ES2011050B3 - Procedimiento de reformacion catalitica a traves de por lo menos dos lechos de catalizador. - Google Patents
Procedimiento de reformacion catalitica a traves de por lo menos dos lechos de catalizador.Info
- Publication number
- ES2011050B3 ES2011050B3 ES87400221T ES87400221T ES2011050B3 ES 2011050 B3 ES2011050 B3 ES 2011050B3 ES 87400221 T ES87400221 T ES 87400221T ES 87400221 T ES87400221 T ES 87400221T ES 2011050 B3 ES2011050 B3 ES 2011050B3
- Authority
- ES
- Spain
- Prior art keywords
- catalyst
- load
- bed
- beds
- support
- 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
- 239000003054 catalyst Substances 0.000 title abstract 8
- 230000003197 catalytic effect Effects 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 4
- VJYFKVYYMZPMAB-UHFFFAOYSA-N ethoprophos Chemical compound CCCSP(=O)(OCC)SCCC VJYFKVYYMZPMAB-UHFFFAOYSA-N 0.000 abstract 2
- 229910052736 halogen Inorganic materials 0.000 abstract 2
- 150000002367 halogens Chemical class 0.000 abstract 2
- 229910052697 platinum Inorganic materials 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 abstract 1
- 229910052782 aluminium Inorganic materials 0.000 abstract 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract 1
- 238000001833 catalytic reforming Methods 0.000 abstract 1
- 229910052733 gallium Inorganic materials 0.000 abstract 1
- 229910052732 germanium Inorganic materials 0.000 abstract 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 229910052738 indium Inorganic materials 0.000 abstract 1
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 abstract 1
- 150000002902 organometallic compounds Chemical class 0.000 abstract 1
- 229910052702 rhenium Inorganic materials 0.000 abstract 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 abstract 1
- 229910052716 thallium Inorganic materials 0.000 abstract 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 abstract 1
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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
- C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
- C10G35/09—Bimetallic catalysts in which at least one of the metals is a platinum group metal
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
PROCEDIMIENTO DE REFORMADO CATALITICO DE UNA CARGA DE HIDROCARBUROS EN EL QUE LA CARGA ATRAVIESA SUCESIVAMENTE AL MENOS DOS LECHOS DE CATALIZADORES, EL PRIMER LECHO ATRAVESADO POR LA CARGA ES UN LECHO DE UN PRIMER CATALIZADOR A BASE DE UN SOPORTE QUE CONTIENE PLATINO, RENIO, Y AL MENOS UN HALOGENO Y AL MENOS EL ULTIMO LECHO ATRAVESADO POR LA CARGA QUE ES UN LECHO MOVIL DE UN SEGUNDO CATALIZADOR A BASE DE UN SOPORTE QUE CONTIENE PLATINO Y AL MENOS UN METAL ADICIONAL M ELEGIDO EN EL GRUPO FORMADO POR EL ESTAÑO, EL GALIO, EL GERMANIO, EL INDIO, EL PLOMO Y EL TALIO Y AL MENOS UN HALOGENO, M HABIENDO SIDO INTRODUCIDO DICHO METAL SOBRE EL SOPORTE CON LA AYUDA DE UN COMPUESTO ORGANOMETALICO Y SIENDO LA PROPORCION PONDERAL DEL SEGUNDO CATALIZADOR DEL 25 AL 55% A LA MASA TOTAL CATALITICA UTILIZADA EN EL CONJUNTO DE LOS LECHOS CATALITICOS. LA CARGA ATRAVIESA SUCESIVAMENTE CON PREFERENCIA AL MENOS DOS LECHOS FIJOS DEL PRIMER CATALIZADOR Y AL MENOS UN LECHO MOVIL DEL SEGUNDO CATALIZADOR, Y EL SOPORTEDE DOS CATALIZADORES ES PREFERENTEMENTE ALUMINICO. EL PROCEDIMIENTO PERMITE OBTENER GASOLINAS DE CALIDAD (NUMERO DE OCTANOS SUPERIOR A 95) DURANTE LARGOS PERIODOS.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR8601551A FR2593824B1 (fr) | 1986-02-03 | 1986-02-03 | Procede de reformage catalytique a travers au moins trois lits de catalyseur |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2011050B3 true ES2011050B3 (es) | 1989-12-16 |
