Liquid crystalline polyurethane elastomer and method for producing same

Abstract

A liquid crystalline polyurethane elastomer is produced by reacting an isocyanate component, a high-molecular-weight polyol component and a mesogenic diol represented by formula (1), and having a crosslinking site that is introduced by a tri-functional or higher isocyanate in the isocyanate component and/or a high-molecular-weight polyol having a number average molecular weight of 400 or more and less than 7000 and having three or more hydroxy groups, in the high-molecular-weight polyol component, wherein the melting point of a mesogenic unit does not exist in a temperature range lying between the glass transition temperature (Tg) and the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) of the polyurethane elastomer, and a liquid crystal is developed at a temperature between the Tg and the Ti. (In the formula, X represents an alkylene group having 3 to 20 carbon atoms; and Y represents a single bond, —N═N—, —CO—, —CO—O— or —CH═N—). ##STR00001##

Claims

1. A liquid crystalline polyurethane elastomer, which is produced by reacting at least an isocyanate component, a high-molecular-weight polyol and a mesogenic diol represented by general formula (1) with one another, and has a crosslinking site that is introduced by a tri-functional or higher isocyanate in the isocyanate component and/or the high-molecular-weight polyol having three or more hydroxy groups, wherein the melting point of a mesogenic unit does not exist in a temperature range lying between the glass transition temperature (Tg) and the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) of the polyurethane elastomer, and a liquid crystal is developed at a temperature between the Tg and the Ti, and wherein the high-molecular-weight polyol has a number average molecular weight of 400 or more and less than 7000, ##STR00006## wherein in the formula, X represents an alkylene group having 3 to 20 carbon atoms; and Y represents a single bond, —N═N—, —CO—, —CO—O— or —CH═N—.

2. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents a single bond, —N═N— or —CO— is used; the glass transition temperature (Tg) is −50 to 30° C.; and the (liquid crystal phase)-to-(isotropic phase)transition temperature (Ti) is 35 to 85° C.

3. The liquid crystalline polyurethane elastomer according to claim 2, wherein the mesogenic diol when Y represents a single bond, —N═N— or —CO— is used; the blending amount of the mesogenic diol is 10 to 50 wt % based on the total material components; and the molecular weight between crosslinks is 1500 to 20000.

4. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents a single bond, —N═N— or —CO— is used; the blending amount of the mesogenic diol is 10 to 50 wt % based on the total material components; and the molecular weight between crosslinks is 1500 to 20000.

5. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents —CO—O— is used; the glass transition temperature (Tg) is −60° C. or higher and less than 30° C.; and the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) is 30 to 130° C.

6. The liquid crystalline polyurethane elastomer according to claim 5, wherein the mesogenic diol when Y represents —CO—O— is used; the blending amount of the mesogenic diol is 30 to 80 wt % based on the total material components; and the molecular weight between crosslinks is 2500 to 25000.

7. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents —CO—O— is used; the blending amount of the mesogenic diol is 30 to 80 wt % based on the total material components; and the molecular weight between crosslinks is 2500 to 25000.

8. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents —CH═N— is used; the glass transition temperature (Tg) is −50 to 30° C.; and the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) is 35 to 120° C.

9. The liquid crystalline polyurethane elastomer according to claim 8, wherein the mesogenic diol when Y represents —CH═N— is used; the blending amount of the mesogenic diol is 15 to 70 wt % based on the total material components; and the molecular weight between crosslinks is 1500 to 25000.

10. The liquid crystalline polyurethane elastomer according to claim 1, wherein the mesogenic diol when Y represents —CH═N— is used; the blending amount of the mesogenic diol is 15 to 70 wt % based on the total material components; and the molecular weight between crosslinks is 1500 to 25000.

11. A method for producing a liquid crystalline polyurethane elastomer of claim 1, which method comprises reacting at least an isocyanate component and a high-molecular-weight polyol to synthesize an isocyanate-terminated prepolymer and reacting the resulting isocyanate-terminated prepolymer with a mesogenic diol, wherein the high-molecular-weight polyol has a number average molecular weight of 400 or more and less than 7000.

Description

MODE FOR CARRYING OUT THE INVENTION

(1) The liquid crystalline polyurethane elastomer of the present invention is obtained by reacting at least an isocyanate component, a high-molecular-weight polyol component and a mesogenic diol represented by the following general formula (1):

(2) ##STR00003##
(In the formula, X represents an alkylene group having 3 to 20 carbon atoms; and Y represents a single bond, —N═N—, —CO—, —CO—O— or —CH═N—.)

