US4077931A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Thermoset water-in-oil emulsions
Assignee: Ashland LLC
•
Filing: 1975-07-31
•
Granted: 1978-03-07
•
Expires: 1995-07-31
Abstract
Abstract Pumpable or pourable thermosetting water-in-oil emulsions comprising water as the continuous phase and a mixture containing an unsaturated polyester and copolymerizable solvent such as styrene as the continuous phase, wherein polyesters of a molecular weight of about 1800 or more and a peroxide-cobalt-tertiary amine curing system are employed.
Inventors
- 👤 Robert H. Leitheiser
- 👤 Casimir C. Peloza
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 04:27
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/66; C08G63/668; C08G63/676; C08F; C08F299/00; C08F299/02; C08F299/04; C08F299/0407; C08F299/0414; C08G18/00; C08G18/06; C08G18/28; C08G18/67; C08G18/68; C08G63/02; C08G63/12; C08G63/52; C08G63/54; C08G63/68; C08G63/682; C08G63/6824; C08G63/6828; C08G2110/00; C08G2110/0083
Claims Analysis
Total Claims: 40
Claim 1
Independent Claim
153 words
A method for producing shapeable water-in-resin composition which is polymerizable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion, comprising water emulsified in an oil phase, by agitating: water; peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000, said polyester including reaction product of polycarboxylic acid, at least a portion of which is α,β ethylenically unsaturated, and polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to solvent being in the range of 10:1 to 1:10.
Claim 2
Independent Claim
153 words
A method for producing shapeable water-in-resin composition which is polymerizable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion, comprising water emulsified in an oil phase, by agitating: water; peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000, said polyester including reaction product of polycarboxylic acid, at least a portion of which is α,β ethylenically unsaturated, and polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to solvent being in the range of 10:1 to 1:10.
Claim 3
Dependent Claim
20 words
The method of claim 1 wherein the polyester has a mean molecular weight in the range of 2200 to 50,000.
Claim 4
Dependent Claim
20 words
The method of claim 1 wherein the polyester has a mean molecular weight in the range of 2800 to 30,000.
Claim 5
Dependent Claim
22 words
The method of claim 1 wherein the polyester includes a reaction product of: α,β ethylenically unsaturated acid; saturated acid; and polyhydric alcohol.
Claim 6
Dependent Claim
31 words
The method of claim 4 wherein the saturated acid is oxalic acid, malonic acid, adipic acid, succinic acid, glutaric acid, sebacic acid, azelaic acid, phthalic acid, isophthalic acid, or terephthalic acid.
Claim 7
Dependent Claim
46 words
The method of claim 4 wherein the saturated acid is phthalic acid, isophthalic acid, or terephthalic acid, in an amount up to 5 moles per mole of unsaturated acid which is sufficient to impart appreciable compressive strength, tensile strength, and impact resistance to the thermoset product.
Claim 8
Dependent Claim
12 words
The method of claim 6 wherein the saturated acid is isophthalic acid.
Claim 9
Dependent Claim
16 words
The method of claim 1 wherein said polyester includes tetrachlorophthalic acid, tetrabromophthalic acid or chlorendic acid.
Claim 10
Dependent Claim
21 words
The method of claim 1 wherein the weight ratio of polyester to solvent is in the range of 1:4 to 2:1
Claim 11
Dependent Claim
21 words
The method of claim 1 wherein the weight ratio of polyester to solvent is in the range of 1:2 to 2:1.
Claim 12
Independent Claim
165 words
A method for producing shapeable water-in-resin composition which is polymerizeable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, said emulsion including: peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 and includes reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic or terephthalic acid, and (B) dihydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and copolymerizeable solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to copolymerizeable solvent being in the range of 10:1 to 1:10.
Claim 13
Independent Claim
165 words
A method for producing shapeable water-in-resin composition which is polymerizeable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, said emulsion including: peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 and includes reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic or terephthalic acid, and (B) dihydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and copolymerizeable solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to copolymerizeable solvent being in the range of 10:1 to 1:10.
Claim 14
Dependent Claim
17 words
The method of claim 11 wherein the polyester has a mean molecular weight of 2200 to 50,000.
Claim 15
Dependent Claim
17 words
The method of claim 11 wherein the polyester has a mean molecular weight of 2800 to 30,000.
Claim 16
Dependent Claim
11 words
The method of claim 11 wherein the copolymerizable solvent is styrene.
