosis are composed of either asymmetric membranes or composite membranes. Asymmetric membranes have been produced from various polymeric materials such as cellulose derivatives, polyamides, polyimides, polybenzimidazo)es, polyarylene oxides, polysulfoneamides and other polymeric materials, in which the semipermeability of the membrane resluts from the function of a thin dense skin layer located at one surface of the membrane, with the remaining major part of the membrane providing a more porous supporting layer formed by the same polymer. On the other hand, the composite membranes such as those called "PA-300" and "NS-200", etc. have been developed recently, wherein the semipermeability results from the function of an ultrathin solute barrier layer of one material which is formed separately and is supported on an underlying porous substrate that may be made from a different polymer from the ultrathin film. The performance of the membrane is determined by the thickness of the thin dense skin layer or the ultrathin solute barrier layer. Accordingly, a thinner layer leads the membrane to higher performance, especially in respect of solvent permeability. It is accordingly difficult to obtain a high performance semipermeable membrane having good solute rejection, because the thin dense skin layer or the ultrathin solute barrier layer possesses poor resistance to deformation and abrasion at the time of membrane fabrication and of membrane element fabrication. In addition, when a semipermeable membrane made of cellulose acetate has been used for substantial periods of time, the decrease of rejection performance of the membrane may have been caused by hydrolysis of tlle membrane. Moreover, when semipermeable membranes or melnbralle elements are free of faults, defects in tlie thin dense skin layer or the ultrathin solute barrier layer may be caused by minor mechanical shocks or deformation during long term operation of reverse osmosis or ultrafiltration. Therefore, it is important to be able to treat the membrane with a supplemental material in order to improve or to rejuvenate the solute rejection performance of the membrane. Various materials have been hitherto proposed for improving the rejection performance of semipermeable membranes. For example, U.S. Patent No. 3,877,978 discloses such treatment using a supplemental polymeric material containing a substantial amount of acetyl groups comprising a copolymer of vinyl acetate and acids such as maleic acid, crotonic acid and lower alkyl esters of acrylic acid G.L. Dalton et al have recently reviewed the supplemental polymer coatings in revise osmosis improvement and regeneration in 1'DESALINATION'1 24, 235 (1978). But these materials could only be applied for rejuvenating a membrane which has degenerated over long term operation, or which has a mechanical defect. It is an object of the present invention to provide a membrane treating agent which is useful not only for rejuvenation of a degenerated semipermeable membrane but also for improvement of the semipermeable membrane without proportional decrease in the flow rate of water therethrough. Another object of the present invention is to provide a membrane treating agent which can be applied without troublesome procedures in use. In accordance with the present invention, the yield rate of the membrane and of the element can be heightened by apply ing the membrane treatment for overcoming the defects. The useful life of the membrane can be lengthened by means of the rejuvenation treatment. A high performance, particular ly rejection performance of the membrane, can be attained with a membrane treating agent of this invention to the previously unattained level of normal membrane fabrication methods. In the description which follows specific characterizations will be used and reference will be had to drawings and to specific examples all in the interest of clarity of explanation. These terms and references are not intended to define or to limit the scope of the invention, which is defined in the appended claims. IN THE DRAWINGS The Figure is a diagram showing change of the membrane performance of a semipermeable membrane treated with a membrane treating agent of the present invention. In the drawing, (1) represents initial membrane performance; (2) represents degenerated membrane performance; (3) represents rejuvenated membrane performance, and (4) represents improved membrane performance. Referring now to the modified vinyl polymers which are effective for rejuvenating and