(3) As the isocyanate component, it is preferable to use a tri-functional or higher isocyanate, and particularly preferable to use a tri-functional isocyanate so as to form a network by introducing a crosslinking site into the liquid crystalline polyurethane elastomer. The tri-functional or higher isocyanates include, for example, triisocyanates (e.g., triphenylmethane triisocyanate, tris(isocyanatephenyl)thio-phosphate, lysine ester triisocyanate, 1,3,6-hexamethylene triisocyanate, 1,6,11-undecane triisocyanate, 1,8-diisocyanate-4-isocyanate methyloctane, and bicycloheptane triisocyanate) and tetraisocyanates (e.g., tetraisocyanate silane). These may be used alone or in combination of two or more thereof. It may also be possible to use a polymerized diisocyanate. As used herein, the term ‘polymerized diisocyanate’ refers to any of polymerized isocyanate derivatives produced by addition of three or more molecules of diisocyanate, or refers to a mixture of the isocyanate derivatives. For example, the isocyanate derivative may be of (1) trimethylolpropane adduct type, (2) biuret type, (3) isocyanurate type, or the like. In particular, the isocyanurate type is preferred.

(4) As the isocyanate component, it is preferable to use only the tri-functional or higher isocyanate, but diisocyanates may be used in combination within a range that does not impair the object of the present invention. The diisocyanates include, for example, aromatic diisocyanates such as 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, 2,2′-diphenyl methane diisocyanate, 2,4′-diphenyl methane diisocyanate, 4,4′-diphenyl methane diisocyanate, 1,5-naphthalene diisocyanate, p-phenylene diisocyanate, m-phenylene diisocyanate, p-xylylene diisocyanate and m-xylylene diisocyanate, aliphatic diisocyanates such as ethylene diisocyanate, 2,2,4-trimethyl hexamethylene diisocyanate and 1,6-hexamethylene diisocyanate, and cycloaliphatic diisocyanates such as 1,4-cyclohexane diisocyanate, 4,4′-dicyclohexyl methane diisocyanate, isophorone diisocyanate and norbornane diisocyanate. These may be used alone or as a mixture of two or more thereof.

(5) As the high-molecular-weight polyol component, it is preferable to use a high-molecular-weight polyol having a number average molecular weight of 400 or more and less than 7000 and having three or more hydroxyl groups so as to form a network by introducing a crosslinking site into the liquid crystalline polyurethane elastomer. The number average molecular weight of such a polyol component is preferably 400 to 6000, more preferably 700 to 5000. The number of hydroxyl groups is more preferably 3. The high-molecular-weight polyol includes polyether polyols, polyester polyols, polycarbonate polyols, polyester polycarbonate polyols, and the like. These polyols may be used alone or in combination of two or more thereof. Among these, it is particularly preferred to use a polyether polyol.

(6) It is preferable to use only the high-molecular-weight polyol component having a number average molecular weight of 400 or more and less than 7000 and having three or more hydroxyl groups, but other high-molecular-weight polyols may be used in combination within a range that does not impair the object of the present invention.

(7) In addition to the high-molecular-weight polyol component, an active hydrogen group-containing low molecular weight compound may be used within a range that does not impair the object of the present invention. The active hydrogen group-containing low molecular weight compound refers to a compound having a molecular weight of less than 400, examples thereof include a low molecular weight polyol such as ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 2,3-butanediol, 1,6-hexanediol, neopentyl glycol, 1,4-cyclohexanedimethanol, 3-methyl-1,5-pentanediol, diethylene glycol, triethyleneglycol, 1,4-bis(2-hydroxyethoxy)benzene, trimethylolpropane, glycerin, 1,2,6-hexanetriol, pentaerythritol, tetramethylolcyclohexane, methyl glucoside, sorbitol, mannitol, dulcitol, sucrose, 2,2,6,6-tetrakis(hydroxymethyl)cyclohexanol, diethanolamine, N-methyldiethanolamine, triethanolamine and the like; a low molecular weight polyamine such as ethylenediamine, tolylenediamine, diphenylmethanediamine, diethylenetriamine and the like; an alcoholamines such as monoethanolamine, 2-(2-aminoethylamino) ethanol, monopropanolamine and the like. These active hydrogen group-containing low molecular weight compound may be used alone or as a mixture of two or more thereof.

(8) The mesogenic diol represented by the general formula (1) has a biphenyl skeleton (Y is a single bond), an azobenzene skeleton (Y is —N═N—), a benzophenone skeleton (Y is —CO—), an ester skeleton (Y is —CO—O—), or an imine skeleton (Y is —CH═N—). These may be used alone or in combination of two or more thereof. In particular, it is preferable to use those having a biphenyl skeleton, an ester skeleton, or an imine skeleton. In the formula (1), X is an alkylene group having 3 to 20 carbon atoms, preferably an alkylene group having 5 to 10 carbon atoms. Of the mesogenic diol represented by the general formula (1), it is particularly preferred to use 4,4′-bis(6-hydroxyhexyloxy)biphenyl or 4,4′-bis(6-hydroxydecane-1-oxy) biphenyl.

