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US4358550A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparation of aqueous solutions of water-soluble polymers

Assignee: Hercules LLC
•
Filing: 1981-07-14
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Granted: 1982-11-09
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Expires: 2001-07-14
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Abstract

Abstract An improved process is provided for rapidly dissolving water-soluble polymer gels in which the gels are subjected to the steps of extrusion, cutting of the extruded gels, forming a slurry of gel particles, subjecting the slurry to high shear forces, and finally mixing the resulting slurry and water to form a dilute aqueous solution of polymer. The improvement comprises cutting of the water-soluble polymer gel, prior to extrusion, into pieces of gel of a size which are small enough to fit into space defined between adjacent flights of the extruder at the feed inlet of the extruder. The process enables dilute aqueous solutions to be prepared on a batch or continuous basis with good reproducibility of polymer concentration in the solution being prepared.

Inventors

  • 👤 Louis Jacono
  • 👤 Thomas O. Mumper

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 20:27
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/03; B; B29; B29B; B29B9/00; B29B9/02; B29B9/06; B29B9/16; B29K; B29K2033/00; B29K2105/00; B29K2105/0058; B29K2105/0061; C08J2333/00

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 326 words
An improved process for preparing dilute aqueous solutions of water-soluble polymer having an intrinsic viscosity of at least one deciliter per gram measured in 2 normal sodium chloride at 25.5° C. from gels of said polymer, said process comprising the steps of: (a) extruding the water-soluble polymer gels into flowing water through die holes in an extrusion die plate, said die holes having diameters of from at least about 0.06 inch to about 0.50 inch, forming polymer gel strands, (b) cutting the extruding polymer gel strands at the exterior surface of the extrusion die plate to a length of less than about 0.75 inch, forming a slurry of the cut gel particles in the flowing water, (c) subjecting the slurry of gel particles of step (b) to high shearing forces immediately after formation of said slurry such that no substantial dissolution of the gel particles occurs prior to subjecting of said particles to said high shearing forces, said forces being sufficient to reduce the particle size of the cut gel particles to less than about 0.030 inch in greatest dimension, and (d) mixing the resultant slurry of fine gel particles and additional water under low shear conditions sufficient to maintain the suspension of particles in water, rapidly forming a dilute aqueous solution of polymer, the improvement in the extrusion step of said process, which comprises cutting the water soluble polymer gel, prior to feeding of the polymer gel to an extruder having a feed inlet, and an extruder screw having screw flights for the extruding of said polymer gel, into pieces of gel of a size which are at least containable within the volume of the extruder which can be defined between adjacent flights of the extruder screw at the feed inlet of said extruder and feeding the cut pieces of water soluble polymer gel to said extruder so that there is no substantial bridging of said polymer gel at the feed inlet of the extruder.
Claim 2
Dependent Claim 326 words
An improved process for preparing dilute aqueous solutions of water-soluble polymer having an intrinsic viscosity of at least one deciliter per gram measured in 2 normal sodium chloride at 25.5° C. from gels of said polymer, said process comprising the steps of: (a) extruding the water-soluble polymer gels into flowing water through die holes in an extrusion die plate, said die holes having diameters of from at least about 0.06 inch to about 0.50 inch, forming polymer gel strands, (b) cutting the extruding polymer gel strands at the exterior surface of the extrusion die plate to a length of less than about 0.75 inch, forming a slurry of the cut gel particles in the flowing water, (c) subjecting the slurry of gel particles of step (b) to high shearing forces immediately after formation of said slurry such that no substantial dissolution of the gel particles occurs prior to subjecting of said particles to said high shearing forces, said forces being sufficient to reduce the particle size of the cut gel particles to less than about 0.030 inch in greatest dimension, and (d) mixing the resultant slurry of fine gel particles and additional water under low shear conditions sufficient to maintain the suspension of particles in water, rapidly forming a dilute aqueous solution of polymer, the improvement in the extrusion step of said process, which comprises cutting the water soluble polymer gel, prior to feeding of the polymer gel to an extruder having a feed inlet, and an extruder screw having screw flights for the extruding of said polymer gel, into pieces of gel of a size which are at least containable within the volume of the extruder which can be defined between adjacent flights of the extruder screw at the feed inlet of said extruder and feeding the cut pieces of water soluble polymer gel to said extruder so that there is no substantial bridging of said polymer gel at the feed inlet of the extruder.

References Cited (Backward Citations)

US1671079A Cited
US2245640A Cited
USB579153I5 Cited
US4113688A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-11-08 1986-05-10 1986-11-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-11-08 1990-05-10 1990-11-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-11-08 1994-05-10 1994-11-09 $7700.00 Window Closed / Lapsed

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