Abstract:
Copolyamide desalination membranes formed by interfacial polymerization on a microporous support are disclosed. The copolyamide is formed by copolymerization of m-phenylene diamine with cyclohexane-1,3,5-tricarbonyl chloride and any of isophthaloyl chloride, terephthaloyl chloride, or cyclohexane dicarbonyl chlorides wherein the average functionality of the acyl chlorides is from 2.20 to 2.40.

Description:
CROSS REFERENCE TO RELATED APPLICATION 
     This application is a continuation-in-part of Ser. No. 07/341,037 filed Apr. 20, 1989. 
    
    
     FIELD OF THE INVENTION 
     The present invention relates to composite membranes suitable for use in reverse osmosis processes such as the desalination of aqueous solutions. More particularly the present invention relates to a multilayer membrane in which one layer is a copolymer of meta-phenylenediamine with cyclohexane-1,3,5-tricarbonyl chloride and at least one difunctional acyl chloride. 
     BACKGROUND OF THE INVENTION 
     Permselective membranes suitable for use in desalination of aqueous solutions are the subject of numerous patents. U.S. Pat. No. 4,719,062 discloses permselective multilayer membrane in which there is a microporous polysulfone substrate layer and a superposed polyamide layer made from an aromatic diamine and trimesoyl chloride or cyclohexane-1,3,5-tricarboxyl chloride optionally containing up to 50% of either terephthaloylchloride or isophthaloyl chloride. Cadotte U.S. Pat. No. 4,277,344 permselective multi-layer membranes in which there is a microporous polysulfone substrate layer and a superposed polyamide layer made from an aromatic triacid halide and an aromatic diamine. Scala et al. U.S. Pat. No. 3,744,642 discloses multilayer membranes in which one layer is a porous substrate and the juxtaposed layer is a polyamide, a polyphenylester, or a polysulfonamide. Weyland et al. U.S. Pat. No. 3,649,687 discloses the use of 1,3,5-cyclohexane tricarbonyl chloride in the production of crosslinking agent: 1,3,5-cyclohexane triisocyanate. U.S. Pat. Nos. 4,520,044 and 4,529,646 disclose permselective multilayer membranes in which there is a microporous polysulfone support and a polyamide layer made using 1,3,5-cyclohexane tricarbonyl chloride and a diamine. 
     U.S. Pat. No. 4,626,468 discloses permselective multilayer membranes in which there is a microporous polysulfone support and a polyamide layer made from meta-phenylenediamine and based on polymerized acid chloride present from 10 to 80 weight percent repeating units derived from trimesoyl chloride, 90 to 15 weight percent repeating units derived from cyclohexane-1,3,5-tricarbonyl chloride and up to 40 weight percent repeating units derived from isophthaloyl chloride, terephthaloyl chloride or mixtures thereof. 
     U.S. Pat. No. 4,783,346 discloses a multistage process for preparing interfacially polymerized polyamide reverse osmosis membranes on a microporous support. The process involves first applying a solution containing from 1 to 10 wt % of an aromatic diamine having 1 or 2 rings and then a solution of a mixture of acyl chlorides having a combined average per acyl chloride-containing molecule of 2.2 to 4 acyl chloride groups in a solvent immiscible with the first solvent applied to the microporous substrate. Then a solution of different acyl chlorides is applied to the substrate. The individual acyl chlorides in this second solution can have 2.2 to 4 acyl chloride groups attached to an alkylene aliphatic group of 4 to 12 carbon atoms or an aromatic or cycloaliphatic group having 1 or 2 rings and containing 6 to 14 carbon atoms. 
     U.S. Pat. No. 4,643,829 discloses a multilayer membrane for performing reverse osmosis comprising a porous support and a layer formed of poly(meta-phenylenecyclohexane-1,3,5-tricarboxamide). 
     SUMMARY OF THE INVENTION 
     The present invention is a multilayer membrane comprising a microporous support layer and a superposed layer of a copolyamide derived from m-phenylenediamine with cyclohexane-1,3,5-tricarbonyl chloride and either cycloaliphatic or aromatic diacyl chlorides. 
     In a preferred embodiment the microporous substrate is a polysulfone, and the average pore size of polysulfone is less than about 20 nanometers in diameter The substrates used were tested and no pores of greater than 100 nm were detected. Our electron photomicrography indicated that few pores are more than five or ten nanometers in diameter. 
     A convenient method of preparation of the membrane of the invention is by interfacial condensation polymerization, that is contacting the polysulfone substrate with a solution of meta-phenylenediamine, and then contacting the polysulfone substrate with a solution of the acid chlorides being used. The cyclohexane tricarbonyl chloride used can be the cis form, the trans form or mixtures thereof. This method yields very thin films since the reaction is diffusion controlled and self-limiting. 
     In the membranes of this invention the microporous substrate will normally be about 0.5 to 5 mils thick, and the copolyamide layer will normally be about 20 to 200 nanometers thick. 
     DETAILED DESCRIPTION 
     The procedures of Cadotte U.S. Pat. No. 4,277,344 or Sundet U.S. Pat. Nos. 4,520,044, 4,719,062 or 4,529,646 are illustrative of the conditions needed for preparing composite membranes of this type. The process consists essentially of several steps, as set forth below: 
