Polycarbonate Resin and Method for Preparing Same
US-2024150521-A1 · May 9, 2024 · US
US10907012B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10907012-B2 |
| Application number | US-201213652070-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 15, 2012 |
| Priority date | Apr 14, 2010 |
| Publication date | Feb 2, 2021 |
| Grant date | Feb 2, 2021 |
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A novel polycarbonate diol is useful as a raw material for producing a polycarbonate diol-based polyurethane with a high degree of hardness, superior abrasion resistance, and superior hydrophilicity. The polyurethane is useful in paints, coating agents, synthetic leathers, artificial leathers, and highly-functional elastomers, or the like. The polycarbonate diol is also useful for producing an active-energy radiation curable polymer composition giving a cured film having superior contamination resistance and high degree of hardness. The curable polymer composition contains a urethane(meth)acrylate oligomer obtained from the polycarbonate diol. The polycarbonate diol is obtained, for example, by reacting two specific types of diols with diester carbonate in the presence of a transesterification catalyst. The catalyst has a metal of Group 1 or 2 on the periodic table. A metal content of the transesterification catalyst is 100 weight ppm or less.
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What is claimed is: 1. A polycarbonate diol, obtained by reacting (i) at least one diol selected from isosorbide, isomannide, and isoidide, (ii) a diol having 1 to 15 carbons which may contain a hetero atom, and (iii) a diester carbonate, wherein: the reaction of (i), (ii), and (iii) is carried out in the presence of a transesterification catalyst; the transesterification catalyst is either a compound containing a metal of Group 1 of the periodic table or a compound containing a metal of Group 2 of the periodic table; the polycarbonate diol contains the transesterification catalyst in an amount of 100 ppm or less, calculated as a weight ratio of catalyst metal in the polycarbonate diol; the number average molecular weight of the polycarbonate diol is 250 to 5,000; at least part of a molecular chain of the polycarbonate diol contains a repeating unit (A) and a repeating unit (B) where X is a divalent group having 1 to 15 carbons which may contain a hetero atom; and the polycarbonate diol has a terminal (A) ratio (I) of 1.2 to 1.8, the terminal (A) ratio (I) being calculated by the following formula: terminal ( A ) ratio ( I )={(number of terminal units ( A ) in molecular chain)/(total number of terminal units ( A ) and terminal units ( B ) in molecular chain)}/{(number of units ( A ) in molecular chain)/(total number of units ( A ) and units ( B ) in molecular chain)}. 2. The polycarbonate diol according to claim 1 , wherein the polycarbonate diol contains the transesterification catalyst in an amount of 0.1 to 100 ppm, calculated as a weight ratio of catalyst metal in the polycarbonate diol. 3. The polycarbonate diol according to claim 1 , wherein the transesterification catalyst is a compound containing a metal of Group 2 of the periodic table. 4. The polycarbonate diol according to claim 1 , wherein the highest temperature during the reaction of (i), (ii), and (iii) is less than 180° C. 5. The polycarbonate diol according to claim 1 , wherein the number average molecular weight of the polycarbonate diol is 250 to 900. 6. A method for obtaining the polycarbonate diol of claim 1 , comprising: reacting (i) at least one diol selected from isosorbide, isomannide, and isoidide, (ii) a diol having 1 to 15 carbons which may contain a hetero atom, and (iii) a diester carbonate, in the presence of a transesterification catalyst, to obtain a polycarbonate diol: wherein: the transesterification catalyst is either a compound containing a metal of Group 1 of the periodic table or a compound containing a metal of Group 2 of the periodic table; and the highest temperature during the reaction of (i), (ii), and (iii) is less than 180° C. 7. The method according to claim 6 , wherein the transesterification catalyst is a compound containing a metal of Group 2 of the periodic table. 8. The polycarbonate diol according to claim 1 , wherein the diester carbonate (iii) is diphenyl carbonate. 9. The polycarbonate diol according to claim 1 , wherein the polycarbonate diol comprises unreacted diester carbonate in an amount of 1 weight % or less, based on the total weight of the polycarbonate diol. 10. The polycarbonate diol according to claim 1 , wherein the diol (i) contains 20 ppm or less of formic acid. 11. The polycarbonate diol according to claim 1 , wherein 5% or less of all molecular chain terminals of the polycarbonate diol are either an alkyloxy group or an aryloxy group. 12. The polycarbonate diol according to claim 1 , wherein the Hazen color number value (APHA value: according to JIS K0071-1) of the polycarbonate diol is 100 or less. 13. The polycarbonate diol according to claim 1 , wherein the molecular weight distribution (Mw/Mn) of the polycarbonate diol is 1.5 to 3.5. 14. A method, comprising: reacting the polycarbonate diol according to claim 1 and a polyisocyanate to obtain a prepolymer; and reacting the prepolymer with a chain extender. 15. A method, comprising: mixing the polycarbonate diol according to claim 1 , a polyisocyanate, and a chain extender together at once; and reacting the obtained mixture. 16. The polycarbonate diol according to claim 1 , wherein 95% or more of molecular chain terminals of the polycarbonate diol are hydroxyl groups. 17. The method according to claim 6 , wherein 95% or more of molecular chain terminals of the obtained polycarbonate diol are hydroxyl groups. 18. The polycarbonate diol according to claim 1 , wherein the highest temperature during the reaction of (i), (ii), and (iii) is less than 180° C., wherein the number average molecular weight of the polycarbonate diol is 250 to 900, and wherein the molecular weight distribution (Mw/Mn) of the polycarbonate diol is 1.5 to 3.5.
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