Production Process of Glycolide

{
  "publication_number": "US2011263875A1",
  "country": "US",
  "kind": "A1",
  "title": "Production Process of Glycolide",
  "abstract": "The invention provides a production process of glycolide comprising the respective steps of: Step 1 of heating a mixture containing a glycolic acid oligomer and a high boiling polar organic under normal or reduced pressure to reflux the mixture and at that time, conducting a total reflux operation in a reflux time within a range of 0.1 to 20 hours under conditions that substantially the whole amount of a distillate distilled out of a reflux system containing the mixture is refluxed into the reflux system; Step 2 of heating the mixture after the total reflux operation or a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation to conduct depolymerization; and Step 3 of collecting glycolide from a co-distillate.",
  "claims": [
    "1. A production process of glycolide comprising a step of heating a mixture containing a glycolic acid oligomer and a high boiling polar organic solvent, thereby depolymerizing the glycolic acid oligomer in a solution phase, the process comprising the respective steps of: (1) Step 1 of heating the mixture containing the glycolic acid oligomer and the high boiling polar organic solvent having a boiling point within a range of 230 to 450° C. under normal or reduced pressure to reflux the mixture and at that time, conducting a total reflux operation in a reflux time within a range of 0.1 to 20 hours under conditions that substantially the whole amount of a distillate distilled out of a reflux system containing the mixture is refluxed into the reflux system; (2) Step 2 of heating the mixture after the total reflux operation or a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation under normal or reduced pressure to a temperature at which the glycolic acid oligomer is depolymerized to depolymerize the glycolic acid oligomer in a solution phase, and moreover co-distilling glycolide formed by the depolymerization out of the depolymerization reaction system containing the mixture together with the high boiling polar organic solvent into the outside of the depolymerization reaction system; and (3) Step 3 of collecting glycolide from the co-distillate. 2. The production process according to claim 1, wherein the glycolic acid oligomer is a low-molecular weight polyglycolic acid having a weight-average molecular weight of 20,000 or lower. 3. The production process according to claim 1, wherein the high boiling polar organic solvent is a polyalkylene glycol diether represented by the following formula 1: [Chem. 1] X 1 - OR 1 - O p Y (1) (in the formula, R 1 is a methylene group, or a linear or branched alkylene group having 2 to 8 carbon atoms, X 1 is a hydrocarbon group, Y is an alkyl group having 2 to 20 carbon atoms or an aryl group, and p is an integer of 1 or greater, with the proviso that when p is 2 or greater, plural R 1 groups may be the same or different from each other.) and having a molecular weight of 150 to 450. 4. The production process according to claim 1, wherein the mixture used in Step 1 is a mixture further containing, as a solubilizing agent, at least one non-basic organic compound selected from the group consisting of monohydric alcohols, polyhydric alcohols, phenols, monovalent aliphatic carboxylic acids, polyvalent aliphatic carboxylic acids, aliphatic amides, aliphatic imides, polyalkylene glycol diethers having a molecular weight higher than 450 and sulfonic acids, said compounds each having a boiling point of 180° C. or higher, in addition to the glycolic acid oligomer and the high boiling polar organic solvent. 5. The production process according to claim 4, wherein the monohydric alcohols are polyalkylene glycol monoethers represented by the following formula 2: [Chem. 2] HOR 2 - O q X 2 (2) (in the formula, R 2 is a methylene group, or a linear or branched alkylene group having 2 to 8 carbon atoms, X 2 is a hydrocarbon group, and q is an integer of 1 or greater, with the proviso that when q is 2 or greater, plural R 2 groups may be the same or different from each other.) and having a boiling point of 250° C. or higher. 6. The production process according to claim 4, wherein the polyhydric alcohols are polyalkylene glycols represented by the following formula 3: [Chem. 3] HOR 3 - O r H (3) (in the formula, R 3 is a methylene group, or a linear or branched alkylene group having 2 to 8 carbon atoms, and r is an integer of 1 or greater, with the proviso that when r is 2 or greater, plural R 3 groups may be the same or different from each other.) and having a boiling point of 250° C. or higher. 