(9) The blending amount of the mesogenic diol when Y is a single bond, —N═N—, or —CO— is preferably 10 to 50 wt %, more preferably 15 to 40 wt %, based on the total material components.

(10) The blending amount of the mesogenic diol when Y is —CO—O— is preferably 30 to 80 wt %, more preferably 35 to 80 wt %, still more preferably 35 to 60 wt %, based on the total material components.

(11) The blending amount of the mesogenic diol when Y is —CH═N— is preferably 15 to 70 wt %, more preferably 20 to 60 wt %, based on the total material components.

(12) The liquid crystalline polyurethane elastomer of the present invention may be prepared by a prepolymer method or a one-shot method, but the liquid crystalline polyurethane elastomer is prepared preferably by the prepolymer method comprising the reaction of an isocyanate component with a high-molecular-weight polyol component to synthesize an isocyanate-terminated prepolymer, which is then allowed to react with a mesogenic diol.

(13) In the case of using a mesogenic diol when Y is a single bond, —N═N—, or —CO—, the number of isocyanate groups of the isocyanate component is preferably 2 to 6, more preferably 2 to 4, in the synthesis of the isocyanate-terminated prepolymer, relative to the number of active hydrogen groups (such as a hydroxyl group) of an active hydrogen group-containing compound. Further, in that case, the NCO wt % is preferably adjusted to 4 to 20 wt %, more preferably 4 to 14 wt %, in the synthesis of an isocyanate-terminated prepolymer.

(14) In the case of using a mesogenic diol when Y is —CO—O—, the number of isocyanate groups of the isocyanate component is preferably 2 to 10, more preferably 2 to 8, in the synthesis of the isocyanate-terminated prepolymer, relative to the number of active hydrogen groups (such as a hydroxyl group) of an active hydrogen group-containing compound. Further, in that case, the NCO wt % is preferably adjusted to 4 to 30 wt %, more preferably 4 to 26 wt %, in the synthesis of an isocyanate-terminated prepolymer.

(15) In the case of using a mesogenic diol when Y is —CH═N—, the number of isocyanate groups of the isocyanate component is preferably 2 to 10, more preferably 2 to 7, in the synthesis of the isocyanate-terminated prepolymer, relative to the number of active hydrogen groups (such as a hydroxyl group) of an active hydrogen group-containing compound. Further, in that case, the NCO wt % is preferably adjusted to 4 to 30 wt %, more preferably 4 to 25 wt %, in the synthesis of an isocyanate-terminated prepolymer.

(16) The liquid crystalline polyurethane elastomer of the present invention can be prepared using known urethane formation techniques such as a melting method or a solution method. A catalyst that promotes the known polyurethane reaction, such as tertiary amines and the like, may be used.

(17) In the case of using a mesogenic diol when Y is a single bond, —N═N—, or —CO—, the liquid crystalline polyurethane elastomer has a molecular weight between crosslinks of preferably 1500 to 20000, more preferably 2000 to 18000. Also, in that case, the glass transition temperature (Tg) of the liquid crystalline polyurethane elastomer is preferably −50 to 30° C., more preferably −50 to 25° C. Further, in that case, the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) is preferably 35 to 85° C., more preferably 35 to 75° C.

(18) In the case of using a mesogenic diol when Y is —CO—O—, the liquid crystalline polyurethane elastomer has a molecular weight between crosslinks of preferably 2500 to 25000, more preferably 3000 to 25000. Also, in that case, the glass transition temperature (Tg) of the liquid crystalline polyurethane elastomer is preferably −60° C. or higher and less than 30° C., more preferably −60 to 25° C., still more preferably −30 to 20° C. Further, in that case, the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) is preferably 30 to 130° C., more preferably 30 to 115° C., still more preferably 30 to 105° C.

(19) In the case of using a mesogenic diol when Y is —CH═N—, the liquid crystalline polyurethane elastomer has a molecular weight between crosslinks of preferably 1500 to 25000, more preferably 2000 to 22000, still more preferably 3000 to 20000. Also, in that case, the glass transition temperature (Tg) of the liquid crystalline polyurethane elastomer is preferably −50 to 30° C., more preferably −50 to 25° C., still more preferably −45 to 20° C. Further, in that case, the (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) is preferably 35 to 120° C., more preferably 35 to 100° C.

(20) Further, the liquid crystalline polyurethane elastomers of the present invention are those having rubbery elasticity when a liquid crystal is developed, and the storage elastic modulus when a liquid crystal is developed is preferably from 0.01 to 500 MPa, more preferably 0.05 to 100 MPa.

EXAMPLES

(21) Description will be given of the invention with examples, while the invention is not limited to description in the examples.