     A microporous substrate with an average pore size of less than 20 nm in a diameter is prepared. This may be accomplished with a polysulfone, cast from a 15% solution thereof in dimethylformamide and immediately quenched in water to precipitate the polysulfone and extract the solvent. The adequacy of quality of these membranes is conveniently checked by a programmed pressurization with nitrogen to determine that the amount of nitrogen passed at up to 200 psi is very small. 
     This miscroporous substrate (dried and stored, or fresh and wet) is then loaded with an aqueous solution of the aromatic diamine at a concentration of 0.5-10%, preferably 1--3% in the water, and the excess solution removed from the surface by some draining, rolling or sponging procedure. The concentration of the diamine is an important factor in the performance of the resulting composite. Too low a diamine concentration results in a sacrifice in salt rejection with a gain in flux. Too high a concentration of diamine results in a loss in flux. 
     If desired the cast polysulfone can be quenched in an aqueous solution containing 0.1-10% by weight, preferably 0.5-5% by weight and most preferably 1-3% by weight aromatic diamine. This technique often produces a composite membrane superior to that obtained using the two step aqueous quench followed by loading with diamine process described above. 
     The loaded substrate is then immersed in a solution of the mixed acid chlorides in Freon® TF chlorofluorocarbon liquid or hexane or mixtures thereof (solvents which do not adversely affect the porous structure of the polysulfone substrate) for 5-90 seconds, preferably 10-35 seconds at room temperature. Formation of the polyamide causes the originally shiny substrate to develop a dull finish. 
     The resulting composite is then dried at temperatures of 20°-100° C., preferably 50° -70° C., for periods of 5-180 seconds, preferably 15-60seconds, to establish adhesion of the surface polyamide to the polysulfone substrate. 
     The residual diamine and reaction byproducts are extracted by soaking in water, or preferably in a plurality of aqueous solutions of a lower alkanol followed by soaking in water. This is suitably done at temperatures of 20° to 70° C. 
     The present invention relates to the discovery that copolyamide rejection layers prepared with mixtures of cyclohexane-1,3,5-tricarbonyl chloride and a variety of bifunctional cyclic acid chlorides show minimum salt passages at functionalities in the range of 2.20-2.40. The preferred acyl chloride functionalities for the copolymers containing terephthaloyl chloride is 2.23-2.30. The preferred acyl chloride functionalities for the copolymers containing isophthaloyl chloride is 2.23-2.38. At higher functionalities the flux constants trend higher at some sacrifice to salt rejection and at lower functionalities the salt rejection deteriorate catastrophically. This is a preferred composition range. (Functionality is the apparent average number of carbonyl chloride groups present per acyl chloride reactant molecule of the mixture of di- and trifunctional acyl chlorides present in the reactant solution). 
     The most important factors in the preparation of a salt-rejecting layer on a composite membrane by the process of interfacial polyamidation, in addition to concentration of reactants appear to be: 
     (a) the functionality of the acid chloride which determines in large part the time and conversion (in polyamide formation) at which a cross-linked polyamide gel is formed and separates from solution, and 
     (b) those other structural features (geometry, etc) of the reactants that determine the transient solubility of the polyamide in the poor solvents normally employed in the formation of such composites. 
     The advantage gained by modifying the cyclohexane tricarbonylchloride with cyclic diacid chlorides quite clearly derives from a changed morphology in the polyamide deposit, but whether this change results from the decreased degrees of branching or from the increased solubility of the polyamide chain or from the lower concentration of carboxyl groups in the final polyamide has not been definitely established. At average functionalities below the optimum for any particular diacid dichloride the salt rejection of the polyamide deposit begins to deteriorate rapidly. This may simply be the effect of the lost branching function. 
     At minor modification (15 to 40% with functionality 2.81 to 2.53) the primary effect of the cyclic difunctional acid chlorides is to increase the flux of the membrane, often with increased salt passage. At 50 to 75% (with functionality 2.43 to 2.20), however, (using cyclic difunctional acid chlorides) the flux decreases along with the salt passage. At 75% (using cyclic difunctional acid chlorides with functionality 2.20) the system begins to fail with a rapid increase in both salt passage and flux becoming apparent at about 80% (with functionality 2.16). 
     The interfacial polyamidation process by which the polyamide layer is formed largely determines the conditions: suitable temperatures are from 0° C. to the boiling point of the organic solvent employed, suitable pressures are near atmospheric, with reaction times of 5 to 100 seconds. Substituent groups in the diacid chloride must not interfere with the polyamidation reaction. 
    
