Production of high molecular weight polyhalobisphenol polycarbonates

Abstract: This invention relates to high molecular weight polyhalobisphenol polycarbonates which are produced by adding phosgene to a polyhalobisphenol in the alkali metal phenate form whereby the chloroformates of the bisphenol are formed and then adding an activated pyridine such as 4-aminoyridines or 2-substituted pyridines to generate a high molecular weight polycarbonate having an inherent viscosity in the range from about 0.4 to about 0.9. These high molecular weight polycarbonates have high glass transition temperatures, good solvent and fire resistance and good hydrolytic stability. These polycarbonates are suitable for use in preparing hollow fibers for gas separations.

Description: This invention relates to an interfacial process for the production of high molecular weight polyhalobisphenol polycarbonates using activated pyridine catalysts. It is known from U.S. 3,912,687 that tetrahalobisphenols have a reduced reactivity due to steric hindrance and low pK values and that the preparation of polycarbonate resins from these phenols using the interfacial technique can be accomplished with relatively large amounts of trialkylamine catalysts and a two-stage reactor. However, it has been found that this process gives low molecular weight resins. It is also known from U.S. Patent 4,286,085 and U.S. Patent 3,530,094 that substituted pyridine catalysts can be used to make high molecular weight polycarbonates from bisphenol A. However, U.S. Patent 4,286,085 teaches the addition of the catalyst before the phosgenation step and this does not give high molecular weight polycarbonates when tetrahalobisphenols are used. Other patents such as 2,970,131; 4,262,113; 4,286,085; and 4,291,151 generally teach the preparation of high molecular weight polycarbonates from tetrahalobisphenols but they do not have examples of the use of these hindered phenols for support. These known procedures adaptable to the preparation of high molecular weight bisphenol-A polycarbonate (U.S. 4,286,085, U.S. 2,970,131, U.S. 4,262,113, U.S. 4,286,086, U.S. 4,291,151) are not satisfactory for preparing high molecular weight polycarbonate (PC) from the hindered halobisphenols. The tetrabromobisphenol-A polycarbonates (TBBA-PC) prepared using these known procedures have inherent viscosity less than 0.3 (42,000 weight average molecular weight). The polymer obtained is brittle (see Controls 1-5). U.S. 3,912,687 describes the details of the preparation of TBBA-PC. The highest molecular weight reported is 50,000. The polymer has a relative viscosity of 1.18 or an inherent viscosity of 0.33. Generally, to possess a useful ductility, the polycarbonates must have a molecular weight higher than a critical molecular weight. It is found that the critical weight average molecular weight of TBBA-PC is 60,000 which corresponds to the inherent viscosity of 0.4 or the degree of polymerization of 35. For example, for applications such as solvent cast film or solution spinning fiber, the polycarbonate must have an inherent viscosity of above 0.4 so that tough film or fiber can be prepared. EP-A-242 147, which has an earlier priority date but is published after the priority date of the subject application, discloses high molecular weight carbonate homopolymers of 3, 3', 5, 5'- tetrabromo-or 3, 3', 5, 5' -tetrachlorobisphenol, having an inherent viscosity > 0.4. The present invention is directed to a process wherein high molecular weight polyhalobisphenol polycarbonates are prepared using activated pyridine catalysts. The resultant resins having an inherent viscosity greater than 0.4 and preferably in the range of from 0.4 to 0.9 are useful fire retardant polycarbonates. The resins have high glass transition temperature (Tg=265°C for the polycarbonate made from tetrabromobisphenol A), good solvent resistance and good hydrolytic stability. Tough film or fiber can be prepared from the polymer. The resins prepared from tetrabromobisphenol A are also useful to prepare hollow fibers for gas separations. The process of this invention comprises the following steps: (A) mixing a polyhalobisphenol, a halogenated solvent, and sufficient aqueous alkali metal hydroxide to obtain a mixture having said bisphenol in the alkali metal form, (B) adding phosgene and additional aqueous hydroxide to said mixture whereby the pH of said mixture is maintained in the range of from 8 to 13, whereby a