(22) [Measurement and Evaluation Method]

(23) (Calculation of Content of Mesogenic Diol)

(24) The content of the mesogenic diol in the polyurethane elastomer was calculated by the following equation.
Content of mesogenic diol (wt %)={(Weight of mesogenic diol)/(Weight of total material components of polyurethane elastomer)}×100
(Calculation of Molecular Weight Between Crosslinks)

(25) The molecular weight between crosslinks of the polyurethane elastomer was calculated by the following equation.
Molecular weight between crosslinks=(Weight of total material components of polyurethane elastomer)/(A×B)
A=(Hydroxyl value of high-molecular-weight polyol having three or more hydroxyl groups)/56.1
B=(Weight of high-molecular-weight polyol having three or more hydroxyl groups)/(Number of hydroxyl groups of high-molecular-weight polyol×1000)
(Measurement of Glass Transition Temperature (Tg) of Polyurethane Elastomer, Melting Point (Tm) of Mesogenic Unit, and (Liquid Crystal Phase)-to-(Isotropic Phase) Transition Temperature (Ti))

(26) The Tg, Tm, and Ti were measured under the condition of 20° C./min using a differential scanning calorimeter DSC (manufactured by Hitachi High-Tech Science Corp., trade name: X-DSC 7000).

(27) (Evaluation of Liquid Crystallinity)

(28) The presence or absence of liquid crystal development of the polyurethane elastomer was evaluated by using a polarization microscope (manufactured by Nikon Corporation, trade name: LV-100POL) and a differential scanning calorimeter DSC (manufactured by Hitachi High-Tech Science Corp., trade name: X-DSC 7000) under the condition of 20° C./min.

(29) (Discriminating Method of Melting Point (Tm) of Mesogenic Unit and (Liquid Crystal Phase)-to-(Isotropic Phase) Transition Temperature (Ti))

(30) Discrimination of melting point (Tm) of a mesogenic unit and (liquid crystal phase)-to-(isotropic phase) transition temperature (Ti) was performed under the conditions of 2°/min and 20° C./min by using a polarization microscope (manufactured by Nikon Corporation, trade name: LV-100POL) and an X-ray diffraction apparatus (Rigaku Corporation, trade name: RINT-Ultima III).

(31) (Measurement of Storage Elastic Modulus (E′) when Liquid Crystal is Developed)

(32) The storage elastic modulus of the polyurethane elastomer when a liquid crystal is developed therein was measured under the conditions of 2° C./min, strain 2%, and 10 Hz using a VES (manufactured by Ueshima Seisakusho Co., Ltd., trade name: fully automatic viscoelasticity analyzer VR-7110).

EXAMPLE IN CASE OF USING MESOGENIC DIOL WHEN Y IS A SINGLE BOND

Production Example 1

(33) (Synthesis of Mesogenic Diol)

(34) After ethanol (manufactured by Nacalai Tesque Inc.) 1.5 L was placed in a reaction vessel, sodium hydroxide (manufactured by Nacalai Tesque Inc.) 120 g was added thereto and the mixture was dissolved. Thereafter, 4,4′-biphenol (manufactured by Tokyo Chemical Industry Co., Ltd.) 140 g was added thereto and the mixture was heated under reflux for 30 minutes. Then, 6-chloro-1-hexanol (manufactured by Tokyo Chemical Industry Co., Ltd.) 451 g was dropwise added thereto, and the reaction solution was stirred at 90° C. for 12 hours. After that, the reaction solution was subjected to suction filtration and the resulting precipitates were washed with water, recrystallized from a mixed solvent of DMF (manufactured by Mitsubishi Gas Chemical Company, Inc.)/ethanol (1/3), and further recrystallized from 1-butanol (manufactured by Nacalai Tesque Inc.) to obtain 4,4′-bis(6-hydroxyhexyloxy)biphenyl 170 g.

Production Example 2

(35) (Synthesis of Isocyanate-Terminated Prepolymer A)

(36) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1030, number of hydroxyl groups: 3, number average molecular weight: 1000) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 74.4 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer A (NCO index: 3, isocyanate content: 13.7 wt %).

Production Example 3

(37) (Synthesis of Isocyanate-Terminated Prepolymer B)

(38) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1030, number of hydroxyl groups: 3, number average molecular weight: 1000) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 49.6 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer B (NCO index: 2, isocyanate content: 8.01 wt %).

Production Example 4

(39) (Synthesis of Isocyanate-Terminated Prepolymer C)

(40) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 903, number of hydroxyl groups: 3, number average molecular weight: 1500) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 53.0 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer C (NCO index: 3, isocyanate content: 11.2 wt %).

Production Example 5

(41) (Synthesis of Isocyanate-Terminated Prepolymer D)

(42) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 3030, number of hydroxyl groups: 3, number average molecular weight: 1000) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 26.1 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer D (NCO index: 3, isocyanate content: 6.7 wt %).

