Process for preparing polysuccinimides from maleamic acid

Abstract: A process is provided for preparing polysuccinimides by forming a polymerization mixture comprising poly(alkylene glycol), maleamic acid and, optionally, one or more other amic acid, heating the mixture to an elevated temperature, and maintaining the mixture at the elevated temperature to form polysuccinimides. Poly(amino acids) can be prepared by hydrolysing the polysuccinimides.

Description: The present invention is concerned with a process for preparing polysuccinimides. In particular, the present invention is concerned with a process for preparing polysuccinimides from maleamic acid, and optionally other amic acids, in poly(alkylene glycol). Several methods are known for obtaining polysuccinimide which, when hydrolyzed to form the corresponding poly(amino acid), is useful as an absorbent, hard-surface cleaner, water-treatment additive for boiler waters and cooling towers, and as a detergent additive acting as a builder, anti-filming agent, dispersant, sequestering agent and encrustation inhibitor. However, all of the previously known methods for preparing polysuccinimide suffer from the drawbacks of excessively long process times, expensive starting materials, or require the handling of solid materials which poses many difficulties in a manufacturing environment. United States Patent 5,057,597 to Koskan discloses a solid-phase process for preparing polysuccinimide by fluidizing an amino acid with agitation in a nitrogen atmosphere at a temperature of at least 180°C for three to six hours. The resultant polysuccinimide is then hydrolyzed to form a poly(amino acid). United States Patent 4,839,461 to Boehmke, et al. discloses a process for preparing poly(aspartic acid) by combining maleic acid or maleic anhydride and an ammonia solution in a molar ratio of 1:1-1.5. The mixture is then heated to 120°-150°C. and the resulting solution of ammonium salt and maleic acid is evaporated, leaving a crystal mash. The crystal mash is then melted, during which time the waters of condensation and crystallization distill off. A porous mass of poly(aspartic acid) results. The entire process requires six to eight hours to complete. Japanese Patent 52-0088773 B assigned to Ajinomoto, discloses a solvent-based process for preparing poly(aspartic acid). The process described therein utilizes a hydrohalic acid salt of aspartic acid anhydride in one or more organic solvents. The solvents disclosed are organic acids such as propionic acid, butyric acid, and valeric acid; alcohols such as tert-butyl alcohol and tert-amyl alcohol; esters such as ethyl acetate and butyl acetate; ketones such as methyl isobutyl ketone and cyclohexanol; ethers such as tetrahydrofuran and dioxane; halogenated hydrocarbons such as ethylene dichloride and dichlorobenzene; hydrocarbons such as toluene, xylene and decalin; and amides such as dimethylformamide. These solvents may impart additional hazards, expense, odor, toxicity and removal steps to obtain the final product. The prior art methods for the synthesis of polysuccinimides and poly(amino acids) are time consuming, complex and/or use large volumes of volatile organic solvents or inert gases. We have now found a solvent process for producing polysuccinimides. In particular, we have found a solvent process for producing polysuccinimides which may not require a product separation step. According to the present invention there is provided a process for preparing polysuccinimides, which comprises: a) forming a polymerization mixture comprising poly(alkylene glycol) of molecular weight from 300 to 30,000, maleamic acid and, optionally, one or more other amic acid; b) heating the mixture to an elevated temperature; and c) maintaining the mixture at the elevated temperature to form polysuccinimides. As used herein in connection with the present invention, "polysuccinimides" refers to polymeric materials which contain succinimide moieties in the polymer chain and may contain other moieties, and "polysuccinimide" refers to polymeric materials which contain only such moieties. The poly(alkylene glycols) useful in the present invention are those which are fluid at the reaction temperature. Suitable poly(alkylene glycols) include poly(tetramethylene glycol), poly(ethylene glycol), and poly(propylene glycol). The poly(alkylene glycol) can also be terminated at one or both ends by carboxylic acids, alkyl groups of from 1 to 30 carbon atoms, or amines, or alkylamines in which the alkyl group contains from 1 to 10 carbon atoms, or any combination thereof. Therefore, in one embodiment of the present invention the poly(alkylene