Use of polyimides as separation membranes.

Abstract: Polyimide-based separation membranes of this invention are made from polyimides having repeating units of the general formulas (A) and (B) wherein Ar₁ and Ar₃ are tetravalent aromatic radicals containing at least one aromatic ring, Ar₂ is a divalent aromatic radical containing at least one aromatic ring, R₁ and R₂ are organic radicals, R₃ to R₆ are monovalent hydrocarbon radicals, and n is an integer from 1 to 50 at a mole ratio (A)/(B) of 5/95 to 95/5, have high gas permeation coefficients, high mechanical strength, and excellent heat resistance, and are useful for separation and concentration of mixed gases.

Description: Field of the Invention and Related Art Statement : This invention relates to the use of polyimides as separation membranes and, more particularly, to polyimide-based separation membranes containing specific silicone blocks in polyimide matrixes. Polyimides from pyromellitic dianhydride and aromatic diamines, from biphenyltetracarboxylic dianhydrides and aromatic diamines, or from aliphatic acid dianhydrides and aromatic diamines have been disclosed in USP No. 4, 378, 400, Japan Tokkyo Kokai Koho Nos. 60-82, 103 (1985), and 60-257, 805 (1985) as polyimide-based materials for gas separation membranes. All of the polyimides reported, however, show low gas transmission rates and their application to gas separation requires a larger membrane area, which would increase the cost of separation and make commercialization difficult. Silicone membranes, for example of polydimethylsiloxanes, have been known for enrichment of oxygen. A membrane of this type has a high gas permeation coefficient but low mechanical strength, which has made it difficult to decrease the membrane thickness or eventually to increase the gas transmission rates. In addition, the membrane in question shows low gas permselectivity and it is mandatory to build a large apparatus to maintain an adequate gas separation capacity. Furthermore, mixed gases to be separated sometimes occur at elevated temperatures and, in such cases, the materials for separation membranes need to be heat-resistant and mechanically strong. Object and Summary of the Invention: This invention has resulted from the attempts to solve the above-mentioned problems and it is an object of this invention to provide novel separation membranes possessing high gas permeation coefficient and permselectivity, excellent mechanical property, thermal stability and low moisture resistancy. Another object of this invention is to provide polyimide-based separation membranes which have a microphase separated structure and perform excellently in gas transmission and gas separation with high mechanical properties and heat resistance. A further object of this invention is to provide polyimide-based separation membranes which are applicable to the separation and concentration of mixed gases and is particularly useful for the separation of oxygen and nitrogen. This invention relates to the use of polyimides as separation membranes wherein the polyimides have repeating units of the general formulas (A) and (B) wherein Ar₁ and Ar₃ are tetravalent aromatic radicals containing at least one aromatic ring, Ar₂ is a divalent aromatic radical containing at least one aromatic ring, R₁ and R₂ are divalent organic radicals, R₃ to R₆ are monovalent hydrocarbon radicals, and n is an integer from 1 to 50 at a mole ratio (A)/(B) of 5/95 to 95/5. According to this invention, the tetravalent aromatic radicals Ar₁ and Ar₃ in the repeating units of the general formulas (A) and (B) may, for example, be as follows: The aromatic radicals Ar₁ and Ar₃ in a given polyimide structure may be identical to each other or each may contain two or more different radicals. The divalent aromatic radical Ar₂ in the general formula (A) may be as follows: R₇ and R₈ are monovalent hydrocarbon radicals, and p and q are integers from 0 to 4. Like Ar₁ and Ar₃, the radical Ar₂ in a given polyimide structure may be one and the same radical or a mixture of two or more radicals. The organic radicals R₁ and R₂ and the hydrocarbon radicals R₃, R₄, R₅, and R₆ in the repeating unit of the general formula (B) are not limited to any particular radicals, but R₁ and R₂ are preferably any of wherein m is an integer from 1 to 3 and R₃, R₄, R₅, and R₆ are preferably methyl or phenyl. The integer n in the repeating unit of the general formula (B) is from 1 to 50, preferably from 1 to 30. The polyimides containing diaminosiloxane blocks to be used in this invention have the mole ratio of the repeating unit of the general formula (A) to that of the general formula (B) in the range of 5/95 to 95/5, preferably 10/90 to 90/10. Separation membranes of good properties and performance intended by this invention cannot be obtained