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US4216077A
Expired / Lapsed
US
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Method of cracking under hydrogen pressure for the production of olefins
Assignee: Carbonisation et Charbons Actifs CECA SA
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Filing: 1978-07-05
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Granted: 1980-08-05
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Expires: 1998-07-05
Abstract
Abstract A hydrocarbon feedstock derived from crude oil or other sources is subjected continuously to thermal cracking under pressure and in the presence of hydrogen in order to convert the feedstock to products of lower molecular weight containing high proportions of olefinic components. In a first processing step, a catalytic hydrogenating pretreatment is performed at a temperature within the range of 300° C. to 600° C. and under a pressure within the range of 12 to 85 bars. In a second step, a thermal cracking treatment is performed under a pressure within the range of 10 to 70 bars with residence times of less than 0.5 second and at a temperature within the range of 625° C. to 1,000° C., the quantity of hydrogen employed being such that the molar concentration in the effluents is at least equal to 20%.
Inventors
- 👤 Edgar Chahvekilian
- 👤 Rene Brouard
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 21:58
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/12; C10G2400/00; C10G2400/20
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
175 words
A continuous process whereby a hydrocarbon feedstock is subjected to thermal cracking under pressure and in the presence of hydrogen to convert said feedstock to products of lower molecular weight containing high proportions of olefinic components, wherein said method comprises the steps of: (a) conducting a catalytic hydrogenating pretreatment at a temperature from about 300° and 600° C. and a pressure from about 12 to 85 bars to modify the molecular structures of the feedstock, to lighten the feedstock and to desulphurize said feedstock, said pretreatment being conducted in a catalytic reactor interposed in a preheating/vaporization circuit of the thermal cracking process proper; and immediately thereafter; (b) conducting a thermal cracking treatment of the pretreated feedstock in the presence of hydrogen and the absence of steam under a pressure from about 10 to 70 bars with a residence time of less than 0.5 second and at a temperature from about 625° C. to 1,000° C., the quantity of hydrogen employed being such that its molar concentration in the effluents is at least equal to 20%.
Claim 2
Dependent Claim
175 words
A continuous process whereby a hydrocarbon feedstock is subjected to thermal cracking under pressure and in the presence of hydrogen to convert said feedstock to products of lower molecular weight containing high proportions of olefinic components, wherein said method comprises the steps of: (a) conducting a catalytic hydrogenating pretreatment at a temperature from about 300° and 600° C. and a pressure from about 12 to 85 bars to modify the molecular structures of the feedstock, to lighten the feedstock and to desulphurize said feedstock, said pretreatment being conducted in a catalytic reactor interposed in a preheating/vaporization circuit of the thermal cracking process proper; and immediately thereafter; (b) conducting a thermal cracking treatment of the pretreated feedstock in the presence of hydrogen and the absence of steam under a pressure from about 10 to 70 bars with a residence time of less than 0.5 second and at a temperature from about 625° C. to 1,000° C., the quantity of hydrogen employed being such that its molar concentration in the effluents is at least equal to 20%.
Claim 3
Dependent Claim
30 words
A process according to claim 1, wherein the hydrogen present in the treated hydrocarbon feedstock contains inert components, components which do not give rise to undersirable reactions or mixtures thereof.
Claim 4
Dependent Claim
27 words
A process according to claim 1, wherein said method further comprises recycling at least a portion of coproducts from the thermal cracking step to the pretreatment step.
Claim 5
Dependent Claim
34 words
A process according to claim 1, wherein at least a portion of the hydrogen is introduced between the hydrogenating pretreatment step and thermal cracking step, together with at least a portion of other reactants.
Claim 6
Dependent Claim
19 words
A process according to claim 1, wherein said process is applied to petroleum distillates containing high proportions of sulphur.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-08-05 | 1984-02-04 | 1984-08-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-08-05 | 1988-02-04 | 1988-08-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-08-05 | 1992-02-04 | 1992-08-05 | $7700.00 | Window Closed / Lapsed |