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Asphaltic paving compositions and method of preparation from solid organic wastes

Assignee: Mobil Oil AS
•
Filing: 1978-04-20
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Granted: 1979-12-04
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Expires: 1998-04-20
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Abstract

Abstract Asphaltic compositions comprising waste material are obtained by heating a mixture of solid organic waste, sulfur, and a liquefaction solvent to a temperature of 300° F. to 1000° F. to provide asphaltic pitch-like compositions which are useful as paving binders and coating compositions. The method for producing paving compositions is compatible with current petroleum refining technology and affords a low-cost method of waste disposal.

Inventors

  • 👤 Wilton F. Espenscheid

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 22:36
CPC Classifications
C; C08; C08L; C08L95/00; E; E01; E01C; E01C7/00; E01C7/08

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 133 words
A process for liquefaction of solid organic waste material to provide asphaltic compositions suitable for use as paving binders which comprises forming a slurry of comminuted solid organic waste with sulfur and a petroleum solvent having a boiling point between about 450° F. and 1100° F. which has (a) an H Ar proton content between about 30 and 50 percent, (b) a H.sub.α proton content of at least 30 percent, (c) a H.sub.β proton content below 20 percent, (d) a H.sub.γ proton content below 13 percent, and (e) a H.sub.α /H.sub.β proton ratio above about 1.4; heating the slurry at a temperature in the range between about 300° F. and 1000° F. for a period of time sufficient to dissolve the slurry, and thereafter recovering a flowable heavy oil having a pitch-like consistency.
Claim 2
Dependent Claim 133 words
A process for liquefaction of solid organic waste material to provide asphaltic compositions suitable for use as paving binders which comprises forming a slurry of comminuted solid organic waste with sulfur and a petroleum solvent having a boiling point between about 450° F. and 1100° F. which has (a) an H Ar proton content between about 30 and 50 percent, (b) a H.sub.α proton content of at least 30 percent, (c) a H.sub.β proton content below 20 percent, (d) a H.sub.γ proton content below 13 percent, and (e) a H.sub.α /H.sub.β proton ratio above about 1.4; heating the slurry at a temperature in the range between about 300° F. and 1000° F. for a period of time sufficient to dissolve the slurry, and thereafter recovering a flowable heavy oil having a pitch-like consistency.
Claim 3
Dependent Claim 46 words
A process in accordance with claim 1 wherein the amount of solvent is in the range between about 0.1 and 0.5 parts by weight per part by weight of waste and the sulfur is present in an amount ranging from 0.5 to 50 percent by weight.
Claim 4
Dependent Claim 17 words
A process in accordance with claim 1 wherein the petroleum solvent is a FCC main column bottoms.
Claim 5
Dependent Claim 16 words
A process in accordance with claim 1 wherein the petroleum solvent is a TCC syntower bottoms.
Claim 6
Dependent Claim 15 words
A process in accordance with claim 3 wherein the solid organic waste is municipal refuse.
Claim 7
Dependent Claim 14 words
A process in accordance with claim 3 wherein the solid organic waste is wood.
Claim 8
Dependent Claim 16 words
A process in accordance with claim 3 wherein the solid organic waste is agricultural cellulosic byproduct.
Claim 9
Dependent Claim 16 words
A process in accordance with claim 3 wherein the solid organic waste is newsprint and cardboard.
Claim 10
Dependent Claim 9 words
The composition produced by the method of claim 3.
Claim 11
Dependent Claim 151 words
A process for liquefaction of solid organic waste material to provide asphaltic compositions suitable for use as paving binders which comprises forming a slurry of comminuted solid organic waste and a petroleum solvent having a boiling point between about 450° F. and 1100° F. which has (a) an H Ar proton content between about 30 and 50 percent, (b) a H.sub.α proton content of at least 30 percent, (c) a H.sub.β proton content below 20 percent, (d) a H.sub.γ proton content below 13 percent, and (e) a H.sub.α /H.sub.β proton ratio above about 1.4; heating the slurry at a temperature in the range between about 300° F. and 1000° F. for a period of time sufficient to dissolve the slurry, cooling the mixture to below about 300° F., adding from 0.5 to 50 percent by weight sulfur to said mixture, and thereafter recovering a flowable heavy oil having a pitch-like consistency.
Claim 12
Dependent Claim 151 words
A process for liquefaction of solid organic waste material to provide asphaltic compositions suitable for use as paving binders which comprises forming a slurry of comminuted solid organic waste and a petroleum solvent having a boiling point between about 450° F. and 1100° F. which has (a) an H Ar proton content between about 30 and 50 percent, (b) a H.sub.α proton content of at least 30 percent, (c) a H.sub.β proton content below 20 percent, (d) a H.sub.γ proton content below 13 percent, and (e) a H.sub.α /H.sub.β proton ratio above about 1.4; heating the slurry at a temperature in the range between about 300° F. and 1000° F. for a period of time sufficient to dissolve the slurry, cooling the mixture to below about 300° F., adding from 0.5 to 50 percent by weight sulfur to said mixture, and thereafter recovering a flowable heavy oil having a pitch-like consistency.

References Cited (Backward Citations)

US3317447A Cited
US3733255A Cited
US3843339A Cited

USPTO Annuity & Maintenance Windows

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

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