NL7503437A - Hydrogenation of aromatics-rich feedstocks - with catalysts contg. nickel, tungsten and fluorine on alumina - Google Patents
Hydrogenation of aromatics-rich feedstocks - with catalysts contg. nickel, tungsten and fluorine on aluminaInfo
- Publication number
- NL7503437A NL7503437A NL7503437A NL7503437A NL7503437A NL 7503437 A NL7503437 A NL 7503437A NL 7503437 A NL7503437 A NL 7503437A NL 7503437 A NL7503437 A NL 7503437A NL 7503437 A NL7503437 A NL 7503437A
- Authority
- NL
- Netherlands
- Prior art keywords
- aromatics
- hydrogenation
- tungsten
- alumina
- fluorine
- Prior art date
Links
Classifications
-
- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/22—Halogenating
- B01J37/26—Fluorinating
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
- C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
- C10G45/48—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/50—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum or tungsten metal, or compounds thereof
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Hydrocarbon feedstocks contg. >=10 wt.% aromatics are hydrogenated in the presence of a presulphided catalyst consisting mainly of Ni, W, F and Al2O3, with a Ni=W atomic ratio of 2.5-3.8:1, an Ni content of 10-30 (pref. 15-25) wt.% an F content of 0.25-5.0 wt.%, and an S:Ni atomic ratio of 0.7-1.5:1. Hydrogenation is pref. effected at 260-427 degrees C with an H2 partial pressure of 14.1-282 kg/cm2, a gas circulation rate (60-100% H2) of 12.46-267 Nm3/hl, and an LHSV of 0.25-10 w/w/hr. The process can be used to convert kerosene and aromatics-rich cycle oils into catalytic cracking stocks for the prodn. of gasoline blending components. Inclusion of F in the catalyst increases the degree of aromatics satn. per pass from ca. 30% to >=40%, giving a 2-3% increase in the prodn. of gasoline blending components during subsequent catalytic cracking.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US45410374A | 1974-03-25 | 1974-03-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
NL7503437A true NL7503437A (en) | 1975-09-29 |
Family
ID=23803317
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NL7503437A NL7503437A (en) | 1974-03-25 | 1975-03-21 | Hydrogenation of aromatics-rich feedstocks - with catalysts contg. nickel, tungsten and fluorine on alumina |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS50130724A (en) |
NL (1) | NL7503437A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994012593A1 (en) * | 1992-11-25 | 1994-06-09 | Union Oil Company Of California | Catalytic aromatic saturation in the presence of halide |
-
1975
- 1975-03-21 NL NL7503437A patent/NL7503437A/en not_active Application Discontinuation
- 1975-03-24 JP JP3459675A patent/JPS50130724A/ja active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994012593A1 (en) * | 1992-11-25 | 1994-06-09 | Union Oil Company Of California | Catalytic aromatic saturation in the presence of halide |
Also Published As
Publication number | Publication date |
---|---|
JPS50130724A (en) | 1975-10-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
BV | The patent application has lapsed |