US4405444A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and means for charging foamed residual oils in contact with fluid solid particulate material
Assignee: Ashland LLC
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Filing: 1982-11-08
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Granted: 1983-09-20
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Expires: 2002-11-08
Abstract
Abstract Method to improve mixing water-and charge in a hydrocarbon conversion unit comprising foaming the charge with a foaming agent e.g. selected from the group consisting of sulfonates or polymer resins (preferably some oil soluble, some water soluble).
Inventors
- 👤 Oliver J. Zandona
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:10
CPC Classifications
C; C10; C10G; C10G9/00; C10G9/28; C10G9/32; B; B01; B01J; B01J4/00; B01J4/001; B01J4/002; B01J8/00; B01J8/18; B01J8/1818; B01J8/1827; B01J8/24; B01J8/38; B01J8/384; B01J8/388; C10G11/00; C10G11/14; C10G11/18; C10G25/00; C10G25/06; C10G25/09; C10G29/00; C10G29/16; B01J2208/00; B01J2208/00796; B01J2208/00893; B01J2208/00902
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
132 words
A method for upgrading a high boiling portion of crude oil comprising metallo-organic and Conradson carbon producing compounds to form gasoline, lower and higher boiling hydrocarbon streams which comprises: A. charging a high boiling portion of crude oil as a thick foam to the lower portion of a riser conversion zone; B. charging fluidizable solid particle material at an elevated temperature in the range of 704° C. (1300° F.) up to about 815° C. (1500° F.) in intimate contact with said foamed oil feed to form a suspension thereof, C. passing said formed suspension through a riser conversion zone under conditions of restricted residence time and temperature promoting desired conversion of the oil feed, and D. recovering a hydrocarbon conversion product separated from catalyst particles following traverse of said riser conversion zone.
Claim 2
Independent Claim
132 words
A method for upgrading a high boiling portion of crude oil comprising metallo-organic and Conradson carbon producing compounds to form gasoline, lower and higher boiling hydrocarbon streams which comprises: A. charging a high boiling portion of crude oil as a thick foam to the lower portion of a riser conversion zone; B. charging fluidizable solid particle material at an elevated temperature in the range of 704° C. (1300° F.) up to about 815° C. (1500° F.) in intimate contact with said foamed oil feed to form a suspension thereof, C. passing said formed suspension through a riser conversion zone under conditions of restricted residence time and temperature promoting desired conversion of the oil feed, and D. recovering a hydrocarbon conversion product separated from catalyst particles following traverse of said riser conversion zone.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein the solid particle material is either a cracking catalyst or has little if any cracking activity.
Claim 4
Dependent Claim
28 words
The method of claim 1 wherein the high boiling portion of crude oil is a residual oil or reduced crude comprising components boiling above 552° C. (1025° F.).
Claim 5
Dependent Claim
20 words
The method of claim 1 wherein the high boiling oil feed comprises up to 40 volume percent of vacuum resid.
Claim 6
Dependent Claim
38 words
The method of claim 1 wherein the charged oil foam is prepared by contacting preheated oil feed and liquid water with a purge gas in an orifice restriction under conditions particularly promoting the formation of thick oil foam.
Claim 7
Dependent Claim
56 words
The method of claim 1 wherein separation of the suspension following traverse of the riser conversion zone is by ballistic separation in cooperation with a single stage cyclone separator, the hydrocarbon conversion products are separated as vaporous products from solid particles comprising carbonaceous products of hydrocarbon conversion and separated solid are contacted with a stripping gas.
Claim 8
Dependent Claim
43 words
The method of claim 6 wherein separated solid particles comprising carbonaceous deposits are regenerated by combustion of carbonaceous deposits with an oxygen containing gas during flow through one or more contact zones comprising dense and dispersed phase contact with combustion promoting gaseous material.
Claim 9
Dependent Claim
33 words
The method of claim 7 wherein separation of a dispersed phase of solids in transporting flue gases is accomplished by ballistic separation permitting the use of single stage cyclone separation in combination therewith.
Claim 10
Dependent Claim
21 words
The method of claim 1 wherein foaming of the oil feed is accomplished at velocities up to and including sonic velocities.
Claim 11
Dependent Claim
23 words
The method of claim 1 wherein the oil feed is expanded from 50 to 100 volume of foam per volume of oil feed.
Claim 12
Dependent Claim
44 words
The method of claim 5 wherein a water stream obtained from the product fractionator and a gaseous stream selected from product dry gas, product wet gas, CO 2 and light gaseous hydrocarbons is used as a purge gas in the production of oil foam.
Claim 13
Independent Claim
110 words
A method for upgrading a reduced crude comprising metallo-organic compounds which comprises, A. heating said reduced crude to a temperature within the range of 204° C. to 316° C. (400° F. to 600° F.), B. passing the heated reduced crude at an elevated pressure up to about 100 psig admixed with liquid water and a purge gas through an orifice restriction causing substantial foaming of said reduced crude feed, C. contacting said foamed reduced crude with hot fluidizable solid particle to form a suspension thereof traversing an elongated confined reaction zone, and D. recovering a conversion product of said suspension following traverse of said reaction zone separate from solid particles.
Claim 14
Independent Claim
110 words
A method for upgrading a reduced crude comprising metallo-organic compounds which comprises, A. heating said reduced crude to a temperature within the range of 204° C. to 316° C. (400° F. to 600° F.), B. passing the heated reduced crude at an elevated pressure up to about 100 psig admixed with liquid water and a purge gas through an orifice restriction causing substantial foaming of said reduced crude feed, C. contacting said foamed reduced crude with hot fluidizable solid particle to form a suspension thereof traversing an elongated confined reaction zone, and D. recovering a conversion product of said suspension following traverse of said reaction zone separate from solid particles.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-09-19 | 1987-03-21 | 1987-09-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-09-19 | 1991-03-21 | 1991-09-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-09-19 | 1995-03-21 | 1995-09-20 | $7700.00 | Window Closed / Lapsed |