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US3870692A Expired / Lapsed US ⏱️ 0.0 years remaining

Selective hydroperoxidation of polyolefins in an aqueous slurry

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1971-07-12
•
Granted: 1975-03-11
•
Expires: 1991-07-12
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Abstract

Abstract Polyolefins are selectively hydroperoxidized in an aqueous slurry with an ozone-oxygen mixture at temperatures between 65* and 100* C. for a time which does not exceed one hour to introduce sufficient hydroperoxides for later graft copolymerization while minimizing formations of higher oxidation products of the polymer and limiting molecular weight degradation.

Inventors

  • 👤 Tad L Patton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 01:20
CPC Classifications
C; C08; C08F; C08F255/00; C08F255/02; C08F255/023; C08F8/00; C08F8/06

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 110 words
A process for selective hydroperoxidation of finely divided solid polypropylene particles, which consists essentially of: contacting a cationic surfactant-free, slurry of said polypropylene, having a particle size of about 30 to 1,000 microns in water with a 50 to 90 mg. of ozone per liter of air mixture as the sole free radical initiator, at a temperature within the range of from 75* C. to 95* C., and for a time sufficient to obtain a hydroperoxide concentration in said polypropylene between 0.014 and 0.050 weight percent, whereby formation of higher oxidation products than hydroperoxides is significantly less than said formation at temperatures outside said 75* C. to 95* C. range.
Claim 2
Dependent Claim 110 words
A process for selective hydroperoxidation of finely divided solid polypropylene particles, which consists essentially of: contacting a cationic surfactant-free, slurry of said polypropylene, having a particle size of about 30 to 1,000 microns in water with a 50 to 90 mg. of ozone per liter of air mixture as the sole free radical initiator, at a temperature within the range of from 75* C. to 95* C., and for a time sufficient to obtain a hydroperoxide concentration in said polypropylene between 0.014 and 0.050 weight percent, whereby formation of higher oxidation products than hydroperoxides is significantly less than said formation at temperatures outside said 75* C. to 95* C. range.
Claim 3
Dependent Claim 106 words
A PROCESS FOR SELECTIVE HYDROPEROXIDATION OF FINELY DIVIDED SOLID POLYPROPYLENE PARTICLES, WHICH CONSISTS ESSENTIALLY OF: CONTACTING A CATIONIC SURFACTANT-FREE, SLURRY OF SAID POLYPROPYLENE, HAVING A PARTICLE SIZE OF ABOUT 30 TO 1,000 MICRONS IN WATER WITH A 50 TO 90 MG. OF OZONE PER LITER OF AIR MIXTURE AS THE SOLE FREE RADICAL INITIATOR, AT A TEMPERATURE WITHIN THE RANGE OF FROM 75*C. TO 95*C., AND FOR A TIME SUFFICIENT TO OBTAIN A HYDROPEROXIDE CONCENTRATION IN SAID POLYPROPYLENE BETWEEN 0.014 AND 0.050 WEIGHT PERCENT, WHEREBY FORMATION OF HIGHER OXIDATION PRODUCTS THAN HYDROPEROXIDES IS SIGNIFICANTLY LESS THAN SAID FORMATION AT TEMPERATURES OUTSIDE SAID 75*C. TO 95*C. RANGE.
Claim 4
Dependent Claim 106 words
A PROCESS FOR SELECTIVE HYDROPEROXIDATION OF FINELY DIVIDED SOLID POLYPROPYLENE PARTICLES, WHICH CONSISTS ESSENTIALLY OF: CONTACTING A CATIONIC SURFACTANT-FREE, SLURRY OF SAID POLYPROPYLENE, HAVING A PARTICLE SIZE OF ABOUT 30 TO 1,000 MICRONS IN WATER WITH A 50 TO 90 MG. OF OZONE PER LITER OF AIR MIXTURE AS THE SOLE FREE RADICAL INITIATOR, AT A TEMPERATURE WITHIN THE RANGE OF FROM 75*C. TO 95*C., AND FOR A TIME SUFFICIENT TO OBTAIN A HYDROPEROXIDE CONCENTRATION IN SAID POLYPROPYLENE BETWEEN 0.014 AND 0.050 WEIGHT PERCENT, WHEREBY FORMATION OF HIGHER OXIDATION PRODUCTS THAN HYDROPEROXIDES IS SIGNIFICANTLY LESS THAN SAID FORMATION AT TEMPERATURES OUTSIDE SAID 75*C. TO 95*C. RANGE.
Claim 5
Dependent Claim 18 words
A process in accordance with claim 1 wherein said polypropylene has a molecular weight of at least 10,000.
Claim 6
Dependent Claim 21 words
A process in accordance with claim 1 wherein the ozone treat rate is from 18 to 225 mg O3/lb of polymer/min.
Claim 7
Dependent Claim 25 words
A process in accordance with claim 1 wherein the polyolefin is polypropylene powder having a particle size within the range from 100 to 600 microns.
Claim 8
Dependent Claim 21 words
A process in accordance with claim 1 wherein the ozone treat rate is from 25 to 55 mg O3/lb of polymer/min.
Claim 9
Dependent Claim 51 words
A process in accordance with claim 1 wherein the temperature is from 78* to 94* C., the time of oxidation is about 8 minutes, the amount of ozone reacted is about 236 to 271 mg/100 g polymer, and the ROOH concentration in the polymer is about 0.044 to 0.045 wt. %.

References Cited (Backward Citations)

US2911398A Cited
US3069382A Cited
US3284541A Cited
US3322711A Cited
US3458597A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-03-10 1978-09-09 1979-03-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-03-10 1982-09-09 1983-03-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-03-10 1986-09-09 1987-03-11 $7700.00 Window Closed / Lapsed

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