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US4539099A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the removal of solids from an oil

Assignee: Nalco Energy Services LP
•
Filing: 1984-09-20
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Granted: 1985-09-03
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Expires: 2004-09-20
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Abstract

Abstract A process for removing suspended solids particularly difficultly filterable inorganic solids from an oil obtained as a refinery process bottom fraction from both steam and catalytic cracking units (e.g. catalytic cracker bottoms) or from coal conversion processes (e.g. coal tar) by adding to the oil an agglomerating agent comprising an oxyalkylated phenol formaldehyde resin glycol ester whereby said solids are clustered together into readily filterable agglomerates.

Inventors

  • 👤 Philip Merchant
  • 👤 R. Roger Wunderlich

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 00:04
CPC Classifications
C; C10; C10G; C10G31/00; C10G31/09

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 96 words
A process for reducing the particulate solids content of a hydrocarbon oil fraction comprising: providing a hydrocarbon oil fraction boiling in the range of from about 200° C. to about 550° C.; treating said hydrocarbon oil fraction with an agglomeration aid wherein the resulting mixture contains from 10 to 1000 weight parts per million of said aid based on the total weight of said mixture, said agglomeration aid comprising oxyalkylated phenol formaldehyde resin glycol ester of Mw ranging from 500 to 50,000; and, recovering a hydrocarbon oil bottoms portion having a reduced content of filterable solids.
Claim 2
Dependent Claim 96 words
A process for reducing the particulate solids content of a hydrocarbon oil fraction comprising: providing a hydrocarbon oil fraction boiling in the range of from about 200° C. to about 550° C.; treating said hydrocarbon oil fraction with an agglomeration aid wherein the resulting mixture contains from 10 to 1000 weight parts per million of said aid based on the total weight of said mixture, said agglomeration aid comprising oxyalkylated phenol formaldehyde resin glycol ester of Mw ranging from 500 to 50,000; and, recovering a hydrocarbon oil bottoms portion having a reduced content of filterable solids.
Claim 3
Dependent Claim 30 words
The process of claim 1 wherein said bottom fraction had at least 1000 weight parts per million (WPPM) of filterable solids and said recovered portion had less than 500 WPPM.
Claim 4
Dependent Claim 29 words
The process of claim 1 wherein said aid is an ethoxylated-propoxylated C 4 -C 9 alkyl phenol formaldehyde resin glycol ester of a Mw ranging from 2,000 to 15,000.
Claim 5
Dependent Claim 29 words
The process of claim 1 wherein said treating is at a temperature of from 35° C. to 250° C. and for residence times ranging from 0.3 to 10 days.
Claim 6
Dependent Claim 13 words
The process of claim 1 wherein said fraction is a refinery bottoms fraction.
Claim 7
Dependent Claim 24 words
The process of claim 1 wherein said fraction is coal tar having a Kinematic viscosity at 50° C. of no more than 330 centistokes.
Claim 8
Dependent Claim 22 words
The process of claim 2 wherein said aid is a succinate and present in said mixture in from 10 to 250 ppm.
Claim 9
Dependent Claim 21 words
The process of claim 5 wherein said solids are predominantly catalytic cracker fines having a diameter of less than 100 microns.
Claim 10
Dependent Claim 13 words
The process of claim 6 wherein said solids are substantially all inorganic solids.

References Cited (Backward Citations)

US2609931A Cited
US2756196A Cited
US3282827A Cited
US3450627A Cited
US3563885A Cited
US4056462A Cited
US4177134A Cited
US4250021A Cited
US4396498A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-09-02 1989-03-04 1989-09-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-09-02 1993-03-04 1993-09-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-09-02 1997-03-04 1997-09-03 $7700.00 Window Closed / Lapsed

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