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US4283230A Expired / Lapsed US ⏱️ 0.0 years remaining

Air-treated propane-precipitated asphalt

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1980-01-10
•
Granted: 1981-08-11
•
Expires: 2000-01-10
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Abstract

Abstract Propane-precipitated asphalt is contacted with a stream of air at 200 DEG C. and above to increase the softening point of the asphalt. The resulting asphalt base, having a softening point of about 65 DEG -300 DEG C., is then blended with 5-60 weight percent liquid sulfur-treated petroleum fraction, having an equivalent atmospheric boiling point range of 370 DEG -500 DEG C., to yield paving grade quality asphalt cement composition.

Inventors

  • 👤 Dominick Clementoni
  • 👤 Luke W. Corbett

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 14:00
CPC Classifications
C; C08; C08L; C08L95/00

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 149 words
A process for preparing an asphalt cement composition comprising the step of: blending a propane-precipitated asphalt base, air-treated at elevated temperature and having a softening point of about 65°-300° C. as measured by ASTM D 36-76, with about 5-60 wt.%, based on the total weight of said asphalt base, of a 1-10 wt.% sulfur-treated liquid petroleum fraction having an atmospheric equivalent boiling range, of about 370°-500° C., thereby producing an asphalt cement composition being of ASTM viscosity grade AC-21/2, AC-5, AC-10, AC-20 or AC-40 and meeting the requirements of ASTM D 3381-76 or AASHTO M 226-73, and exhibiting a higher viscosity at 60° C., as measured by the procedure of ASTM STP 532 (1973), in which said viscosity is interpolated at a penetration level of 90 decimillimeters at 25° C., than a comparative non-air treated composition derived from the same propane-precipitated asphalt, whose softening point has not been increased.
Claim 2
Dependent Claim 149 words
A process for preparing an asphalt cement composition comprising the step of: blending a propane-precipitated asphalt base, air-treated at elevated temperature and having a softening point of about 65°-300° C. as measured by ASTM D 36-76, with about 5-60 wt.%, based on the total weight of said asphalt base, of a 1-10 wt.% sulfur-treated liquid petroleum fraction having an atmospheric equivalent boiling range, of about 370°-500° C., thereby producing an asphalt cement composition being of ASTM viscosity grade AC-21/2, AC-5, AC-10, AC-20 or AC-40 and meeting the requirements of ASTM D 3381-76 or AASHTO M 226-73, and exhibiting a higher viscosity at 60° C., as measured by the procedure of ASTM STP 532 (1973), in which said viscosity is interpolated at a penetration level of 90 decimillimeters at 25° C., than a comparative non-air treated composition derived from the same propane-precipitated asphalt, whose softening point has not been increased.
Claim 3
Dependent Claim 23 words
The process of claim 1 wherein said propane-precipitated asphalt is derived from a crude oil having a gravity of above about 20° API.
Claim 4
Dependent Claim 20 words
The process of claim 1 wherein said propane-precipitated asphalt is air-treated at a temperature of about 200° to 300° C.
Claim 5
Dependent Claim 25 words
The process of claim 1 wherein said air-treated asphalt base has a softening point of about 80° to 140° C., as measured by ASTM D-36-76.
Claim 6
Dependent Claim 34 words
The process of claim 1 wherein said air-treated asphalt base is blended with about 10 to 40 weight percent, based on total weight of said asphalt base, with said sulfur treated liquid petroleum fraction.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein said liquid petroleum fraction is treated with about 2-6 wt.% sulfur.
Claim 8
Dependent Claim 14 words
The process of claim 1 wherein said liquid petroleum fraction is an extract oil.
Claim 9
Dependent Claim 14 words
The process of claim 1 wherein said liquid petroleum fraction is vacuum gas oil.
Claim 10
Dependent Claim 26 words
The process of claim 1 wherein said asphalt cement composition further meets the specifications of ASTM D 3381-76, Table 2, or AASHTO M 226-76, Table II.
Claim 11
Dependent Claim 204 words
A process for preparing an asphalt cement composition comprising the steps of: (a) contacting a molten propane-precipitated asphalt, derived from a residuum of a crude oil, having a gravity of above about 20° API, with a stream of air at a temperature of above about 200° C. resulting in an air-treated asphalt base having a higher softening point than said propane-precipitated asphalt and being in the temperature range of about 65°-300° C., as measured by ASTM D-36-76; and (b) blending said air-treated asphalt base, at a temperature of about 125°-150° C., with about 5-60 wt.%, based on the total weight of said asphalt base, of a 1-10 wt.% sulfur-treated liquid petroleum fraction having an atmospheric equivalent boiling range of about 370°-500° C., thereby producing an asphalt cement composition being of ASTM viscosity grade AC-21/2, AC-5, AC-10, AC-20 or AC-40 and meeting the requirements of ASTM D 3381-76 or AASHTO M 226-73, and exhibiting a higher viscosity at 60° C., as measured by the procedure of ASTM STP 532 (1973), in which said viscosity is interpolated at a penetration level of 90 decimillimeters at 25° C., than a comparative non-air treated composition derived from the same propane-precipitated asphalt, whose softening point has not been increased.
Claim 12
Dependent Claim 204 words
A process for preparing an asphalt cement composition comprising the steps of: (a) contacting a molten propane-precipitated asphalt, derived from a residuum of a crude oil, having a gravity of above about 20° API, with a stream of air at a temperature of above about 200° C. resulting in an air-treated asphalt base having a higher softening point than said propane-precipitated asphalt and being in the temperature range of about 65°-300° C., as measured by ASTM D-36-76; and (b) blending said air-treated asphalt base, at a temperature of about 125°-150° C., with about 5-60 wt.%, based on the total weight of said asphalt base, of a 1-10 wt.% sulfur-treated liquid petroleum fraction having an atmospheric equivalent boiling range of about 370°-500° C., thereby producing an asphalt cement composition being of ASTM viscosity grade AC-21/2, AC-5, AC-10, AC-20 or AC-40 and meeting the requirements of ASTM D 3381-76 or AASHTO M 226-73, and exhibiting a higher viscosity at 60° C., as measured by the procedure of ASTM STP 532 (1973), in which said viscosity is interpolated at a penetration level of 90 decimillimeters at 25° C., than a comparative non-air treated composition derived from the same propane-precipitated asphalt, whose softening point has not been increased.
Claim 13
Dependent Claim 11 words
An asphalt cement composition prepared by the process of claim 1.
Claim 14
Dependent Claim 11 words
The asphalt cement composition of claim 11 further comprising mineral aggregate.
Claim 15
Dependent Claim 28 words
A process for paving a road surface comprising the step of applying to said surface a paving grade asphalt cement composition prepared by the process of claim 1.

References Cited (Backward Citations)

GB610629A Cited
GB956313A Cited
FR1380095A Cited
US3317447A Cited
US3793189A Cited
US3977891A Cited
US4024076A Cited
US3960585A Cited
US4139397A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-10 1985-02-09 1985-08-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-10 1989-02-09 1989-08-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-10 1993-02-09 1993-08-11 $7700.00 Window Closed / Lapsed

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