Manufacturing method of organic zinc catalyst and manufacturing method of polyalkylene carbonate resin

Patent metadata

Field	Value
Publication number	US-2016194442-A1
Application number	US-201414917219-A
Country	US
Kind code	A1
Filing date	Oct 30, 2014
Priority date	Oct 30, 2013
Publication date	Jul 7, 2016
Grant date	—

Abstract

The present invention relates to a manufacturing method of an organic zinc catalyst having more uniform and finer particle size and showing a more improved activity in a polymerization process for manufacturing a polyalkylene carbonate resin, and a manufacturing method of the polyalkylene carbonate resin using the organic zinc catalyst obtained by the manufacturing method of the organic zinc catalyst, the manufacturing method of an organic zinc catalyst including: forming a zinc dicarboxylate-based catalyst by reacting a zinc precursor with C3-C20 dicarboxylic acid, wherein the reaction step is performed under a condition in which the number of moles of the dicarboxylic acid is more than that of the zinc precursor in a reaction system, throughout the entire reaction step.

First claim

1 . A manufacturing method of an organic zinc catalyst comprising:
forming a zinc dicarboxylate-based catalyst by reacting a zinc precursor with C3-C20 dicarboxylic acid, wherein the reaction step is performed under a condition in which the number of moles of the dicarboxylic acid is more than that of the zinc precursor in a reaction system, throughout the entire reaction steps.

2 . The manufacturing method of claim 1 , wherein:
the dicarboxylic acid has a molar ratio of 1.05 to 1.5 relative to 1 mol of the zinc precursor.

3 . The manufacturing method of claim 1 , wherein:
the zinc precursor includes a zinc compound selected from the group consisting of zinc oxide, zinc sulfate (ZnSO 4 ), zinc chlorate (Zn(ClO 3 ) 2 ), zinc nitrate (Zn(NO 3 ) 2 ), zinc acetate (Zn(OAc) 2 , and zinc hydroxide.

4 . The manufacturing method of claim 1 , wherein:
the C3-C20 dicarboxylic acid includes an aliphatic dicarboxylic acid selected from the group consisting of a malonic acid, a glutaric acid, a succinic acid, and an adipic acid, or an aromatic dicarboxylic acid selected from the group consisting of a terephthalic acid, an isophthalic acid, a homophthalic acid, and a phenylglutaric acid.

5 . The manufacturing method of claim 1 , wherein:
the reaction step is performed in a liquid medium, and is performed by separately adding a solution or a dispersion liquid containing the zinc precursor to a solution or a dispersion liquid containing the dicarboxylic acid two or more times.

6 . The manufacturing method of claim 5 , wherein:
the reaction step is performed by adding the solution or the dispersion liquid containing the zinc precursor to the solution to the solution or the dispersion liquid containing the dicarboxylic acid at an equal time interval with an amount at which the total used amount of the zinc precursor is separated into two to ten parts.

7 . The manufacturing method of claim 5 , wherein:
the reaction step is performed by dropping the solution or the dispersion liquid containing the zinc precursor in droplet forms onto the solution or the dispersion liquid containing the dicarboxylic acid.

8 . The manufacturing method of claim 5 , wherein:
the liquid medium includes at least one solvent selected from the group consisting of toluene, hexane, DMF, ethanol and water.

9 . The manufacturing method of claim 1 , wherein:
the organic zinc catalyst in a particle shape having an average particle size of 0.8 μm or less and a particle size standard deviation of 0.2 μm or less is manufactured.

10 . The manufacturing method of claim 1 , wherein:
the organic zinc catalyst having a surface area of 1.8 m 2 /g or more is manufactured.

11 . The manufacturing method of claim 1 , wherein:
the reaction step is performed at a temperature of 50 to 130° C. for 1 to 10 hours.

12 . An organic zinc catalyst in a particle shape having an average particle size of 0.5 μm or less and a particle size standard deviation of 0.04 μm or less, wherein the organic zinc catalyst is a zinc dicarboxylate-based catalyst obtained by reacting a zinc precursor with C3-C20 dicarboxylic acid.

13 . The organic zinc catalyst of claim 12 , wherein:
the organic zinc catalyst has a surface area of 1.8 m 2 /g or more.

14 . A manufacturing method of a polyalkylene carbonate resin comprising:
polymerizing an epoxide and a monomer including carbon dioxide in the presence of the organic zinc catalyst manufactured by the method of claim 1 .

15 . The manufacturing method of claim 14 , wherein:
the manufacturing method is performed in an organic solvent by solution polymerization comprising: the organic electronic device of claim 17 .

Assignees

• Lg Chemical Ltd

Inventors

• Kim Sung-Kyoung
• Park Seung Young
• Cho Hyun Ju

Classifications

• C08G64/34 Primary

  and cyclic ethers · CPC title

• C07C51/412

  by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part · CPC title

• B01J31/2239

  Bridging ligands, e.g. OAc in Cr2(OAc)4, Pt4(OAc)8 or dicarboxylate ligands · CPC title

• B01J31/12 Primary

  containing organo-metallic compounds or metal hydrides · CPC title

• C08K5/0091

  Complexes with metal-heteroatom-bonds · CPC title