Family
ID=9331814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES87400221T Expired ES2011050B3 (es) | 1986-02-03 | 1987-01-30 | Procedimiento de reformacion catalitica a traves de por lo menos dos lechos de catalizador. |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4737262A (es) |
| EP (1) | EP0233116B1 (es) |
| JP (1) | JP2544917B2 (es) |
| CA (1) | CA1293467C (es) |
| DE (1) | DE3760424D1 (es) |
| ES (1) | ES2011050B3 (es) |
| FR (1) | FR2593824B1 (es) |
| GR (1) | GR3000138T3 (es) |
Families Citing this family (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4935566A (en) * | 1987-11-17 | 1990-06-19 | Mobil Oil Corporation | Dehydrocyclization and reforming process |
| EP0393099B1 (en) * | 1987-11-17 | 1994-02-23 | Mobil Oil Corporation | A dehydrogenation catalystsynthesis and its use |
| US4929333A (en) * | 1989-02-06 | 1990-05-29 | Uop | Multizone catalytic reforming process |
| US4985132A (en) * | 1989-02-06 | 1991-01-15 | Uop | Multizone catalytic reforming process |
| US4929332A (en) * | 1989-02-06 | 1990-05-29 | Uop | Multizone catalytic reforming process |
| US5221465A (en) * | 1990-12-14 | 1993-06-22 | Exxon Research And Engineering Company | High activity, high yield tin modified platinum-iridium catalysts, and reforming process utilizing such catalysts |
| US5269907A (en) * | 1990-12-14 | 1993-12-14 | Exxon Research And Engineering Co. | Process for reforming at low severities with high-activity, high-yield, tin modified platinum-iridium catalysts |
| CA2055929A1 (en) * | 1990-12-14 | 1992-06-15 | William C. Baird, Jr. | Process for reforming at low severities with high activity, high yield tin modified platinum-iridium catalysts |
| US5106809A (en) * | 1990-12-14 | 1992-04-21 | Exxon Research And Engineering Company | High activity, high yield tin modified platinum-iridium catalysts, and reforming process utilizing such catalysts |
| US5203988A (en) * | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
| US5190638A (en) * | 1991-12-09 | 1993-03-02 | Exxon Research And Engineering Company | Moving bed/fixed bed two stage catalytic reforming |
| US5190639A (en) * | 1991-12-09 | 1993-03-02 | Exxon Research And Engineering Company | Multiple fixed-bed reforming units sharing common moving bed reactor |
| US5354451A (en) * | 1991-12-09 | 1994-10-11 | Exxon Research And Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming |
| US5196110A (en) * | 1991-12-09 | 1993-03-23 | Exxon Research And Engineering Company | Hydrogen recycle between stages of two stage fixed-bed/moving-bed unit |
| EP0616632B1 (en) * | 1991-12-09 | 1999-08-25 | Exxon Research And Engineering Company | Reforming with two fixed-bed units, each having a moving-bed tail reactor sharing a common regenerator |
| US5211838A (en) * | 1991-12-09 | 1993-05-18 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with interstage aromatics removal |
| FR2704864B1 (fr) | 1993-05-06 | 1995-11-17 | Inst Francais Du Petrole | Procede d'hydroreformage catalytique. |
| FR2735487B1 (fr) * | 1995-06-16 | 1997-08-22 | Inst Francais Du Petrole | Procede de transformation catalytique d'hydrocarbures en composes aromatiques avec un catalyseur contenant des metaux alcalins ou alcalino-terreux |
| US5858205A (en) * | 1997-05-13 | 1999-01-12 | Uop Llc | Multizone catalytic reforming process |
| FR2770535B1 (fr) * | 1997-10-31 | 1999-12-10 | Inst Francais Du Petrole | Procede d'hydroreformage catalytique |