if the mole ratio (A)/(B) falls outside of this range. A satisfactory gas permeation coefficient is not obtained at a ratio of less than 5/95 while sufficiently high heat resistance, mechanical properties, and gas permselectivity are not obtained at a ratio of more than 95/5. The polyimide-based separation membranes of this invention can generally be prepared by the react ion of aromatic tetracarboxylic acid dianhydrides, aromatic diamines, and diaminosiloxanes of the general formula (C) wherein R₁ and R₂ are divalent organic radicals, R₃ to R₆ are monovalent hydrocarbon radicals, and n is an integer from 1 to 50. Examples of the diaminosiloxanes of the general formula (C) useful for the preparation of the polyimide-based separation membranes of this invention include Such diaminosiloxanes may be used singly or mixed. The average of the integer n in the above-mentioned diaminosiloxanes is normally from 1 to 50, preferably from 1 to 30. The aromatic diamines from which the aromatic radical Ar₂ is derived in the preparation of the polyimide-based separation membranes of this invention should preferably show affinity to the diaminosiloxanes and contain at least two aromatic rings. The following processes are available for the preparation of the polyimide-based separation membranes described above. (1) A diaminosiloxane of the general formula (C) and the aromatic diamine are dissolved in a polymerization solvent, the tetracarboxylic acid dianydride is added as a solid or as a solution in the polymerization solvent, and the resulting mixture is allowed to react. (2) The tetracarboxylic acid dianhydride is dissolved or dispersed in a polymerization solvent, the diaminosiloxane is added and allowed to react, the aromatic diamine is then added as a solid or as a solution in the polymerization solvent and allowed to react. (3) The tetracarboxylic acid dianhydride is dissolved or dispersed in a polymerization solvent, the aromatic diamine is added as a solid or as a solution in the polymerization solvent, the diaminosiloxane is then added and allowed to react, and the aromatic diamine is added and allowed to react. (4) The tetracarboxylic acid dianhydride and all the amine components are simultaneously added to a polymerization solvent and allowed to react. (5) The tetracarboxylic acid dianhydride and all the amine commponents are introduced into a reactor, a polymerization solvent is added, and the mixture is allowed to react. Of the processes described above, the process (2) is best suited for the preparation of polyimide-based separation membranes containing a uniform dispersion of the diaminosiloxane blocks. Here, the tetracarboxylic acid dianhydride in whole is dissolved or dispersed in a polymerization solvent, a diaminosiloxane of the general formula (C) or its solution in the polymerization solvent is added to form siloxane-modified polybasic carboxylic acids of the formula wherein Ar₁, R₁, R₂, and R₃ to R₆ are as defined previously and the solution containing the acids is mixed with the aromatic diamine. A process such as this yields polyimide-based separation membranes containing microphase separated structures corresponding to the length of the siloxane blocks and showing excellent gas transmission, gas separation, mechanical properties, and heat resistance. The solvents applicable to the reaction in question are exemplified by aprotic polar solvents such as N-methyl-2-pyrrolidone, N,N-dimethylacetamide, dimethylformamide, dimethyl sulfoxide, and hexamethylphosphoramide, phenols such as m-cresol, o-cresol, m-chlorophenol, and o-chlorophenol, and ethers such as diethylene glycol dimethyl ether (diglyme), diethylene glycol diethyl ether, dioxane, and tetrahydrofuran. These solvents can be used singly or mixed. In addition, nonpolar solvents such as benzene, benzonitrile, butyrolactone, xylene, toluene, and cyclohexane may be used in part as levelling or emulsifying agent. Diethylene glycol dimethyl ether (diglyme) is particularly desirable as it is a good solvent for the diaminosiloxanes and is used preferably at a proportion of 30% by weight or more of the total polymerization solvent. The first-stage reaction for the preparation of the polyimide precursors is preferably carried out at a relatively low temperature of, for example, 50 °C or less. It is desirable for the polyimide precursors containing the diaminosiloxane blocks to have a molecular weight sufficiently high for the formation of films, namely to have a logarithmic viscosity (inherent viscosity) (η inh ) of 0.3 or more, preferably 0.5 or more, as determined in N-methyl-2-pyrrolidone at a concentration of 0.5 g/dl at 30 °C. The logarithmic viscosity is defined as η inh = ℓn(η rel )/c wherein c is the concentration of the polymer solution expressed in grams of the polymers per 100 ml of