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1. WO2014148416 - METHOD FOR MANUFACTURING CATALYTIC CRACKING CATALYST FOR HYDROCARBON OIL

Publication Number WO/2014/148416
Publication Date 25.09.2014
International Application No. PCT/JP2014/057074
International Filing Date 17.03.2014
IPC
B01J 37/00 2006.01
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
37Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
B01J 29/08 2006.01
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
04having base-exchange properties, e.g. crystalline zeolites, pillared clays
06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
08of the faujasite type, e.g. type X or Y
B01J 29/16 2006.01
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
04having base-exchange properties, e.g. crystalline zeolites, pillared clays
06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
08of the faujasite type, e.g. type X or Y
16containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
C10G 11/05 2006.01
CCHEMISTRY; METALLURGY
10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
GCRACKING 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
11Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
02characterised by the catalyst used
04Oxides
05Crystalline alumino-silicates, e.g. molecular sieves
CPC
B01J 21/16
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
21Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
16Clays or other mineral silicates
B01J 2229/42
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
2229Aspects of molecular sieve catalysts not covered by B01J29/00
30After treatment, characterised by the means used
42Addition of matrix or binder particles
B01J 23/8472
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
23Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
70of the iron group metals or copper
76combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
84with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
847Vanadium, niobium or tantalum ; or polonium
8472Vanadium
B01J 29/005
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
005Mixtures of molecular sieves comprising at least one molecular sieve which is not an aluminosilicate zeolite, e.g. from groups B01J29/03 - B01J29/049 or B01J29/82 - B01J29/89
B01J 29/084
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
04having base-exchange properties, e.g. crystalline zeolites
06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
08of the faujasite type, e.g. type X or Y
084Y-type faujasite
B01J 29/83
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
82Phosphates
83Aluminophosphates (APO compounds)
Applicants
  • コスモ石油株式会社 COSMO OIL CO., LTD. [JP]/[JP]
Inventors
  • 坂 祐司 SAKA Yuji
Agents
  • 赤塚 賢次 AKATSUKA Kenji
Priority Data
2013-05933922.03.2013JP
Publication Language Japanese (JA)
Filing Language Japanese (JA)
Designated States
Title
(EN) METHOD FOR MANUFACTURING CATALYTIC CRACKING CATALYST FOR HYDROCARBON OIL
(FR) PROCÉDÉ DE PRODUCTION D'UN CATALYSEUR DE CRAQUAGE CATALYTIQUE POUR HUILE HYDROCARBONÉE
(JA) 炭化水素油の接触分解触媒の製造方法
Abstract
(EN)
Provided is a method for easily manufacturing a catalytic cracking catalyst for hydrocarbon oil having high cracking activity when used on heavy hydrocarbon oil and allowing production with a high yield ratio of a gasoline fraction with a high octane value. A method for manufacturing a catalytic cracking catalyst for hydrocarbon oil, characterized in that when the solid content is converted, an aqueous slurry is produced containing 20-50 mass% of a zeolite having a sodalite cage structure, 10-30 mass% of silica sol in terms of SiO2 conversion, 0.1-21 mass% of a first aluminum phosphate in terms of Al2O3⋅3P2O5 conversion, and 5-65 mass% of a clay mineral, after which the slurry is aged for 5-200 minutes and then spray-dry processed.
(FR)
Cette invention concerne un procédé permettant de produire facilement un catalyseur de craquage catalytique pour huile hydrocarbonée ayant une activité de craquage élevée quand il est utilisé sur une huile hydrocarbonée lourde et permettant la production à un taux de rendement élevé d'une fraction d'essence à indice d'octane élevé. Le procédé de production d'un catalyseur de craquage catalytique pour huile hydrocarbonée selon l'invention est caractérisé en ce que, quand la teneur solide est convertie, une suspension aqueuse épaisse est obtenue, ladite suspension épaisse contenant 20-50 % en poids d'une zéolithe ayant la structure en cage du sodalite, 10-30 % en poids d'un sol de silice en termes de conversion du SiO2, 0,1-21 % d'un premier phosphate d'aluminium en termes de conversion d'Al2O3⋅3P2O5, et 5-65 % en poids de minéraux argileux, après quoi la suspension épaisse est vieillie pendant 5-200 minutes, puis séchée par atomisation.
(JA)
重質炭化水素油に対する分解活性が高く、オクタン価が高いガソリン留分を高い得率で生産することができる炭化水素油の接触分解触媒を簡便に製造する方法を提供する。 炭化水素油の接触分解触媒を製造する方法であって、固形分換算したときに、ソーダライトケージ構造を有するゼオライトを20~50質量%、シリカゾルをSiO換算で10~30質量%、第一リン酸アルミニウムをAl・3P換算で0.1~21質量%および粘土鉱物を5~65質量%含有する水性スラリーを調製した後、5~200分間熟成し、次いで噴霧乾燥処理することを特徴とする炭化水素油の接触分解触媒の製造方法である。
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