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US4120778A
Expired / Lapsed
US
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Process for the conversion of hydrocarbons in atmospheric crude residue
Assignee: Shell USA Inc
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Filing: 1977-09-09
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Granted: 1978-10-17
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Expires: 1997-09-09
Abstract
Abstract A process is disclosed for the conversion of a hydrocarbon oil vacuum distillation residue to one or more atmospheric distillates by a processing sequence comprising vacuum fractionation, catalytic cracking or hydrocracking, atmospheric fractionation, hydrotreating, atmospheric fractionation, and vacuum fractionation with certain recycle of intermediate streams to achieve efficient, economic operation.
Inventors
- 👤 Frans Goudriaan
- 👤 Jakob VAN Klinken
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 16:14
CPC Classifications
C; C10; C10G; C10G69/00; C10G65/00; C10G65/14; C10G69/14
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
215 words
A process for the preparation of atmospheric hydrocarbon oil distillates from a hydrocarbon oil residue obtained by atmospheric distillation which comprises: (a) fractionating said residue by vacuum distillation into a vacuum distillate and a vacuum residue, (b) cracking said vacuum distillate in a cracking zone comprising either a catalytic cracking zone or a hydrocracking zone to obtain a cracked product, (c) fractionating said cracked product by atmospheric fractionation distillation into at least one light distillate product, a cracked intermediate fraction and a cracked residue, and recycling at least part of said cracked intermediate fraction or said cracked residue to the cracking zone of step (b), (d) hydrotreating the vacuum residue from step (a) in a catalytic hydrotreating zone under such conditions that more than 50% by weight of the total feed to the catalytic hydrotreating zone is converted to a product having a lower boiling point than the feed, (e) fractionating said hydrotreated product by atmospheric fractionation distillation into at least one light atmospheric distillate product, a hydrotreated intermediate fraction and a hydrotreated residue, (f) fractionating said hydrotreated residue by vacuum distillation into a vacuum distillate and a hydrotreated vacuum residue, and then, (g) recycling at least 50% by weight of the hydrotreated vacuum residue from step (f) to the cracking zone of step (b).
Claim 2
Dependent Claim
215 words
A process for the preparation of atmospheric hydrocarbon oil distillates from a hydrocarbon oil residue obtained by atmospheric distillation which comprises: (a) fractionating said residue by vacuum distillation into a vacuum distillate and a vacuum residue, (b) cracking said vacuum distillate in a cracking zone comprising either a catalytic cracking zone or a hydrocracking zone to obtain a cracked product, (c) fractionating said cracked product by atmospheric fractionation distillation into at least one light distillate product, a cracked intermediate fraction and a cracked residue, and recycling at least part of said cracked intermediate fraction or said cracked residue to the cracking zone of step (b), (d) hydrotreating the vacuum residue from step (a) in a catalytic hydrotreating zone under such conditions that more than 50% by weight of the total feed to the catalytic hydrotreating zone is converted to a product having a lower boiling point than the feed, (e) fractionating said hydrotreated product by atmospheric fractionation distillation into at least one light atmospheric distillate product, a hydrotreated intermediate fraction and a hydrotreated residue, (f) fractionating said hydrotreated residue by vacuum distillation into a vacuum distillate and a hydrotreated vacuum residue, and then, (g) recycling at least 50% by weight of the hydrotreated vacuum residue from step (f) to the cracking zone of step (b).
Claim 3
Dependent Claim
87 words
A process according to claim 1, wherein in step (d) the catalytic hydrotreatment is carried out as a two-stage process and that the first stage is effected in the presence of a quantity of H 2 S corresponding to an H 2 S content of the gas at the reactor inlet of more than 10%v and the second stage in the presence of a quantity of H 2 S corresponding to an H 2 S content of the gas at the reactor inlet of less than 5%v.
Claim 4
Dependent Claim
64 words
A process according to claim 1, wherein in step (b) catalytic cracking is carried out at an average temperature of from 400° to 550° C., a pressure of from 1 to 10 bar, a space velocity of from 0.25 to 4 kg.kg -1 .h -1 and a rate of catalyst replenishment of from 0.1 to 5 tonnes of catalyst per 100 tonnes of feed.
Claim 5
Dependent Claim
65 words
A process according to claim 1, wherein in step (b) hydrocracking is carried out as a two-stage process in the presence of a weakly or moderately acidic catalyst comprising one or more metals having hydrogenation activity on a carrier in the first stage and a moderately or strongly acidic catalyst comprising one or more metals having hydrogenation activity on a carrier in the second stage.
Claim 6
Dependent Claim
37 words
A process according to claim 1, wherein in step (b) hydrocracking is carried out as a two-stage process and that the whole reaction product from the first stage is used as the feed for the second stage.
Claim 7
Dependent Claim
58 words
A process according to claim 1, wherein in step (b) hydrocracking is carried out at an average temperature of from 250° to 450° C., a hydrogen partial pressure of from 25 to 300 bar, a space velocity of from 0.1 to 10 kg.l -1 .h -1 and a hydrogen-to-feed ratio of from 200° to 3000 Nl.kg -1 .
Claim 8
Dependent Claim
62 words
A process according to claim 1 wherein in step (d) the catalytic hydrotreatment is carried out as a two-stage process in the presence of a catalyst consisting of more than 80%w silica in the first stage and a catalyst comprising one or more metals having hydrogenation activity on a carrier, which carrier consists of more than 40%w alumina, in the second stage.
Claim 9
Dependent Claim
60 words
A process according to claim 1, wherein in step (d) the catalytic hydrotreatment is carried out at an average temperature of from 375° to 475° C., a hydrogen partial pressure of from 25 to 300 bar, a space velocity of from 0.1 to 1.5 kg.l -1 .h -1 and a hydrogen-to-feed ratio of from 250 to 2500 Nl.kg -1 .
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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) | 1981-10-16 | 1982-04-17 | 1982-10-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-16 | 1986-04-17 | 1986-10-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-16 | 1990-04-17 | 1990-10-17 | $7700.00 | Window Closed / Lapsed |