improving a rejection performance of semipermeable membranes in accordance with the present invention, each has an acetoxy group and at least one group comprising either or both of the Formulas (I) and (II): EMI4.1 (II) -o-R-(-CooH)n wherein R is a radical selected from the group consisting of aliphatic, aromatic and heterbcyclic radicals having 1 to 9 carbon atoms, and n is an integer from 1 to 3. Examples of groups represented by the Formula (I) are the following groups represented by the Formulas (A) to (G), the preferable ones being (A) and (B): EMI5.1 Examples of the groups represented by Formuls (II) are the following: (H) -O-CH2COOH (I) -O-CH2CH2COOH The modified vinyl polymers can be derived from homopolymers or copolymers of vinyl acetate. Ethylene, vinyl chloride, styrene, N-vinyl pyrrolidone etc. can be employed as a comonomer with vinyl acetate. In the concrete, the modified vinyl polymers of the present invention are polymers having repeating units represented by the Formula (III) as the polymer main chain: EMI6.1 wherein a, b and c are molar fractions which satisfy the following equations: 0.9 ) a , 0.2 a + b + c = t 0.8 ) b > b , 0.1 0.4 ) c > 0 and wherein X is at least one radical selected from the group represented by the Formulas (I) and (II) and Y is at least one radical selected from the group consisting of -OH, 5, -Cl, -Br, -I, -C6H5, and EMI6.2 Such groups represented by the Formulas (I) and (11) alter the vinyl polymer into a water soluble vinyl polymer having excellent affinity and adsorption-ability for semipermeable membranes, particularly for membranes made of cellulose acetate. By adding a semipermeable membrane with an effective amount of a modified vinyl polymer containing an acetoxy group and a group represented by the Formulas (I) and (11), the rejection performance of the membrane can be remarkably potentiated, even if the modified vinyl polymer is not insolubi lived. The modification is well achieved by reacting polyvinyl acetate, its copolymers and their partially or fully saponified polymers, with at least one compound selected from the group consisting of dibasic acids, tribasic acids, tetrabasic acids, acid anhydrides thereof and/or acid chlorides thereof 0 The more preferred modified vinyl polymers used in the present invention are modified polymers having the group represented by the Formula (A) or (B) and are obtained by reac- ting a partially saponified vinyl acetate with maleic anhydride or succinic anhydride. The molar fractions a, b and c in the modified vinyl polymer represented by the Formula (III) should satisfy the aforementioned equations, and should preferably satisfy the following equation: 0.8 ) a > 004 0.4 > b > 0.1 Q.2 ) c =) O Wlet the molar fractions aw b and c do not satisfy the above equations, it is not possible to obtain a modified vinyl polymer having good water solubility and excellent capacity for rejuvenating or improving the rejection performance of the membrane. Such modified vinyl polymers can be easily prepared by methods well known in prior-art, for example those disclosed in U.S. Patent-Noe 1,672,195 and Japanese Patent Publication No. 16,150/1965. OzB'of the representative methods for preparing the modified vinyl polymers is as follows: : 1) hydroJysing or saponifying a polyvinyl acetate with aqueous alkali or acid solutions, 2) reacting a partially saponified polyvinyl acetate with various carboxylic acids, for example, a dibasic acid such as succinic acid, maleic acid, phthalic acid, tribasic acids such as propane tricarboxylic acid, trimellitic acid, te-tra- basic acids such as butane tetracarboxylic acid and pyrromel- litic acid, and their acid anhydrides and their acid halides as well Tulle modified vinyl polymers of the present invention may also be obtained by reacting a partially saponified polyvinyl acetate with acrylonitrile or cyan ions and formaldehyde, and then hydrolising the resulting cyan ometiiylated or cyanoethylated polyvinyl acetate. The water solubility of the modified vinyl polymers obtained by reacting tije partially saponified polyvinyl acetate with the carboxylic acids depends on the reaction ratio of the carboxylic acids to the partially saponified vinyl polymers. When tlie reaction ratio of the carboxylic acids to the part icily sapoiiified vinyl acetate is lower, the solubility of tlie modified polymers becomes poor. However, these modified vinyl polymers can be converted to water soluble polymers by controlSing the pH in an aqueous solution by adding alkali