Production Example 6

(43) (Synthesis of Isocyanate-Terminated Prepolymer E)

(44) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 2020, number of hydroxyl groups: 2, number average molecular weight: 2000) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 26.1 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer E (NCO index: 3, isocyanate content: 6.7 wt %).

Production Example 7

(45) (Synthesis of Isocyanate-Terminated Prepolymer F)

(46) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 850, number of hydroxyl groups: 3, number average molecular weight: 7000) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 52.5 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer F (NCO index: 3, isocyanate content: 3.3 wt %).

Production Example 8

(47) (Synthesis of Isocyanate-Terminated Prepolymer G)

(48) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 430, number of hydroxyl groups: 3, number average molecular weight: 400) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 260 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer G (NCO index: 3, isocyanate content: 16.14 wt %).

Production Example 9

(49) (Synthesis of Isocyanate-Terminated Prepolymer H)

(50) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 430, number of hydroxyl groups: 3, number average molecular weight: 400) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 174 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer H (NCO index: 2, isocyanate content: 23.84 wt %).

Production Example 10

(51) (Synthesis of Isocyanate-Terminated Prepolymer I)

(52) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 720, number of hydroxyl groups: 2, number average molecular weight: 700) 100 g and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) 49.6 g were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer I (NCO index: 2, isocyanate content: 8.01 wt %).

Example 1

(53) (Preparation of Polyurethane Elastomer)

(54) Dehydrated DMF (manufactured by Wako Pure Chemical Industries, Ltd.) 60 ml was placed in a reaction vessel, to which was added 4,4′-bis(6-hydroxyhexyloxy)biphenyl 10 g, and the mixture was dissolved. Thereafter, isocyanate-terminated prepolymer A 18.85 g prepared in Production Example 2 and a catalyst (manufactured by Tosoh Corporation, trade name: TEDA-L33) 0.1 g were added to the reaction vessel, followed by stirring at 80° C. for 30 minutes. Then, defoamed reaction solution was poured into a mold which had been previously heated to 80° C., and cured at 80° C. to prepare a cured sheet. DMF in the cured sheet obtained was removed with a vacuum dryer to produce a polyurethane elastomer sheet.

Examples 2 to 5 and Comparative Examples 1 to 5

(55) A polyurethane elastomer sheet was produced in the same manner as in Example 1, except that the starting materials and the blending amounts shown in Table 1 are employed. The T-9 in Table 1 is a catalyst manufactured by Toei Chemical Industries, Co., Ltd.

(56) TABLE-US-00001 TABLE 1 Storage elastic Molecular modulus (MPa) Mesogenic Mesogenic weight when a liquid Prepolymer diol diol content Catalyst between Tg Tm Ti Liquid crystal is (g) (g) (wt %) (g) crosslinks (° C.) (° C.) (° C.) crystallinity developed Example 1 A (15.90) 10 39 TEDA-L33 (0.1) 2988 10 — 60 Present 1~100 Example 2 B (27.27) 10 27 TEDA-L33 (0.1) 2150 20 — 84 Present 1~100 Example 3 C (19.80) 10 34 TEDA-L33 (0.1) 3420 −3 — 63 Present 0.1~100.sup.  Example 4 D (8.93), E(26.8) 10 18 T-9 (0.1) 14517 −24 — 48 Present 0.01~1    Example 5 D (7.15), E(28.58) 10 18 T-9 (0.1) 17744 −43 — 36 Present 0.01~1    Comparative F (92.71) 10 9.7 T-9 (0.1) 8638 −51 — — Absent — Example 1 Comparative G (9.15) 10 52.2 — 2394 66 77 102  Present 750~1000  Example 2 Comparative H (13.53) 10 43 — 1429 — — — Absent — Example 3 Comparative D (3.57), E(32.2) 10 18 T-9 (0.1) 33874 — — — Absent — Example 4 Comparative I (27.27) 10 27 T-9 (0.1) — −4 115  121  Present — Example 5

(57) The polyurethane elastomers of Examples 1 to 5 were those exhibiting a liquid crystallinity, showing a low liquid crystal-developing temperature, and having rubbery elasticity when a liquid crystal is developed therein. The polyurethane elastomer of Comparative Example 1 did not develop a liquid crystallinity because of a small content of the mesogenic diol. Since the content of the mesogenic diol in the polyurethane elastomer of Comparative Example 2 is too much, the melting point (Tm) of a mesogenic unit exists at a temperature between the Tg and the Ti, resulting in failure to develop the liquid crystallinity at the low temperature. Since the polyurethane elastomer of Comparative Example 3 has a too small molecular weight between crosslinks, it did not have a rubbery elasticity. Since the polyurethane elastomer of Comparative Example 4 has a too large molecular weight between crosslinks, it did not cure. Since the polyurethane elastomer of Comparative Example 5 has no crosslinking site, it could not inhibit the crystallinity of a mesogenic unit and the melting point (Tm) of a mesogenic unit exists, causing no development of a liquid crystallinity at room temperature. Moreover, such polyurethane elastomers were those having an increased fluidity when a liquid crystal is developed therein and having no rubbery elasticity.

