ES2043859T3 - Catalizador de isomerizacion de parafinas y su produccion. - Google Patents
Catalizador de isomerizacion de parafinas y su produccion.Info
- Publication number
- ES2043859T3 ES2043859T3 ES88311980T ES88311980T ES2043859T3 ES 2043859 T3 ES2043859 T3 ES 2043859T3 ES 88311980 T ES88311980 T ES 88311980T ES 88311980 T ES88311980 T ES 88311980T ES 2043859 T3 ES2043859 T3 ES 2043859T3
- Authority
- ES
- Spain
- Prior art keywords
- catalyst
- less
- alumina
- weight
- peak
- 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 - Lifetime
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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- 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
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
- C10G45/62—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing platinum group metals or compounds thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Lubricants (AREA)
Abstract
SE DESCRIBE UN CATALIZADOR PARA ISOMERIZACION DE CERAS, QUE COMPRENDE UN COMPONENTE DE HIDROGENACION METALICO DEL GRUPO VIII SOBRE ALUMINA QUE CONTIENE ALUMINA FLUORADA. EL CATALIZADOR TIENE UNA RELACION N/AL DE CONTENIDO DE N EN LA SUPERFICIE DE 0,01 O MENOS, POR ESPECTROSCOPIA FOTOELECTRONICA DE RAYOS-X, UN CONTENIDO DE FLUOR TOTAL DE 2-10 %, UN CONTENIDO DE FLUOR SUPERFICIAL DEFINIDO COMO LA CANTIDAD DE FLUOR EN UNA CAPA QUE SE EXTIENDE DESDE LA SUPERFICIE EXTERIOR A UNA PROFUNDIDAD DE 0,254 MM DE MENOS QUE 3 % EN PESO, SIENDO LA CONCENTRACION DE FLUOR SUPERFICIAL MENOR QUE LA CONCENTRACION DE FLUOR DEL CONJUNTO, Y UNA ALTURA DE PICO DE HIDRATO DE HIDROXIFLUORURO DE ALUMINIO DE 60 O MENOS, DETERMINADA COMO LA CANTIDAD RELATIVA DE HIDRATO REPRESENTADO POR UN PICO EN EL PATRON DE DIFRACCION DE RAYOS-X (XRD) DE 2(VACIO) = 0,566 NM, CUANDO UN NIVEL DE HIDRATO DE 100 CORRESPONDE A LA ALTURA DE PICO DE XRD PRODUCIDA POR UN MATERIAL DE REFERNCIA QUE CONSTA DE 0,6 % EN PESO DE PLATINO 150 M2/G (TAU)-ALUMINA QUE CONTIENE 7,2 % EN PESO DE FLUOR OBTENIDO DE UN MODO ESPECIFICO. TAMBIEN SE DESCRIBE UN METODO PARA PRODUCIR EL CATALIZADOR DE ISOMERIZACION DE CERA DEBIL, E INCLUYE TRATAR UN SOPORTE CON CARGA DE METAL DEL GRUPO VIII CON UNA FUENTE DE FLUOR EN CONDICIONES ESPECIFICAS, Y CALENTAR EL SOPORTE FLUORADO EN UN INTERVALO DE TEMPERATURAS FINAL ESPECIFICO DURANTE UN TIEMPO ESPECIFICADO.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13479587A | 1987-12-18 | 1987-12-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2043859T3 true ES2043859T3 (es) | 1994-01-01 |
Family
ID=22465046
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES88311980T Expired - Lifetime ES2043859T3 (es) | 1987-12-18 | 1988-12-16 | Catalizador de isomerizacion de parafinas y su produccion. |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0321300B1 (es) |
JP (1) | JPH01281148A (es) |
AU (1) | AU608396B2 (es) |
DE (1) | DE3873290T2 (es) |
ES (1) | ES2043859T3 (es) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NO885553L (no) * | 1987-12-18 | 1989-06-19 | Exxon Research Engineering Co | Katalysator for hydroisomerisering og hydrokrakking av voks for aa fremstille flytende hydrokarbon-brennstoff. |
US4919786A (en) * | 1987-12-18 | 1990-04-24 | Exxon Research And Engineering Company | Process for the hydroisomerization of was to produce middle distillate products (OP-3403) |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2668866A (en) * | 1951-08-14 | 1954-02-09 | Shell Dev | Isomerization of paraffin wax |
BE627517A (es) * | 1962-01-26 | |||
US4612293A (en) * | 1985-09-27 | 1986-09-16 | Phillips Petroleum Company | Upgrading of spent butane isomerization catalyst to pentane isomerization catalyst |
-
1988
- 1988-12-16 EP EP88311980A patent/EP0321300B1/en not_active Expired - Lifetime
- 1988-12-16 ES ES88311980T patent/ES2043859T3/es not_active Expired - Lifetime
- 1988-12-16 AU AU26942/88A patent/AU608396B2/en not_active Ceased
- 1988-12-16 DE DE19883873290 patent/DE3873290T2/de not_active Expired - Fee Related
- 1988-12-19 JP JP63320303A patent/JPH01281148A/ja active Pending
Also Published As
Publication number | Publication date |
---|---|
DE3873290D1 (de) | 1992-09-03 |
DE3873290T2 (de) | 1993-02-25 |
EP0321300A2 (en) | 1989-06-21 |
AU608396B2 (en) | 1991-03-28 |
AU2694288A (en) | 1989-06-22 |
EP0321300A3 (en) | 1989-08-30 |
EP0321300B1 (en) | 1992-07-29 |
JPH01281148A (ja) | 1989-11-13 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG2A | Definitive protection |
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