Claim 17
Independent Claim
277 words
A method for producing shapeable water-in-resin composition which is polymerizable to a thermoset cellular solid product which comprises: forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, by bringing together under vigorous agitation water and an oil phase, said emulsion including peroxide catalyst in an effective amount in the range of 0.001 to 10% by weight of the copolymerizeable solvent referred to below; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in said oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase, said amount being sufficient to accelerate catalysis by the peroxide catalyst; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 as calculated from the formula: MW = 2(56,100)/R.sub.n wherein MW is mean molecular weight and R n is reactivity number, being the sum of the acid value and the hydroxyl value attained in an esterification reaction which forms the polyester, said polyester including the esterification reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic, or terephthalic acid in an amount up to 5 moles per mole of unsaturated acid, which is sufficient to impart appreciable compressive strength, tensile strength, and impact resistance to the thermoset product; and (B) dihydric alcohol; and styrene as copolymerizeable solvent for said polyester; the weight ratio of polyester and copolymerizeable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizeable solvent being in the range of 1:2 to 2:1.
Claim 18
Independent Claim
277 words
A method for producing shapeable water-in-resin composition which is polymerizable to a thermoset cellular solid product which comprises: forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, by bringing together under vigorous agitation water and an oil phase, said emulsion including peroxide catalyst in an effective amount in the range of 0.001 to 10% by weight of the copolymerizeable solvent referred to below; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in said oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase, said amount being sufficient to accelerate catalysis by the peroxide catalyst; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 as calculated from the formula: MW = 2(56,100)/R.sub.n wherein MW is mean molecular weight and R n is reactivity number, being the sum of the acid value and the hydroxyl value attained in an esterification reaction which forms the polyester, said polyester including the esterification reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic, or terephthalic acid in an amount up to 5 moles per mole of unsaturated acid, which is sufficient to impart appreciable compressive strength, tensile strength, and impact resistance to the thermoset product; and (B) dihydric alcohol; and styrene as copolymerizeable solvent for said polyester; the weight ratio of polyester and copolymerizeable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizeable solvent being in the range of 1:2 to 2:1.
Claim 19
Dependent Claim
17 words
The method of claim 15 wherein the polyester has a mean molecular weight of 2200 to 50,000.
Claim 20
Independent Claim
154 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion, comprising water emulsified in an oil phase, by agitating: water; peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000, said polyester including reaction product of polycarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated, and polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; the weight ratio of polyester to copolymerizable solvent being in the range of 10:1 to 1:10; and polymerizing said water-in-oil emulsion for forming the cellular solid material.
Claim 21
Independent Claim
154 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion, comprising water emulsified in an oil phase, by agitating: water; peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000, said polyester including reaction product of polycarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated, and polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizeable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; the weight ratio of polyester to copolymerizable solvent being in the range of 10:1 to 1:10; and polymerizing said water-in-oil emulsion for forming the cellular solid material.
Claim 22
Dependent Claim
20 words
The method of claim 17 wherein the polyester has a mean molecular weight in the range of 2200 to 50,000.
Claim 23
Dependent Claim
20 words
The method of claim 17 wherein the polyester has a mean molecular weight in the range of 2800 to 30,000.
Claim 24
Dependent Claim
21 words
The method of claim 17 wherein the polyester includes a reaction product of: α,β-ethylenically unsaturated acid; saturated acid; and polyhydric alcohol.
Claim 25
Dependent Claim
31 words
The method of claim 20 wherein the saturated acid is oxalic acid, malonic acid, adipic acid, succinic acid, glutaric acid, sebacic acid, azelaic acid, phthalic acid, isophthalic acid, or terephthalic acid.
Claim 26
Dependent Claim
46 words
The method of claim 20 wherein the saturated acid is phthalic acid, isophthalic acid, or terephthalic acid, in an amount up to 5 moles per mole of unsaturated acid which is sufficient to impart appreciable compressive strength, tensile strength, and impact resistance to the thermoset product.
Claim 27
Dependent Claim
12 words
The method of claim 22 wherein the saturated acid is isophthalic acid.
Claim 28
Dependent Claim
16 words
The method of claim 17 wherein said polyester includes tetrachlorophthalic acid, tetrabromophthalic acid or chlorendic acid.
Claim 29
Dependent Claim
23 words
The method of claim 17 wherein the weight ratio of polyester and solvent to water is in the range of 1:4 to 2:1.
Claim 30
Dependent Claim
21 words
The method of claim 17 wherein the weight ratio of polyester to solvent is in the range of 1:2 to 2:1.