EXAMPLE IN CASE OF USING MESOGENIC DIOL WHEN Y IS —CO—O—

Production Example 1

(58) (Synthesis of Mesogenic Diol)

(59) To a reaction vessel were added p-hydroxybenzoic acid (manufactured by Nacalai Tesque Inc.) 103.5 g, hydroquinone (manufactured by Nacalai Tesque Inc.) 82.5 g, boric acid (manufactured by Nacalai Tesque Inc.) 1.5 g, and xylene (manufactured by Nacalai Tesque Inc.) 450 ml, and the mixture was stirred and concentrated sulfuric acid (manufactured by Nacalai Tesque Inc.) 2.1 g was dropwise added thereto. Then, the mixture was heated under reflux for 5 hours using a Dean-Stark tube. Thereafter, the reaction product was subjected to suction filtration to obtain a solid material. The obtained solid was neutralized with 1% aqueous sodium hydrogen carbonate solution (250 ml). Thereafter, the solid was collected by filtration, washed with water, and dried in vacuo. Then, the dried product was recrystallized from a mixed solvent of acetone and water to obtain 4-hydroxyphenyl p-hydroxybenzoate (105.77 g) as a white powder.

(60) Subsequently, 4-hydroxyphenyl p-hydroxybenzoate (90 g), potassium carbonate (162 g), and DMF (manufactured by Mitsubishi Gas Chemical Company, Inc.) 700 ml were placed in a reaction vessel, and the mixture was heated to 60° C. Thereafter, 6-chloro-1-hexanol (manufactured by Tokyo Chemical Industry Co., Ltd.) 160 g was dropwise added to the reaction vessel, and the mixture was heated under ref lux at 90° C. for 23 hours. After addition of 1 L of water to the reaction vessel, concentrated sulfuric acid (manufactured by Nacalai Tesque Inc.) was further added thereto until the mixture became acidic, and the solvent was distilled under reduced pressure. The resulting solid was purified by wet column chromatography (SiO.sub.2, ethyl acetate/hexane) and recrystallized from ethyl acetate to obtain the following compound A (6 g) as a white solid.

(61) ##STR00004##

Production Example 2

(62) (Synthesis of Isocyanate-Terminated Prepolymer B)

(63) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 903, number of hydroxyl groups: 3, number average molecular weight: 1500) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer B (NCO index: 3, isocyanate content: 11 wt %).

Production Example 3

(64) (Synthesis of Isocyanate-Terminated Prepolymer C)

(65) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 903, number of hydroxyl groups: 3, number average molecular weight: 1500) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer C (NCO index: 6.6, isocyanate content: 21.9 wt %).

Production Example 4

(66) (Synthesis of Isocyanate-Terminated Prepolymer D)

(67) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1020, number of hydroxyl groups: 2, number average molecular weight: 1000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer D (NCO index: 6.6, isocyanate content: 21.9 wt %).

Production Example 5

(68) (Synthesis of Isocyanate-Terminated Prepolymer E)

(69) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1030, number of hydroxyl groups: 3, number average molecular weight: 1000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer E (NCO index: 6.6, isocyanate content: 25.4 wt %).

Production Example 6

(70) (Synthesis of Isocyanate-Terminated Prepolymer F)

(71) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 720, number of hydroxyl groups: 2, number average molecular weight: 700) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer F (NCO index: 6.6, isocyanate content: 25.4 wt %).

Production Example 7

(72) (Synthesis of Isocyanate-Terminated Prepolymer G)

(73) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 3030, number of hydroxyl groups: 3, number average molecular weight: 3000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer G (NCO index: 5, isocyanate content: 11.7 wt %).

Production Example 8

(74) (Synthesis of Isocyanate-Terminated Prepolymer H)

(75) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 850, number of hydroxyl groups: 3, number average molecular weight: 7000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer H (NCO index: 5, isocyanate content: 6.1 wt %).

Production Example 9

(76) (Synthesis of Isocyanate-Terminated Prepolymer I)

(77) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 430, number of hydroxyl groups: 3, number average molecular weight: 400) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer I (NCO index: 2.5, isocyanate content: 17.5 wt %).

