Patent EP0347003A1 successfully refreshed from Google Patents.
EP0347003A1
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EP
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Process for the conversion of a hydrocarbonaceous feedstock
Assignee: Shell Internationale Research Maatschappij BV
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Filing: 1989-06-14
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Granted: —
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Expires: 2009-06-14
Abstract
Abstract Process for the conversion of a hydrocarbonaceous feedstock having an end boiling point of at most 330 °C, which process comprises contacting the feedstock with a zeolitic catalyst comprising a zeolite with a pore diameter of 0.3 to 0.7 nm at a temperature above 500 °C during less than 10 seconds.
Inventors
- 👤 Ian Ernst Maxwell
- 👤 Der Eijk Jjohan Meindert Van
- 👤 Jaydeep Biswas
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-10-29 17:49
CPC Classifications
C; C10; C10G; C10G25/00; C10G11/00; C10G11/02; C10G11/04; C10G11/05
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
52 words
A process for the conversion of a hydrocarbonaceous feedstock having an end boiling point of at most 330 °C, which process comprises contacting the feedstock with a zeolitic catalyst comprising a zeolite with a pore diameter of 0.3 to 0.7 nm at a temperature above 500 °C during less than 10 seconds.
Claim 2
Dependent Claim
52 words
A process for the conversion of a hydrocarbonaceous feedstock having an end boiling point of at most 330 °C, which process comprises contacting the feedstock with a zeolitic catalyst comprising a zeolite with a pore diameter of 0.3 to 0.7 nm at a temperature above 500 °C during less than 10 seconds.
Claim 3
Dependent Claim
21 words
A process according to claim 1, in which the feedstock is contacted with the zeolitic catalyst during 0.2 to 6 seconds.
Claim 4
Dependent Claim
18 words
A process according to claim 1 or 2, in which the temperature is from 500 to 900 °C.
Claim 5
Dependent Claim
16 words
A process according to claim 3, in which the temperature is from 550 to 800 °C.
Claim 6
Dependent Claim
32 words
A process according to any one of claims 1 to 4, in which the zeolitic catalyst comprises as zeolites substantially only zeolites with a pore diameter of from 0.3 to 0.7 nm.
Claim 7
Dependent Claim
30 words
A process according to any one of the preceding claims wherein the zeolite has a pore diameter of 0.5 to 0.7 nm and the temperature is up to 750 °C.
Claim 8
Dependent Claim
34 words
A process according to any one of claims 1 to 6, in which the zeolite is selected from the group consisting of crystalline metal silicates having a ZSM-5 structure, ferrierite, erionite and mixtures thereof.
Claim 9
Dependent Claim
21 words
Process according to any one of claims 1 to 7, in which the zeolite is in substantially in its hydrogen form.
Claim 10
Dependent Claim
21 words
A process according to any one of claims 1 to 8, in which the pressure is from 1 to 10 bar.
Claim 11
Dependent Claim
27 words
A process according to any one of claims 1 to 9, in which the catalyst/feedstock weight ratio is from 1 to 150:1, preferably from 20 to 120:1.
Claim 12
Dependent Claim
21 words
A process according to any one of claims 1 to 10, which is carried out in a moving bed of catalyst.
Claim 13
Dependent Claim
25 words
A process according to any one of claims 1 to 11, in which the feedstock has an initial boiling point of at least -45 °C.
Claim 14
Dependent Claim
18 words
A process according to claim 12, in which the feedstock comprises C₃₋₄-hydrocarbons, naphtha, gasoline, kerosine or mixtures thereof.
Claim 15
Dependent Claim
15 words
A process according to claim 1, substantially as described hereinbefore with reference to the Examples.
Claim 16
Dependent Claim
19 words
A hydrocarbonaceous product, or a fraction thereof, when obtained by the process of any one of the preceding claims.
References Cited (Backward Citations)
US3140322A
Cited
US3856659A
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US3886060A
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US4218344A
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US4100218A
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US4390413A
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US4310440A
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