US4284139A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for stimulating and upgrading the oil production from a heavy oil reservoir
Assignee: ConocoPhillips Co
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Filing: 1980-02-28
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Granted: 1981-08-18
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Expires: 2000-02-28
Abstract
Abstract A process for thermally stimulating and upgrading oil production from a heavy oil reservoir wherein the heavy oil produced from the reservoir is combined with a hydrogen donor diluent and the mixture is subjected to thermal cracking to upgrade the heavy oil into more valuable hydrocarbon products. The cracked products are fractionated into a light end vapor fraction, an intermediate liquid fraction, a gas oil fraction and a pitch fraction, and at least a portion of the gas oil fraction is hydrogenated by contacting it with a hydrogen-containing gas stream to produce the hydrogen donor diluent combined with the heavy oil. The pitch fraction is subjected to partial oxidation to produce the hydrogen-containing gas stream and a by-product gas stream containing steam which is combined with additional steam and injected into the heavy oil reservoir to enhance the mobility of heavy oil contained therein. The light end vapor fraction and unreacted hydrogen-containing gas produced by the process are utilized as fuel in the process. The intermediate liquid fraction produce and portion of the gas oil fraction not hydrogenated are readily transportable from the process.
Inventors
- 👤 Glenn A. Sweany
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 23:00
CPC Classifications
C; C10; C10G; C10G69/00; C10G69/02; C10G47/00; C10G47/32; C10G47/34; C10G49/00; E; E21; E21B; E21B36/00; C10G2400/00; C10G2400/06; E21B43/00; E21B43/34
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
51 words
A process for stimulating and upgrading the oil production from a heavy oil reservoir comprising the steps of: (a) combining heavy oil produced from said reservoir with a hydrogen donor diluent; (b) subjecting the mixture of heavy oil and hydrogen donor diluent to thermal cracking in a hydrogen donor diluent furnace;
Claim 2
Dependent Claim
51 words
A process for stimulating and upgrading the oil production from a heavy oil reservoir comprising the steps of: (a) combining heavy oil produced from said reservoir with a hydrogen donor diluent; (b) subjecting the mixture of heavy oil and hydrogen donor diluent to thermal cracking in a hydrogen donor diluent furnace;
Claim 3
Dependent Claim
168 words
(c) fractionating the cracked products from said hydrogen donor diluent furnace into a light end vapor fraction, an intermediate liquid fraction, a gas oil fraction and a pitch fraction; (d) hydrogenating at least a portion of said gas oil fraction by contacting said portion with a hydrogen-containing gas stream in a hydrotreater to produce the hydrogen donor diluent combined with said heavy oil in accordance with step (a) and an unreacted hydrogen-containing gas stream effluent; (e) subjecting said pitch fraction to partial oxidation to produce the hydrogen-containing gas stream utilized in step (d) and a by-product gas stream; (f) generating steam in a steam generator; (g) combining said steam generated in step (f) with the by-product gas stream from step (e); (h) injecting said combined steam-by-product gas stream into said heavy oil reservoir to thereby stimulate the production of heavy oil therefrom; and (i) utilizing said light end vapor fraction from step (c) and said unreacted hydrogen-containing gas stream effluent from step (d) as fuel for said process.
Claim 4
Dependent Claim
168 words
(c) fractionating the cracked products from said hydrogen donor diluent furnace into a light end vapor fraction, an intermediate liquid fraction, a gas oil fraction and a pitch fraction; (d) hydrogenating at least a portion of said gas oil fraction by contacting said portion with a hydrogen-containing gas stream in a hydrotreater to produce the hydrogen donor diluent combined with said heavy oil in accordance with step (a) and an unreacted hydrogen-containing gas stream effluent; (e) subjecting said pitch fraction to partial oxidation to produce the hydrogen-containing gas stream utilized in step (d) and a by-product gas stream; (f) generating steam in a steam generator; (g) combining said steam generated in step (f) with the by-product gas stream from step (e); (h) injecting said combined steam-by-product gas stream into said heavy oil reservoir to thereby stimulate the production of heavy oil therefrom; and (i) utilizing said light end vapor fraction from step (c) and said unreacted hydrogen-containing gas stream effluent from step (d) as fuel for said process.
