Patent US3987124A successfully refreshed from Google Patents.
← Back to Patent Explorer
US3987124A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for production of polymeric polyblends

Assignee: Monsanto Co
•
Filing: 1975-06-17
•
Granted: 1976-10-19
•
Expires: 1995-06-17
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract This invention relates to an improved process for producing polyblends wherein said process has unexpectedly high rates of polymerization wherein a polymerizable mixture of a monovinylidene aromatic monomer and a diene rubber are partially polymerized en masse through phase inversion with the partially polymerized mixture being suspended in an inert liquid and the polymerization essentially completed; the improvement comprising utilizing a particular catalyst system, in combination with, a saturated aliphatic acid containing 12 to 20 carbon atoms and a compound selected from the group consisting of hydrated salts and water in the mass and suspension polymerization steps of the process. Said catalyst system having a half life of less than one hour at 130° C., and a 10 hour half life at a temperature of 95° to 115° C.

Inventors

  • 👤 Norman L. Hardwicke
  • 👤 Raymond A. Barkhuff, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 18:48
CPC Classifications
C; C08; C08F; C08F291/00; C08F291/02

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 234 words
In a polymerization process for preparing polyblends having the following steps of (a) dissolving a graftable rubbery polymer in a polymerizable monomer formulation comprising at least one monovinylidene aromatic monomer to form a polymerizable mixture, (b) mass polymerizing with agitation said mixture to a partially polymerized mixture having a grafted, inverted and dispersed rubber phase, (c) suspending said partially polymerized mixture in an inert liquid, (d) suspension polymerizing said partially polymerized mixture to higher conversions and (e) recovering the suspending polyblend from said suspension, the improvement which comprises utilizing a peroxide catalyst having a half life of less than one hour at a temperature of 130° C., and a 10 hour half life at a temperature of 95° to 115° C., in combination with a saturated aliphatic acid containing 12 to 20 carbon atoms and a hydrated salt in steps (b) and (d) wherein step (b) is carried out at a temperature of from 95° to 125° C., polymerizing said polymerizable mixture to a conversion of about 10 to 45 percent and step (d) at a temperaure of from 110° to 150° C., polymerizing said partially polymerized mixture to essentially complete conversion and wherein said hydrated salt is present in step (b) in an amount of from about 0.01 to 1.0 percent by weight based on said monomers and in step (d) from about 0.10 to 1.0 percent by weight based on said monomers.
Claim 2
Dependent Claim 234 words
In a polymerization process for preparing polyblends having the following steps of (a) dissolving a graftable rubbery polymer in a polymerizable monomer formulation comprising at least one monovinylidene aromatic monomer to form a polymerizable mixture, (b) mass polymerizing with agitation said mixture to a partially polymerized mixture having a grafted, inverted and dispersed rubber phase, (c) suspending said partially polymerized mixture in an inert liquid, (d) suspension polymerizing said partially polymerized mixture to higher conversions and (e) recovering the suspending polyblend from said suspension, the improvement which comprises utilizing a peroxide catalyst having a half life of less than one hour at a temperature of 130° C., and a 10 hour half life at a temperature of 95° to 115° C., in combination with a saturated aliphatic acid containing 12 to 20 carbon atoms and a hydrated salt in steps (b) and (d) wherein step (b) is carried out at a temperature of from 95° to 125° C., polymerizing said polymerizable mixture to a conversion of about 10 to 45 percent and step (d) at a temperaure of from 110° to 150° C., polymerizing said partially polymerized mixture to essentially complete conversion and wherein said hydrated salt is present in step (b) in an amount of from about 0.01 to 1.0 percent by weight based on said monomers and in step (d) from about 0.10 to 1.0 percent by weight based on said monomers.
Claim 3
Dependent Claim 155 words
In a polymerization process for preparing polyblends having the following steps of (a) dissolving a graftable rubbery polymer in a polymerizable monomer formulation comprising at least one monovinylidene aromatic monomer to form a polymerizable mixture, (b) mass polymerizing with agitation said mixture to a partially polymerized mixture having a grafted, inverted and dispersed rubber phase, (c) suspending said partially polymerized mixture in an inert liquid, (d) suspension polymerizing said partially polymerized mixture to higher conversions and (e) recovering the suspending polyblend from said suspension, the improvement which comprises utilizing in combination t-butyl perbenzoate, stearic acid and MgSO 4 .7H 2 O in steps (b) and (d) wherein step (b) is carried out at a temperature of from 95° to 125° C., polymerizing said polymerizable mixture to a conversion of about 10 to 45 percent and step (d) at a temperature of from 110° to 150° C., polymerizing said partially polymerized mixture to essentially complete conversion.
Claim 4
Dependent Claim 155 words
In a polymerization process for preparing polyblends having the following steps of (a) dissolving a graftable rubbery polymer in a polymerizable monomer formulation comprising at least one monovinylidene aromatic monomer to form a polymerizable mixture, (b) mass polymerizing with agitation said mixture to a partially polymerized mixture having a grafted, inverted and dispersed rubber phase, (c) suspending said partially polymerized mixture in an inert liquid, (d) suspension polymerizing said partially polymerized mixture to higher conversions and (e) recovering the suspending polyblend from said suspension, the improvement which comprises utilizing in combination t-butyl perbenzoate, stearic acid and MgSO 4 .7H 2 O in steps (b) and (d) wherein step (b) is carried out at a temperature of from 95° to 125° C., polymerizing said polymerizable mixture to a conversion of about 10 to 45 percent and step (d) at a temperature of from 110° to 150° C., polymerizing said partially polymerized mixture to essentially complete conversion.

References Cited (Backward Citations)

US3439065A Cited
US3448175A Cited
US3428712A Cited
US3579612A Cited
US3644587A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-10-19 1980-04-19 1980-10-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-10-19 1984-04-19 1984-10-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-10-19 1988-04-19 1988-10-19 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag