CONTINUOUS PROCESS FOR POLYASPARTIC ACID SYNTHESIS

Abstract: Polysuccinimide, polyaspartic acid and salts of polyaspartic acid may be prepared by means of heating aspartic acid in the presence of sodium bisulfate. The molecular weight of the polymers may be increased from that obtained without the use of sodium bisulfate. The polysuccinimide, polyaspartic acid or salt of polyaspartic acid obtained have low color. Polyaspartic acid may be obtained in this manner directly from the effluent of an immobilized cell or enzyme column which catalyzes the production of L-aspartic acid without the necessity of intermediate isolation steps.

Description: CONTINUOUS PROCESS FOR POLYASPARTIC ACID SYNTHESIS FIELD OF THE INVENTION This mvention relates to a process for the production of polysuccinimide by sodium bisulfate catalyzed thermal polymenzation of aspartic acid and the conversion of said polysuccinimide to polyaspartic acid and salts of polyaspartic acid by hydrolysis DESCRIPTION OF RELATED ART Polyaspartic acid produced thermally consists of a mixture of α and β linkages of D and L aspartic acid The cc linkage can be obtamed predominantly by hydrolysis of anhydropolyaspartic acid (a synonym for polysuccinimide) by hydrolysis with acid and the β linkage can be obtained predominant.} by base hydrolysis of anhydropolyaspartic acid as revealed b Pιvco\ a. el al , (H Pivcova, V Saudek and H Drobmk, "C N M R Study of the structure of poly (aspartic acid) Polymer, 23, 1237-1241, 1982) Their data (Table 1, p 1238, Table 3, p 1239) showed that thermallv prepared polysuccinimide was completely hydrolyzed (paragraph 2, col 1, p 1239) with the vanous acids and bases used and that the β fraction was above 57% m every case of base hydrolysis The salts of polyaspartic acid m both and β form, and of \ ary g molecular weight and branching, have been found to be useful as fertilizers, detergent anti-redeposition agents, detergent builders, detergent co-builders, plant growth promotion agents, tartar control agents, corrosion inhibition agents, as dispersants of clay, coal, minerals, pigments, and as scale inhibition agents for calcium, barium and strontium salts, m dishwashing detergents, in boiler and cooling water, and for reverse osmosis membranes One of the primary charactenstics that makes them aluable in this respect is the fact that they are biodegradable, whereas other matenals that are presently used for this purpose arc either not biodegradable, e g , polyacrylic acid over 1000 molecular weight (m v. ), or harmful to the environment, e g , polyphosphonc acid It has also been reported that vanance m m w of the polv aspartates gives differmg activity in these uses and an appropriate m w can be found for each use through evaluation of the differing molecular weights by one of ordinary skill m the art Thermally prepared polyaspartate was used in the prevention of boiler scale by changing the crystal structure of calcium salts resulting in the formaϋon of a soft scale (Sang et al, The use of polymers for retardation of scale formation Natl Cone Res Dev [Rep ] (Isr ), 150, 1977) Polyaspartic acid. m w 6,000, was found to be superior to polyglutamate, m w 14,400, polyvinyl sulfonate. m \\ 5300, and polyacrylic acid, m w 6,000, in that it gave 66% retardation of total scale and 90% retardation of calcium sulfate scale The thermal preparation of polyaspartic acid has been known for quite some time and the use of phosphoric acid to catalyze the reaction has also been demonstrated in U S Pat 3,052,655, where Fox used temperatures of 140-210° C with 85% or higher concentrations of phosphoπc acid Harada, et al (Thermal polycondensation of free amino acids with polyphosphonc acid Ongins Prcbiol systems Their Mol Matπces, Proc Conf, Wakulla Spπngs, FL, 289, 1963) obtained polyaspartic acid from aspartic acid and phosphoric acid at temperatures over 100 r C over a time penod of 50-250 hrs, but required temperatures over 170° C when phosphoπc acid was absent U S Pat 4,839,461 discloses a method for making polyaspartic acid from maleic acid and ammonia by reactmg these constituents m a 1 1-1 5 molar ratio b\ raising the temperature to 120°- 150°C over a peπod of 4-6 hours and maintaining it for 0-2 hours The molecular weight range obtained by this method was 1,000-4,000 with a cluster at 1,800-2,000 U S Pat 5,057,597 discloses a method for the polycondensation of aspartic acid to produce polyaspartic acid by heatmg the aspartic acid in a fluidized bed reactor to 221 ° C for a period of 3-6 hours in a nitrogen atmosphere followed by conventional alkaline hydrolysis Dessaigne (Comp rend 31, 432-434 [1850]) prepared condensation products which gave aspartic acid on treatment with nitnc or hydrochionc acid by dry distillation of the acid ammonium salts of malic, fumaric or maleic acid at unspecified times and temperatures U S Pat 5,219,952, discloses the production ofhigh molecular weight polysuccinimide and high molecular weight polyaspartic acid from maleic anhydnde and ammonia by means of adding these ingredients to polysuccinimide previously prepared at greater than 1 °C and then heatmg at greater than 150°C U S Pat 5,221,733, discloses the manufacture of pol\ aspartic acid in a rotary tray drier by heatmg L-aspartic acid to at least 440°F U S Pat 5,296,578, discloses the production of polysuccinimide and polyaspartic acid from maleic anhydnde and ammonia by heatmg at greater than 170°C until a theoretical yield of 70% or more is obtained U S Pat 5,288,783 discloses the preparation of salt of polyaspartic acid by reactmg ammonia and fumaπc acid, maleic acid or malic acid at temperatures above 190-350°C for a period of less than 4 hrs It also discloses the use of a twin screw extruder at temperatures above 160°C U S Pat 5,315,010, discloses polyaspartic acid manufacture by introducing L-aspartic acid mto a plate dner and elevating the temperature to 370°F until a conversion of at least 80% has been obtauied U S Pat 5,319, 145, discloses a method for preparing polysuccimmides with a rotary tray dryer by introducing L-aspartic acid mto the dryer and heating to 120° to 300°C for 1 to 10 hrs U S Pat 5,367,047 discloses the preparaUon of salt of polyaspartic acid by reactmg ammonia and fumanc acid, maleic acid or malic acid at temperatures above 190-350°C for a penod of less than 4 hrs It also discloses the use of a twm screw extruder at temperatures above 160°C U S 5,371,180, discloses a process for the preparation of polysuccinimide and polyaspartic acid by reacting fumanc acid or maleic acid and maleic anhydnde and ammoma into a twin shaft extruder which is self cleaning and heating to 100° to 300°C U S Pat 5,373,088, discloses the production of polyaspartic acid from maleic acid and ammonia by heating solid ammonium maleate to at least 170°C and maintainmg the temperature until polysuccinimide is obtained The production of L-aspartic acid bv an enzyme or immobilized cell column has been disclosed Summary of the Invention Polymers of aspartic acid which are suitable for fertilizers, detergent anti-redeposition agents, detergent builders, detergent co-builders, growth promotion agents, tartar control agents, corrosion inhibition agents, as dispersants of clay, coal, minerals, pigments, and as scale inhibition agents for calcium, baπum and strontium salts, in dishwashing detergents, in boiler and cooling water, and for reverse osmosis membranes, may be obtained by heating aspartic acid in the presence of sodium bisulfate, followed by hydrolysis of the resulting polysuccinimide Either D-aspartic acid. L-aspartic acid or mixtures ofthe two may be used as the aspartic acid ofthe invention The same product is obtained upon sufficient heatmg to effect polymeπzaϋon and the formaUon of polysuccinimide destroys the configuration around the asymmetπc carbon We have found that sodium bisulfate serves as a catalyst for the production of high molecular weight polysuccinimide and through its hydrolysis, polyaspartic acid and salts of polyaspartic acid The color of this reaction is very low and the mateπals are stπkingly similar to those of polyaspartic acid prepared with phosphoπc acid as the catalyst The sodium bisulfate concentration is preferably greater than 12% and less than 75% by weight of aspartic acid A mixture of sulfuπc acid and a source of the sodium ion for neutralization of a sodium salt by such compounds as NaOH, NaHC0 3 , Na O j thus providing sodium bisulfate through the reaction ofthe sulfuric acid by the added base, at a concentration which is withm the limits given above may also be used Heating aspartic acid in the presence of the sodium bisulfate, at a temperature of 150° to 350° C, until such time as polysuccinimide has been formed to the desired degree readily effects the polymeπzation to polysuccinimide A preferred temperature range of 200° to 300° C and an especially preferred range of 220° to 280°C provide rapid polymeπzation under these conditions When the theoretical quantity of water formed in the production of polysuccinimide