Claim 5
Dependent Claim
19 words
The process of claim 1 wherein said partial oxidation process is carried out utilizing air as the oxidizing gas.
Claim 6
Dependent Claim
35 words
The process of claim 2 wherein said intermediate liquid fraction and the portion of said gas oil fraction from step (c) not hydrogenated in accordance with step (d) are transported from said process by pipeline.
Claim 7
Dependent Claim
31 words
The process of claim 1 wherein said hydrogen-containing gas stream utilized in step (d) is first subjected to a shift reaction whereby the hydrogen content of said gas stream is increased.
Claim 8
Dependent Claim
198 words
In a process for stimulating oil production from a heavy oil reservoir wherein steam is injected into the reservoir to enhance the mobility of the heavy oil therein, the improvement comprising: (a) combining heavy oil produced from said reservoir with a hydrogen donor diluent; (b) subjecting the mixture of heavy oil and hydrogen donor diluent to thermal cracking; (c) fractionating the cracked products from step (b) into a light end vapor fraction, an intermediate liquid fraction, a gas oil fraction and a pitch fraction; (d) hydrogenating at least a portion of said gas oil fraction by contacting said portion with a hydrogen-containing gas stream to produce the hydrogen donor diluent combined with said heavy oil in accordance with step (a) and an unreacted hydrogen-containing gas stream effluent; (e) subjecting said pitch fraction to partial oxidation to produce the hydrogen-containing gas stream utilized in accordance with step (d) and a by-product gas stream; (f) combining the by-product gas stream from step (e) with said steam prior to injecting said steam into said reservoir; and (g) utilizing said light end vapor fraction from step (c) and said unreacted hydrogen-containing gas stream effluent from step (d) as fuel for said process.
Claim 9
Dependent Claim
198 words
In a process for stimulating oil production from a heavy oil reservoir wherein steam is injected into the reservoir to enhance the mobility of the heavy oil therein, the improvement comprising: (a) combining heavy oil produced from said reservoir with a hydrogen donor diluent; (b) subjecting the mixture of heavy oil and hydrogen donor diluent to thermal cracking; (c) fractionating the cracked products from step (b) into a light end vapor fraction, an intermediate liquid fraction, a gas oil fraction and a pitch fraction; (d) hydrogenating at least a portion of said gas oil fraction by contacting said portion with a hydrogen-containing gas stream to produce the hydrogen donor diluent combined with said heavy oil in accordance with step (a) and an unreacted hydrogen-containing gas stream effluent; (e) subjecting said pitch fraction to partial oxidation to produce the hydrogen-containing gas stream utilized in accordance with step (d) and a by-product gas stream; (f) combining the by-product gas stream from step (e) with said steam prior to injecting said steam into said reservoir; and (g) utilizing said light end vapor fraction from step (c) and said unreacted hydrogen-containing gas stream effluent from step (d) as fuel for said process.
Claim 10
Dependent Claim
19 words
The process of claim 5 wherein said partial oxidation process is carried out utilizing air as the oxidizing gas.
Claim 11
Dependent Claim
43 words
The process of claim 6 wherein said intermediate liquid fraction and the portion of said gas oil fraction from step (c) not hydrogenated in accordance with step (d) are transported from said process to a point of use or further processing by pipeline.
Claim 12
Dependent Claim
28 words
The process of claim 5 wherein said hydrogen-containing gas stream used in step (d) is first subjected to a shift reaction whereby the hydrogen content thereof is increased.
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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) | 1984-08-17 | 1985-02-16 | 1985-08-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-08-17 | 1989-02-16 | 1989-08-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-08-17 | 1993-02-16 | 1993-08-18 | $7700.00 | Window Closed / Lapsed |