hydroxides such as sodium hydroxide, potassium hydroxide or ammonium hydroxide, organic amines, etc. By ciiangiiig tlie water solubility (pH) of the modified vinyl polymers before and after treating the semipermeable membrane, rejection performance and performance durability of the semipermeable membrane can be controlled. But the modified vinyl polymers of the present invention have such good affinity and absorption-ability relative to the semipermeable membrane, that the membrane treating effect does not disappear even after long-term operation. The content of acetoxy groups contained in the modified vinyl polymers is preferably within the range of about 20 to 90 molar more preferably about 40 to 80 mols relative to the repeating units of the modified vinyl polymer chain. The insolubilization or fixation of the modified vinyl polymers may be achieved by treating various reagents which have reactivity to tlie groups represented by the Formula (I). Examples of such rea6reit include multivalent organic amines, etc. Tii membrane treating agent of tile present invention may be awl vied to semipermeable membranes having various shapes such ab films, tubes, or hollow fibers, or Loeb type asymmetric or composite membranes which comprise various organic polymers such as cellulose esters, ployamides, polybenzimidazoles, etc. The membrane treating agents of the present invention give an excellent effect to the semipermeable membrane comprising cellulose esters, partic ularly cellulose acetate. The membrane treating agents of the present invention are employed as either aqueous solutions, organic solvent solutions or dispersions, etc. containing an effective amount of the modified vinyl polymer, However, the membrane treating agents are usually used as aqueous solutions containing about 0.0001 to 1.0* by weight, preferably about 0.0003 to 0.01* by weight of the modified vinyl polymer. The pH of such aqueous solution is preferably about 3 to 9, more preferably about 4 to 8. The addition of surfactant to the aqueous solution may give good effects in somecases. Membrane treating can be achieved by well-known methods, for example dipping the membrane into the acqueous solution containing the membrane treating agent, spraying the aqueous solution on the membrane or, more easily, the membrane treating agent may be added to the feed solution during the operation of the reverse osmosis or ultrafiltration procedure. The following examples are illustrative of the invention: EXAMPLE 1 A modified vinyl polymer was prepared by reacting partially saponified polyvinyl acetate with maleic anllydride as follows: 10 grd-ms of partially saponified polyvinyl acetate (average molecular weight (MW):1700, degree of saponification: 40*) was dissolved in 100 milliliters of dimethylsulfoxide, after which 20 grams of maleic anhydride were added and stirred for 24 hours at room temperature. A white polymeric matti'i.'iI was obtained by mixing the aforementioned solution with 500 milliliters of water. The material was filtered, washed with 1()O milliliters of water and then dried for 24 liUlil'b iii a vacuum. This polylller was dissolved in a dilute ammonia water and was stored as a 10% solution having a pH of 7, at a room tempe. ature. The infrared spectra of this polymer showed strong absorption at 1730 cm-1 (ester linkage#VC=O) and 1240 cm -1 (esteric #VC-O), and a newsabsorption at 1575cm-1 (ionic carboxylate). EXAMPLE 2 A cellulose acetate asymmetric reverse osmosis membrane was evaluated under tlie following conditions: Feed : 3.5* sodium chloride Temperature : 25 0C Operating 2 pressure : 56 Kg/cn Flow Rate : lm/sec. Initially, tile asymmetric membrane exhibited a salt rejection of 98.7* and a water flux of 0.30m3/m2 day. The modified vinyl polymer obtained in Example 1 was added to a feed solution (3.5% sodium chloride) so that the polymer was supplied to tlie membrane at about 100 ppm while the evaluation was continued. After an hour, salt rejection improved to 99.35% and water flux was reduce to 0.25m3/m2 dey. After this' tlie feed solution was changed to fresh 3.5* sodiijiii chloride; performance improved by the treatment was maintained even after 24 hours test. This effect is illustrated in the drawing. The number (1) designates ills tidal membrane performance, and (4) in the drawing is improved membrane performance after treatment by this eawpi. EXAMPLE 3 A modified vinyl polymer was prepared by using succinic anhydride instead of maleic anhydride. The other conditions were the same as Example 