glycol) is selected from: poly(tetramethylene glycol); poly(ethylene glycol); poly(propylene glycol); poly(tetramethylene glycol), poly(ethylene glycol), and poly(propylene glycol) which are terminated at one or both ends by carboxylic acids, alkyl groups of from 1 to 30 carbon atoms, amines, alkylamines in which the alkyl group copntains from 1 to 10 carbon atoms; and combinations thereof. Preferably the poly(alkylene glycol) is selected from poly(ethylene glycol), methyl-terminated poly(ethylene glycol), and poly(propylene glycol). More preferably, the poly(alkylene glycol) is poly(ethylene glycol). The molecular weight of the poly(alkylene glycol) is from 300 to 30,000, and preferably from 1,000 to 15,000. The poly(alkylene glycol) is preferably added to the polymerization mixture at a level of from 2 to about 90 percent by weight relative to the maleamic acid, preferably from 20 to 90, and most preferably from 30 to 85, percent by weight relative to the maleamic acid. When used, the one or more other amic acid may, for example, be present in an amount of up to 80 percent by weight (based on the weight of maleamic acid). Preferably, when used, the one or more other amic acid is present at a level of from 5 to about 70 percent by weight based on the weight of the maleamic acid. Most preferably, when used the one or more other amic acid is present at a level of from 10 to 60 percent by weight based on the weight of maleamic acid. Preferred other amic acids are the amic acids of mesaconic acid, methylenemalonic acid, itaconic acid, citraconic acid, aconitic acid, alkylmaleic acids, alkenylsuccinic acids, monoethylenically unsaturated oligomers of poly(acrylic acid), monoethylenically unsaturated oligomers of poly(methacrylic acid), butene-1,3,4-tricarboxylic acid, monomethyl maleate, monomethyl itaconate, acrylic acid, methacrylic acid, and crotonic acid. More preferably the one or more other amic acid is selected from itaconic acid, monomethyl maleate, monomethyl itaconate, acrylic acid, methacrylic acid, and crotonic acid. The atmosphere of the polymerization is preferably substantially free of oxygen, including the oxygen present in air. An atmosphere substantially free of oxygen is preferred since, at the temperatures needed for the polycondensation reaction to occur, the poly(alkylene glycols) will oxidize, discolor or degrade. Suitable means for achieving an atmosphere substantially free of oxygen includes blanketing, sweeping or bubbling the reactor with an inert gas, preferably nitrogen, or conducting the polymerization at reduced pressure. The elevated temperature for the process of the present invention must be high enough to provide polycondensation. The preferred temperature will vary with the operating conditions. For example, the preferred temperature may increase as the ratio of maleamic acid and the one or more other amic acid to poly(alkylene glycol) increases, or as the pressure at which the polycondensation is conducted increases. However, the preferred temperature may decrease, for example, in the presence of azeotropic solvents. In general, the preferred elevated temperature is from 120 to 250°C. The polysuccinimides are formed by a condensation reaction. It is therefore desirable to remove the by-products, such as water or alcohol, which are liberated in order to drive the reaction toward completion. Suitable means of removing water include addition of one or more azeotropic solvents to the polymerization mixture such as toluene, xylene, or tetralin, and removing the azeotropic distillate from the polymerization mixture. Another means of removing the water is by adding to the polymerization mixture one or more drying agents such as aluminosilicates. Another means of removing the water is by bubbling an inert gas through the polymerization mixture, or sweeping an inert gas over the surface of the polymerization mixture. Another means of removing the water is by conducting the polymerization under reduced pressure. The polymerization can be conducted as a batch or continuous process. Suitable reactors include batch tank reactors, continuous stirred tank reactors, plug-flow reactors, pipe reactors and scraped-wall reactors. The temperature of the reaction must be sufficient to effect the condensation reaction. This temperature will vary according to whether an azeotropic solvent is employed and the pressure at which the polymerization is conducted which can be subatmospheric, atmospheric or supraatmospheric. The products which result from the process of the present invention are solutions, suspensions or dispersions of polysuccinimides in poly(alkylene