has been removed, which occurs in a time directly proportional to the temperature, the reaction mixture is allowed to cool Time and temperature may be vaπed to obtain both the optimum color and molecular weight Lower temperatures take longer times to achieve the w increase than do higher temperatures, while both time and temperature may affect the color of the final product The polysuccmimide thus formed can be used to make other useful products or may be hydrolyzed to a salt of polyaspartic acid with either the ct or β linkage, the result depending on the hydrolyzmg agent The hydrolysis may be earned out in water or in organic solvent Formulations ofthe salts of polyaspartic acid prepared in this manner have the excellent performance in the uses given above and have the advantage of being of significantly higher in molecular weight range than do the polymers formed by the thermal polymeπzation of aspartic acid without any catalyst The use of phosphoπc acid as a catalyst will give the same molecular weights and color, but has the disadvantage of being environmental.} harmful due to eutrophication in lakes and streams to which the mateπals ultimately pass as the\ are used as descnbed as above Although the phosphates may be washed from the polysucctnimides successf ulh due to their differing solubilities, low level contamination is always possible and potentially harmful to the environment Additionally the extra steps required to nd the polysuccinimide of the phosphates are costly, whereas the addition of base to the polysuccinimide formed merely incorporates additional sodium sulfate as the end product, which is itself a component of man} of the end use formulations, especially detergents The invention also mcludes a process for the production of a polyaspartate salt in which the L- aspartic is prepared enzymatically b} passing an aqueous solution of ammonium fumarate over a bed of immobilized cells or immobilized enzyme column, in which the enzyme is aspartase or in which the cells contain aspartase, to produce an aqueous solution of ammonium aspartate Without further purification the column effluent may be basified by addition to the solution of ammonium aspartate of a quantity of a base equimolar to the aspartate This bases may be selected from the group of bases consistmg of sodium hydroxide, sodium bicarbonate, sodium carbonate, potassium hydroxide, potassium bicarbonate and potassium carbonate Reducing the volume ofthe basified solution by means of evaporation of a part of the aqueous solution at constant heat and reduced pressure or increased heat and reduced or atmospheπc pressure results in the removal of the ammonia contained in the solution Subsequentl} acidifying the solution with an equimolar quantity of sulfuric acid produces a solution of aspartic acid and sodium bisulfate Upon heating the solution in a suitable reactor at a temperature of 1 10°-300° for a sufficient length of time that at least 60% ofthe aspartic acid is converted to polysuccmimide The length of time required depends on the temperature to which the solution is heated The water of solution is first removed and then the water of condensation must be removed to effect the polymeπzation As disclosed in the patents above, vanous reactors are suitable for this removal The polymenzation step can be earned out discontinuously or continuously in suitable reactors Reactors to be employed discontinuously are, for example, kneading machines or paddle dners All high-viscosity reactors which allow removal of the water vapor released, preferably those havmg large reaction volumes, and preferably also those having kinematic self-cleaning ofthe surfaces which come mto contact with the product and likewise preferably those with shaft heating can be employed Machines of coπosion-resistant matenal, for example stainless steel, are preferably employed for corrosion resistance Twin screw extruders built according to these principles have been shown to be effective reactors for this reaction At this point an optional step may be inserted m which the virtually insoluble polysuccmimide is washed with water to remove the sodium bisulfate which has a high degree of solubility in water The polysuccinimide formed may be hydrolyzed with a base selected from the group of bases consisting of sodium hvdroxide, sodium bicarbonate, sodium carbonate ammonium hydroxide, ammonia, potassium hydroxide, potassium carbonate and potassium bicarbonate to provide solution of a salt of polyaspartic acid At this