MY104604A - Use of an aluminosilicate-type catalyst containing gallium in aromatising light cuts containing five to seven carbon atoms per molecule. - Google Patents
Use of an aluminosilicate-type catalyst containing gallium in aromatising light cuts containing five to seven carbon atoms per molecule.Info
- Publication number
- MY104604A MY104604A MYPI90002195A MYPI19902195A MY104604A MY 104604 A MY104604 A MY 104604A MY PI90002195 A MYPI90002195 A MY PI90002195A MY PI19902195 A MYPI19902195 A MY PI19902195A MY 104604 A MY104604 A MY 104604A
- Authority
- MY
- Malaysia
- Prior art keywords
- aromatising
- aluminosilicate
- carbon atoms
- per molecule
- atoms per
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 4
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 title abstract 2
- 229910052733 gallium Inorganic materials 0.000 title abstract 2
- 125000004432 carbon atom Chemical group C* 0.000 title 1
- 150000001336 alkenes Chemical class 0.000 abstract 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 abstract 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 abstract 1
- 229910052731 fluorine Inorganic materials 0.000 abstract 1
- 239000011737 fluorine Substances 0.000 abstract 1
- 239000011159 matrix material Substances 0.000 abstract 1
- 239000000126 substance Substances 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
- C10G35/095—Catalytic reforming characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
- B01J29/405—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/7049—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
- B01J29/7053—A-type
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/16—After treatment, characterised by the effect to be obtained to increase the Si/Al ratio; Dealumination
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
THE INVENTION CONCERNS THE USE OF A ZEOLITE CATALYST IN AROMATISING A LIGHT C5- C7 CUT, EITHER WITH OR WITHOUT OLEFINS BEING OLEFINS BEING PRESENT.THE AROMATISING PROCESS IS CARRIED OUT IN AT LEAST TWO FIXED BED REACTORS, AT LEAST ONE REACTOR BEING USED TO REGENERATE THE CATALYST. THE CATALYST IS IN THE FORM OF EXTRUSIONS AND IS GENERALLY OF THE FOLLOWING COMPOSTION, BY WEIGHT:(A) 0.01 TO 10% BY WEIGHT OF GALLIUM(B) 0.1 TO 99.49% OF A MATRIX (C) 0.5 TO 99.89% OF A ZEOLITE OF APPROXIMATELY THE FOLLOWING CHEMICAL FORMULA; M2/N O, A12 O3, X SIO2 WHERE M REPRESENTS A METALLIC PROTON AND/OR CATION,N IS THE VALENCY OF THE CATION, X IS A NUMBER FORM 12 TO 1000;THE ZEOLITE HAS AN MFI STRUCTURE AND IS FURTHER SYNTHESISED IN A FLUORIDE MEDIUM; IT HAS A FLUORINE CONTENT OF FROM 0.01 TO 1.5% BY WEIGHT, INCORPORATED IN THE SYNTHESISING PROCESS.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8917028A FR2655981B1 (en) | 1989-12-20 | 1989-12-20 | USE OF A CATALYST OF THE ALUMINOSILICATE TYPE CONTAINING GALLIUM IN THE FLAVORING OF LIGHT CUTS CONTAINING 5 TO 7 CARBON ATOMS PER MOLECULE. |
FR909001997A FR2658506B2 (en) | 1989-12-20 | 1990-02-16 | USE OF A CATALYST OF THE ALUMINOSILICATE TYPE CONTAINING GALLIUM IN THE FLAVORING OF LIGHT CUTS CONTAINING 5 TO 7 CARBON ATOMS PER MOLECULE. |
Publications (1)
Publication Number | Publication Date |
---|---|
MY104604A true MY104604A (en) | 1994-04-30 |
Family
ID=26227752
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MYPI90002195A MY104604A (en) | 1989-12-20 | 1990-12-18 | Use of an aluminosilicate-type catalyst containing gallium in aromatising light cuts containing five to seven carbon atoms per molecule. |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0434491B1 (en) |
KR (1) | KR0169726B1 (en) |
CN (1) | CN1028223C (en) |
AU (1) | AU6830590A (en) |
DE (1) | DE69000576T2 (en) |
FR (1) | FR2658506B2 (en) |
MY (1) | MY104604A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2692260B1 (en) * | 1992-06-16 | 2001-08-31 | Inst Francais Du Petrole | Process for the aromatization of hydrocarbons having 5 to 12 carbon atoms per molecule. |
US5576256A (en) * | 1994-05-23 | 1996-11-19 | Intevep, S.A. | Hydroprocessing scheme for production of premium isomerized light gasoline |
EP0923987A1 (en) * | 1997-12-22 | 1999-06-23 | Institut Français du Pétrole | Catalyst comprising a zeolithe EUO and its use in the isomerisation of aromatic C8 compounds |
CN101458217B (en) * | 2007-12-12 | 2011-02-09 | 中国石油天然气股份有限公司 | Method for calculating relative content of clay minerals in quasi clastic rock gap filler |
US8524966B1 (en) * | 2012-05-14 | 2013-09-03 | Uop Llc | Catalysts for improved cumene production and method of making and using same |
CN103664475B (en) * | 2012-09-05 | 2016-02-10 | 中国石油化工股份有限公司 | Low-carbon hydrocarbon aromatization method |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8306531D0 (en) * | 1983-03-09 | 1983-04-13 | British Petroleum Co Plc | Catalytic activity of aluminosilicate zeolites |
FR2567868A1 (en) * | 1984-07-20 | 1986-01-24 | Raffinage Cie Francaise | NOVEL PROCESS FOR THE SYNTHESIS OF ALUMINOSILICATE-LIKE ZEOLITES, PRODUCTS OBTAINED THEREBY, AND THE USE THEREOF |
GB8520978D0 (en) * | 1985-08-21 | 1985-09-25 | British Petroleum Co Plc | Production of aromatics |
FR2634140B1 (en) * | 1988-07-12 | 1990-09-14 | Inst Francais Du Petrole | GALLIUM-CONTAINING ALUMINOSILICATE TYPE CATALYST AND ITS USE IN FLAVORING C2-C4 LIGHT GASES |
-
1990
- 1990-02-16 FR FR909001997A patent/FR2658506B2/en not_active Expired - Lifetime
- 1990-12-06 EP EP90403475A patent/EP0434491B1/en not_active Expired - Lifetime
- 1990-12-06 DE DE9090403475T patent/DE69000576T2/en not_active Expired - Fee Related
- 1990-12-18 MY MYPI90002195A patent/MY104604A/en unknown
- 1990-12-18 KR KR1019900020856A patent/KR0169726B1/en not_active IP Right Cessation
- 1990-12-19 AU AU68305/90A patent/AU6830590A/en not_active Abandoned
- 1990-12-20 CN CN90106067A patent/CN1028223C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0434491B1 (en) | 1992-12-09 |
AU6830590A (en) | 1991-06-27 |
CN1052619A (en) | 1991-07-03 |
FR2658506B2 (en) | 1992-07-10 |
DE69000576T2 (en) | 1993-04-15 |
CN1028223C (en) | 1995-04-19 |
DE69000576D1 (en) | 1993-01-21 |
KR910011712A (en) | 1991-08-07 |
FR2658506A2 (en) | 1991-08-23 |
KR0169726B1 (en) | 1999-01-15 |
EP0434491A1 (en) | 1991-06-26 |
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