IP Library Granted Patent US 8,124,241
Granted Patent B2
US 8,124,241 · App. 12/224,533 · Granted Feb 28, 2012

Process for producing multilayer polymide film

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Quick Facts
Patent No.
US 8,124,241
App. No.
12/224,533
Granted
Feb 28, 2012
Kind
B2
Abstract

It is an object of the present invention to provide a method for manufacturing a multilayer polyimide film, uniform in film thickness and rate of dimensional change in the width direction of the film, which has a thermoplastic polyimide layer or the like serving as an adhesive layer. The object is attained by a method for manufacturing a multilayer polyimide film by width-spreading and flow-casting at least two types of polyimide resin solutions or polyimide precursor resin solutions fed into a multilayer coextrusion die including a plurality of flow channels, the method being characterized in that the thickness of each layer of the multilayer film is controlled by adding a solvent to the resin solutions to be fed into at least one of the flow channels and by adjusting, independently of the amounts of the resin solutions to be fed, the amount of the solvent to be added.

Claims (26)

1. A method for manufacturing a multilayer polyimide film in which a thickness of each layer is controlled, including the steps of: preparing at least two types of polyimide resin solutions or polyimide precursor resin solutions; feeding the resin solutions to a multilayer coextrusion die via a plurality of flow channels, respectively; and width-spreading and flow-casting the resin solutions, the method comprising the steps of:

adding a solvent to the resin solutions to be fed into at least one of the flow channels; and

adjusting, independently of amounts of the resin solutions to be fed, an amount of the solvent to be added.

2. The method as set forth in claim 1 , wherein:

the multilayer coextrusion die is a three-layer coextrusion die; and

the solvent is added only to a resin solution to be fed into a flow channel corresponding to a central layer.

3. The method as set forth in claim 1 , further comprising the step of adding, to the resin solutions to be fed into at least one of the flow channels, a solution containing a chemical dehydrating agent and an imidization catalyst.

4. The method as set forth in claim 3 , wherein:

the multilayer coextrusion die is a three-layer coextrusion die; and

the solution containing the chemical dehydrating agent and the imidization catalyst is added only to a resin solution to be fed into a flow channel corresponding to a central layer.

5. The method as set forth in claim 3 , further comprising the step of adjusting, independently of an amount of the solution, containing the chemical dehydrating agent and the imidization catalyst, to be added, the amount of the solvent to be added.

6. The method as set forth in claim 1 , wherein:

one of the at least two types of polyimide resin solutions or polyimide precursor resin solutions is a non-thermoplastic polyimide solution or a precursor resin solution thereof; and

the other one of the at least two types of polyimide resin solutions or polyimide precursor resin solutions is a thermoplastic polyimide solution or a precursor resin solution thereof.

7. The method as set forth in claim 6 , wherein:

the multilayer coextrusion die is a three-layer coextrusion die;

the non-thermoplastic polyimide solution or the precursor resin solution thereof is fed into a flow channel corresponding to a central layer; and

the thermoplastic polyimide solution or the precursor resin solution thereof is fed into two remaining flow channels.

8. A multilayer polyimide film, having at least two types of polyimide layers, which is obtained by a manufacturing method including the steps of: preparing at least two types of polyimide resin solutions or polyimide precursor resin solutions; feeding the resin solutions to a multilayer coextrusion die via a plurality of flow channels, respectively; and width-spreading and flow-casting the resin solutions, the method further including the steps of: adding a solvent to the resin solutions to be fed into at least one of the flow channels; and adjusting, independently of amounts of the resin solutions to be fed, an amount of the solvent to be added,

the multilayer polyimide film having layers each of whose deviations in component ratio of film thickness in a film-width direction falls within a range of not less than −10% to not more than 10%.

9. The multilayer polyimide film as set forth in claim 8 , wherein the multilayer polyimide film is a multilayer film obtained by laminating, on at least one surface of a non-thermoplastic polyimide layer, an adhesive layer containing a thermoplastic polyimide.

10. The multilayer polyimide film as set forth in claim 8 , wherein the deviation in component ratio of film thickness in the film-width direction falls within a range of not less than −5% to not more than 5%.

11. A multilayer polyimide film, having at least two types of polyimide layers, which is obtained by a manufacturing method including the steps of: preparing at least two types of polyimide resin solutions or polyimide precursor resin solutions; feeding the resin solutions to a multilayer coextrusion die via a plurality of flow channels, respectively; and width-spreading and flow-casting the resin solutions, the method further including the steps of: adding a solvent to the resin solutions to be fed into at least one of the flow channels; and adjusting, independently of amounts of the resin solutions to be fed, an amount of the solvent to be added,

the multilayer polyimide film having a deviation of not less than −0.05% to not more than 0.05% in rate of dimensional change in a film-width direction.

12. The multilayer polyimide film as set forth in claim 11 , wherein the multilayer polyimide film is a multilayer film obtained by laminating, on at least one surface of a non-thermoplastic polyimide layer, an adhesive layer containing a thermoplastic polyimide.

13. The multilayer polyimide film as set forth in claim 11 , wherein the deviation in rate of dimensional change in the film-width direction falls within a range of not less than −0.03% to not more than 0.03%.

Assignments (1)
CHANGE OF ADDRESS Recorded Jan 15, 2014
From: KANEKA CORPORATION
To: KANEKA CORPORATION
Reel/Frame 032019/0901 →