| FR2770421B1 (fr) * | 1997-10-31 | 1999-12-10 | Inst Francais Du Petrole | Procede de preparation de catalyseurs utilisables dans les reactions de transformation de composes organiques |
| FR2770520B1 (fr) * | 1997-10-31 | 1999-12-10 | Inst Francais Du Petrole | Procede d'hydrogenation selective des composes insatures |
| FR2770521B1 (fr) * | 1997-10-31 | 1999-12-10 | Inst Francais Du Petrole | Procede de deshydrogenation d'hydrocarbures aliphatiques satures en hydrocarbures olefiniques |
| US6190534B1 (en) * | 1999-03-15 | 2001-02-20 | Uop Llc | Naphtha upgrading by combined olefin forming and aromatization |
| US6406614B1 (en) | 1999-12-22 | 2002-06-18 | Phillips Petroleum Company | Method for zeolite platinization |
| US7267987B2 (en) * | 2003-01-06 | 2007-09-11 | Uop Llc | Process and assembly for simultaneously evaluating a plurality of catalysts |
| US7811447B2 (en) * | 2007-08-01 | 2010-10-12 | Uop Llc | Method of transferring particles from one pressure zone to another pressure zone |
| US7803326B2 (en) * | 2007-08-01 | 2010-09-28 | Uop Llc | Hydrocarbon conversion unit including a reaction zone receiving transferred catalyst |
| US7799729B2 (en) * | 2009-02-23 | 2010-09-21 | Uop Llc | Reforming catalyst |
| EP2725094A1 (en) | 2012-10-29 | 2014-04-30 | Nederlandse Organisatie voor toegepast- natuurwetenschappelijk onderzoek TNO | Epithelial tissue model |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2814599A (en) * | 1953-04-17 | 1957-11-26 | Kellogg M W Co | Group iii metal compound promoted platinum or palladium catalyst |
| US3415737A (en) * | 1966-06-24 | 1968-12-10 | Chevron Res | Reforming a sulfur-free naphtha with a platinum-rhenium catalyst |
| FR2031984A5 (es) * | 1969-02-14 | 1970-11-20 | Raffinage Cie Francaise | |
| US3702294A (en) * | 1971-05-10 | 1972-11-07 | Universal Oil Prod Co | Trimetallic hydrocarbon conversion catalyst and uses thereof |
| US3772183A (en) * | 1971-12-17 | 1973-11-13 | Standard Oil Co | Reforming petroleum hydrocarbons with gallium-promoted catalysts |
| FR2206124B1 (es) * | 1972-11-10 | 1976-08-20 | Inst Francais Du Petrole | |
| SE365375B (es) * | 1972-12-18 | 1974-03-18 | Ericsson Telefon Ab L M | |
| US4507401A (en) * | 1983-04-01 | 1985-03-26 | At&T Bell Laboratories | Intermetallic catalyst preparation |
| FR2545380B1 (fr) * | 1983-05-05 | 1988-04-08 | Catalyse Soc Prod Francais | Procede de fabrication de catalyseurs de conversion d'hydrocarbures |
| FR2560205B1 (fr) * | 1984-02-23 | 1988-07-15 | Inst Francais Du Petrole | Procede de reformage catalytique |
-
1986
- 1986-02-03 FR FR8601551A patent/FR2593824B1/fr not_active Expired
-
1987
- 1987-01-30 EP EP87400221A patent/EP0233116B1/fr not_active Expired
- 1987-01-30 ES ES87400221T patent/ES2011050B3/es not_active Expired
- 1987-01-30 DE DE8787400221T patent/DE3760424D1/de not_active Expired
- 1987-02-03 JP JP62023404A patent/JP2544917B2/ja not_active Expired - Fee Related
- 1987-02-03 CA CA000528881A patent/CA1293467C/fr not_active Expired - Lifetime
- 1987-02-03 US US07/010,596 patent/US4737262A/en not_active Expired - Lifetime
-
1989
- 1989-08-28 GR GR89400071T patent/GR3000138T3/el unknown
Also Published As
| Publication number | Publication date |
|---|---|
| GR3000138T3 (en) | 1990-11-29 |
| DE3760424D1 (en) | 1989-09-14 |
| FR2593824B1 (fr) | 1988-11-04 |
| JP2544917B2 (ja) | 1996-10-16 |
| CA1293467C (fr) | 1991-12-24 |
| EP0233116B1 (fr) | 1989-08-09 |
| JPS62192488A (ja) | 1987-08-24 |
| US4737262A (en) | 1988-04-12 |
| FR2593824A1 (fr) | 1987-08-07 |
| EP0233116A1 (fr) | 1987-08-19 |
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