point an optional step ma> be inserted m which the polyaspartate solution is treated with hydrogen peroxide to reduce color This step may be mcluded with or without the water wash step to provide the same color reduction Such hydrolysis may also be earned out in detergent formulations contammg one or more of these bases The object of this mvention is to provide a means of preparing polysuccmimide by means of heatmg in the presence of sodium bisulfate as a catalyst Another object of the invention is to provide means of prepanng polyaspartic acid and salts of polyaspartic acid b\ hvdrolyzing the polysuccmimide formed in the reaction Yet another object of the invention is to prov ide a high m w polysuccmimide, polyaspartic acid and salts of polyaspartic acid Still another object of this mvention is to provide a polysuccinimide, polyaspartic acid or salt of polyaspartic acid having low color Yet another object of this invention is the preparation of a polyaspartic acid that is not contaminated by phosphorous or phosphorous containing compounds A further object ofthe invention is to provide a means of producmg polyaspartic acid direcdy from the effluent of an immobilized cell or enzyme column which catalyzes the production of L-aspartic acid without the necessity of intermediate isolation steps Detailed Description of the Embodiments. Example 1. Thermal Polymerization of L- Aspartic Acid at 220 °C. L-aspartic acid was rapidly mixed at 220° C for 20 mm lo give polysuccinimide as a pink powder This solid was slumed with aqueous sodium hydroxide at 60° -70° C The resultant clear red- brown solution of sodium polyaspartate was subjected to analysis by gel permeation chromatography (GPC) GPC was earned out on a 1 5 X 14 cm column of SEPHADEX G-75 ( a registered trademark of Pharmacia, Piscataway, NJ for pore exclusion chromatographic medium), usmg a mobile phase of 5 5 g NaH 2 P0 4 and 5 7 g N-t-HP0 4 per 4 L of distilled water at a flow rate of 0 5 mL/min, with detection at 220 nm Under these conditions the polymer had a retention time of 33 min Example 2. Thermal Polymerization of Mono- mmonium Maleate at 250° C. Maleic anhydnde was added to water to provide maleic acid, after which one equivalent of ammoma was added to prepare an aqueous slurry of mono-ammonium maleate This slurry was rapidh- mixed at 250°C for 20 mm to give polysuccinimide as a water insoluble, pinkish-tan friable powder This solid was dissolved in an aqueous solution of sodium hydroxide to form a clear red-brown solution of sodium polyaspartate GPC was carried out as in Example 1 and the retention time of this polymer was 38 mm Example 3. Thermal Polymerization of L-Aspartic Acid at 260-265 °C at 30% H 3 P0 4 concentration. L-aspartic acid was slumed with 85% H 3 P0 4 , in a 7 3 weight aspartic acid to 85% H,P0 4 weight, ratio and heated with comminution due to the action of the reactor blades, at 260-265 ° C for 30 min to give polysuccinimide as a pmk powder This solid was slurried with one equivalent of aqueous sodium hydroxide and maintained at 60° -70° C until the polysuccinimide had gone into solution, indicating the formation ofthe water soluble sodium polyaspartate The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as in Example 1, and had a retention time of 25 5 mm Example 4. Thermal Polymerization of L-Aspartic Acid at 260-265 °C at 30% H 3 PO„ concentration. L-aspartic acid was slurπcd with 85% H,P0 4 . in a 7 3 ratio and heated with agitation at 260-265 " C for 10 mm to give polysuccmimide as a pink powder This solid was slurried with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as Example 1, and had a retention time of 26 mm Example 5. Thermal Polymerization of L-Aspartic Acid at 230-235 °C at 25% H 3 P0 4 concentration L-aspartic acid was slurπcd with 85% H 3 P0 4 , in a 75 25 ratio and heated with mixing and kneading at 230-235° C for 30 min to give polysuccinimide as a pink powder This solid was slumed with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as in Example 1 , and had a retention time of 26 mm Example 6. Thermal Polymerization of L-Aspartic Acid at 260-265°C at 20% H ( PO„ concentration. L-aspartic acid was slumed with 85% H,PO., in a 8 2 ratio and heated with comminution at 260- 265 ° C for 10 min to give polysuccinimide as a pink powder This solid was slumed with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as m Example 1, and had a retention time of 27 mm Example 7. Thermal Polymerization of L-Aspartic Acid at 150-210°C at 16% H 3 P0 4 