mixture of bischloroformate and monochloroformate from the bisphenol are formed, (C) adding a catalytic amount of an activated pyridine selected from the group consisting of 4-aminopyridines and 2-substituted pyridines and additional aqueous hydroxide whereby said pH is maintained, and (D) recovering said high molecular weight polycarbonate. These polyhalobisphenols are well known from U.S. 3,912,687. They include aromatic dihydroxy compounds of the general formula in which R is chlorine, bromine, or mixtures thereof, and X is C₁-C₆ alkylene, cycloalkylene, a single bond, -O-, -S-, -SO-, -SO₂-, -CO- or They also include 2,2-bis(4-hydroxy-3-bromophenyl)propane, 2,2-bis(4-hydroxy-3-chlorophenyl)propane, 2,2-bis(4-hydroxy-2,3,5,6-tetrabromophenyl)propane and 2,2-bis(4-hydroxy-2,3,5,6-tetrachlorophenyl)propane. The catalysts used in this invention are activated pyridines or their salts having electron donor substitutents such as alkyl or dialkylamino groups. The preferred activated pyridines are 4-aminopyridines of general formula (II): in which R¹ and R² are alkyl groups, a polymer chain, or can be bridged to form cycloalkylene groups. The dialkylamino group or related group activates the pyridine by donating electron to N in the ring by resonance effect as shown by Angew. Chem. Int. Ed. Engl., 17, 569 (1978), G. Höfle, W. Steglich and H. Vorbrüggen: Examples of 4-dialkylaminopyridines are: 4-dimethylaminopyridine, 4-pyrrolidinopyridine poly(N,N-dialkylaminopyridine) as shown by L. J. Mathias, R.V. Vaidyn and R. M. Bloodworth, Polymer Preprints, 26(2), 182 (1985). The preferred activated pyridines are 2-substituted pyridines of general formula (III) wherein R is alkyl, cycloalkyl, or a polymer chain. The group in the 2 position activates the pyridine by donating electron to N in the ring by inductive effects. Examples of the 2-substituted pyridines are: methyl, ethyl, isopropyl or polyvinyl pyridine having the formula The activated pyridines of formulas (II) and (III) with additional alkyl groups can also be used: where R₃ are alkyl groups. The amount of catalyst used varies according to the specific bisphenol used and the reaction temperature. In general, an effective or a catalytic amount of the catalyst is in the range of from 0.02 to 10 mole percent based on the moles of the bisphenol used. A preferred range is from 0.05 to 5 mole percent. The temperature of the reaction is generally kept in the range of from 20°C to 50°. However, temperatures over or under this can be used if desired. Examples of useful halogenated solvents are chlorobenzene, chloroform, carbon tetrachloride, 1,2-dichloroethane, methylene chloride, 1,1,2-trichloroethane, tetrachloroethane, and mixtures thereof. Normally, from 1.5 to 2 moles of phosgene will be used per mole of bisphenol in this reaction. A slight excess of phosgene is used in order to achieve complete reaction. The pH of the reaction mixture is maintained in the range of from 8 to 13 depending on the bisphenol used and preferably in the range of from 9 to 11. The present invention is also directed to the high molecular weight polyhalobisphenol polycarbonate produced in accordance with the practice of this invention. It includes carbonate homopolymer of polyhalobisphenol or carbonate copolymers of two or more different polyhalobisphenols with bisphenol A. Additionally, the production of high molecular weight randomly branched polyhalobisphenol polycarbonate and copolyester-polycarbonate are included within the scope of this invention. The weight average molecular weight (Mw) and number average molecular weight (Mn) of the polycarbonate from hindered bisphenols were measured by size exclusion chromatography using polycarbonate from bisphenol A as a standard. The inherent viscosity of the polycarbonate was measured in methylene chloride at 25°C with concentration at 5 gms/l. An emperical relationship between Mw and inherent viscosity for TBBA-PC was obtained as follows: Mw = 327000 x η 1.7 The degree of polymerization was calculated by dividing Mn by the weight of a repeating unit (569.8 for TBBA-PC). The inherent viscosity (η) is calculated from the relative viscosity using the following equation: The following examples and controls are presented to further illustrate the invention. CONTROL I This control illustrates an unsuccessful attempt to prepare high molecular weight TBBA-PC using benzyltrimethyl ammonium chloride as a catalyst. Benzyltrimethyl ammonium chloride