the solvent and (η rel ) is relative viscosity or the ratio of the flow rate of the polymer solution to that of the solvent as determined in a capillary viscometer. The polyimide precursors thus obtained are imidized in such manners as the following. (1) The precursor is directly dehydrated into polyimide by heating. (2) The polyamic acid solution is mixed with an imidization catalyst such as a tertiary amine or an acid anhydride, cast on a support such as a glass plate, and dehydrated at room temperature or under heat into polyimide. (3) The precursor is thrown into a large quantity of a poor solvent such as acetone and the separated powder is filtered and dried by heating to form polyimide. (4) The precursor is dehydrated in an imidization catalyst such as a tertiary amine or an acid anhydride or in an organic solution containing such a catalyst at room temperature or under heat to form polyimide. The following processes are applicable to the preparation of the separation membranes of this invention. (1) The polyimide precursor solution is cast on a support such as a glass plate and heat-treated. (2) The polyimide precursor solution is cast on a support, gelled by immersion in a bad solvent such as water, alcohol, and hexane, dried, and heat-treated. (3) The precursor is pre-imidized in a solvent, cast into a film, dried, and heat-treated. (4) The polyimide solution is cast on a support, gelled by immersion in a solvent as in (2) above, dried, and heat-treated. Of the above-mentioned processes, a desirable one is based on making the polyimide precursor solution into a membrane followed by the imidization reaction and another is based on dissolving the polyimides of this invention having the repeating units of the general formulas (A) and (B) at a specified mole ratio (A)/(B) ratio in an adequate solvent, making the solution into a membrane, and removing the solvent. The thickness of the membrane, although not subject to any restriction, normally ranges from 1 to 100 µ m . The membrane may be flat or hollow fibers. The formulations for the polyimide-based separation membranes of this invention may contain other resins, in particular other polyimides, antioxidants, heat stabilizers, ultraviolet absorbers, colorants, and fillers in addition to the aforesaid polyimides. The polyimide membranes thus prepared possess high heat resistance, gas transmission rates, permselectivities, and mechanical strength and are useful for separation membranes. The polyimide-based separation membranes of this invention excel in selective permeation of gases, possess sufficient mechanical strength and ease of handling required for practical applications, and are useful for enriching a desired component in mixed gases in many areas such as the following: recovery of helium from natural gas; concentration of hydrogen from the effluent stream in the hydrogenation reaction; enrichment of oxygen for the aeration in wastewater treatment, for the fermentation industries, for the boilers and incinerators requiring high combustion temperatures, for medical oxygen respirators, and for the aeration of fish farming ponds; for separation of oxygen, nitrogen, hydrogen, carbon dioxide, carbon monoxide, helium, argon, ammonia, alkanes (for example, methane and ethane), alkenes (for example, ethylene and propylene), steam, hydrogen sulfide, alkanols (for example, methanol and ethanol), and other gases and vapors separable by membrane permeation, for example, uranium and hexafluorouranium. Detailed Description of the Preferred Embodiments : This invention is explained in detail with reference to the accompanying examples and comparative examples, without being limited thereto. Example 1 Into a 500-ml four-necked flask fitted with a thermometer and a stirrer were introduced 32.2g (0.1 mole) of benzophe nonetetracarboxylic acid dianhydride (BTDA) and 500 g of diethylene glycol dimethyl ether (diglyme) with stirring, 9.0 g (0.0069 mole) of diaminosiloxane of the following structure (amine equivalent 650) was added slowly in drops, and the mixture was allowed to react for about 30 minutes. Upon completion of the reaction, 38.2 g (0.0931 mole) of bis(4,4′-aminophenoxyphenyl)propane (BAPP) was added and the mixture was stirred for 5 hours to yield a yellow transparent solution of polyimide precursors. The precursors showed a logarithmic viscosity of 0.7. The diglyme solution of the polyimide precursors thus obtained was cast on a glass plate with a doctor knife and the resulting thin membrane was heated at 60 °C for 30 minutes, at 180 °C for 30 minutes, and at 220 °C for 1 hour to yield a polyimide membrane with a thickness of 40µ m having a microphase separated structure. The polyimide membrane obtained was tested for tensile modulus of elasticity (ASTM D-882-64T), tensile strength (ASTM