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US3862078A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for converting coarse aqueous polymer emulsion to fine emulsion

Assignee: BURKE OLIVER W JUN
•
Filing: 1973-01-15
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Granted: 1975-01-21
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Expires: 1993-01-15
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Abstract

Abstract The preparation of stable aqueous latices from solvent dispersions of elastomers and other high polymer compositions has presented problems including excessive viscosity during processing and foaming, which have produced losses and increased costs. Herein combinations of steps are disclosed which reduce or eliminate various of these problems and enable the preparation of stable latices of high solids content. The process in common with that of related copending applications is characterized, inter alia, by the establishment of a flow of steam as a continuous phase into which an emulsion of a cement of the polymer is dispersed as an aerosol of latex droplets in a solvent-vapor continuum, followed by coalescence of the latex droplets and separation of the resulting coalesced liquid phase from the resulting solvent-vapor phase. In one embodiment of the present method an aqueous emulsion is prepared the dispersed phase of which principally comprises particles of precursor latex particle size and which may contain a lesser proportion of particles of greater than precursor latex particle size. This emulsion is converted to a stable latex by subjecting the same to special conditions which cause selective agglomeration of the particles of greater than precursor latex particle size, and removing the so agglomerated particles to yield a latex essentially free of particles of greater than colloidal size. In preferred embodiments provision is made for the continuous production of aqueous emulsion of polymer solvent cement essentially entirely of precursor latex particle size, which may be of narrow size distribution, or may have imparted thereto a wider size distribution, or an altered particle size or viscosity or both. As in the processes of my prior applications hereinafter referred to, the separation of the gaseous and liquid latex phases is effected by impinging the same on a liquid body, preferably a flow of partially concentrated liquid latex; and preferred arrangements for generating the aerosol, for effecting the said impingement, for effecting concentration of the latex under controlled conditions minimizing the formation of coagulum therefrom, and for recovering the latex from the gaseous phases, are also disclosed, which may be employed in lieu of or together with other features of said copending applications. In certain embodiments, in addition, special provisions are made for eliminating, from the latex, particles of greater than colloidal size by controlling the heating and stripping operations so that in combination, such larger particles are essentially avoided and/or agglomerated or coagulated and removed to yield latex essentially free of greater than colloidal sized particles. In other embodiments special provisions are made for altering the viscosity of the aqueous polymer/solvent emulsion and/or of the latex product, by special treatment of at least a part thereof before delivery from the system. Furthermore, special provisions are made for cOagulum removal and recovery, and to contribute to a more expeditious processing of the materials into stable latices and a reduction in coagulum losses and increase in efficiency.

Inventors

  • 👤 Jr Oliver W Burke

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 20:46
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/03; C09; C09K; C09K23/00; C09K23/017

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 46 words
Process as claimed in claim 1, which further comprises: d. impinging the flow passing through at least one of said homogenizing unit orifices as maintained in step (c) against the free tip of a vibrating reed before it leaves the outlet chamber of said homogenizing unit.
Claim 2
Dependent Claim 21 words
Process as claimed in claim 2, in which said step (d) is effected in the most downstream of said homogenizing units.
Claim 3
Dependent Claim 20 words
Process as claimed in claim 2, in which said step (d) is effected in a plurality of said homogenizing units.
Claim 4
Dependent Claim 19 words
Process as claimed in claim 2, in which said step (d) is effected in each of said homogenizing units.
Claim 5
Dependent Claim 36 words
Process as claimed in claim 1, in which the pressure raising means of the several homogenizing units are operated to produce high pressures in at least two of said units differing by at least 50 psig.
Claim 6
Dependent Claim 37 words
Process as claimed in claim 1, in which the pressure raising means of the successive homogenizing units are operated to produce high pressures increasing from unit to unit in the downstream direction by at least 50 psig.
Claim 7
Dependent Claim 44 words
Process as claimed in claim 1, in which a portion of the flow of emulsion passing through the restricted orifice of one of said homogenizing units is continuously recycled to broaden the size distribution of the precursor latex size particles of the converted emulsion.
Claim 8
Dependent Claim 47 words
Process as claimed in claim 1, in which a portion of the flow of emulsion passing through the restricted orifice of one of said homogenizing units is continuously recycled within the unit to broaden the size distribution of the precursor latex size particles of the converted emulsion.
Claim 9
Dependent Claim 41 words
Process as claimed in claim 1, in which any recycle of the flow through the restricted orifices of said units is essentially minimized so as to maintain a narrow size distribution of the precursor latex size particles in the converted emulsion.
Claim 10
Dependent Claim 39 words
Process as claimed in claim 1, in which the flow discharged from the most downstream of said units is split and recombined after the particle size of one portion thereof is altered by passing it through a separate homogenizer.
Claim 11
Dependent Claim 31 words
Process as claimed in claim 1, in which the emulsion removed from the flow to one unit in step (c) is recycled to a point upstream of the next preceding unit.
Claim 12
Dependent Claim 33 words
Process as claimed in claim 1, in which the emulsion removed from the flow to one unit in step (c) is recycled to a point upstream of the most upstream of said units.
Claim 13
Dependent Claim 45 words
Process including the steps of claim 1, which further comprises d. conveying the emulsion from the most downstream of said units to a point of delivery, and e. treating at least a portion of the emulsion being conveyed in step (d) to reduce its viscosity.
Claim 14
Dependent Claim 23 words
Process as claimed in claim 14, wherein in step (e) the emulsion is subjected to treatment to enlarge the average particle size thereof.
Claim 15
Dependent Claim 24 words
Process as claimed in claim 14, wherein in step (e) the emulsion is treated to reduce the quantity of emulsifier in its aqueous phase.
Claim 16
Dependent Claim 24 words
Process as claimed in claim 15, wherein in step (e) the emulsion is treated to reduce the quantity of emulsifier in its aqueous phase.
Claim 17
Dependent Claim 31 words
Process as claimed in claim 1, wherein the fine emulsion added to the flow in step (c) (1) is emulsion which has been discharged from the most downstream of said units.
Claim 18
Dependent Claim 27 words
Process as claimed in claim 14, wherein the fine emulsion added to the flow in step (c) (1) is emulsion which has been conveyed through step (d).

References Cited (Backward Citations)

US3071555A Cited
US3301810A Cited
US3277037A Cited
US3320220A Cited
US3437624A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-01-20 1978-07-22 1979-01-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-01-20 1982-07-22 1983-01-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-01-20 1986-07-22 1987-01-21 $7700.00 Window Closed / Lapsed

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