Branched poly(arylene sulfide) resin and method for producing same

Patent metadata

Field	Value
Publication number	US-9255350-B2
Application number	US-201113638227-A
Country	US
Kind code	B2
Filing date	Mar 22, 2011
Priority date	Mar 31, 2010
Publication date	Feb 9, 2016
Grant date	Feb 9, 2016

Abstract

Disclosed are a branched poly(arylene sulfide) resin having a melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec −1 of 65 to 450 Pa·s, a maximum draft ratio of 6500 or more, and a degree of whiteness of 65 or more; moreover, a branched poly(arylene sulfide) resin preferably having a dependence of melt viscosity on shear rate of 1.4 to 2.6 or a melt stability of 0.85 to 1.30; and a method for producing a branched poly(arylene sulfide) resin, wherein a sulfur source and a dihaloaromatic compound are caused to undergo a polymerization reaction at a temperature of 170 to 290° C. in the organic amide solvent in the presence of a polyhaloaromatic compound in an amount of 0.0001 to 0.01 mol per mol of the fed sulfur source.

First claim

The invention claimed is:

1. A method for producing a branched poly(arylene sulfide) resin having characteristics (a) to (e) described below,
wherein the method comprises causing a sulfur source and a dihaloaromatic compound to undergo a polymerization reaction, and
wherein the polymerization reaction is one in which the sulfur source and the dihaloaromatic compound are caused to undergo a polymerization reaction at a temperature of 170 to 270° C. in an organic amide solvent, then at a time when the conversion of the dihaloaromatic compound has become 30% or more, a polyhaloaromatic compound in an amount of 0.0001 to 0.008 mol per mol of the fed sulfur source is added to a polymerization reaction mixture, at the same time or thereafter a phase separating agent is added, subsequently the temperature of the polymerization reaction mixture is raised, and then the polymerization reaction is continued at a temperature of 240 to 290° C.:
(a) the melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec −1 is 65 to 450 Pa·s;
(b) the measured maximum draft ratio, VS D /V 0 , is 6500 or more, wherein the maximum draft ratio is measured by melting a dry polymer at 310° C., discharging the melted polymer at a discharging rate (V 0 ) of 0.05 mm/min, and varying a take-up speed from 5 m/min to 500 m/min over 1 minute, and VS D is a rate at the time when the discharged material is broken;
(c) the degree of whiteness is 65 or more;
(d) the dependence of melt viscosity on shear rate, which is the ratio of a melt viscosity measured at a temperature of 310° C. and a shear rate of 200 sec −1 to a melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec −1 is from 1.4 to 2.6; and
(e) the melt stability, which is the ratio of a melt viscosity after retention at a temperature of 310° C. and a shear rate of 1200 sec −1 for 30 minutes to a melt viscosity after retention at a temperature of 310° C. and a shear rate of 1200 sec −1 for 5 minutes, is from 0.85 to 1.30.

2. The method for producing a branched poly(arylene sulfide) resin according to claim 1 , wherein the method comprises the following steps 1 to 4:
(1) dehydration step 1 of heating a mixture containing an organic amide solvent, a sulfur source containing an alkali metal hydrosulfide, and an alkali metal hydroxide, thereby removing at least part of a distillate containing moisture from a system containing the mixture to the outside of the system;
(2) feeding step 2 of mixing the mixture remaining in the system in the dehydration step with a dihaloaromatic compound, thereby preparing a fed mixture containing an organic amide solvent, a sulfur source, an alkali metal hydroxide, moisture, and a dihaloaromatic compound;
(3) earlier polymerization step 3 of heating the fed mixture to a temperature of 170 to 270° C., thereby causing the sulfur source and the dihaloaromatic compound to undergo a polymerization reaction in the organic amide solvent containing the moisture, and at a time when the conversion of the dihaloaromatic compound has become 30% or more, adding a polyhaloaromatic compound in an amount of 0.0001 to 0.008 mol per mol of the fed sulfur source to a polymerization reaction mixture, and at the same time or thereafter, a phase separation agent is added; and
(4) later polymerization step 4 of continuing the polymerization reaction at a temperature of 240 to 290° C.

3. The method for producing a branched poly(arylene sulfide) resin according to claim 2 , wherein in dehydration step 1, dehydration is carried out until the amount of moisture becomes 0.01 to 2 mol per mol of the fed sulfur source.

4. The method for producing a branched poly(arylene sulfide) resin according to claim 2 , wherein in feeding step 2 , the fed mixture containing components is prepared so that the proportions of the respective components per mol of the fed sulfur source will become 0.95 to 1.09 mol for the alkali metal hydroxide, 0.01 to 2 mol for the moisture, and 0.950 to 1.200 mol for the dihaloaromatic compound.

5. The method for producing a branched poly(arylene sulfide) resin according to claim 2 , wherein in earlier polymerization step 3, the polyhaloaromatic compound and the phase separation agent are added to the polymerization reaction mixture when the conversion of the dihaloaromatic compound has become 30 to 98%.

6. The method for producing a branched poly(arylene sulfide) resin according to claim 5 , wherein in earlier polymerization step 3, the addition of the phase separation agent is carried out after a time when the polyhaloaromatic compound was added and by a time when the conversion of the dihaloaromatic compound becomes 95%.

7. The method for producing a branched poly(arylene sulfide) resin according to claim 2 , wherein in earlier polymerization step 3, water is added as the phase separation agent into the polymerization reaction mixture at a time when the conversion of the dihaloaromatic compound has become 30% or more so that the amount of moisture contained in the polymerization reaction mixture will become more than 2 moles but not more than 10 mol per mol of the fed sulfur source.

8. The method for producing a branched poly(arylene sulfide) resin according to claim 2 , wherein the polyhaloaromatic compound is added to the polymerization reaction mixture at a time when the conversion of the dihaloaromatic compound has become 80% or more.

9. The method for producing a branched poly(arylene sulfide) resin according to claim 1 , wherein the polymerization reaction is carried out with further addition of a polymerization aid.

10. The method for producing a branched poly(arylene sulfide) resin according to claim 9 , wherein the polymerization aid is water and a metal salt of an organic carboxylic acid.

11. The method for producing a branched poly(arylene sulfide) resin according to claim 1 , wherein the method is provided with more than one washing step of washing the poly(arylene sulfide) resin produced by a polymerization reaction with a hydrophilic organic solvent containing water in a proportion of 1 to 30% by mass.

Assignees

• Taniguchi Shingo
• Sakabe Hiroshi
• Yoshida Yui
• Sunagawa Kazuhiko
• Kureha Corp

Inventors

• Taniguchi Shingo
• Sakabe Hiroshi
• Yoshida Yui
• Sunagawa Kazuhiko

Classifications

• D01F6/765 Primary

  from polyarylene sulfides · CPC title

• Y10T428/249921

  Web or sheet containing structurally defined element or component · CPC title

• C08G75/0231

  containing chain-terminating or chain-branching agents · CPC title

• C08G75/0281

  Recovery or purification · CPC title

• C08G75/0254

  using metal sulfides · CPC title