    
     EXAMPLES 
     EXAMPLE 1 
     Copolyamides of m-phenylenediamine with cyclohexane-1,3,5,-tricarbonyl chloride and terephthaloyl chloride. 
     A 16% solution of Udel P3500, a polysulfone derived from bisphenol A and p,p 1  -dichlorodiphenyl sulfone having a molecular weight of about 35,000, in N,N-dimethylformamide, containing 0.2% Gafac RE610 (a surfactant which is a free acid, derived from a complex organic phosphate ester) and 0.6% water, was cast on a glass plate with a Gardner knife set at 6 mils (0.15 mm), then quenched promptly in deionized water, extracted in deionized water for three minutes before loading with aqueous m-phenylenediamine for three minutes at the concentrations indicated in Table 1 below. The microporous substrates so obtained exhibit relatively smooth surfaces with pores averaging less than 20 nm in diameter as seen with an electron microscope. Much larger pores (more than 100 nm in diameter) adversely affect salt rejection, but are difficult to find by microscopy. Their frequency was qualitatively assessed by measuring the amount of nitrogen gas forced through the wet substrate as the gas pressure was increased slowly (1 psi per second) up to 200 psi. For a substrate area of 50 cm 2 , a volume of less than 10 ml of N 2  and preferably less than 5 ml was sought in this test. After removal of the surface droplets by rolling with a soft sponge rubber roller, the loaded polysulfone substrate was immersed in a solution of the acid chlorides in FREON TF (1,1,2-trichloro-1,2,2-trifluoroethane), at the concentrations indicated in Table 1. After 15 seconds of immersion, the membranes were drained for five seconds, then rinsed in FREON TF for ten seconds before drying in air for five minutes. The membranes were extracted in 15% aqueous ethanol at 25° C. for five minutes, 10% aqueous ethanol at 45° C. for five minutes, 5% aqueous ethanol at 65° C. for five minutes and in water at 80° C. for five minutes before storing in deionized water. Their permeability properties were determined in magnetically-stirred test cells of a standard design after a preliminary flush for one hour with a 15% aqueous ethanol solution at 70-80 psi (483-552 kPa). Measurements were made at 225 psi (1551 kPa) feed pressure with a feed solution containing 0.2% sodium chloride and 0.02% sodium azide as biocide. All the data presented were obtained after 16-22 hours of operation. 
     In the tables MPD stands for m-phenylenediamine, HTMesCl stands for cyclohexane-1,3,5-tricarbonyl chloride, Ratio stands for the weight ratio of HTMesCl to the difunctional acyl chloride being used, Fncl stands for functionality which is average number of acyl chloride groups present per acyl chloride molecules present, %SP stands for % salt passage, and Kw is determined by the formula ##EQU1## 
     