Claim 31
Independent Claim
159 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion having water emulsified in oil phase, said emulsion including peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a molecular weight in the range of 1800 to 100,000 and includes reaction product of (A) polycarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and (B) polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to solvent being in the range of 10:1 to 1:10; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 32
Independent Claim
159 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion having water emulsified in oil phase, said emulsion including peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a molecular weight in the range of 1800 to 100,000 and includes reaction product of (A) polycarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and (B) polyhydric alcohol; and ethylenically unsaturated solvent which is copolymerizable with said polyester; the weight ratio of polyester and solvent to water being in the range of 1:10 to 10:1; and the weight ratio of polyester to solvent being in the range of 10:1 to 1:10; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 33
Independent Claim
182 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase by adding water while vigorously agitating the oil phase, said emulsion including: peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 and includes a reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic, or terephthalic acid, and (B) dihydric alcohol; and ethylenically unsaturated solvent which is copolymerizable with said polyester; the weight ratio of polyester and copolymerizable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizable solvent being in the range of 1:2 to 2:1; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 34
Independent Claim
182 words
A method for producing thermoset cellular solid material which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase by adding water while vigorously agitating the oil phase, said emulsion including: peroxide catalyst; cobalt salt promoter; tertiary aromatic amine promoter; said cobalt salt promoter and tertiary aromatic amine promoter being present in the oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 and includes a reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophthalic, or terephthalic acid, and (B) dihydric alcohol; and ethylenically unsaturated solvent which is copolymerizable with said polyester; the weight ratio of polyester and copolymerizable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizable solvent being in the range of 1:2 to 2:1; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 35
Dependent Claim
17 words
The method of claim 28 wherein the polyester has a mean molecular weight of 2200 to 50,000.
Claim 36
Dependent Claim
17 words
The method of claim 28 wherein the polyester has a mean molecular weight of 2800 to 30,000.
Claim 37
Dependent Claim
11 words
The method of claim 28 wherein the copolymerizable solvent in styrene.
Claim 38
Independent Claim
286 words
A method for producing shapeable water-in-oil resin composition which is polymerizable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, by bringing together under vigorous agitation water and an oil phase, said emulsion including: water; peroxide catalyst in an effecive amount in the range of 0.001 to 10% by weight of the copolymerizable solvent referred to below; cobalt salt promoter and tertiary aromatic amine promoter being present in said oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase, said amount being sufficient to accelerate catalysis of the peroxide catalyst; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 as calculated from the formula: MW = 2(56,100)/R.sub.n wherein MW is mean molecular weight and R n is reactivity number, being the sum of the acid value and the hydroxyl value attained in an esterification reaction which forms the polyester, said polyester including the esterification reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophtalic, or terephthalic acid, in an amount up to 5 moles per mole of unsaturated acid, which is sufficient to impart appreciable compressive strength, tensile strength and impact resistance to the thermoset product; and (B) dihydric alcohol; and styrene as copolymerizable solvent for said polyester; the weight ratio of polyester and copolymerizable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizable solvent being in the range of 1:2 to 2:1; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 39
Independent Claim
286 words
A method for producing shapeable water-in-oil resin composition which is polymerizable to a thermoset cellular solid product which comprises forming a pumpable water-in-oil emulsion having water emulsified in an oil phase, by bringing together under vigorous agitation water and an oil phase, said emulsion including: water; peroxide catalyst in an effecive amount in the range of 0.001 to 10% by weight of the copolymerizable solvent referred to below; cobalt salt promoter and tertiary aromatic amine promoter being present in said oil phase in an amount in the range of about 0.1 to 5% by weight of the oil phase, said amount being sufficient to accelerate catalysis of the peroxide catalyst; unsaturated polyester which has a mean molecular weight in the range of 1800 to 100,000 as calculated from the formula: MW = 2(56,100)/R.sub.n wherein MW is mean molecular weight and R n is reactivity number, being the sum of the acid value and the hydroxyl value attained in an esterification reaction which forms the polyester, said polyester including the esterification reaction product of (A) dicarboxylic acid, at least a portion of which is α,β-ethylenically unsaturated acid and, as saturated acid, phthalic, isophtalic, or terephthalic acid, in an amount up to 5 moles per mole of unsaturated acid, which is sufficient to impart appreciable compressive strength, tensile strength and impact resistance to the thermoset product; and (B) dihydric alcohol; and styrene as copolymerizable solvent for said polyester; the weight ratio of polyester and copolymerizable solvent to water being in the range of 1:4 to 2:1; and the weight ratio of polyester to copolymerizable solvent being in the range of 1:2 to 2:1; and polymerizing the water-in-oil emulsion without breaking said emulsion for forming the cellular solid material.
Claim 40
Dependent Claim
17 words
The method of claim 32 wherein the polyester has a mean molecular weight of 2200 to 50,000.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-03-06 | 1981-09-05 | 1982-03-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-03-06 | 1985-09-05 | 1986-03-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-03-06 | 1989-09-05 | 1990-03-07 | $7700.00 | Window Closed / Lapsed |