concentration. L-aspartic acid was slumed with 85% H 3 P0 4 , in a 84 16 ratio and heated with comminution at 150-210° C for 4 hr to give polysuccmimide as a pink powder This solid was slurried with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as in Example 1, and had a retention time of 27 mm Example 8. Thermal Polymerization of L-Aspartic Acid at 200-235°C at 12.8% H-SO„ concentration. L-aspartic acid was slurned with 98% H 2 S0 4 , in a 87 2 12 8 ratio and heated with comminution at 200-235 ° C for 20 min to give polysuccmimide as a pink powder This solid was slurned with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, carried out as in Example 1, and had a retention time of 33 5 min Example 9. Thermal Polymerization of L-Aspartic Acid at 230-235 °C at 50% H 2 S0 4 concentration. L-aspartic acid was slurned with 98% H 2 S0 4 , a l l molar ratio and heated with comminution at 190-205 ° C for 30 nun to give a water soluble, black product which contamed veπ, little polysuccmimide Example 10. Thermal Polymerization of L-Aspartic Acid at 260-265 °C at 50% NaHS0 4 concentration. L-aspartic acid was slurned with NaHS0 4 , in a 1 1 molar ratio and heated with comminution at 260-265° C for 30 mm to give polysucci mide as a pink powder This solid was slurned with aqueous sodium hydroxide at 60° -70° C The resultant clear red-brown solution of sodium polyaspartate was subjected to analysis by GPC, earned out as in Example 1 , and had a retention time of 27 5 min Example 11. Thermal Polymerization of L-Aspartic Acid at 230-235°C at 50% NaHS0 4 concentration. L-aspartic acid (6 7 g, 0 05 moles) was slumed with NaHS0 4 , (7 0 g, 0 05 moles), a 1 1 molar ratio, in 20 mL of water and heated with tumbling in a rotary evaporator at 230-235° C for 13 mm to give 11 6 g of white semi-solids A 1 0 g portion of this semi-solid was slumed with 1 mL of aqueous 40% sodium hydroxide The resultant clear pale yellow solution of sodium polyaspartate was subjected to analysis by GPC, earned out as in Example 1, and had a retention time of 35 mm The remaining 106 g was then tumbled at 230-235° C for 10 min to give 9 9 g of tan solids A 1 0 g portion was dissolved in 1 g of water contaimng 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1, showed a broad peak of soώum polyaspartate centered at 29 mm The remaining 8 9 g was then tumbled at 230-235° C for 10 mm to give 8 8 g of tan solids A 1 0 g portion was dissolved in 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1, showed a broad peak of sodium polyaspartate centered at 26 mm Addition of 0 1 g of 30% H 2 0 2 gave a clear pale yellow solution whose GPC was unchanged Example 12. Conversion of an L-aspartic acid enzyme column production stream. Passage of a 1 5 M solution of ammonium fumarate, pH 8 5, over an enzyme column contammg immobilized aspartase or microbial cells contammg the enzyme aspartase, gives a solution that is 1 5 M m L-aspartic acid and 1 7 M in ammoma Solutions contammg these proportions may be used to test the effectiveness of treatments ofthe enzyme column effluents Other levels of ammonium fumarate may be used to prepare L-aspartic acid as indicated by Calton ( Preparation of L- Aspartic Acid, Biocatalytii Production of Ammo Acids & Derivatives, Hanser, Munich, 1992) To a solution containing 100 g (0 0752 moles) of L-aspartic acid, 1 44 g (0 08 moles) NH 3 and 89 g of water was added 3 1 g of 97% NaOH (0 075 moles), thus preparing a solution of the The solution was concentrated by evaporation at ambient pressure, with heating to 27 g of a clear solution havmg no odor of NH 3 and a pH of 75 An aqueous solution of H 2 S0 4 (98%, 7 5 g 20 g of water) was added and the resultant slurry of white solids was comminuted at 260-265°C for 30 nun to give 15 8 g of tan solids Theoretical yield for this reaction is 16 3 g A 7 9 g portion was dissolved m 15 mL of water containing 3 g NaOH and the resultant clear, light brown solution had a pH of 10 5 and the GPC, earned out as in Example 1, showed a retention time of 28 mm Example 13. Conversion of an L-aspartic acid enzyme column production stream. An artificial effluent from an immobilized cell column was prepared contammg 10 0 g (0 0752 moles) of L-aspartic acid, 1 36 g (0 08 moles) NH 3 and 50 g of water (accordmg to US Pat 4,436,813) The solution was treated with 40 g Na-CO j (0075 equivalents) to basify The resulting solution (pH 10) was concentrated by evaporation at elevated temperature to achieve removal of excess ammoma, to a volume of 25 mL of