is described as an effective catalyst for producing high molecular weight bisphenol A polycarbonate in U.S. Patent 2,970,131. The reactor was charged with tetrabromobisphenol-A (TBBA) (205 g, 0.377 mole), methylene chloride (200 ml) and water (100 ml). Nitrogen was purged through the reaction mixture for 10 minutes. Benzyltrimethyl ammonium chloride (2.3 g, 0.0123 mole) was added to the reaction mixture. The caustic feed reservoir was charged with 120 g of 50 percent NaOH. Phosgene (50 g, 0.51 mole) was introduced into the reaction mixture in 30 minutes maintaining the reaction mixture at pH 10 by pumping caustic from the reservoir. After adding the phosgene, the pH of the mixture was raised to 12.5 and stirring was continued for 30 minutes. An extra amount of phosgene (ca 10 g) was used to adjust the pH of the reaction mixture to 7. The organic layer was washed three times with water. Molecular weight analysis of the organic layer indicated that only low molecular weight TBBA-PC was obtained (Mw < 10,000). This control demonstrates that a catalyst for bisphenol A polycarbonate may not necessarily be a catalyst for TBBA polycarbonate. CONTROL II This control illustrates another unsuccessful attempt to prepare high molecular weight TBBA-PC with triethylamine as a catalyst using a conventional process of making high molecular weight polymer from bisphenol A (U.S. Patent 3,275,601). The reactor was charged with TBBA (205 g, 0.377 mole), methylene chloride (2000 ml) and water (1000 ml). Nitrogen was purged through the reaction mixture for 10 minutes. The caustic reservoir was charged with 120 g of 50 percent NaOH. Phosgene (50 g, 0.510 mole) was introduced into the reaction mixture in 30 minutes and keeping the reaction solution at pH 10 by pumping the caustic from the reservoir. After adding the phosgene, the pH of the mixture was raised to 12.5 and 2 ml of TEA was added. The reaction was stirred for 1 hour. Phosgene was added to bring the reaction mixture to pH 7. The organic layer was washed three times with water. Molecular weight analysis of the organic layer indicated that only low molecular weight of TBBA-PC was obtained (Mw < 10,000). CONTROL III Using the same conditions as Control II, bisphenol A gave a high molecular weight (100,000 Mw) polycarbonate. A comparison of Controls II and III shows that while bisphenol A can be readily converted into a high molecular weight polycarbonate, the same conditions using tetrabromobisphenol A results in a low molecular weight polymer. CONTROL IV This control illustrates an attempt to prepare high molecular weight TBBA-PC using dimethylaminopyridine (DMAP) as a catalyst under the similar conditions that U.S. Patent 4,286,085 claims to produce high molecular weight PC from bisphenol A. To the reactor was charged TBBA (543.9 g, 1.0 moles), methylene chloride (1300 g), water (228 g), DMAP (1.63 g, 0.0133 mole), and 15 percent NaOH (624 g, 2.34 moles). Phosgene (104 g, 1.061 moles) was then added to the reaction in 30 minutes while keeping pH 9 by adding 15 percent NaOH. After 30 minutes, additional sodium hydroxide was added to adjust the reaction mixture to pH 11. Molecular weight analysis of the organic layer indicated that low molecular weight TBBA-PC was obtained (35,000 Mw). The inherent viscosity of the polycarbonate was 0.25. CONTROL V This example illustrates an unsuccessful attempt to prepare high molecular weight TBBA-PC using TEA as a catalyst similar to the process described in U.S. Patent 3,912,687. The reactor was charged with TBBA (409.5 g, 0.753 mole), methylene chloride (2000 ml), water (1000 ml) and TEA (2.7 g, 0.027 mole). Phosgene (93 g, 0.949 mole) was introduced into the reaction mixture in 30 minutes, keeping the pH of the solution at 9-10 by adding 50 percent caustic (180 g, 2.25 mole). After adding the phosgene, a second portion of methylene chloride (1000 ml) was added and the pH was raised to 12. The mixture was stirred for two hours. More phosgene was added to adjust the mixture to pH 7. The organic phase was washed three times with water. After evaporation of the solvent, TBBA-PC having a weight average molecular weight of 37,000 was obtained. The polymer had a relative viscosity of 1.13. The reported value of relative viscosity of TBBA polymer in U.S. Patent 3,912,687 was 1.18 or Mw=50,000. Several duplicate runs were made. The molecular weight of the polymer obtained was not very reproducible and varied from 30,000 to 50,000. The relative viscosity of 1.18 corresponds to the inherent viscosity of 0.33. Example 1 A five-necked round bottom flask fitted with a pH electrode, subsurface gas inlet tube, thermometer, caustic inlet port, and electric paddle stirrer and set in an ice water bath is purged with nitrogen. Tetrabromobisphenol A (409.5 g 0.753 mole) was charged to the reactor followed by methylene chloride (1000 ml), water (1500 ml), and phenol (0.5 g, 0.0053 mole). The mixture was adjusted to pH 10 by adding 50 percent caustic (119.5 g, 1.494 moles). The reaction temperature was 25±3°C. Phosgene (110 g, 1.11 moles) was introduced into the reaction mixture in 30 minutes while maintaining pH 10 by adding caustic (15 g, 0.187 mole). A sample of the reaction mixture was analyzed and found to have 70 percent by weight of the bischloroformate of TBBA and 30 percent by weight of the monochloroformate of TBBA. The reaction mixture was diluted with methylene chloride (2000 ml). Dimethylaminopyridine (0.2 g in 10 ml CH₂Cl₂) was added to the reaction mixture. The reaction mixture was stirred for 30 minutes while caustic (118 g, 1.475 moles) was added to keep the pH at 10. The caustic addition was stopped and phosgene (10 g, 0.1 mole) was added to bring the pH to 7. The organic layer was washed three times with water. A film obtained from the washed polymer solution had a weight average molecular weight of 140,000. The polycarbonate obtained had an inherent viscosity of 0.60. Example 2 The procedure of Example 1 was repeated without using phenol as a terminator. The result was a TBBA polycarbonate with a weight average molecular weight of 240,000 and an inherent viscosity of 0.85. Example 3 A five-necked round bottom flask fitted with a pH electrode, subsurface gas inlet tube, thermometer, caustic inlet port, and electric paddle stirrer and set in an ice water bath is purged with nitrogen. Tetrachlorobisphenol A (146.4 g, 0.4 mole) was charged to the reactor followed by methylene chloride (325 ml), and water (480 ml). the mixture was adjusted to pH 10 by adding 50 percent caustic solution. The reaction temperature was 25±3°C. Phosgene (80 g, 0.81 mole) was introduced into the reaction mixture in 30 minutes while maintaining pH 10 by adding 50 percent caustic solution. At this stage, all tetrachlorobisphenol A has reacted. The reaction mixture was diluted with methylene chloride (300 ml). Dimethylaminopyridine (0.21 g, 0.00172 mole) was added to the reaction mixture. The reaction mixture was stirred for 30 minutes while adding caustic to keep the pH at 10. The caustic addition was stopped and phosgene (5 g, 0.05 mole) was added to bring the pH to 7. Total 50 weight percent caustic used was 270-300 g (or 3.4 to 3.75 moles). The organic layer was washed three times with water. A film obtained from the washed polymer solution had a weight average molecular weight of 250,000 or an inherent viscosity of 0.90. Examples 4-5 The procedure of Example 2 was repeated using 2.8 grams of 2-picoline and 2-propyl pyridine, respectively to obtain high molecular weight polycarbonates. The results are set forth in the table. Control VI The procedure of Example 2 was repeated using 2.8 grams of 4-picoline. The results are set forth in the table. Example 6-7 The procedure of Example 1 was repeated using 0.32 and 0.91 grams of phenol, respectively. The results are set forth in the table. The following conclusions can be drawn from the facts set forth in the above table. The results from Controls I-IV indicate that the known procedure for preparing high molecular weight bisphenol A PC are not satisfactory for making high molecular weight TBBA-PC. The results of Control V indicate that the teaching in U.S. 3,912,687 gives low molecular weight polycarbonates. The maximum molecular weight obtained was Mw=50,000 (inherent viscosity = 0.35) even though no terminator was used. The results in Examples 2 and 3 indicate that the process of this invention gives a high molecular weight product. Examples 1, 2, 6 and 7 indicate that the process of this invention allows one to prepare controlled molecular weight polycarbonate from TBBA. The results of Experiments 2, 4 and 5 indicate that activated pyridines with the general structures (II) and (III) on pages 4 and 6 above are required to obtain the desired high molecular weights. The substituted pyridines such as 4-methylpyridine which does not have the general structures gives only low molecular weight.