Example 1

(78) (Preparation of Polyurethane Elastomer)

(79) Dehydrated DMF (manufactured by Wako Pure Chemical Industries, Ltd.) 3 ml was placed in a reaction vessel, and to this was added the compound A (0.5 g) prepared in Production Example 1. After dissolving the mixture, the isocyanate-terminated prepolymer B (0.88 g) prepared in Production Example 2 was added to the reaction vessel, and the mixture was stirred at 80° C. for 30 minutes. Then, defoamed reaction solution was poured into a mold which had been previously heated to 80° C., and cured at 80° C. to prepare a cured sheet. DMF in the cured sheet obtained was removed with a vacuum dryer to produce a polyurethane elastomer sheet.

Examples 2 to 4 and Comparative Examples 1 to 3

(80) A polyurethane elastomer sheet was produced in the same manner as in Example 1, except that the starting materials and the blending amounts shown in Table 2 are employed.

(81) TABLE-US-00002 TABLE 2 Storage elastic Compund A: Compound A: Molecular modulus (MPa) mesogenic mesogenic weight when a liquid Prepolymer diol diol content between Tg Tm Ti Liquid crystal is (g) (g) (wt %) crosslinks (° C.) (° C.) (° C.) crystallinity developed Example 1 B (0.88) 0.5 36 3559 −8.4 — 34 Present    1~100 Example 2 C (0.13), D (0.31) 0.5 53 22876 −2.1 — 103 Present 0.01~1 Example 3 E(0.19), F (0.19) 0.5 56 12856 12 — 64 Present 0.01~1 Example 4 G (0.83) 0.5 37 6379 −24 — 51 Present  0.1~10 Comparative H (1.21) 0.5 29 11756 −32 — — Absent — Example 1 Comparative C (0.11), D(0.33) 0.5 53 27451 — — — Absent — Example 2 Comparative I (0.56) 0.5 47 2188 — — — Present — Example 3

(82) The polyurethane elastomers of Examples 1 to 4 were those exhibiting a liquid crystallinity, showing a low liquid crystal-developing temperature, and having rubbery elasticity when a liquid crystal is developed therein. The polyurethane elastomer of Comparative Example 1 did not develop a liquid crystallinity because of a small content of the mesogenic diol. The polyurethane elastomer of Comparative Example 2 did not cure because it had a too large molecular weight between crosslinks. The polyurethane elastomer of Comparative Example 3 did not develop a liquid crystal because it had a too small molecular weight between crosslinks.

EXAMPLE IN CASE OF USING MESOGENIC DIOL WHEN Y IS —CH═N—

Production Example 1

(83) (Synthesis of Mesogenic Diol)

(84) 4-Aminophenol (manufactured by Tokyo Chemical Industry Co., Ltd.) 223 g, 4-hydroxybenzaldehyde (manufactured by Tokyo Chemical Industry Co., Ltd.) 250 g, acetic acid 1.8 g, and ethanol (manufactured by Nacalai Tesque Inc.) 800 ml were placed in a reaction vessel, and the mixture was heated under reflux for 3 hours. After cooling the reaction mixture to room temperature, water was added to the reaction vessel and the mixture was subjected to suction filtration to obtain a solid. The obtained solid was dried in vacuo and recrystallized from ethanol to obtain 4,4′-dihydroxybenzylideneaniline (335 g) as a white solid.

(85) Then, 4,4′-dihydroxybenzylideneaniline (175 g), 6-chloro-1-hexanol (manufactured by Tokyo Chemical Industry Co., Ltd.) 335 g, potassium carbonate (manufactured by Nacalai Tesque Inc.) 340 g, and DMF (manufactured by Mitsubishi Gas Chemical Company, Inc.) 1.5 L were placed in the reaction vessel, and the mixture was heated under reflux for 20 hours. After cooling the mixture to room temperature, hydrochloric acid was added to the reaction vessel until the reaction solution became acidic. Thereafter, water was added to the reaction vessel, and the mixture was subjected to suction filtration to obtain a solid. The resulting solid was dried in vacuo and recrystallized from water/ethanol (1/3) to obtain the following compound A (241 g) as a white solid.

(86) ##STR00005##

Production Example 2

(87) (Synthesis of Isocyanate-Terminated Prepolymer B)

(88) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 903, number of hydroxyl groups: 3, number average molecular weight: 1500) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer B (NCO index: 6.6, isocyanate content: 21.9 wt %).

Production Example 3

(89) (Synthesis of Isocyanate-Terminated Prepolymer C)

(90) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1030, number of hydroxyl groups: 3, number average molecular weight: 1000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer C (NCO index: 3, isocyanate content: 13.7 wt %).

Production Example 4

(91) (Synthesis of Isocyanate-Terminated Prepolymer D)

(92) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 3030, number of hydroxyl groups: 3, number average molecular weight: 3000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer D (NCO index: 2.5, isocyanate content: 5.18 wt %).