                       TABLE 1______________________________________                        RatioMPD     HTMesCl   TCl   HTMesCl/     % SP/Run  %       w/v %     w/v % TCl     Fncl.                                     Kw______________________________________1-a  1.4     0.16      --    100/0   3.00 2.52/8.831-b  &#34;       0.096     0.064 60/40   2.53 2.33/9.751-c  &#34;       0.080     0.080 50/50   2.43 1.68/8.991-d  &#34;       0.064     0.096 40/60   2.33 2.63/8.08                                     1.81/8.531-e  &#34;       0.056     0.104 35/65   2.29 1.78/7.401-f  &#34;       0.048     0.112 30/70   2.24 1.76/7.051-g  &#34;       0.040     0.120 25/75   2.20 1.96/6.581-h  &#34;       0.032     0.128 20/80   2.16 4.19/6.18                                     2.75/6.631-i  1.7     0.064     0.096 40/60   2.33 2.85/8.00                                     1.96/7.701-j  &#34;       0.056     0.104 35/65   2.29 2.05/7.401-k  &#34;       0.048     0.112 30/70   2.24 3.38/6.63                                     1.81/6.951-l  &#34;       0.040     0.120 25/75   2.20 2.31/6.361-m  2.0     0.080     0.080 50/50   2.43 3.30/7.721-n  &#34;       0.056     0.104 35/65   2.29 2.09/7.081-o  &#34;       0.048     0.112 30/70   2.24 1.76/6.751-p  &#34;       0.032     0.128 20/80   2.16 2.19/6.68______________________________________ 
    
     EXAMPLE 2 
     Copolyamides of m-phenylenediamine with cyclohexane 1,3,5-tricarbonyl chloride and isophthaloyl chloride. 
     A solution in N,N-dimethylformamide containing 16% Udel P3500, 0.2% Gafac RE610 and 0.6% water was cast with a Gardner knife at a setting of 6 mils (0.15 mml) on a clean glass plate and quenched in deionized water at 23°-25° C. The microporous substrate so obtained was extracted for three minutes in deionized water, then soaked in a 1.4% solution of m-phenylenediamine in water for three minutes. This loaded substrate was rolled free of surface droplets with a soft sponge rubber roller, and immersed for 15 seconds in a solution of acid chlorides in FREON TF as indicated in Table 2 below. The membranes were then drained for 5-6 seconds, immersed in a 0.02 w/v% solution of cyclohexane-1,3,5-tricarbonyl chloride for 10 seconds, and finally dried for five minutes in laboratory air. 
     The membranes were extracted five minutes in 15% ethanol at 25° C., five minutes in 10% ethanol at 45° C., five minutes in 5% ethanol to 65° C. and five minutes in water at 80° C. They were tested in magnetically-stirred cells of standard design for 16-20 hours at 225 psi with a feed solution containing 0.2% sodium chloride and sodium azide as biocide. the permeability properties are expressed in the table below as percent salt passage and the flux constant, Kw, in meters/second/TeraPascal. In Tables 2 and 3 ICl stands for isophthaloyl chloride. 
     
                       TABLE 2______________________________________HTMesCl     IClRun  w/v %       w/v %   Ratio   Fncl.                                 % SP/Kw______________________________________2-a  0.080       0.080   50/50   2.43 1.13/8.022-b  0.064       0.096   40/60   2.33 0.88/6.922-c  0.048       0.112   30/70   2.24 1.22/6.082-d  0.032       0.128   20/80   2.16 12.14/4.71______________________________________ 
    
     Additional membranes, prepared by the same procedure, except for the final extraction at 75° C. instead of 80° C., were tested at different time intervals to confirm the results. 
     EXAMPLE 3 
     Copolyamides of m-phenylenediamine with cyclohexane-1,3,5-tricarbonyl chloride and cyclohexane-1,4-dicarbonyl chloride. 
     Substrates prepared as in the preceding example were loaded with 1.6% MPD at 25° C. for three minutes, then rolled free of surface droplets with a soft sponge rubber roller. They were reacted for fifteen seconds with mixtures of HTMesCl and cyclohexane-1,4-dicarbonyl chloride (the trans isomer) as indicated in Table 4 below, then with 0.02 w/v% HTMesCl for ten seconds before drying fo five minutes in the laboratory air. After extraction by the procedure described in the preceding example the membranes were subjected to the standard testing protocol and gave the following results after 22 hours. 
     
                       TABLE 4______________________________________HTMesCl     HTClRun  w/v %       w/v %   Ratio   Fncl.                                 % SP/Kw______________________________________5-a  0.120       0.032   79/21   2.74 3.37/8.945-b  0.080       0.065   55/45   2.49  2.28/10.755-c  0.064       0.077   45/55   2.39  2.01/11.455-d  0.048       0.090   35/65   2.29 1.76/9.86______________________________________