GB1140778A - Process for the conversion of hydrocarbon oils - Google Patents
Process for the conversion of hydrocarbon oilsInfo
- Publication number
- GB1140778A GB1140778A GB77768A GB77768A GB1140778A GB 1140778 A GB1140778 A GB 1140778A GB 77768 A GB77768 A GB 77768A GB 77768 A GB77768 A GB 77768A GB 1140778 A GB1140778 A GB 1140778A
- Authority
- GB
- United Kingdom
- Prior art keywords
- range
- dehydrogenation
- catalyst
- oil
- dehydroisomerization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/128—Halogens; Compounds thereof with iron group metals or platinum group metals
- B01J27/13—Platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/90—Regeneration or reactivation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
Abstract
1,140,778. Conversion of hydrocarbons. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 5Jan.,1968, No. 777/68. Heading C5E. A process for the conversion of hydrocarbon oils comprises (1) dehydrogenating and dehydroisomerizing a hydrocarbon oil boiling below 220‹ C. over a catalyst containing one or more metals of groups VI B and/or VIII of the Periodic Table of Elements deposited on a refractory carrier, at a temperature in the range of from 400‹ to 540‹ C., a pressure in the range of from 7 to 55 atmospheres gauge, a liquid hourly space velocity in the range of from 4 to 15 volumes of oil per hour per volume of catalyst and a mole ratio of hydrogen to oil in the range of from 2À5 to 1 to 12 to 1 and (2) hydrocracking the dehydrogenated and dehydroisomerized hydrocarbon oil at a temperature in the range of from 250 to 450‹ C., a pressure in the range of from 7 to 55 atmospheres gauge, a liquid hourly space velocity in the range of from 1 to 5 volumes of oil per hour per volume of catalyst and a mole ratio of hydrogen to oil in the range of from 1 to 1 to 12 to 1 over a catalyst containing one or more of the metals rhenium, copper, silver, iron, cobalt, nickel, chromium, tungsten, molybdenum, platinum and palladium deposited on a molecular sieve carrier or intimately associated with an acid-acting refractory support, the intimate association having been achieved by contacting the support in hydrogel form with an aqueous solution of one or more soluble compounds of the said metal or metals, or by precipitating the support in hydrogel form in the presence of an aqueous solution of one or more soluble compounds of the said metal or metals. The dehydrogenation and dehydroisomerization result in the formation of aromatics and in the formation of sixmembered rings at the expense of five-membered rings. The dehydrogenation and dehydroisomerization may take place in a single reactor or in two consecutive reactors; in the latter case dehydrogenation is the main reaction in the first reactor and dehydroisomerization is the main reaction in the second reactor. The hydrocracking stage may be followed by a further dehydrogenation stage. The catalyst for the dehydrogenation and dehydroisomerization stages may comprise chromium, molybdenum, tungsten, iron, cobalt, nickel, ruthenium, rhodium, palladium, osmium, iridium, or platinum, supported on alumina containing not more than 5% of silica. Chlorine and/or fluorine may also be included. When an acidacting refractory support is used in the hydrocracking stage it may comprise from 50 to 90% of silica and 50 to 10% of one or more of alumina, magnesia, zirconia and boria. The hydrocracking catalyst may contain from 0À1 to 5% by weight of fluorine. They may be, but preferably are not, sulphided. The catalyst for the second dehydrogenation stage may be similar to that in the first dehydrogenation stage, and a preferred composition is 0À1 to 1% by weight of platinum and 0À1 to 1% by weight of chlorine on a carrier consisting of alumina containing not more than 0À5% by weight of silica.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB77768A GB1140778A (en) | 1968-01-05 | 1968-01-05 | Process for the conversion of hydrocarbon oils |
FR1585561D FR1585561A (en) | 1968-01-05 | 1968-10-08 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB77768A GB1140778A (en) | 1968-01-05 | 1968-01-05 | Process for the conversion of hydrocarbon oils |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1140778A true GB1140778A (en) | 1969-01-22 |
Family
ID=9710341
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB77768A Expired GB1140778A (en) | 1968-01-05 | 1968-01-05 | Process for the conversion of hydrocarbon oils |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1585561A (en) |
GB (1) | GB1140778A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2125343A1 (en) * | 1971-02-11 | 1972-09-29 | Shell Int Research |
-
1968
- 1968-01-05 GB GB77768A patent/GB1140778A/en not_active Expired
- 1968-10-08 FR FR1585561D patent/FR1585561A/fr not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2125343A1 (en) * | 1971-02-11 | 1972-09-29 | Shell Int Research |
Also Published As
Publication number | Publication date |
---|---|
FR1585561A (en) | 1970-01-23 |
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