a clear solution which had no odor of NH 3 and a pH of 7 0 H 2 S0 4 (98%, 7 4 g) was added (dropping the pH to 1 and forming 0 075 equivalent of sodium bisulfate) The resultant slurry of white solids was mixed vigorously at 260-265°C for 30 min to give polysuccinimide (14 8 g of tan solids) A 1 0 g portion was dissolved in 1 mL of water containing 1 g of aqueous 40% NaOH to provide an aqueous solution of sodium polyaspartate GPC, carried out as in Example 1 , showed a retention time of 28 5 mm The remaimng 13 8 g of polysuccinimide was then agitated at 260-265° C for 10 mm to give 13 6 g of tan solids A 1 0 g portion was dissolved in 1 g of water contaimng 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1, showed a broad peak centered at 27 min Addition of 0 15 g of 30% H 2 0 2 gave a clear pale yellow solution whose GPC was unchanged The remaining 12 6 g was then agitated at 260-265° C for 10 min to give 12 1 g of tan solids A 1 0 g portion was dissolved m 1 g of water containing 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1, showed a broad peak centered at 27 mm Example 14. Thermal polymerization of L-aspartic acid and NaHS0 4 at 260-265°C. A slurry of 6 7 g (0 05 moles) of L-aspartic acid and 14 g NaHS0 3 Η 2 0 (0 01 moles) in 20 mL of water was tumbled m a salt bath at 260-265°C for 2 min to remov e the water and the residual white solids were tumbled at 260-265° C for 5 nun The solids were allowed to cool to room temperature, pulverized and then heated for an additional 5 mm at 260-265° C to gnc 17 1 g of tan solids (theory 16 8 g) A 1 0 g portion was dissolved in 1 g of water containing 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, carried out as in Example 1 showed a broad peak centered at 32 mm The remaining 16 1 g was then agitated at 260-265° C for 10 min to give 15 2 g of tan solids A 1 0 g portion was dissolved in 1 g of water containing 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1 , showed a broad peak centered at 26 5 un The remaimng 14 2 g was then agitated at 260-265° C for 10 min to give 14 0 g of light brown solids A 1 0 g portion was dissolved in 1 g of water containing 1 g of aqueous 40% NaOH to give a clear brown solution GPC of this solution, earned out as in Example 1 , showed a broad peak centered at 26 0 mm Example 15. Thermal polymerization of L-aspartic acid and NaHS0 4 at 190-210°C. Ten lbs of an aqueous slurry (pH 1 0, density, 1 6) composed of 3 76 lbs ( 12 8 moles) of L- aspartic acid, 3 43 lbs (12 9 moles) of sodium hydrogen sulfate and 2 81 lbs of water was placed in a heated reactor at 200° -225° C The slurry was heated for 180 minutes with comminution by the blades of the reactor and samples were taken at 90, 120 and 180 min During the first 30 mm The reactants became a white semi-solid paste and their temperature ranged from 100°- 1 0°C Duπng the next 30 mm, the reactants tumed to a viscous semi-solid melt as their temperature rose to 190° C At this pomt, the melt turned to a bπttle solid which was rapidly pulveπzed by the reactor's impeller to a white powder The powder was agitated in the reactor as the temperature climbed to 210° C The polysuccmimide formed and NaHSO, weighed 5 58 lbs (95% of theoretical 6 16 lbs) For GPC, 1 0 g samples ofthe product were slumed with 1 0 g of water and dissolved in 0 9 g 40% aqueous NaOH to give clear light tan solutions of sodium polyaspartate and sodium sulfate The results of the GPC, earned out as in Example 1 , showed a broad peak at 26 5 mm for the 90 mmute sample The peak shifted to 26 mm for the 120 mm sample and remained at that molecular weight for the 180 mm sample In order to wash the sodium bisulfate from the polysuccmimide, a 50 g portion of the polysuccinimide-sodium bisulfate mixture was slumed m 50 mL of water at 90-95°C for 30 mm The slurry was readily filtered usmg Whatman # 1 filter paper The wet cake of solids was πnsed with 15 mL of water and reslumed as before The solids were again collected and nnsed and the filter cake was dπed for 12 hrs at 65 °C to give 22 4 g (theoretical yield of 22 2 g of polysuccinimide if the sodium bisulfate was oπgmally present as pyrosulfate, which is anhydrous and 23 3 g if the sodium bisulfate was present as the monohydrate) of off-white powder which was essentially pure polysuccinimide Analysis of the residual ash ga e less than 0 065%, the lower limit ofthe assav A 5 0 g portion of the NaHS0 4 free polysuccmimide prepared above was slurned in 15 g of water at 95- 100° C To this was added 2 5 g Na 