Production Example 5

(93) (Synthesis of Isocyanate-Terminated Prepolymer E)

(94) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 2020, number of hydroxyl groups: 2, number average molecular weight: 2000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer E (NCO index: 2.5, isocyanate content: 5.18 wt %).

Production Example 6

(95) (Synthesis of Isocyanate-Terminated Prepolymer F)

(96) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 850, number of hydroxyl groups: 3, number average molecular weight: 7000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer F (NCO index: 3, isocyanate content: 3.23 wt %).

Production Example 7

(97) (Synthesis of Isocyanate-Terminated Prepolymer G)

(98) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 1020, number of hydroxyl groups: 2, number average molecular weight: 1000) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer G (NCO index: 6.6, isocyanate content: 22.0 wt %).

Production Example 8

(99) (Synthesis of Isocyanate-Terminated Prepolymer H)

(100) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 430, number of hydroxyl groups: 3, number average molecular weight: 400) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer H (NCO index: 2, isocyanate content: 15.3 wt %).

Production Example 9

(101) (Synthesis of Isocyanate-Terminated Prepolymer I)

(102) Polypropylene glycol (manufactured by Asahi Glass Co., Ltd., trade name: EXCENOL 720, number of hydroxyl groups: 2, number average molecular weight: 700) and 2,4-tolylene diisocyanate (Nippon Polyurethane Industry Co., Ltd., trade name: T-100) were placed in a reaction vessel, stirred under a nitrogen stream, and reacted to obtain an isocyanate-terminated prepolymer I (NCO index: 2, isocyanate content: 8.01 wt %).

Example 1

(103) (Preparation of Polyurethane Elastomer)

(104) Dehydrated DMF (manufactured by Wako Pure Chemical Industries, Ltd.) 3 ml was placed in a reaction vessel, and to this was added the compound A (0.5 g) prepared in Production Example 1. After dissolving the mixture, the isocyanate-terminated prepolymer B (0.46 g) prepared in Production Example 2 was added to the reaction vessel, and the mixture was stirred at 80° C. for 30 minutes. Then, defoamed reaction solution was poured into a mold which had been previously heated to 80° C., and cured at 80° C. to prepare a cured sheet. DMF in the cured sheet obtained was removed with a vacuum dryer to produce a polyurethane elastomer sheet.

Examples 2 and 3 and Comparative Examples 1 to 4

(105) A polyurethane elastomer sheet was produced in the same manner as in Example 1, except that the starting materials and the blending amounts shown in Table 3 are employed.

(106) TABLE-US-00003 TABLE 3 Storage elastic Compund A: Compound A: Molecular modulus (MPa) mesogenic mesogenic weight when a liquid Prepolymer diol diol content between Tg Tm Ti Liquid crystal is (g) (g) (wt %) crosslinks (° C.) (° C.) (° C.) crystallinity developed Example 1 B (0.46) 0.5 52 6713 16 — 56 Present 1~100 Example 2 C (0.74) 0.5 40 3076 −1 — 92 Present 1~100 Example 3 D(1.47), E(0.49) 0.5 20 18335 −43 — 39 Present 0.01~1    Comparative F (3.14) 0.5 14 9032 −53 — — Absent — Example 1 Comparative B (0.12), G(0.35) 0.5 52 26775 — — — Absent — Example 2 Comparative H (0.66) 0.5 43 1447 47 — 64 Present 800~1000  Example 3 Comparative I (1.22) 0.5 29 — −7 82 103  Present — Example 4

(107) The polyurethane elastomers of Examples 1 to 3 were those exhibiting a liquid crystallinity, showing a low liquid crystal-developing temperature, and having rubbery elasticity when a liquid crystal is developed therein. The polyurethane elastomer of Comparative Example 1 did not develop a liquid crystallinity because of a small content of the mesogenic diol. The polyurethane elastomer of Comparative Example 2 did not cure because it had a too large molecular weight between crosslinks. Since the polyurethane elastomer of Comparative Example 3 has a too small molecular weight between crosslinks, it did not have a rubbery elasticity. Since the polyurethane elastomer of Comparative Example 4 has no crosslinking site, it could not inhibit the crystallinity of a mesogenic unit and the melting point (Tm) of a mesogenic unit exists, causing no development of a liquid crystallinity at room temperature. Moreover, such polyurethane elastomers were those having an increased fluidity when a liquid crystal is developed therein and having no rubbery elasticity.

INDUSTRIAL APPLICABILITY

(108) Since the liquid crystalline polyurethane elastomer of the present invention exhibits a characteristic response behavior such that said elastomer extends in the orientation direction by an increase in the degree of the liquid crystal orientation due to a tensile stress applied, and shrinks by a decrease in the degree of the liquid crystal orientation due to heating applied thereto, it is possible to apply the liquid crystalline polyurethane elastomer to various fields such as actuators and the like.