1 The cellulose acetate asymmetric reverse osmosis membrane before treatment exhibited a salt rejection of 97.27* and a water flux of /.36m3/m2 day under the same conditions as Example 2. Membrane treatment was accomplished by adding the modified vinyl polymer to the feed solution at 10 ppm, while the evaluation was continued. After 24 hours the salt rejection 32 improved to 99037* and the water flux was reduced to O.33m /m day. This performance did not change after 24 hours' operation on a fresh sodium chloride solution. EXAMPLE 4 A cellulose acetate asymmetric membrane was immersed in an aqueous solution containing 0.15% of sodium bicarbonate and sodium carbonate for 20 hours at 30 C, in which the pH was 11. By this immersion the membrane performance was reduced by hydrolysis, the salt rejection decreased to'95.0% from 98.0* and the water flux increased to O.70ín3/m day froin 0.60m3/m2 day under the following conditions: Feed s 0.25* sodium chloride Temperature : 250C Operating 30 pressure 30 ppw of tlie modified vinyl polymer obtained in Example 1 were added to the solution and the evaluation was continued for all bour. Then membrane performance was rejuvenated, and found to eiIibjt a salt rejection of 97.7* and a water flux of 0.60m3/m2 day, wllich was maintained after 24 hours' operation using a fresh feed solution. EXAMPLE 5 Asymmetrie cellulose acetate membranes were piled on a polyethylene net ("Vexar" made by E.I. duPont de Nemours & Co.) and evaluated under the following conditions: Fuzed : 0.15* NaCl Operating Pressure: 30 Kg/cm2 Temperature : 250C The membrane performance was degenerated by deformation. Tlie membrane treatment was performed by using the modified vinyl polymer of Example 1 while the concentration was changed. The results are listed in Table 1. TABLE 1 Before Treatment Modified Vinyl After Treatment (degenerated) Polymer (concentration) (one hour Water flux Rejection (Z) Water flux (ppm) Rejection (%) (m3/m2. day (m3/m2 day) 80.1 - 1.13 0.5 95.8 - 0.76 82.7 - 1.06 7.5 97.8 - 0.67 82.5 - 1.08 15.0 98.0 - 0.67 82.5 - 1.10 30 98.5 - 0.60 EXAMPLE 6 The spirally wound cellulose acetate membrane element for sea water desalination (SC-5100 made by Toray Inc. of Tokyo, Japan), exhibited a salt rejection of 96% and a water flux of 2.1 m3day.element under the following conditions: 2 Operating Pressure : 56 Kg/cm2 Brine Flow Rate : 8 Liters/min. Recovery : 16% Feed Concentration : 3.5% sodium chloride 30 ppm of modified vinyl polymer was added to the feed solution, and after 5 hours' operations the salt rejection was improved to 99.24* and the water flux. was reduced to 1.6 m3 day element. This performance was maintained for 24 hours after the feed solution was changed to a fresh 3.5* sodium chloride solution. EXAMPLE 7 A spirally wound cellulose acetate membrane element for brackish water desalination (SC-3100 made by Toray, Inc. of Tokyo Japan) exhibited 98.1% salt rejection and 3.91 m3day. element water flux under the following conditions: Operating Pressure : 30 KG/cm2 Temperature : 250C Feed Solution : 0015 sodium chloride Recovery : 30% The membrane treatment was performed as in Example 6. After 5 hours'' operation salt rejection improved to 99.3% and the water flux was 3.33m3 day.element . Improved performance was maintained after 540 hours operation followed by treatment; the membrane exhibited 99.2* salt rejection and 3.2 m3-day.element water flux. EXAMPLE 8 A cellulose acetate asymmetric reverse osmosis membrane was evaluated in the same manner as in Example-2, but the membrane was deformed as in Example 5. The membrane per formance was 88% salt rejection and 0.4m3/m2. day water flux. This membrane was regenerated to 97% salt rejection and 0.32 m3/m2 day water flux, after the membrane treatment using an aqueous solution containing 50 ppm of the modified vinyl polymer of Example 1. This effect is also illustrated in Figure 1, where (2) is degenerated membrane performance and (3) is rejuvenated membrane performance. EXAMPLE 9 A two stage water desalination system using spirally wound cellulose acetate membrane elements was degenerated after 4000 hours operation. The degenerated performance of the first stage was rejuvenated by applying the membrane treating agent of Example 3. Tile rejection performance of the membrane element recovered from 912 to 93% with slight decrease of flux. The membrane treating agent was added at a level of 5 ppm in sea water for 10 minutes. This effect was maintained after 2000 hours operation which followed.

