DK1960101T3 - Fremgangsmåde til fremstilling af en hydrobehandlingskatalysator - Google Patents

Fremgangsmåde til fremstilling af en hydrobehandlingskatalysator Download PDF

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DK1960101T3
DK1960101T3 DK06839237.2T DK06839237T DK1960101T3 DK 1960101 T3 DK1960101 T3 DK 1960101T3 DK 06839237 T DK06839237 T DK 06839237T DK 1960101 T3 DK1960101 T3 DK 1960101T3
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catalyst
acid
group
solution
component
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DK06839237.2T
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Cecelia A Radlowski
Gill M Malick
Colleen T Miedona
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Advanced Refining Technologies Llc
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    • 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
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19—Molybdenum
    • 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
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • B01J23/882—Molybdenum and cobalt
    • 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
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • 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
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • B01J31/34—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of chromium, molybdenum or tungsten
    • 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
    • B01J37/02—Impregnation, coating or precipitation
    • 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
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0203—Impregnation the impregnation liquid containing organic compounds
    • 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
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0213—Preparation of the impregnating solution
    • 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
    • B01J37/08—Heat treatment
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/10—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing platinum group metals or compounds thereof
    • 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
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/60—Reduction reactions, e.g. hydrogenation
    • B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
    • B01J2231/641—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)

Claims (6)

1. Fremgangsmåde til fremstilling af en hydrobehandlingskatalysator omfattende: (I) tilvejebringe mindst følgende komponenter: (A) mindst én calcineret perforeret bærer med et vandporevolumen; (B) katalytiske aktive metaller der er nyttige i hydrobehandling af carbonhydrider, hvilke metaller i form af mindst én komponent tilvejebringer mindst ét metal fra gruppe VIB fra det periodiske system og mindst én komponent tilvejebringer mindst ét metal fra gruppe VIII fra det periodiske system; (C) mindst ét chelateringsmiddel, hvor chelateringsmidlet er en hyd roxyca rboxy I sy re; (D) vand i en mængde der er tilstrækkelig til at danne en opløsning eller dispersion omfattende de katalytiske aktive metaller og det mindst ene chelateringsmiddel; og (E) eventuelt, mindst én phosphor-indeholdende syrekomponent; (II) bringe komponenten (I)(A) i kontakt med opløsning eller dispersion omfattende (I)(B), (I)(C), (I)(D) og eventuelt (I)(E) i en tidsrum og ved en temperatur der er tilstrækkelig til at danne en blanding og til at imprægnere bæreren med en egnet mængde af komponenterne (I)(B) og (I)(C) og eventuelt (I)(E); (III) i det omfang at volumenet af opløsningen eller dispersion er lig med eller overstiger vandporevolumenet af bæreren der adskiller den imprægnerede bærer fra den overskydende opløsning eller dispersion; og (IV) opvarme den imprægnerede bærer til en temperatur på 400°F til 420°F (204,4°C til 215,5°C) i en periode på mindre end 1 time så at ingen væsentlig sønderdeling af det mindst ene chelateringsmiddel forårsages.
2. Fremgangsmåden ifølge krav 1, hvor det mindst ene metal fra gruppe VIB er valgt fra gruppen bestående af molybdæn og wolfram og hvor det mindst ene metal fra gruppe VIII er valgt fra gruppen bestående af kobolt og nikkel.
3. Fremgangsmåden ifølge krav 1, hvor det mindst ene hydroxycarboxylsyre er valgt fra gruppen bestående af glycolsyre, hydroxypropionsyre, hydroxysmørsyre, hydroxyhexanonsyre, vinsyre, æblesyre, glycerinsyre, citronsyre og gluconsyre.
4. Fremgangsmåden ifølge krav 1, for den perforerede bærer er mindst et medlem valgt fra gruppen bestående af silica, silica-gel, silica-aluminiumoxid, aluminiumoxid, titanium, titanium-aluminiumoxid, zirconium-aluminiumoxid, zirconium, bortrioxid, terran, kaolin, magnesiumsilicat, magnesiumcarbonat, magnesiumoxid, aktivt kul, bauxit, kiselgur, pimpsten, natur ler, syntetisk ler, kationisk ler eller anionisk ler såsom saponit, bentonit, kaolin, sepiolit eller hydrotalcit, og blandinger deraf.
5. Fremgangsmåden ifølge krav 1, hvor: (A) molforholdet af Gruppe VIII metal til Gruppe VIB metal er 0,05 til 0,75, og hvor Gruppe VIII-metalkomponenten tilvejebringes af en komponent med en vandig opløselighed på mindre end 0,05 mol/100 ml (ved 18°C); eller (B) hvor den mindst ene phosphor-indeholdende syrekomponent er en oxygeneret uorganisk phosphor-indeholdende syre og er til stede i en mængde der er tilstrækkelig til at tilvejebringe elementær phosphor til Gruppe VIB-metal-molforhold på 0,01 to 0,80,
6. Fremgangsmåden ifølge krav 1, hvor mængden af chelateringsmidlet der skal sættes til katalysatoren er 0,05 til 5 molær gange det totale antal mol af metallerne fra Gruppe VIB og Gruppe VIII og mængden af hydroxycarboxylsyre på den imprægnerede perforerede bærer før opvarmningen overstiger mængden i katalysatoren efter opvarmning med 1 til 10 vægtprocent.
DK06839237.2T 2005-12-14 2006-12-11 Fremgangsmåde til fremstilling af en hydrobehandlingskatalysator DK1960101T3 (da)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US71454505P 2005-12-14 2005-12-14
PCT/US2006/046947 WO2007070394A2 (en) 2005-12-14 2006-12-11 Method of making hydroprocessing catalyst

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DK06839237.2T DK1960101T3 (da) 2005-12-14 2006-12-11 Fremgangsmåde til fremstilling af en hydrobehandlingskatalysator
DK14182114.0T DK2823886T3 (da) 2005-12-14 2006-12-11 Fremgangsmåde til at fremstille en hydrobehandlings-katalysator

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US (3) US8877671B2 (da)
EP (2) EP2823886B1 (da)
JP (1) JP5909036B2 (da)
KR (1) KR100979984B1 (da)
CN (1) CN101330972B (da)
CA (1) CA2631703C (da)
DK (2) DK1960101T3 (da)
PL (2) PL2823886T3 (da)
RU (1) RU2415708C2 (da)
TW (1) TWI369249B (da)
WO (1) WO2007070394A2 (da)

Families Citing this family (80)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2823886B1 (en) * 2005-12-14 2019-08-14 Advanced Refining Technologies, LLC Method of making hydroprocessing catalyst
US7951746B2 (en) * 2006-10-11 2011-05-31 Exxonmobil Research And Engineering Company Bulk group VIII/group VIB metal catalysts and method of preparing same
US7807599B2 (en) * 2007-10-31 2010-10-05 Chevron U. S. A. Inc. Hydroconversion processes employing multi-metallic catalysts and method for making thereof
US8128811B2 (en) * 2008-04-11 2012-03-06 Exxonmobil Research And Engineering Company Hydroprocessing using rejuvenated supported hydroprocessing catalysts
JP2010214297A (ja) * 2009-03-17 2010-09-30 Inst Mexicano Del Petroleo 重質原油と残油の脱メタル用カーボン担体触媒
SG175405A1 (en) * 2009-04-29 2011-12-29 Chevron Usa Inc Hydroconversion multi-metallic catalyst and method for making thereof
US8383543B2 (en) 2009-04-29 2013-02-26 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
US7964525B2 (en) 2009-04-29 2011-06-21 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
US8080492B2 (en) 2009-04-29 2011-12-20 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
US8058203B2 (en) 2009-04-29 2011-11-15 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
US7931799B2 (en) 2009-04-29 2011-04-26 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
SG178430A1 (en) 2009-08-24 2012-04-27 Albemarle Europe Sprl Solutions and catalysts comprising group vi metal, group viii metal, phosphorous and an additive
JP5599212B2 (ja) * 2010-03-30 2014-10-01 千代田化工建設株式会社 炭化水素油の水素化処理触媒及びその製造方法、並びにそれを用いた炭化水素油の水素化処理方法
FR2963251B1 (fr) 2010-07-29 2012-07-27 IFP Energies Nouvelles Procede d'hydrotraitement d'une coupe hydrocarbonee de point d'ebullition superieur a 250°c en presence d'un catalyseur sulfure prepare au moyen d'un oligosaccharide cyclique
BR112013003002B1 (pt) * 2010-08-13 2019-04-02 Shell Internationale Research Maatschappij B.V. Composição contendo aditivo polar e agente quelante útil no hidroprocessamento de suprimentos hidrocarbonetos e método de sua produção e utilização
BR112013003125B1 (pt) * 2010-08-13 2019-11-05 Shell International Research Maatschappij B.V processo para restauração de atividade catalítica para um catalisador de hidroprocessamento gasto
US9376637B2 (en) 2010-08-13 2016-06-28 Shell Oil Company Method of making a hydroprocessing catalyst with a single step metal and chelant incorporation, the catalyst, and the use of the catalyst
BR112013002989B1 (pt) * 2010-08-13 2019-04-02 Shell Internationale Research Maatschappij B.V. Composição de catalisador de hidroprocessamento e método para produzir uma composição de catalisador de hidroprocessamento
KR101159303B1 (ko) 2010-10-19 2012-06-25 에스케이이노베이션 주식회사 킬레이트된 전이 금속을 이용한 선택산화탈황용 촉매의 제조 방법
KR101816318B1 (ko) * 2010-12-09 2018-01-12 에스케이이노베이션 주식회사 수소 처리 촉매 및 이의 제조방법
JP5773644B2 (ja) * 2010-12-28 2015-09-02 日揮触媒化成株式会社 水素化処理触媒の再生方法
FR2972648B1 (fr) 2011-03-18 2013-04-26 Ifp Energies Now Catalyseur utilisable en hydrotraitement comprenant des metaux des groupes viii et vib et preparation avec de l'acide citrique et du succinate de dialkyle c1-c4
CA2839881C (en) 2011-06-22 2020-08-18 Shell Internationale Research Maatschappij B.V. A hydroprocessing catalyst and methods of making and using such a catalyst
WO2013003328A1 (en) * 2011-06-28 2013-01-03 Shell Oil Company An ether amine additive impregnated composition useful in the catalytic hydroprocessing of hydrocarbons, a method of making such composition
CN102935370B (zh) * 2011-08-16 2015-09-16 中国石油化工股份有限公司 一种c5石油树脂加氢催化剂、其制备方法及其应用
FR2984764B1 (fr) * 2011-12-22 2014-01-17 IFP Energies Nouvelles Procede de preparation d'un catalyseur utilisable en hydrotraitement et hydroconversion
WO2014039735A2 (en) 2012-09-05 2014-03-13 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
TWI604040B (zh) * 2012-11-08 2017-11-01 China Petrochemical Technology Co Ltd Hydrotreating catalyst, its manufacturing method and application thereof
US20140206915A1 (en) 2013-01-18 2014-07-24 Chevron U.S.A. Inc. Paraffinic jet and diesel fuels and base oils from vegetable oils via a combination of hydrotreating, paraffin disproportionation and hydroisomerization
RU2527573C1 (ru) * 2013-06-05 2014-09-10 Федеральное государственное бюджетное учреждение науки Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук Катализатор для переработки тяжелого нефтяного сырья и способ его приготовления
CN103386321B (zh) * 2013-07-31 2015-04-22 陕西煤业化工技术研究院有限责任公司 一种煤焦油加氢脱氮催化剂及其制备方法
CA2926759C (en) * 2013-11-07 2021-11-30 Shell Internationale Research Maatschappij B.V. Process for preparing a hydrotreating catalyst
CN104646007B (zh) * 2013-11-22 2017-03-15 中国石油天然气股份有限公司 一种渣油加氢脱金属催化剂及其制备和应用
JP6378902B2 (ja) * 2014-03-10 2018-08-22 日本ケッチェン株式会社 水素化処理触媒、当該触媒の製造方法、並びに当該触媒を用いる炭化水素油の水素化処理方法
US9657248B1 (en) * 2014-03-14 2017-05-23 Biosystems Consulting, Inc. Systems, devices, compositions, and/or methods for de-sulphurizing acid gases
US10376873B2 (en) * 2014-04-24 2019-08-13 Advanced Refining Technologies Llc Method of preparing high activity hydrotreating catalysts
CN105013497B (zh) * 2014-04-24 2017-12-22 中国石油化工股份有限公司 一种加氢催化剂及其应用
US10370600B2 (en) * 2014-04-24 2019-08-06 Advanced Refining Technologies Llc High activity hydrotreating catalysts and processes using the same
CN106457223A (zh) * 2014-04-24 2017-02-22 先进炼制技术有限公司 高活性加氢处理催化剂
US10369558B2 (en) * 2014-04-24 2019-08-06 Advanced Refining Technologies Llc High activity hydrotreating catalysts
JP6909879B2 (ja) * 2014-06-20 2021-07-28 日揮グローバル株式会社 炭化水素油の水素化脱硫触媒、その製造方法、および水素化脱硫方法
JP6646349B2 (ja) * 2014-06-20 2020-02-14 日揮グローバル株式会社 炭化水素油の水素化脱硫触媒の製造方法及び炭化水素油の水素化脱硫方法
FR3023184B1 (fr) * 2014-07-04 2019-12-27 IFP Energies Nouvelles Catalyseur d'hydrotraitement a densite de molybdene elevee et methode de preparation.
CN105498849B (zh) * 2014-09-25 2017-12-22 中国石油化工股份有限公司 一种加氢催化剂及其应用
CN105498816B (zh) * 2014-09-25 2017-12-22 中国石油化工股份有限公司 一种加氢催化剂及其应用
US10178756B1 (en) * 2014-10-29 2019-01-08 National Technology & Engineering Solutions Of Sandia, Llc Multifunctional composite coatings for metal whisker mitigation
MY193473A (en) * 2014-12-19 2022-10-14 Shell Int Research Method for preparing a catalyst
CN107645971B (zh) * 2015-04-24 2020-12-18 阿尔比马尔欧洲有限公司 掺杂载体上含金属有机硫化物的加氢处理催化剂
JP6842428B2 (ja) 2015-05-29 2021-03-17 アドバンスド・リフアイニング・テクノロジーズ・エルエルシー 高ｈｄｎ選択性水素化処理触媒
CN105195231B (zh) * 2015-09-21 2018-02-16 中国海洋石油总公司 一种后处理型加氢裂化催化剂的制备方法
AU2016376824B2 (en) * 2015-12-21 2020-04-30 Shell Internationale Research Maatschappij B.V. Hydrogenation catalyst and method for preparing the same
CA3018210C (en) * 2016-03-23 2023-10-10 Shell Internationale Research Maatschappij B.V. High metals content hydrolysis catalyst for catalytic reduction of sulfur in a gas stream
GB201607609D0 (en) * 2016-04-29 2016-06-15 Scg Chemicals Co Ltd And Scg Packaging Public Company Ltd Catalyst and use thereof
US20180057756A1 (en) * 2016-08-23 2018-03-01 Shell Oil Company A polar additive-containing hydroprocessing catalyst and method of making and using thereof
BR102016022467B1 (pt) * 2016-09-28 2022-02-01 Petróleo Brasileiro S.A. - Petrobras Processo para preparação de um catalisador à base de níquel, catalisador à base de níquel, e, seu uso em um processo de reforma a vapor
US10537883B2 (en) 2016-10-07 2020-01-21 King Fahd University Of Petroleum And Minerals Method for producing a hydrodesulfurization catalyst
CN108067243B (zh) * 2016-11-17 2020-03-17 中国石油化工股份有限公司 一种加氢处理催化剂及其制备方法和应用
RU2676260C2 (ru) * 2016-12-28 2018-12-27 федеральное государственное бюджетное образовательное учреждение высшего образования "Самарский государственный технический университет" Катализатор селективной гидроочистки высокосернистого олефинсодержащего углеводородного сырья и способ его приготовления
CN109569699B (zh) * 2017-09-29 2021-11-16 中国石油化工股份有限公司 硫化型加氢催化剂及其制备方法和应用
WO2019090170A1 (en) 2017-11-02 2019-05-09 Chevron U.S.A. Inc. Imms method for petroleum feedstock evaluation
CN109833890B (zh) * 2017-11-24 2021-08-06 中国石油化工股份有限公司 一种渣油加氢催化剂及其制备
CN108385392A (zh) * 2018-04-04 2018-08-10 东莞市联洲知识产权运营管理有限公司 一种基于稀土元素改性的耐热纺织品的制备方法
US11713289B2 (en) * 2018-04-16 2023-08-01 Viridis Chemical, Llc Composition of catalysts for conversion of ethanol to N-Butanol and higher alcohols
CN111097539A (zh) * 2018-10-25 2020-05-05 中国石油化工股份有限公司 一种加氢催化剂的制备方法及加氢催化剂
CN111375421B (zh) * 2018-12-29 2022-10-11 中国石油化工股份有限公司 一种糖类氢解制低碳二元醇催化剂及其制备方法
CN111889107B (zh) * 2019-05-06 2022-07-08 中国石油化工股份有限公司 一种加氢保护催化剂及其制备方法
CN110327975B (zh) * 2019-06-06 2020-05-19 浙江新和成股份有限公司 氢甲酰化催化剂及其制备方法和应用
CN110479333A (zh) * 2019-08-27 2019-11-22 韩宝亭 一种环保型重质油加氢精制催化剂的制备方法
WO2021074343A1 (en) * 2019-10-18 2021-04-22 Shell Internationale Research Maatschappij B.V. Hydroprocessing catalyst having an organic additive with overlaid metals using a chelant and method of making and using such catalyst
EP4045616A1 (en) 2019-10-18 2022-08-24 Shell Internationale Research Maatschappij B.V. Hydroprocessing catalyst having an organic additive with metals incorporated using chelant and method of making and using such catalyst
KR20220082827A (ko) 2019-10-18 2022-06-17 쉘 인터내셔날 리써취 마트샤피지 비.브이. 금속이 오버레이된 유기 첨가제를 갖는 수소화처리 촉매, 및 이러한 촉매의 제조 및 사용 방법
CN112742402B (zh) * 2019-10-30 2022-08-12 中国石油化工股份有限公司 一种加氢脱硫催化剂及其制备方法
CN111389433B (zh) * 2020-01-13 2024-01-23 中纯氢能源科技(泰州)有限公司 一种具有高电催化制氢活性的超薄碳化钼纳米片制备方法
JP7295955B2 (ja) * 2020-02-11 2023-06-21 ヒンドゥスタン ペトロリアム コーポレーション リミテッド 分散型水素化脱硫触媒用組成物およびその製造方法
CN114100615B (zh) * 2020-08-31 2023-08-11 中国石油化工股份有限公司 碳四馏分选择加氢催化剂及其制备方法
CN114643070B (zh) * 2020-12-21 2023-07-28 中国石油化工股份有限公司 加氢脱氮催化剂及其制备方法和应用
CN114643079B (zh) * 2020-12-21 2023-07-28 中国石油化工股份有限公司 加氢脱残炭催化剂及其制备方法和应用
CN113908865A (zh) * 2021-10-25 2022-01-11 中国海洋石油集团有限公司 一种选择性加氢脱芳催化剂及其制备方法与应用
WO2023170700A1 (en) 2022-03-11 2023-09-14 Hindustan Petroleum Corporation Limited Naphtha hydrotreating catalyst and process of preparation thereof
CN116116404B (zh) * 2023-04-19 2023-08-01 浙江工业大学 一种水热法制备加氢催化剂的方法及该催化剂的应用

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3232887A (en) 1962-05-07 1966-02-01 Nalco Chemical Co Stabilized aqueous solutions for use in impregnating catalyst carriers and method of making same
US4382854A (en) * 1978-02-03 1983-05-10 Kaiser Aluminum & Chemical Corporation Ni/Co Mo P on titania-alumina hydrodesulfurizing catalyst and process of hydrodesulfurizing using the same
US4879265A (en) * 1982-08-19 1989-11-07 Union Oil Company Of California Hydroprocessing catalyst and phosphorous and citric acid containing impregnating solution
US4818743A (en) 1983-04-07 1989-04-04 Union Oil Company Of California Desulfurization catalyst and the catalyst prepared by a method
US4500424A (en) 1983-04-07 1985-02-19 Union Oil Company Of California Desulfurization catalyst and process
CA1261815A (en) 1984-11-05 1989-09-26 Mark S. Thompson Preparation of high activity silica-supported hydrotreating catalysts and catalysts thus prepared
JP3244693B2 (ja) * 1990-10-17 2002-01-07 住友金属鉱山株式会社 炭化水素油の水素化処理用触媒の製造方法
JP3244692B2 (ja) * 1990-10-17 2002-01-07 住友金属鉱山株式会社 炭化水素油の水素化処理用触媒の製造方法
US5397956A (en) 1992-01-13 1995-03-14 Tokyo Electron Limited Electron beam excited plasma system
CA2093412C (en) 1992-04-20 2002-12-31 Gerald Verdell Nelson Novel hydroconversion process employing catalyst with specified pore size distribution
JP2900771B2 (ja) * 1992-11-18 1999-06-02 住友金属鉱山株式会社 炭化水素油の水素化処理触媒の製造方法
US5397456A (en) 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
JPH06339635A (ja) 1993-06-01 1994-12-13 Japan Energy Corp 水素化処理触媒の製造方法
JP3802106B2 (ja) 1995-06-08 2006-07-26 日本ケッチェン株式会社 炭化水素油の水素化処理触媒とその製造方法およびその活性化方法
EP0770426B1 (en) * 1995-10-27 2003-05-14 Akzo Nobel N.V. Process for preparing a hydroprocessing catalyst from waste hydroprocessing catalyst
JPH09155197A (ja) 1995-12-14 1997-06-17 Sumitomo Metal Mining Co Ltd 炭化水素油の水素化処理触媒
US6218333B1 (en) * 1999-02-15 2001-04-17 Shell Oil Company Preparation of a hydrotreating catalyst
CA2302969A1 (en) 1999-04-02 2000-10-02 Akzo Nobel Nv Process for effecting ultra-deep hds of hydrocarbon feedstocks
JP4047044B2 (ja) * 2002-03-28 2008-02-13 コスモ石油株式会社 重質油の水素化脱硫触媒、その製造方法及び重質油の水素化脱硫方法
CA2509847C (en) * 2002-12-18 2009-09-01 Cosmo Oil Co., Ltd. Catalyst for hydrotreating gas oil, process for producing the same, and process for hydrotreating gas oil
JP2004290728A (ja) 2003-03-25 2004-10-21 Cosmo Oil Co Ltd 軽油の水素化処理触媒の製造方法及び軽油の水素化処理方法
CN100510019C (zh) 2003-10-03 2009-07-08 阿尔伯麦尔荷兰有限公司 活化加氢处理催化剂的方法
US20050109674A1 (en) 2003-11-20 2005-05-26 Advanced Refining Technologies Llc Hydroconversion catalysts and methods of making and using same
JP4444690B2 (ja) 2004-02-26 2010-03-31 株式会社ジャパンエナジー 水素化処理触媒前駆体およびその製造方法並びに精製炭化水素油の製造方法
RU2366505C2 (ru) 2004-03-03 2009-09-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Носитель катализатора и каталитическая композиция, способы их получения и применения
JP4472556B2 (ja) * 2004-03-26 2010-06-02 コスモ石油株式会社 炭化水素油の水素化処理触媒及びその製造方法並びに炭化水素油の水素化処理方法
EP2823886B1 (en) * 2005-12-14 2019-08-14 Advanced Refining Technologies, LLC Method of making hydroprocessing catalyst

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