ES361495A1 - Process for the Activation of a Catalyst - Google Patents
Process for the Activation of a CatalystInfo
- Publication number
- ES361495A1 ES361495A1 ES361495A ES361495A ES361495A1 ES 361495 A1 ES361495 A1 ES 361495A1 ES 361495 A ES361495 A ES 361495A ES 361495 A ES361495 A ES 361495A ES 361495 A1 ES361495 A1 ES 361495A1
- Authority
- ES
- Spain
- Prior art keywords
- sio
- catalyst
- hydrogel
- mgo
- tio
- 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
-
- 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
- B01J23/74—Iron 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
-
- 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
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A hydrogenative catalyst is prepared by contacting an amorphous acid-acting refractory support in hydrogel form with a solution of one or more Ni, Co and/or Fe compounds and by washing and drying the contacted hydrogel, F being incorporated into the hydrogel prior to the drying step, the hydrogel of the support being substantially Na. All the metal component being incorporated therein by ion exchange, and is characterized in that the catalyst is subjected to a sulphiding treatment with a gas containing at least one S compound at a terminal temperature of at least 500 C. Preferably the catalyst also contains a Cr, Mo or W promoter. Suitable supparts are Al 2 O 3 , SiO 2 , TiO 2 , MgO, SiO 2 -Al 2 O 3 , SiO 2 -MgO, SiO 2 -AlO 3 -ZrO 2 and SiO 2 -TiO 2 . Precalcination immediately before the sulphiding treatment may be carried out at temperatures up to 500 C. The sulphiding treatment is usually done in the presence of H 2 gas.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69121967A | 1967-12-18 | 1967-12-18 | |
| US69113267A | 1967-12-18 | 1967-12-18 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES361495A1 true ES361495A1 (en) | 1970-11-16 |
Family
ID=27104729
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES361495A Expired ES361495A1 (en) | 1967-12-18 | 1968-12-16 | Process for the Activation of a Catalyst |
Country Status (6)
| Country | Link |
|---|---|
| BE (1) | BE725546A (en) |
| DE (1) | DE1814973A1 (en) |
| ES (1) | ES361495A1 (en) |
| FR (1) | FR1595127A (en) |
| GB (1) | GB1188447A (en) |
| NL (1) | NL6818025A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3591487A (en) * | 1969-12-22 | 1971-07-06 | Shell Oil Co | Hydrocracking process improvement by high temperature sulfiding and dry gas processing |
| US5358628A (en) * | 1990-07-05 | 1994-10-25 | Mobil Oil Corporation | Production of high viscosity index lubricants |
-
1968
- 1968-12-16 ES ES361495A patent/ES361495A1/en not_active Expired
- 1968-12-16 GB GB5967668A patent/GB1188447A/en not_active Expired
- 1968-12-16 NL NL6818025A patent/NL6818025A/xx unknown
- 1968-12-16 DE DE19681814973 patent/DE1814973A1/en active Pending
- 1968-12-16 BE BE725546D patent/BE725546A/xx unknown
- 1968-12-16 FR FR1595127D patent/FR1595127A/fr not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| FR1595127A (en) | 1970-06-08 |
| NL6818025A (en) | 1969-06-20 |
| BE725546A (en) | 1969-06-16 |
| DE1814973A1 (en) | 1969-07-10 |
| GB1188447A (en) | 1970-04-15 |
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