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US4098992A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for continuous soluble polypropylene recovery from hydrocarbon polymerization media

Assignee: BP Corp North America Inc
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Filing: 1976-08-09
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Granted: 1978-07-04
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Expires: 1996-08-09
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Abstract

Abstract Polypropylene is recovered from a dilute solution in spent organic polymerization medium in a process comprising: (1) partial steam stripping of volatile components from said medium to form an aqueous phase and a concentrated, water-insoluble phase containing the soluble polypropylene: (2) separating said concentrated water-insoluble phase and leading it into an evaporator: (3) evaporating the remaining volatile components from the separated said water-insoluble phase leaving fluidized polypropylene which when drawn off and solidified is suitable for commercial use.

Inventors

  • 👤 Benjamin P. Belles

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 19:40
CPC Classifications
C; C08; C08J; C08J11/00; C08J11/04; C08J11/06; C08J11/08; C08F; C08F6/00; C08F6/06; C08F6/12; C08J2323/00; C08J2323/02; C08J2323/10; C08J2323/12; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/62

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 149 words
A method for the continuous recovery of soluble polypropylene, having a number average molecular weight in excess of 5,000, from spent polymerization media comprising: a. Steam stripping at a temperature between about 160° F. and about 250° F. under a pressure between about 4 and about 25 psig said media to form a two-phase system comprising an organic phase and an aqueous phase wherein said organic phase comprises between about 50 and 70 weight percent soluble polypropylene; b. decanting said organic phase from said aqueous phase while at a temperature and at a pressure of about said temperature and said pressure of said steam stripping, respectively; and c. removing essentially all remaining volatile material from said organic phase by heating said organic phase to between about 300° F. and 475° F. by means of a heat transfer whereby there is recovered polypropylene of sufficient fluidity to be readily transferred.
Claim 2
Independent Claim 149 words
A method for the continuous recovery of soluble polypropylene, having a number average molecular weight in excess of 5,000, from spent polymerization media comprising: a. Steam stripping at a temperature between about 160° F. and about 250° F. under a pressure between about 4 and about 25 psig said media to form a two-phase system comprising an organic phase and an aqueous phase wherein said organic phase comprises between about 50 and 70 weight percent soluble polypropylene; b. decanting said organic phase from said aqueous phase while at a temperature and at a pressure of about said temperature and said pressure of said steam stripping, respectively; and c. removing essentially all remaining volatile material from said organic phase by heating said organic phase to between about 300° F. and 475° F. by means of a heat transfer whereby there is recovered polypropylene of sufficient fluidity to be readily transferred.
Claim 3
Dependent Claim 18 words
The method of claim 1, wherein step (c) is carried out using a thin film, wiped surface evaporator.
Claim 4
Dependent Claim 16 words
The method of claim 1 wherein the major component of said spent polymerization media is hexane.
Claim 5
Dependent Claim 17 words
The method of claim 1 wherein the polymerization diluent contained in said media is recovered and reutilized.
Claim 6
Independent Claim 152 words
A method for the continuous recovery of soluble polypropylene, having a number average molecular weight in excess of 5,000, from spent polymerization media consisting essentially of: a. Steam stripping at a temperature between about 160° F. and about 250° F. under a pressure between about 4 and about 25 psig said media to form a two-phase system comprising an organic phase and an aqueous phase wherein said organic phase comprises between about 40 and 70 weight percent soluble polypropylene; b. decanting said organic phase from said aqueous phase while at a temperature and at a pressure of about said temperature and said pressure of said steam stripping, respectively; and c. removing essentially all remaining volatile material from said organic phase by heating said organic phase to between about 300° F. and 475° F. by means of a heat transfer surface whereby there is recovered polypropylene of sufficient fluidity to be readily transferred.
Claim 7
Independent Claim 152 words
A method for the continuous recovery of soluble polypropylene, having a number average molecular weight in excess of 5,000, from spent polymerization media consisting essentially of: a. Steam stripping at a temperature between about 160° F. and about 250° F. under a pressure between about 4 and about 25 psig said media to form a two-phase system comprising an organic phase and an aqueous phase wherein said organic phase comprises between about 40 and 70 weight percent soluble polypropylene; b. decanting said organic phase from said aqueous phase while at a temperature and at a pressure of about said temperature and said pressure of said steam stripping, respectively; and c. removing essentially all remaining volatile material from said organic phase by heating said organic phase to between about 300° F. and 475° F. by means of a heat transfer surface whereby there is recovered polypropylene of sufficient fluidity to be readily transferred.
Claim 8
Dependent Claim 12 words
The method of claim 5 wherein said hexane is recovered and reutilized.
Claim 9
Dependent Claim 15 words
The method of claim 5 wherein the major component of said polymerization media is hexane.

References Cited (Backward Citations)

US2801234A Cited
FR1318518A Cited
US3234995A Cited
GB988999A Cited
US3296240A Cited
US3337422A Cited
US3437645A Cited
US3658774A Cited
US3705885A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-07-03 1982-01-02 1982-07-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-07-03 1986-01-02 1986-07-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-07-03 1990-01-02 1990-07-04 $7700.00 Window Closed / Lapsed

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