Claims: Claims for the following Contracting States : AT, BE, CH, DE, FR, GB, IT, LI, NL A process for the production of high molecular weight polyhalobisphenol polycarbonates including carbonate homopolymers of polyhalobisphenol or carbonate copolymers of two or more different polyhalobisphenols with bisphenol A, randomly branched polyhalobisphenol polycarbonate and copolyester-polycarbonate, having an inherent viscosity greater than 0.4 which comprises the steps of (A) mixing a polyhalobisphenol, a halogenated solvent, and sufficient aqueous alkali metal hydroxide to obtain a mixture having said bisphenol in the alkali metal form, (B) adding phosgene to said mixture and additional aqueous hydroxide whereby the pH of said mixture is maintained in the range of from 8 to 13 and whereby mixtures of bischloroformate and monochloroformate of the bisphenols are formed, (C) adding a catalytic amount of an activated pyridine selected from the group consisting of 4-aminopyridines and 2-substituted pyridines and additional aqueous hydroxide whereby said pH is maintained, and (D) recovering said high molecular weight polycarbonate. A process according to claim 1 wherein the activated pyridine is in its salt form. A process as set forth in Claim 1 or 2 wherein said polyhalobisphenolpolycarbonate is prepared from a polyhalobisphenol of the general formula in which R is chlorine, bromine, or mixtures thereof, and X is C₁-C₆ alkylene, cycloalkylene, a single bond, -O-, -S-, -SO-, -SO₂-, -CO- or A process as set forth in Claim 1 or 2 wherein said polyhalobisphenolpolycarbonate is prepared from a polyhalobisphenol of the general formula wherein (1) R¹ is chlorine or bromine and R² = R³ = R⁴ = hydrogen, or (2) R¹ = R² = R³ = R⁴ = Cl or Br, and A process as claimed in Claim 1 wherein the polyhalobisphenol polycarbonates are tetrahalobisphenol A polycarbonates, the polyhalobisphenol is tetrahalobisphenol A and the activated pyridine has either one of the general formulas: in which R¹ and R² are alkyl groups, a polymer chain, or can be bridged to form cycloalkylene groups; or wherein R is alkyl, cycloalkyl, or a polymer chain and where R₃ are alkyl groups or hydrogen. A process as set forth in any of Claims 1-5 wherein a phenolic terminator is added in step A to control the molecular weight. A process as set forth in any one of the preceding claims which comprises the additional step of phosgenating said mixture containing the pyridine catalyst until the reaction is completed. The high molecular weight polyhalobisphenol polycarbonate obtainable by any of the processes as claimed in claims 1-7, with the exception of HMW carbonate homopolymers of 3,3',5,5'-tetrabromo- or 3,3',5,5'-tetrachlorobisphenol, having an I.V. > 0.4. Claims for the following Contracting State : SE A process for the production of high molecular weight polyhalobisphenol polycarbonates including carbonate homopolymers of polyhalobisphenol or carbonate copolymers of two or more different polyhalobisphenols with bisphenol A, randomly branched polyhalobisphenol polycarbonate and copolyester-polycarbonate, having an inherent viscosity greater than 0.4 which comprises the steps of (A) mixing a polyhalobisphenol, a halogenated solvent, and sufficient aqueous alkali metal hydroxide to obtain a mixture having said bisphenol in the alkali metal form, (B) adding phosgene to said mixture and additional aqueous hydroxide whereby the pH of said mixture is maintained in the range of from 8 to 13 and whereby mixtures of bischloroformate and monochloroformate of the bisphenols are formed, (C) adding a catalytic amount of an activated pyridine selected from the group consisting of 4-aminopyridines and 2-substituted pyridines and additional aqueous hydroxide whereby said pH is maintained, and (D) recovering said high molecular weight polycarbonate. A process according to claim 1 wherein the activated pyridine is in its salt form. A process as set forth in Claim 1 or 2 wherein said polyhalobisphenolpolycarbonate is prepared from a polyhalobisphenol of the general formula in which R is chlorine, bromine, or mixtures thereof, and X is C₁-C₆ alkylene, cycloalkylene, a single bond, -O-, -S-, -SO-, -SO₂-, -CO- or A process as set forth in Claim 1 or 2 wherein said polyhalobisphenolpolycarbonate is prepared from a polyhalobisphenol of the general formula wherein (1) R¹ is chlorine or bromine and R² = R³ = R⁴ = hydrogen, or (2) R¹ = R² = R³ = R⁴ = Cl or Br, and A process as claimed in Claim 1 wherein the polyhalobisphenol polycarbonates are tetrahalobisphenol A polycarbonates, the polyhalobisphenol is tetrahalobisphenol A and the activated pyridine has either one of the general formulas: in which R¹ and R² are alkyl groups, a polymer chain, or can be bridged to form cycloalkylene groups; or wherein R is alkyl, cycloalkyl, or a polymer chain and where R₃ are alkyl groups or hydrogen. A process as set forth in any of Claims 1-5 wherein a phenolic terminator is added in step A to control the molecular weight. A process as set forth in any one of the preceding claims which comprises the additional step of phosgenating said mixture containing the pyridine catalyst until the reaction is completed. The high molecular weight polyhalobisphenol polycarbonate obtainable by any of the processes as claimed in claims 1-7.

Inventors: AGUILAR JOSE L, HO THOI H, KAO CHE I, KASSELL FREDERICK B, AGUILAR, JOSE L., HO, THOI H., KAO, CHE I., KASSELL, FREDERICK B.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1988
Main classification: C08G64
IPC codes: C08G64