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US4068062A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymerizing C5 and C6 olefins and diolefins with 3° hydrocarbyl halide to produce narrow molecular weight petroleum resins having low softening points

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1976-07-16
•
Granted: 1978-01-10
•
Expires: 1996-07-16
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Abstract

Abstract A petroleum resin is prepared by a process which comprises polymerizing using a Friedel-Crafts catalyst:

Inventors

  • 👤 Andre Lepert

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 23:02
CPC Classifications
C; C08; C08F; C08F240/00; C08L; C08L57/00; C08L57/02

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 100 words
In the process of preparing a low softening point petroleum resin which comprises polymerising using a Friedel-Crafts catalyst a. a petroleum resin feed comprising C 5 olefins and C 5 diolefins, C 6 olefins and C 6 diolefins or a mixture of C 5 and C 6 olefins and diolefins, said feed being obtained from the cracking of a petroleum feedstock the improvement which comprises including therewith b. at least 0.5 wt.% based on the petroleum resin feed of a tertiary hydrocarbyl halide to obtain a resin of narrowed molecular weight distribution having tackifying properties for natural and synthetic rubbers.
Claim 2
Dependent Claim 100 words
In the process of preparing a low softening point petroleum resin which comprises polymerising using a Friedel-Crafts catalyst a. a petroleum resin feed comprising C 5 olefins and C 5 diolefins, C 6 olefins and C 6 diolefins or a mixture of C 5 and C 6 olefins and diolefins, said feed being obtained from the cracking of a petroleum feedstock the improvement which comprises including therewith b. at least 0.5 wt.% based on the petroleum resin feed of a tertiary hydrocarbyl halide to obtain a resin of narrowed molecular weight distribution having tackifying properties for natural and synthetic rubbers.
Claim 3
Dependent Claim 18 words
A process according to claim 1 wherein at least 1 wt.% of the tertiary hydrocarbyl halide is used.
Claim 4
Dependent Claim 16 words
A process according to claim 2 wherein 1-4 wt.% of the tertiary hydrocarbyl halide is used.
Claim 5
Dependent Claim 17 words
A process according to claim 1 wherein the petroleum feedstock is cracked in the presence of steam.
Claim 6
Dependent Claim 21 words
A process according to claim 1 wherein the petroleum feedstock is cracked at a temperature of between 500° and 870° C.
Claim 7
Dependent Claim 33 words
A process according to claim 1 wherein the cracked feedstock is subjected to fractionation to remove C 2 and C 4 light ends and thermal soaking and distillation to remove cyclic conjugated diolefins.
Claim 8
Dependent Claim 20 words
A process according to claim 6 wherein the thermal soaking takes place at a temperature of 100° to 150° C.
Claim 9
Dependent Claim 16 words
A process according to claim 1 wherein the tertiary hydrocarbyl halide is a tertiary alkyl halide.
Claim 10
Dependent Claim 21 words
A process according to claim 1 wherein the hydrocarbyl chain in the tertiary hydrocarbyl halide contains 1 to 6 carbon atoms.
Claim 11
Dependent Claim 19 words
A process according to claim 4 wherein the tertiary hydrocarbyl halide is tertiary butyl chloride or tertiary butyl bromide.
Claim 12
Dependent Claim 22 words
A process according to claim 1 wherein the Friedel-Craftd catalyst is aluminium chloride, aluminium bromide or liquid aluminium chloride/hydrochloric acid/substituted aromatic complex.
Claim 13
Dependent Claim 16 words
A process according to claim 1 wherein the polymerization temperature is between 30° and 80° C.
Claim 14
Dependent Claim 30 words
A process according to claim 1 wherein the tertiary hydrocarbyl halide is combined with a branched-chain olefin and after polymerization the resin is stripped of unreacted hydrocarbons by flash distillation.

References Cited (Backward Citations)

US2734046A Cited
US2521432A Cited
US2856389A Cited
US2849512A Cited
US2994689A Cited
US2894937A Cited
US2964504A Cited
US3709854A Cited
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US3987123A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-09 1981-07-11 1982-01-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-09 1985-07-11 1986-01-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-09 1989-07-11 1990-01-10 $7700.00 Window Closed / Lapsed

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