BR0212221A - catalisador de craqueamento catalìtico de fluido zeolìtico; método de fabricação de um catalisador de craqueamento catalìtico de fluido com elevado teor de zeólita; método de craqueamento de um gasóleo - Google Patents

catalisador de craqueamento catalìtico de fluido zeolìtico; método de fabricação de um catalisador de craqueamento catalìtico de fluido com elevado teor de zeólita; método de craqueamento de um gasóleo

Info

Publication number
BR0212221A
BR0212221A BRPI0212221-9A BR0212221A BR0212221A BR 0212221 A BR0212221 A BR 0212221A BR 0212221 A BR0212221 A BR 0212221A BR 0212221 A BR0212221 A BR 0212221A
Authority
BR
Brazil
Prior art keywords
catalytic cracking
fluid
cracking catalyst
manufacturing
metakaolin
Prior art date
Application number
BRPI0212221-9A
Other languages
English (en)
Inventor
Clark W Gibson
Mitchell J Willis
George E Gantt
Robert E Barnes
David M Stockwell
Original Assignee
Engelhard Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Engelhard Corp filed Critical Engelhard Corp
Publication of BR0212221A publication Critical patent/BR0212221A/pt

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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0027—Powdering
    • B01J37/0045—Drying a slurry, e.g. spray drying
    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • 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
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/16—Clays or other mineral silicates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

"CATALISADOR DE CRAQUEAMENTO CATALìTICO DE FLUIDO ZEOLìTICO; MéTODO DE FABRICAçãO DE UM CATALISADOR DE CRAQUEAMENTO CATALìTICO DE FLUIDO COM ELEVADO TEOR DE ZEóLITA; E MéTODO DE CRAQUEAMENTO DE UM GASóLEO". Trata-se de um processo in situ para fabricar catalisadores de craqueamento fluido zeolíticos através de secagem por aspersão de (i) caulim hídrico e/ou metacaulim, e (ii) fonte de alumínio calcinado, sendo que a dita fonte de alumínio calcinado é derivada a partir de um caulim ultrafino pulverizado, calcinando-se as microesferas resultantes para converter o caulim hídrico em metacaulim, e reagindo as microesferas compostas de uma mistura de metacaulim e fonte de alumínio calcinado com uma solução alcalina de silicato de sódio. A porcentagem em peso de metacaulim nas microesferas calcinadas é maior que o teor da fonte de alumínio calcinado.
BRPI0212221-9A 2001-08-31 2002-08-07 catalisador de craqueamento catalìtico de fluido zeolìtico; método de fabricação de um catalisador de craqueamento catalìtico de fluido com elevado teor de zeólita; método de craqueamento de um gasóleo BR0212221A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/942,971 US6696378B2 (en) 2001-08-31 2001-08-31 Fluid catalytic cracking catalyst manufacturing process
PCT/US2002/025023 WO2003020423A1 (en) 2001-08-31 2002-08-07 Fcc catalyst manufacturing process

Publications (1)

Publication Number Publication Date
BR0212221A true BR0212221A (pt) 2006-05-23

Family

ID=25478899

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0212221-9A BR0212221A (pt) 2001-08-31 2002-08-07 catalisador de craqueamento catalìtico de fluido zeolìtico; método de fabricação de um catalisador de craqueamento catalìtico de fluido com elevado teor de zeólita; método de craqueamento de um gasóleo

Country Status (11)

Country Link
US (1) US6696378B2 (pt)
EP (1) EP1420883A1 (pt)
JP (1) JP2005526587A (pt)
KR (1) KR20040031018A (pt)
CN (2) CN1330415C (pt)
AU (1) AU2002329711B2 (pt)
BR (1) BR0212221A (pt)
CA (1) CA2458367A1 (pt)
MX (1) MXPA04001888A (pt)
TW (1) TWI226263B (pt)
WO (1) WO2003020423A1 (pt)