2 C0 3 over a period 15 mm At this point an additional 4 7 g portion of polysuccmimide was added (for a total of 9 7 g, 0 1 formula wt ) Over a period of 15 min, an additional 2 75 g of Na ^ was added m small portions to the well stirred slurry at 95°- 100° C And the solutions was stirred for an additional 30 mm to give a clear brown solution, pH 9 5 Hydrogen peroxide (0 1 g, 30%) was added at 60-70° C to decolorize the sodium polyaspartate solution and the previously brown solution became a clear light yellow GPC of this solution, carried out as in Example 1, showed a broad peak of sodium polyaspartate centered at 26 mm Example 16. Thermal polymerization of L-aspartic acid and NaHS0 4 at various ratios and temperatures. Polysuccinimide and sodium polyaspartate were prepared as in Example 15, at the times, temperatures, quantities of L-aspartic acid (L-asp), quantities of NaHS0 4 and the process was sampled at the times shown The polysuccinimide formed was then hydrolyzed as Example 15 and the GPC was run In each case, the polysuccinimide formed was off-white in color with the exception of the run al 300- 305° C where the color ofthe polysuccinimide was slightly darker L-asp NaHS0 4 molar ratio Temp GPC GPC GPC GPC yield yield (g) (g) NaHSO/L-asp °C @10 @20 @30 @60 (g) % nun min min mm theory 67 0 0 260-265 32 32 315 - 49 100 67 031 005 260-265 33 31 32 52 102 67 06 01 260-265 33 315 31 51 93 133 30 025 260-265 30 29 28 121 95 67 30 05 260-265 30 275 27 72 90 67 46 075 260-265 28 26 26 93 98 133 12 10 260-265 265 265 27 225 104 67 76 125 260-265 30 26 275 - 125 100 67 120 20 260-265 32 265 26 160 94 133 120 20 220-225 - - 2ϊ ! 213 98 67 60 10 230-235 35 29 26 108 99 67 60 10 300-305 27 26 265 - 98 90 The data in the table show that the catalytic effect of sodium bisulfate begins to take effect at 5% with a shght decrease in GPC retention time at equivalent times of heating, which would mdicate a slightly higher molecular weight It is also apparent that the time the L-aspartic acid and the sodium bisulfate were heated could be vaned to achieve the molecular weight desired The color was margmally affected by heatmg beyond the time at which the polysuccmimide reached a maximum m w Example 17. Thermal polymerization of L-aspartic acid catalyzed by NaHS0 4 in an oven at 150- 180°C. A slurry of 133 g (1 mole) of L-asp and 120 g (1 mole) of NaHS0 4 m 100 g of water was placed as a 1/4" thick layer m a glass pan an oven at 150-180° C Samples (1 g) were taken at the times in the following table After 8 hrs, 2113 g (corrected for samples removed.974% of theory) The samples were dissolved in 2 g of water and 09 g 40% aqueous NaOH to provide polyaspartic acid for GPC analysis Time (hrs) GPC (mm) color 4 38 pale yellow 5 33 pale yellow 6 28 yellow 8 28 yellow This shows that thm layers ofthe reactants will condense m the same manner as those vigorously stirred and that the time-temperature profile required may be adjusted to provide material of the desirable molecular weight and color Example 18. Hydrolysis of polysuccinimide containing NaHS0 4 with Na 2 C0 3 . A 50 g portion of polysuccmimide prepared by vigorously kneading L-asp with an equivalent weight of NaHS0 4 at a temperature of 220° C for 30 min, was slurned in 150 g of water at 95°C while portions of N-1-CO 3 were added over a peπod of 45 min with evolution of C0 2 A total of 32 g of Na 2 C0 3 was required to achieve a clear tan solution after stirnng several hours at 90° C The addition of 0 5 g of 30% hydrogen peroxide gave a clear yellow solution GPC analysis showed a retention time of 26 5 mm Example 19. Thermal polymerization of L-aspartic acid catalyzed by NaH 2 P0 4 A slurry of 6 7 g (0 05 moles) of L-aspartic acid and 6 9 g (0 05 moles) of NaH 2 P0 4 H 2 0 in 20 g of water was tumbled at 265° C for 30 mm Samples (1 g) were taken at 10, 20 and 30 min Con ected for samples removed, there remamed 10 6 g (theory 10 8 g) of a light tan powder at 30 nun The samples were hydrolyzed and the GPC run as m Example 1 The 30 min sample had a peak at 35 mm and was orange m color, thus showing that NaH 2 P0 4 is not as good a catalyst as NaHS0 4 Example 20. Addition of excess base and NaHS0 4 An artificial effluent from an immobilized cell column was prepared containing 10 0 g (0 0752 moles) of L-aspartic acid, 1 40 g (0 08 moles) NH 3 and 50 g of water was mixed with 6 0 g NaOH (0 15 equivalents) The resulting solution was concentrated by evaporation at elevated temperature to achieve removal of excess ammonia, to