glycol). Poly(alkylene glycols) are useful in many of the applications for the polysuccinimides such as, for example, in detergent formulations. Thus, there is no need for a separation step to isolate the polysuccinimides from the poly(alkylene glycol) when the product is used in a detergent application. If desired, the polysuccinimides can be hydrolyzed, for example by any conventional means, to form the corresponding poly(amino acids), such as poly(aspartic acid). A preferred means of hydrolysis is by contacting the product with an aqueous alkaline solution such as sodium hydroxide or sodium carbonate. The mixtures of polysuccinimides and poly(amino acids) with poly(alkylene glycol) prepared according to the process of the present invention may, for example, be used as absorbents, hard-surface cleaners, water-treatment additives for boiler waters and cooling towers, and as detergent additives. The following Examples are presented to illustrate certain embodiments of the present invention. EXAMPLE 1 Preparation of Polysuccinimide To a 100 milliliter three-neck round bottom flask equipped with a magnetic stirring bar, reflux condenser, and an inlet and outlet for nitrogen was added 5.0 grams of maleamic acid and 5.0 grams of poly(ethylene glycol) having a molecular weight of 8,000. The flask was continuously swept with nitrogen and immersed in an oil bath maintained at 190°C for 3.5 hours and then cooled to room temperature. Analysis by 1 H NMR spectroscopy indicated that no maleamic acid remained and that polysuccinimide was formed. The polysuccinimide was hydrolyzed with dilute aqueous sodium carbonate to form poly(aspartic acid). Analysis by 1 H NMR spectroscopy confirmed that poly(aspartic acid) was formed. EXAMPLE 2 The same procedure was followed as in Example 1 except that poly(ethylene glycol) monomethyl ether having molecular weight of 350 was used; the flask was immersed in an oil bath was maintained at 150-160°C for 1 hour. Analysis by 1 H NMR spectroscopy indicated that no maleamic acid remained and that polysuccinimide was formed.

Claims: A process for preparing polysuccinimides, which comprises: a) forming a polymerization mixture comprising poly(alkylene glycol) of molecular weight from 300 to 30,000, maleamic acid and, optionally, one or more other amic acid; b) heating the mixture to an elevated temperature; and c) maintaining the mixture at the elevated temperature to form polysuccinimides. A process as claimed in claim 1, wherein the poly(alkylene glycol) is selected from: poly(tetramethylene glycol); poly(ethylene glycol); poly(propylene glycol); poly(tetramethylene glycol), poly(ethylene glycol), and poly(propylene glycol) which are terminated at one or both ends by carboxylic acids, alkyl groups of from 1 to 30 carbon atoms, amines, alkylamines in which the alkyl group copntains from 1 to 10 carbon atoms; and combinations thereof. A process as claimed in claim 1, wherein the poly(alkylene glycol) is selected from poly(ethylene glycol), methyl-terminated poly(ethylene glycol), and poly(propylene glycol). A process as claimed in any preceding claim, wherein the polymerization mixture contains poly(alkylene glycol) at a level of from 2 to 90 percent by weight relative to the maleamic acid. A process as claimed in any preceding claim, wherein the one or more other amic acid is selected from the amic acids of mesaconic acid, methylenemalonic acid, itaconic acid, citraconic acid, aconitic acid, alkylmaleic acids, alkenylsuccinic acids, monoethylenically unsaturated oligomers of poly(acrylic acid), monoethylenically unsaturated oligomers of poly(methacrylic acid), butene-1,3,4-tricarboxylic acid, monomethyl maleate, monomethyl itaconate, acrylic acid, methacrylic acid, and crotonic acid. A process as claimed in any preceding claim, wherein the polymerization mixture contains one or more amic acid at a level of up to 80 percent by weight based on the maleamic acid. A process as claimed in any preceding daim, wherein the mixture is maintained at the elevated temperature in an atmosphere substantially free of oxygen. A process as claimed in any preceding claim, which further comprises: hydrolyzing the polysuccinimides to form the corresponding poly(amino acids). Use, as an absorbent, hard-surface cleaner, water treatment additive for boiler waters and cooling towers, or as a detergent additive, of a poly(amino acid) in poly(alkylene glycol).

Inventors: PAIK YI HYON, SIMON ETHAN SCOTT, SWIFT GRAHAM, PAIK, YI HYON, SIMON, ETHAN SCOTT, SWIFT, GRAHAM
Applicants: ROHM & HAAS, ROHM AND HAAS COMPANY
Application year: 1993
Main classification: C08G69
IPC codes: C08G69, C08G63, C08G65, C08G73