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US4032701A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous method for producing a dry, solid polyacrylamide

Assignee: Amcol International Corp
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Filing: 1975-09-05
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Granted: 1977-06-28
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Expires: 1995-09-05
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Abstract

Abstract A process for producing polyacrylamide in a dry and solid form which includes the steps of mixing from 20 to 40% by weight of water and from 60 to 80% by weight of acrylamide to form an aqueous mixture thereof; heating said aqueous mixture to a temperature of between about 50° C and 100° C to form one phase aqueous liquid composition; depositing, on a surface, said one phase aqueous liquid composition and a catalytically effective amount of an aqueous solution of a water soluble polymerization catalyst for the acrylamide, said depositing being done in such a manner so as to form a mixture of said one phase aqueous liquid and said catalytic aqueous solution, said surface being heated to a temperature of between about 50° C and the charring point of polyacrylamide, whereby the acrylamide exothermically polymerizes to form polyacrylamide whereby all the water is evaporated and there is formed a dry, solid polyacrylamide and, after said water has evaporated, removing the polyacrylamide from said surface and, if desired, grinding the polyacrylamide to the desired particle size. It is preferred if the surface is moving at a rate of speed such that the polyacrylamide is brought to the removal point after the water is removed therefrom. In the more preferred exemplary embodiment, the moving surface is in the form of a relatively flat disc moving in a circular manner and is heated by gas burners.

Inventors

  • 👤 John Hughes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 14:23
CPC Classifications
C; C08; C08F; C08F120/00; C08F120/02; C08F120/52; C08F120/54; C08F120/56

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 153 words
A process for producing dry, solid, polyacrylamide which comprises forming an aqueous mixture consisting essentially of from 60% to 80%, by weight, of acrylamide and from 20% to 40%, by weight, of water; heating said aqueous mixture to a temperature of between about 50° C. and 100° C. to form a one phase liquid aqueous composition; depositing, separately on a moving surface (1) said aqueous one phase liquid and (2) a catalytically effective amount of an aqueous solution of a water soluble polymerization catalyst for acrylamide, in such a manner so as to form a mixture of said one phase aqueous liquid and said aqueous solution, said surface being heated to a temperature of between about 50° C. and the charring point of acrylamide whereby the acrylamide exothermically polymerizes to form polyacrylamide thereby causing all of the water to evaporate and forming a dry, solid polyacrylamide and removing said polyacrylamide from said surface.
Claim 2
Dependent Claim 153 words
A process for producing dry, solid, polyacrylamide which comprises forming an aqueous mixture consisting essentially of from 60% to 80%, by weight, of acrylamide and from 20% to 40%, by weight, of water; heating said aqueous mixture to a temperature of between about 50° C. and 100° C. to form a one phase liquid aqueous composition; depositing, separately on a moving surface (1) said aqueous one phase liquid and (2) a catalytically effective amount of an aqueous solution of a water soluble polymerization catalyst for acrylamide, in such a manner so as to form a mixture of said one phase aqueous liquid and said aqueous solution, said surface being heated to a temperature of between about 50° C. and the charring point of acrylamide whereby the acrylamide exothermically polymerizes to form polyacrylamide thereby causing all of the water to evaporate and forming a dry, solid polyacrylamide and removing said polyacrylamide from said surface.
Claim 3
Dependent Claim 28 words
A method according to claim 1 wherein the polymerization catalyst is a member selected from the group consisting of an alkali metal and ammonium sulfite, bisulfite and persulfate.
Claim 4
Dependent Claim 22 words
A method according to claim 1 wherein the polymerization catalyst is selected from the group consisting of sodium bisulfite and ammonium persulfate.
Claim 5
Dependent Claim 29 words
A method according to claim 1 wherein the polymerization catalyst is present in an amount of from 0.1% to 5%, by weight, based on the weight of the acrylamide.
Claim 6
Dependent Claim 14 words
A method according to claim 1 wherein the moving surface is a rotating disc.

References Cited (Backward Citations)

US2983717A Cited
US3242152A Cited
US3042970A Cited
US3663518A Cited
US3755280A Cited
US3732193A Cited
US3820957A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-27 1980-12-27 1981-06-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-27 1984-12-27 1985-06-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-27 1988-12-27 1989-06-28 $7700.00 Window Closed / Lapsed

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