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BR0114097A (pt) * 2000-09-22 2004-03-02 Engelhard Corp Catalisador fcc de zeólita macroporoso; catalisador fluido para craqueamento catalìtico; e método para fabricar um catalisador fluido para craqueamento catalìtico
US20030089640A1 (en) * 2001-10-17 2003-05-15 Rostam Madon FCC catalysts for feeds containing nickel and vanadium
US6656347B2 (en) * 2000-09-22 2003-12-02 Engelhard Corporation Structurally enhanced cracking catalysts
US7101473B2 (en) * 2002-05-31 2006-09-05 Engelhard Corporation Method of enhancing the activity of FCC catalysts
CN1275855C (zh) * 2003-03-28 2006-09-20 中国石油化工股份有限公司 用高岭土合成的纳米级y型沸石及其制备方法
US6942783B2 (en) * 2003-05-19 2005-09-13 Engelhard Corporation Enhanced FCC catalysts for gas oil and resid applications
US20060060504A1 (en) 2004-09-08 2006-03-23 Vierheilig Albert A Additives for metal contaminant removal
CN100377782C (zh) * 2004-09-15 2008-04-02 中国石油化工股份有限公司 一种烃类裂化催化剂的制备方法
CN1332754C (zh) * 2004-09-15 2007-08-22 中国石油化工股份有限公司 一种使用硅粘结剂的裂化催化剂的制备方法
CN101213269B (zh) * 2005-06-29 2012-01-25 格雷斯公司 在流化催化装置中用于轻质烯烃的五元环高硅沸石催化剂
US9108181B2 (en) * 2007-06-20 2015-08-18 Basf Corporation Structurally enhanced cracking catalysts
US8278235B2 (en) * 2007-06-20 2012-10-02 Basf Corporation Structurally enhanced cracking catalysts
CN101952224B (zh) * 2007-11-30 2013-08-21 康宁股份有限公司 沸石基蜂窝体
US8372269B2 (en) * 2009-10-02 2013-02-12 Basf Corporation Heavy metals trapping co-catalyst for FCC processes
US9029291B2 (en) 2011-01-12 2015-05-12 Basf Corporation Rare earth-containing attrition resistant vanadium trap for catalytic cracking catalyst
CN103253684B (zh) * 2012-02-16 2015-04-29 中国石油天然气股份有限公司 一种直接法原位晶化合成小晶粒zsm-5分子筛的方法
US10286391B2 (en) 2012-02-17 2019-05-14 Inaeris Technologies, Llc Catalyst system having meso and macro hierarchical pore structure
US9428695B2 (en) 2013-02-12 2016-08-30 Saudi Basic Industries Corporation Conversion of plastics to olefin and aromatic products with product recycle
US9447332B2 (en) 2013-02-12 2016-09-20 Saudi Basic Industries Corporation Conversion of plastics to olefin and aromatic products using temperature control
US10195593B2 (en) 2014-03-28 2019-02-05 Agency For Science, Technology And Research Method for preparing a sodium faujasite catalyst and its use in producing acrylic acid
KR20180075687A (ko) * 2015-11-24 2018-07-04 바스프 코포레이션 부틸렌 수율을 증가시키기 위한 유동 접촉 분해 촉매
KR102157788B1 (ko) * 2017-07-03 2020-09-18 주식회사 엘지화학 알루미노실리케이트 입자 제조방법 및 이를 포함하는 타이어용 고무 조성물 제조방법
CN108948774A (zh) * 2018-08-31 2018-12-07 邳州市金丰木质纤维粉有限公司 一种木质纤维粉的制备方法
CN112516984A (zh) * 2020-12-23 2021-03-19 山西晋坤矿产品股份有限公司 一种利用煤矸石制备高活性石油催化裂化催化剂的方法

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Also Published As

Publication number Publication date
CN1911501A (zh) 2007-02-14
CN1330415C (zh) 2007-08-08
TWI226263B (en) 2005-01-11
WO2003020423A1 (en) 2003-03-13
KR20040031018A (ko) 2004-04-09
CA2458367A1 (en) 2003-03-13
CN1549746A (zh) 2004-11-24
AU2002329711B8 (en) 2003-03-18
JP2005526587A (ja) 2005-09-08
US20030050181A1 (en) 2003-03-13
US6696378B2 (en) 2004-02-24
AU2002329711B2 (en) 2007-10-04
EP1420883A1 (en) 2004-05-26
MXPA04001888A (es) 2004-06-15

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Legal Events

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B08F Application fees: application dismissed [chapter 8.6 patent gazette]

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B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2108 DE 31/05/2011.