D-882-64T), elongation (ASTM D-882-64T), glass transition temperature (determined by TMA at a test speed of 10 °C/minute in an atmosphere of nitrogen), initial thermal decomposition temperature (temperature at which the 5% weight loss occurs by TGA), moisture absorption (determined at 23 °C and 78% relative humidity), and light transmission (determined at 500 nm). The results are shown in Table 1. The polyimide membrane was also tested for its performance as gas separation membrane with the aid of a gas permeability testing apparatus according to Japanese Industrial Standard JIS Z 1707. The results are shown in Table 2. Comparative Example 1 The reaction was carried out as in Example 1 using 32.2 g (0.01 mole) of BTDA, 41.0 g (0.1 mole) of BAPP, and none of the diaminosiloxane and the resulting solution of the polyimide precursors was made into a polyimide membrane as in Example 1. The polyimide membrane was tested, as in Example 1, for the basic properties and for the performance as a gas separation membrane. The results are shown in Tables 1 and 2. Example 1 Comparative example 1 Tensile modulus of elasticity (kg/mm²) 195 245 Tensile strength (kg/mm²) 10.1 14.5 Elongation (%) 17 13 Glass transition temperature (°C) 201 230 Initial thermal decomposition temperature (°C) 450 515 Moisture absorption (wt%) 0.5 1.0 Light transmission (%) 76.1 70.9 Examples 2 - 25 The reactions were carried out as in Example 1 using the reactants and the solvents shown in Table 3 and the resulting solutions of polyimide precursors were made into polyimide membranes with a thickness in the range of 20 to 40 µ m . The polyimide membranes were tested for the gas permeation coefficient and the permselectivity. The sults are shown in Table 3. The gas permeation coefficient was calculated from the relationship: gas permeation coefficient [cm³ (STP) · cm/cm² · sec · cmHg] = gas transmission rate [ m ℓ(STP)/m² · hr · atm] × membrane thickness (m) × 3.7 × 10⁻⁸ The following abbreviations are used in Table 3: NMP: N-Methyl-2-pyrrolidone DIG: Diethylene glycol dimethyl ether BTDA: 3,3′,4,4′-Benzophenonetetracarboxylic acid dianhydride BPDA: 3,3′,4,4′-Diphenylsulfonetetracarboxylic acid dianhydride 6FBDA: 4,4′-(Hexafluoroisopropylidene)diphthalic acid dianhydride PMDA: Pyromellitic dianhydride BAPP: 2,2-Bis[4-(4-aminophenoxy)phenyl]propane BAPS: Bis[4-(4-aminophenoxy)phenyl] sulfone BAPF: 2,2-Bis[4-(4-aminophenoxy)phenyl]hexafluoropropane TPE-Q: 1,4-Bis(4-aminophenoxy)benzene TPE-R: 1,3-Bis(4-aminophenoxy)benzene BisA-P: 4,4′-[1,4-Phenylenebis(1-methylethylidene)]bisaniline BisA-AF: 2,2-Bis(4-aminophenyl)hexafluoropropane FDA: 9,9-Bis(4-aminophenyl)fluorene GAPD: Bis(3-aminopropyl)tetramethyldisiloxane PSX-A: amine equivalent 1,280 (Mw = 2,560) PSX-B: amine equivalent 650 (Mw = 1,300) PSX-C: amine equivalent 472 (Mw = 944)

Claims: Use of Polyimides as separation membranes wherein the polyimides have repeating units of the general formulas (A) and (B) wherein Ar₁ and Ar₃ are tetravalent aromatic radicals containing at least one aromatic ring, Ar₂ is a divalent aromatic radical containing at least one aromatic ring, R₁ and R₂ are divalent organic radicals, R₃ to R₆ are monovalent hydrocarbon radicals, and n is an integer from 1 to 50 with the mole ratio of (A) to (B) falling in the range of 5/95 to 95/5. Use of polyimides as separation membranes according to claim 1 wherein Ar₁ and Ar₃ in the repeating units (A) and (B) are or radicals of the general formula wherein X is a single bond, -O-, -CO-, SO₂-, or -C(CF₃)₂-. Use of polyimides as separation membranes according to claim 1 or 2, wherein Ar₂ in the repeating unit of the general formula (A) is wherein R₇ and R₈ are monovalent hydrocarbon radicals and p and q are integers from 0 to 4, or a radical of the general formula wherein Y is a single bond, -C(CF₃)₂-, -O-, -C(CH₃)₂-, -SO₂-, -CH₂-, Use of polyimides as separation membranes according to any of the claims 1 to 3, wherein R₁ and R₂ in the repeating unit of the general formula (B) are -(CH₂) m -, wherein m is an integer from 1 to 3. Use of polyimides as separation membranes according to any of the claims 1 to 4, wherein R₃, R₄, R₅, and R₆ in the repeating unit of the general formula (B) are methyl or phenyl. Use of polyimides according to any of the claims 1 to 5 as separation membranes, wherein n in the repeating unit of the general formula (B) is from 1 to 30. Use of polyimides according to any of the claims 1 to 5 as separation membranes , wherein the polyimides have a microphase separated structure. Use of polyimides according to any of claims 1 to 7, as separation membranes for gases.

Inventors: FURUKAWA, MASAYA, FURUKAWA, NOBUYUKI, YAMADA, YASUHARU
Applicants: NIPPON STEEL CHEMICAL CO., LTD.
Application year: 1989
Main classification: C08G73
IPC codes: B01D71, C08G77, C08G73