Method of controlling microdroplet growth in polymeric dispersed liquid crystal

• US 4,673,255 A
• Filed: 06/27/1986
• Issued: 06/16/1987
• Est. Priority Date: 05/22/1986
• Status: Expired due to Term

• Current Assignee: Kent State University
• Original Assignee: Kent State University
• Inventors: West, John, Doane, Joseph W., Golemme, Attilio
• Primary Examiner(s): Arnold, Bruce Y.
• Assistant Examiner(s): Gallivan, Richard F.
• Application Number:
  US06/879,269
• Time in Patent Office: 354 Days
• Field of Search: 350/320, 350/347 V, 350/347 R, 350/350 R, 350/351
• US Class Current: 349/92
• CPC Class Codes: C09K 19/544 as dispersing or encapsulating medium around the liquid crystal
• CPC Class Codes: G02F 1/1334 based on polymer dispersed liquid crystals, e.g. microencapsulated liquid crystals

Abstract

The invention provides a method of controlling the rate of growth of liquid crystal microdroplets formed in situ by the phase separation of a homogeneous solution of liquid crystal and polymer. Temperature, relative concentration and choice of materials determine the microdroplet growth rate and resultant microdroplet size and density. Controlling growth rate allows for fabrication of liquid crystal display devices with optimized display characteristics and response times.

Claims

1. In a method of making liquid crystal microdroplets dispersed in a polymeric matrix by phase separating a homogeneous solution of liquid crystal and polymer, the improvement comprising the step of controlling microdroplet growth so that the microdroplets have a selected average diameter when phase separation is complete.

2. The improvement as claimed in claim 1 wherein the homogeneous solution comprises a curable synthetic polymer and liquid crystal and wherein the step of controlling microdroplet growth is carried out by controlling the rate of curing.

3. The improvement as claimed in claim 2 wherein controlling the rate of curing is carried out by selecting a curable synthetic polymer having a predetermined curing rate at a given temperature.

4. The improvement as claimed in claim 3 including the further step of adjusting the temperature at which curing occurs to accelerate or retard the rate of curing.

5. The improvement as claimed in claim 4 wherein the temperature is about room temperature to 80°

C.

6. The improvement as claimed in claim 4 wherein the temperature is adjusted to yield microdroplets having an average diameter of about 0.1 to 8 microns.

7. The improvement as claimed in claim 2 wherein controlling the rate of curing is carried out by adjusting the intensity of ultraviolet radiation.

8. The improvement as claimed in claim 2 wherein the step of controlling the rate of curing is carried out by adjusting the temperature of which curing occurs.

9. The improvement as claimed in claim 1 wherein the step of controlling microdroplet growth is carried out by adjusting the ratio of liquid crystal to polymer.

10. The improvement as claimed in claim 9 in which the ratio of liquid crystal to polymer is about 1:

9 to about 1;

1 by weight.

11. The improvement as claimed in claim 10 wherein the temperature is about room temperature to 80°

C.

12. The improvement as claimed in claim 10 wherein the temperature is adjusted to yield microdroplets having an average diameter of about 0.1 to 8 microns.

13. The improvement as claimed in claim 1 wherein the homogeneous solution comprises liquid crystal and thermoplastic polymer heated to a temperature sufficient to dissolve the liquid crystal and wherein the step of controlling microdroplet growth is carried out by controlling the rate of cooling of the heated solution.

14. The improvement as claimed in claim 13 wherein the rate of cooling is about 0.2°

to 4°

C. per minute.

15. The improvement as claimed in claim 13 wherein the rate of cooling is effective to yield microdroplets having an average diameter of about 0.1 to 8 microns.

16. The improvement as claimed in claim 1 wherein the ratio of liquid crystal to polymer is about 1:

9 to about 1;

1 by weight.

17. The improvement as claimed in claim 1 wherein the step of controlling microdroplet growth is carried out by adjusting the rate of evaporation of a solvent from the homogeneous solution.