Claims: WE CLAIM: 1. A membrane treating agent for rejuvenating and improving the rejection performance of a semipermeable membrane, said membrane treating agent containing an effective amount of a moclified vinyl polymer having an acetoxy group and at least one group selected from the group con sisting of EMI15.1 (11) -O-R-(-COOH) n wherein R is a radical selected from the group con sisting of aliphatic, aromatic and heterocyclic radicals having from 1 to 9 carbon atoms, and n is an integer from 1 to 3. 2o A membrane treating agent according to Claim 1, wherein the group represented by the Formulas (I) and (11) comprises at least one group selected from the group consisting of EMI15.2 EMI16.1 3. A membrane treating agent according to Claim 1, wherein said modified vinyl polymer is a vinyl polymer derived from a homopolymer or copolymers of vinylacetate. 4. A membrane treating agent according to Claim 1, wherein the said modified vinyl polymer is a vinyl polymer represented by the Formula (III): EMI16.2 wherein a, b and c are molar fractions and satify the following equations: a + b + -1 0.9 > a > 0.2 0.8 > b > 0.1 0.4 > c > 0 X is at least one radical selected from the group represented by the Formula (I) and (II), Y is at least one radical selected from the group consisting of -OH, -H, -Cl, -Br, -I, -C2H5 and EMI17.1 5. A membrane treating agent according to Claim 4, wherein X is at least one radical selected from the group rep resented by the Formulas (A) to (I) in Claim 2, especial ly by Formula (A) or (B). 6. A membrane treating agent according to Claim 4 or 5, wherein Y is -OH. 7. A membrane treating agent according to Claim 4, wherein a, b and c satisfy the following equations: 0.8 > a > 0°4 > Q.1 0.2 c, G - > 0 8. A membrane treating agent according to Claim 1, wherein said modified vinyl polymer is derived from at least one polymer selected from the group consisting of polyvinyl acetate, copolymers comprising the reaction product of vinyl acetate and at least one comonomer of ethylene, vinyl chloride, styrene, N-vinyl pyrrolidone, and their partially or fully saponified polymers. 9. A membrane, treating agent according to Claim 1, wherein the modified vinyl polymer is a polymer comprising the reaction product of -(a) polyvinyl acetate, its copoly mers and their partially or fully saponified polymers and (b) at least one compound selected from the group consisting of dibasic acids, tribasic acids, tetrabasic acids, acid anhydrides thereof and acid chlorides there of. 10. A membrane treating agent according to Claim 1, wherein the membrane treating agent is an aqueous solution con taining about 0.0001 to about 1%, preferably about 0.0003 to O.O1* by weight of the modified vinyl polymer. 11. A membrane treating agent according to Claim 10, wherein the aqueous solution has a pH of about 3 to 9, preferably about 4 to 8. 12. A semipermeable membrane for liquid separation having improved rejection performance, in which the semiper meable membrane has attached thereto an effective amount of a modified vinyl polymer having an acetoxy group and at least one group represented by Formula (I) and/or (II) in Claim 1. 13. A semipermeable membrane having attached thereto a mem brane treating agent according to one of the Claims 2 to 11. 14. A semipermeable membrane according to Claim 12, wherein the semipermeable membrane comprises cellulose ester. 15. A semipermeable membrane according to Claim ] 2, wherein the semipermeable membrane comprises cellulose acetate or a mixture of cellulose acetate and another cellulose ester. 16. A semipermeable membrane according to Claim 12, wherein the semipermeable membrane has at least about 98.so 99.0* of rejection performance operated at 30 Kg/cm2, with an aqueous solution containing by weight 0.5% NaCl, at a temperature of 25 C, and at a pH of 6. 17. A process for preparation of a semipermeable membrane for liquid separation according to one or more of the Claims 12 to 16, comprising: (a) applying to the surface of a cellulose ester semipermeable membrane an aqueous solution con taining a modified vinyl polymer having an acetoxy group and at least one group represented by the Formulas (I) and (it): : EMI19.1 wherein R is a radical selected from the group consis ting of aliphatic, aromatic and heterocyclic radicals having from 1 to 9 carbon atoms, and n is an integer from 1 to 3; (b) improving the salt rejection of a semipermeable mem brane made of cellulose ester by contacting the mem brane with an aqueous solution containing a modified vinyl polymer having an acetoxy group and at least one group represented by the Formulas (I) and (11). 18. Use of a membrane according to one or more of the Claims 12 to 16 in a process for desalination of saline water by reverse. osmosis, the steps comprising (a) contacting the saline water under pressure with a reverse osmosis membrane comprising a cellulose ester, and (b) there after treating the reverse osmosis membrane with a mem brane treating agent of Claim 1 to provide the membrane having at least about 98% of salt rejection.

Inventors: HARUMIYA, NORIHO, KURIHARA, MASARU, UEMURA, TADAHIRO
Applicants: TORAY INDUSTRIES, INC.
Application year: 1980
Main classification: B01D13
IPC codes: B01D67