US4298460A
Expired / Lapsed
US
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Process for processing sulfur-containing heavy oil
Assignee: Eneos Corp
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Filing: 1980-03-24
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Granted: 1981-11-03
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Expires: 2000-03-24
Abstract
Abstract A process for processing a sulfur-containing heavy oil, which comprises: in a first zone, catalytically cracking a sulfur-containing heavy oil in the presence of fluidized catalyst particles containing about 30 to 60 wt % Fe to thereby convert the heavy oil to a light oil, deposit sulfur-containing coke on the catalyst particles, and partially fixing the decomposed sulfur compounds with the reduced iron contained in the catalyst particles as iron sulfide; in a second zone, contacting the catalyst from the first zone with an oxygen containing gas in an amount less than that theoretically required to thereby partially combust the coke on the catalyst, reduce the iron in the catalyst, and fix the sulfur compounds contained in the coke as iron sulfide; and in a third zone, contacting the reduced catalyst from the second zone with steam in a fluidized manner to produce hydrogen and hydrogen sulfide and to convert the reduced iron and iron sulfide in the catalyst to iron oxides, with the iron oxide-containing catalyst obtained in the third zone being recirculated into the second zone to be reduced and a part of the reduced-state catalyst obtained in the second zone being recirculated into the first zone.
Inventors
- 👤 Kuniaki Fujimori
- 👤 Teruo Suzuka
- 👤 Yukio Inoue
- 👤 Shirou Aizawa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 20:09
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/745; B01J23/90; B01J23/94; C; C10; C10G; C10G11/00; C10G11/02; C10G11/14; C10G11/18
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
202 words
A process for processing a sulfur-containing heavy oil, which comprises: in a first zone, catalytically cracking a sulfur-containing heavy oil in a fluidized manner in the presence of reduced-state catalyst particles containing about 30 to 60 wt % Fe to thereby convert the heavy oil to a light oil, depositing sulfur-containing coke on the catalyst particles, and partially fixing the decomposed sulfur compounds with reduced iron contained in the catalyst particles as iron sulfide; in a second zone, contacting the catalyst from the first zone with an oxygen containing gas in an amount less than that theoretically required to thereby partially combust the coke on the catalyst, reduce the iron in the catalyst, and fix the sulfur compounds contained in the coke as iron sulfide; and in a third zone, contacting the reduced-state catalyst from the second zone with steam in a fluidized manner to produce hydrogen and hydrogen sulfide and to convert the reduced iron and iron sulfide in the catalyst to iron oxides, with the iron oxide-containing catalyst obtained in the third zone being recirculated into the second zone to be reduced and a part of the reduced-state catalyst obtained in the second zone being recirculated into the first zone.
Claim 2
Dependent Claim
202 words
A process for processing a sulfur-containing heavy oil, which comprises: in a first zone, catalytically cracking a sulfur-containing heavy oil in a fluidized manner in the presence of reduced-state catalyst particles containing about 30 to 60 wt % Fe to thereby convert the heavy oil to a light oil, depositing sulfur-containing coke on the catalyst particles, and partially fixing the decomposed sulfur compounds with reduced iron contained in the catalyst particles as iron sulfide; in a second zone, contacting the catalyst from the first zone with an oxygen containing gas in an amount less than that theoretically required to thereby partially combust the coke on the catalyst, reduce the iron in the catalyst, and fix the sulfur compounds contained in the coke as iron sulfide; and in a third zone, contacting the reduced-state catalyst from the second zone with steam in a fluidized manner to produce hydrogen and hydrogen sulfide and to convert the reduced iron and iron sulfide in the catalyst to iron oxides, with the iron oxide-containing catalyst obtained in the third zone being recirculated into the second zone to be reduced and a part of the reduced-state catalyst obtained in the second zone being recirculated into the first zone.
Claim 3
Dependent Claim
43 words
The process of claim 1, wherein said catalyst containing about 30 to 60 wt % Fe comprises a combination of two or more iron compounds or natural iron ores and/or an inorganic refractory material and is prepared by pulverizing, granulating, and then calcining.
Claim 4
Dependent Claim
19 words
The process of claim 2, wherein said iron compound is iron chloride, iron oxide, iron sulfate or iron carbonate.
Claim 5
Dependent Claim
17 words
The process of claim 2, wherein said natural iron ore is laterite, siderite, magnetite, hematite or limonite.
Claim 6
Dependent Claim
35 words
The process of claim 1, wherein the reaction in the first zone is conducted at a temperature of about 450° to 600° C. and under a pressure of about 0 to 15 kg/cm 2 G.
Claim 7
Dependent Claim
35 words
The process of claim 1, wherein the reaction in the second zone is conducted at a temperature of about 700° to 900° C. and under a pressure of about 0 to 15 kg/cm 2 G.
Claim 8
Dependent Claim
35 words
The process of claim 1, wherein the reaction in the third zone is conducted at a temperature of about 600° to 850° C. and under a pressure of about 0 to 15 kg/cm 2 G.
Claim 9
Dependent Claim
34 words
The process of claim 1, wherein an auxiliary fuel is introduced in the second zone, while controlling the amount of the auxiliary fuel to adjust the amount of hydrogen generated in the third zone.
Claim 10
Dependent Claim
32 words
The process of claims 1 or 8, wherein the amount of oxygen introduced in the second zone is about 0.2 to 0.6 mol per mol of carbon introduced in the second zone.
Claim 11
Dependent Claim
31 words
The process of claim 1, wherein the amount of steam introduced in the third zone is about 3 mols or more per mol of iron sulfide introduced in the third zone.
Claim 12
Dependent Claim
84 words
A process for processing a sulfur-containing heavy oil, as claimed in claim 1, wherein said sulfur-containing coke is deposited on the catalyst in an amount of about 2 to 8% by weight based on the weight of the catalyst, and further wherein a major portion of the iron oxide-containing catalyst obtained in the third zone is recirculated to the second zone to be reduced and wherein a major portion of the reduced-state catalyst obtained in the second zone is recirculated to the first zone.
References Cited (Backward Citations)
US4224140A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-11-02 | 1985-05-04 | 1985-11-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-02 | 1989-05-04 | 1989-11-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-02 | 1993-05-04 | 1993-11-03 | $7700.00 | Window Closed / Lapsed |