Patent US2305586A successfully refreshed from Google Patents.
Patent US4143086A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4143086A Expired / Lapsed US ⏱️ 0.0 years remaining

Fluid catalytic cracking of amorphous polypropylene

Assignee: Phillips Petroleum Co
•
Filing: 1977-05-02
•
Granted: 1979-03-06
•
Expires: 1997-05-02
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract The propylene values of waste, amorphous polypropylene are recovered at least in part, by charging amorphous polypropylene together with a hydrocarbon feedstock to a catalytic cracking unit.

Inventors

  • 👤 Robert A. Carle
  • 👤 Paul D. Hann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 20:42
CPC Classifications
C; C10; C10G; C10G11/00; C07; C07C; C07C4/00; C07C4/22; C10G1/00; C10G1/08

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 117 words
A process comprising: charging a mixture of amorphous polypropylene containing a titanium catalyst residue and a hydrocarbon feedstock to a catalytic cracking unit, said amorphous polypropylene being present in an amount up to about 2.5 volume percent, based upon the feed to said unit; and contacting the mixture of amorphous polypropylene and feedstock with a catalyst in the catalytic cracking unit to produce an effluent comprising propylene, wherein the cracking catalyst in the catalytic cracking unit is in contact with at least one metal capable of poisoning the catalyst and wherein the titanium catalyst residue in the amorphous polypropylene deactivates at least a portion of the at least one metal that is capable of poisoning the catalyst.
Claim 2
Dependent Claim 117 words
A process comprising: charging a mixture of amorphous polypropylene containing a titanium catalyst residue and a hydrocarbon feedstock to a catalytic cracking unit, said amorphous polypropylene being present in an amount up to about 2.5 volume percent, based upon the feed to said unit; and contacting the mixture of amorphous polypropylene and feedstock with a catalyst in the catalytic cracking unit to produce an effluent comprising propylene, wherein the cracking catalyst in the catalytic cracking unit is in contact with at least one metal capable of poisoning the catalyst and wherein the titanium catalyst residue in the amorphous polypropylene deactivates at least a portion of the at least one metal that is capable of poisoning the catalyst.
Claim 3
Dependent Claim 26 words
A process according to claim 1 wherein said titanium catalyst residue is the reduction product of the reaction of titanium tetrachloride and an alkylaluminum halide compound.
Claim 4
Dependent Claim 27 words
A process according to claim 1 wherein said titanium catalyst residue is the reduction product of the reaction of titanium tetrachloride and a dialkyl aluminum chloride compound.
Claim 5
Dependent Claim 27 words
A process according to claim 3 wherein the amount of titanium catalyst residue in the amorphous polypropylene is approximately 11,000 parts per million parts of amorphous polypropylene.
Claim 6
Dependent Claim 88 words
The process of claim 1 wherein the effluent from said cracking unit is fractionated to at least obtain a propylene cut, a gasoline cut, a light cycle oil, a heavy cycle oil and a bottoms product, wherein said bottoms product is decanted to obtain a decant oil and a slurry oil, and wherein said amorphous polypropylene is thereafter at least partially dissolved in said slurry oil and wherein the resulting mixture of slurry oil and amorphous polypropylene is charged to said catalytic cracking unit together with said feedstock.
Claim 7
Dependent Claim 24 words
The process of claim 5 wherein the amount of said amorphous polypropylene in said slurry oil ranges from 0.5 to about 10 volume percent.
Claim 8
Dependent Claim 14 words
The process of claim 1 wherein said hydrocarbon feedstock is a virgin gas oil.

References Cited (Backward Citations)

US2385326A Cited
US2514332A Cited
US2897136A Cited
US3000990A Cited
US3750600A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-03-05 1982-09-04 1983-03-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-03-05 1986-09-04 1987-03-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-03-05 1990-09-04 1991-03-06 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag