US4533697A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing polyvinyl butyral
Assignee: EIDP Inc
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Filing: 1983-02-18
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Granted: 1985-08-06
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Expires: 2003-02-18
Abstract
Abstract The invention relates to a process for preparing polyvinyl butyral comprising simultaneously introducing into a reaction medium containing a mixture of water and a portion of reactive polyvinyl alcohol, maintained initially at a temperature below about 20° C., a stream of an aqueous solution of polyvinyl alcohol corresponding to the complement of the reactive polyvinyl alcohol and a stream of butyraldehyde and cooling the reaction mixture during the introduction of the polyvinyl alcohol and butyraldehyde. The reaction is also carried out in the presence of an acid catalyst and an emulsifying agent. The polyvinyl butyral obtained is used, after plasticizing, as an interlayer in laminated glass.
Inventors
- 👤 Robert Degeilh
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 14:26
CPC Classifications
B; B32; B32B; B32B17/00; B32B17/06; B32B17/10; B32B17/10005; B32B17/1055; B32B17/10761; C; C08; C08F; C08F8/00; C08F8/48
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
145 words
A process for preparing polyvinyl butyral by reaction of polyvinyl alcohol in aqueous solution and butyraldehyde in the presence of an acid catalyst and an emulsifying agent, which comprises forming an initial reaction medium of a mixture of water and a portion of polyvinyl alcohol to be reacted in an amount sufficient to allow stirring, maintaining the initial reaction medium containing between about 2.5 and 7.5% by weight of polyvinyl alcohol, maintaining the initial reaction medium initially at a temperature between about 5° and 20° C., simultaneously but separately introducing a stream of a polyvinyl alcohol aqueous solution in an amount sufficient to provide the remaining amount of polyvinyl alcohol to be used in the reaction and a stream of butyraldehyde, and maintaining the reaction at a temperature below about 40° C. during the simultaneous but separate introduction of the polyvinyl alcohol and the butyraldehyde.
Claim 2
Dependent Claim
145 words
A process for preparing polyvinyl butyral by reaction of polyvinyl alcohol in aqueous solution and butyraldehyde in the presence of an acid catalyst and an emulsifying agent, which comprises forming an initial reaction medium of a mixture of water and a portion of polyvinyl alcohol to be reacted in an amount sufficient to allow stirring, maintaining the initial reaction medium containing between about 2.5 and 7.5% by weight of polyvinyl alcohol, maintaining the initial reaction medium initially at a temperature between about 5° and 20° C., simultaneously but separately introducing a stream of a polyvinyl alcohol aqueous solution in an amount sufficient to provide the remaining amount of polyvinyl alcohol to be used in the reaction and a stream of butyraldehyde, and maintaining the reaction at a temperature below about 40° C. during the simultaneous but separate introduction of the polyvinyl alcohol and the butyraldehyde.
Claim 3
Dependent Claim
30 words
The process according to claim 1 in which at least a portion of the acid catalyst is introduced at the same time as the stream of butyraldehyde and polyvinyl alcohol.
Claim 4
Dependent Claim
31 words
The process according to claim 2 in which at least a portion of the acid catalyst is introduced in admixture with the stream of polyvinyl alcohol being fed to the reaction.
Claim 5
Dependent Claim
33 words
The process according to claim 1 in which at least a portion of the emulsifying agent is introduced during the reaction at the same time as the stream of polyvinyl alcohol and butyraldehyde.
Claim 6
Dependent Claim
29 words
The process according to claim 4 in which at least a portion of the emulsifying agent is introduced in admixture with the stream of polyvinyl alcohol during the reaction.
Claim 7
Dependent Claim
32 words
The process according to claim 1 in which the introduction of the stream of polyvinyl alcohol and butyraldehyde are introduced to the reaction medium over a period of 30 to 120 minutes.
Claim 8
Dependent Claim
31 words
The process according to claim 1 in which the initial reaction medium contains an amount of polyvinyl alcohol between 1/10 and 1/3 of all of the polyvinyl alcohol to be reacted.
Claim 9
Dependent Claim
17 words
The process according to claim 1 in which the emulsifying agent is sodium dodecylbenzenesulfonate and/or lauryl sulfate.
Claim 10
Dependent Claim
59 words
The process according to claim 1 in which at the end of the introduction of all of the polyvinyl alcohol solution and the butyraldehyde, the reaction mixture is maintained for about 30 minutes at the attained temperature, after which the reaction mixture is brought to a temperature of about 70° C. over a period of 2 to 3 hours.
Claim 11
Dependent Claim
121 words
A process for preparing polyvinyl butyral by reaction of polyvinyl alcohol in aqueous solution and butyraldehyde, in the presence of an acid catalyst and an emulsifying agent, which comprises simultaneously but separately adding (1) a stream of polyvinyl alcohol in an aqueous solution, and (2) a stream of butyraldehyde to a reaction medium containing an excess of polyvinyl alcohol in relation to the theoretical amount necessary to obtain the desired hydroxyl content for the final polyvinyl butyral product, said excess being less than an amount of polyvinyl alcohol corresponding to about 7.5% by weight of the reactive medium, and maintaining the reaction medium initially at a temperature of less than 20° C. prior to addition of the polyvinyl alcohol and butyraldehyde.
Claim 12
Dependent Claim
121 words
A process for preparing polyvinyl butyral by reaction of polyvinyl alcohol in aqueous solution and butyraldehyde, in the presence of an acid catalyst and an emulsifying agent, which comprises simultaneously but separately adding (1) a stream of polyvinyl alcohol in an aqueous solution, and (2) a stream of butyraldehyde to a reaction medium containing an excess of polyvinyl alcohol in relation to the theoretical amount necessary to obtain the desired hydroxyl content for the final polyvinyl butyral product, said excess being less than an amount of polyvinyl alcohol corresponding to about 7.5% by weight of the reactive medium, and maintaining the reaction medium initially at a temperature of less than 20° C. prior to addition of the polyvinyl alcohol and butyraldehyde.
References Cited (Backward Citations)
US3153009A
Cited
US4205146A
Cited
US4230771A
Cited
US4292372A
Cited
US4276351A
Cited
US4390594A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-08-05 | 1989-02-04 | 1989-08-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-08-05 | 1993-02-04 | 1993-08-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-08-05 | 1997-02-04 | 1997-08-06 | $7700.00 | Window Closed / Lapsed |