a volume of 27 mL To this solution H-S0 4 (98%, 14 8 g in 15 rnL of water) was added slowly The resultant slurry of white solids was mixed vigorously al 260-265°C for 30 mm to give 25 2 g of a pink-tan powder contammg polysuccmimide A 1 0 g portion was dissolved m 1 mL of water contammg 1 g of aqueous 40% NaOH to provide an aqueous solution of sodium polyaspartate GPC, earned out as in Example 1, showed a retention time of 26 mm indicating a molecular weight around 10,000 Example 21. Reaction of an aspartic acid stream with low levels of NaHS0 4 . The conditions of Example 20 were repeated but the amount of NaOH was reduced to 3 0 g NaOH (0 075 moles) and the H 2 S0 4 was reduced to 5 5 g (0 056 moles) The product obtained upon thermal polymenzation weighed 13 4 g and was a tan solid containing polysuccinimide A clear brown solution contaimng sodium polyaspartate was obtained from 1 0 g of the tan solids upon reaction with 1 0 g of 40% NaOH in 1 0 mL of water GPC showed a broad peak centered at 27 mm mdicating a molecular weight of 7,000-10,000 It will be apparent to those skilled in the art that the examples and embodiments descnbed herein are by way of illustration and not of limitation, and that other examples mav be utilized without departing from the spirit and scope of the present mvention, as set forth in the appended claims

Claims: Claims We claim 1. A process for the production of a polyaspartate salt comprising the steps of a ) passing an aqueous solution of ammonium fumarate over a bed of immobilized cells, wherein said cells contain aspartase, to produce an aqueous solution of ammomum aspartate, b ) addition to said solution of ammonium aspartate of a sufficient quantity of a base to allow removal o the ammonium ion present in said solution by evaporation, said base selected from the group of bases consisting of sodium hydroxide, sodium bicarbonate, sodium carbonate, potassium hydroxide, potassium bicarbonate and potassium carbonate, c ) reducing the volume of said solution by evaporation thereby removing the ammoma conta ed in the solution, d ) acidifying said solution with a sufficient quantitv of sulfuric acid to produce an aqueous mixture of aspartic acid and sodium bisulfate, e ) mixing and heatmg said mixture m a reactor at a temperature of 1 10°-300° C for a length of time sufficient to convert at least 60% ofthe aspartic acid to polysuccinimide, f ) hydrolyzmg said polysuccinimide with a base selected from the group of bases consisting of sodium hydroxide, sodium bicarbonate, sodium carbonate ammomum hydroxide, ammonia, potassium hydroxide, potassium carbonate and potassium bicarbonate to provide solution of a salt of polyaspartic acid 2. The process of claim 1 further compπsing after step e ) and before step f ) washing said polysuccinimide with water to remove said sodium bisulfate 3. The process of claim 1 further compnsmg step g ) the step addmg hydrogen peroxide to said solution of a salt of polyaspartic acid to reduce color 4. A process for the production of a polysuccmimide comprising the steps of a ) passing an aqueous solution of ammonium fumarate over a bed of immobilized cells, wherein said cells contain aspartase, to produce an aqueous solution of ammonium aspartate, b ) addition to said solution of ammonium aspartate of a sufficient quantity of base to allow removal of the ammonium ion present in said solution by evaporation, said base selected from the group of bases consisting of sodium hydroxide, sodium bicarbonate, sodium carbonate, potassium hydroxide, potassium bicarbonate and potassium carbonate, c ) reducmg the volume of said solution by evaporation thereby removing the ammonia contamed m the solution, d ) acidifying said solution with an sufficient quantit} of sulfuπc acid to produce an aqueous mixture of aspartic acid and sodium bisulfate, e ) mixing and heatmg said mixture in a reactor at a temperature of 1 10°-300° C for a length of time sufficient to convert at least 60% of the aspartic acid to polysuccmimide, 5. The process of claim 5 further compnsmg after step e ) and before step f ) washing said polysuccmimide with water to remove said sodium bisulfate 6. The process of claim 5 further compπsing step e ) the step adding hydrogen peroxide to said mixture of polysuccmimide to reduce color

Inventors: CALTON GARY J, WOOD LOUIS L, CALTON, GARY, J., WOOD, LOUIS, L.
Applicants: CALWOOD CHEM IND INC, CALWOOD CHEMICAL INDUSTRIES, INC.
Application year: 1996
Main classification: C08F283
IPC codes: C08G69, C08G73