7. The production process according to claim 4, wherein the mixture used in Step 1 is a mixture containing the solubilizing agent in a proportion that the molar ratio of the glycolic acid oligomer to the solubilizing agent falls within a range of 1 to 99. 8. The production process according to claim 1, wherein when a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation is used in Step 2, the mixture is a mixture further containing, as a solubilizing agent, at least one non-basic organic compound selected from the group consisting of monohydric alcohols, polyhydric alcohols, phenols, monovalent aliphatic carboxylic acids, polyvalent aliphatic carboxylic acids, aliphatic amides, aliphatic imides, polyalkylene glycol diethers having a molecular weight higher than 450 and sulfonic acids, said compounds each having a boiling point of 180° C. or higher. 9. The production process according to claim 8, wherein the monohydric alcohols are polyalkylene glycol monoethers represented by the following formula 2: [Chem. 4] HOR 2 - O q X 2 (2) (in the formula, R 2 is a methylene group, or a linear or branched alkylene group having 2 to 8 carbon atoms, X 2 is a hydrocarbon group, and q is an integer of 1 or greater, with the proviso that when q is 2 or greater, plural R 2 groups may be the same or different from each other.) and having a boiling point of 250° C. or higher. 10. The production process according to claim 8, wherein the polyhydric alcohols are polyalkylene glycols represented by the following formula 3: [Chem. 5] HOR 3 - O r H (3) (in the formula, R 3 is a methylene group, or a linear or branched alkylene group having 2 to 8 carbon atoms, and r is an integer of 1 or greater, with the proviso that when r is 2 or greater, plural R 3 groups may be the same or different from each other.) and having a boiling point of 250° C. or higher. 11. The production process according to claim 8, wherein when a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation is used in Step 2, the mixture is a mixture containing the solubilizing agent in a proportion that the molar ratio of the glycolic acid oligomer to the solubilizing agent falls within a range of 1 to 99. 12. The production process according to claim 1, wherein in Step 1, the mixture is heated under a reduced pressure of 1 to 30 kPa to conduct the total reflux operation. 13. The production process according to claim 1, wherein the above-described Steps 1 to 3 are performed by a continuous operation according to a process of combining the following respective steps: a) Step a of continuously or intermittently feeding the mixture after the total reflux operation or the glycolic acid oligomer component recovered from the mixture after the total reflux operation, which has been prepared in Step 1, into the depolymerization reaction system; b) Step b of heating the mixture after the total reflux operation or a mixture obtained by adding the high boiling polar organic solvent to the glycolic acid oligomer component recovered from the mixture after the total reflux operation under normal or reduced pressure to a temperature at which the glycolic acid oligomer is depolymerized to continuously depolymerize the glycolic acid oligomer in a solution phase in Step 2, and moreover continuously co-distilling glycolide formed by the depolymerization out of the depolymerization reaction system containing the mixture together with the high boiling polar organic solvent into the outside of the depolymerization reaction system; and (c) Step c of continuously or intermittently collecting the glycolide from a lower layer of the co-distillate cooled into a liquid state by utilizing a difference in specific gravity between a distillate fraction containing the high boiling polar organic solvent and the glycolide in Step 3. 14. The production process according to claim 13, wherein in Step c, the glycolide is continuously or intermittently collected from the lower layer of the co-distillate cooled into the liquid state, and the distillate fraction containing the high boiling polar organic solvent in an upper layer of the co-distillate is continuously or intermittently discharged. 15. The production process according to claim 13, wherein in Step c, the glycolide is continuously or intermittently collected from the lower layer of the co-distillate cooled into the liquid state, and the distillate fraction containing the high boiling polar organic solvent in the upper layer of the co-distillate is continuously or intermittently returned into the depolymerization reaction system."
  ],
  "cpc": [
    "C07D 319/12"
  ],
  "assignees": [
    "KUREHA CORP"
  ],
  "filing_date": "2009-12-09",
  "publication_date": "2011-10-27",
  "priority_date": "2008-12-26",
  "application_number": "US-200913142012-A",
  "family_id": "42287170",
  "citations": [
    "US5830991A",
    "US6916939B2"
  ]
}