JP5057785B2 - 使用済み水素化処理触媒の触媒活性を回復する方法、得られる回復した触媒、および水素化処理方法 - Google Patents
使用済み水素化処理触媒の触媒活性を回復する方法、得られる回復した触媒、および水素化処理方法 Download PDFInfo
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- 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
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/90—Regeneration or reactivation
- B01J23/94—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
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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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/50—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/64—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using alkaline material; using salts
- B01J38/66—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using alkaline material; using salts using ammonia or derivatives thereof
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- 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
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- 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
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
- C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
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- 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
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
- C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
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- 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
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
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- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
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- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
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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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/12—Treating with free oxygen-containing gas
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- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/44—Solvents
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- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/70—Catalyst aspects
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- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
国際公開第WO96/41848号(Sumitomo)は、使用され再生された水素化処理触媒が、少なくとも2つの水酸基および2〜10個の炭素原子を含む添加剤と接触し、添加剤の少なくとも50%が触媒において残存するような条件下で乾燥される方法を開示している。活性化触媒は、水素化処理前に、予め硫化物に変えられる。
欧州特許出願EP第1043069号(Akzo)は、水素化処理触媒が硫化工程に掛けられ、水素化処理触媒が、少なくとも50%のアルミナを含む担体を含み、触媒が、少なくとも1つの水素化金属成分ならびに少なくとも1つの共有結合した窒素原子および少なくとも1つのカルボニル部分を含む有機化合物を含み、有機化合物と全水素化金属含有量との間のモル比が、少なくとも0.01:1である、硫化水素化処理触媒の調製方法を開示している。
国際公開第WO95/31280号は、ある種の高活性触媒および、触媒とキレート剤とを湿潤させ、その様に湿潤させた基体を熟成し、乾燥し、その後、その様に乾燥した基体をか焼することによる、触媒の活性を改善する方法を開示している。
RVA=(評価対象触媒の速度定数)/未使用の参照触媒の速度定数)
(ここで、水素脱硫(HDS)RVAの場合に対しては、速度定数は、1.3のHDS反応次数を仮定して計算され、水素脱窒(HDN)RVAの場合に対しては、速度定数は、1.0のHDN反応次数を仮定して計算される)。
上述の再生触媒のアリコートを、中間キレート処理またはか焼なしで、硫化処理に掛けた。
サンプルBを調製するために、上述の再生触媒のアリコートを、キレート処理に掛けた。再生触媒サンプルを処理するために使用したキレート溶液は、1重量部のDTPA、0.11重量部の水酸化アンモニウム、および10重量部の水を含んでいた。再生サンプルを、標準インシピエントウェットネス手順により、キレート溶液で含浸し、再生触媒の有効細孔容積の約98容量%をキレート溶液で充填した。含浸された再生触媒を、次いで、密閉容器において室温で2週間の熟成期間の間熟成し、熟成触媒を得た。
サンプルCを調製するために、上述の再生触媒のアリコートを、キレート処理に掛けた。再生触媒サンプルを処理するために使用したキレート溶液は、1重量部のDTPA、0.11重量部の水酸化アンモニウム、および10重量部の水を含んでいた。再生サンプルを、標準インシピエントウェットネス手順により、キレート溶液で含浸し、再生触媒の有効細孔容積の約98容量%をキレート溶液で充填した。含浸された再生触媒を、次いで、密閉容器において室温で2週間の熟成期間の間熟成し、熟成触媒を得た。
Claims (6)
- 使用済み非添加剤ベース水素化処理触媒に対して触媒活性を回復させる方法であって、 使用により使用済み触媒となる、使用前の未使用状態における触媒に関して減少した触媒活性を有する、金属成分および支持体材料を含む使用済み非添加剤ベース水素化処理触媒を、溶液と接触させる工程であり、前記溶液が、アミノカルボン酸からなる化合物の群から選択されるキレート剤および溶媒を含み、前記接触が、回復した触媒活性を与えるために、10時間を超える間行われ、その結果前記キレート剤および前記溶媒を導入した熟成触媒をもたらし、前記使用済み水素化処理触媒が、活性金属の1モル当たり0.005モルのキレート剤から活性金属の1モル当たり1モルのキレート剤の範囲において前記キレート剤の量を含む工程、
前記熟成触媒を、前記熟成触媒から前記キレート剤の50重量%未満を除去しながら、前記熟成触媒から前記溶媒の一部分を除去する乾燥温度を含む条件に暴露して、乾燥熟成触媒を得る工程、および
前記乾燥熟成触媒を硫黄処理して、回復した触媒を生成する工程
を含む方法。 - 前記使用済み触媒と前記溶液との接触が、前記溶液の凍結温度から前記溶液の沸騰温度の範囲における熟成温度で行われる、請求項1に記載の方法。
- 前記熟成触媒が前記乾燥熟成触媒の硫黄処理前に暴露される条件が、400℃のか焼温度未満である最大暴露温度を含む、請求項2に記載の方法。
- 前記最大暴露温度が、250℃未満の前記乾燥温度である、請求項3に記載の方法。
- 前記乾燥熟成触媒が、前記キレート剤の濃度を有し、前記熟成触媒から除去される前記キレート剤の部分が、前記使用済み触媒に導入されるキレート剤の25重量%未満である、請求項4に記載の方法。
- 前記熟成触媒から除去される前記キレート剤の前記部分が、前記使用済み触媒に導入されるキレート剤の25重量%未満である、請求項5に記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US53749904P | 2004-01-20 | 2004-01-20 | |
US60/537,499 | 2004-01-20 | ||
PCT/US2005/001825 WO2005070542A1 (en) | 2004-01-20 | 2005-01-19 | A method of restoring catalytic activity of a spent hydrotreating catalyst, the resulting restored catalyst, and a method of hydroprocessing |
Publications (2)
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JP2007518560A JP2007518560A (ja) | 2007-07-12 |
JP5057785B2 true JP5057785B2 (ja) | 2012-10-24 |
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JP2006551268A Active JP5057785B2 (ja) | 2004-01-20 | 2005-01-19 | 使用済み水素化処理触媒の触媒活性を回復する方法、得られる回復した触媒、および水素化処理方法 |
Country Status (12)
Country | Link |
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US (2) | US7820579B2 (ja) |
EP (1) | EP1737571B1 (ja) |
JP (1) | JP5057785B2 (ja) |
KR (1) | KR20060129390A (ja) |
CN (1) | CN1921943A (ja) |
BR (1) | BRPI0506968A (ja) |
CA (1) | CA2553855C (ja) |
DK (1) | DK1737571T3 (ja) |
ES (1) | ES2591240T3 (ja) |
RU (1) | RU2372991C2 (ja) |
WO (1) | WO2005070542A1 (ja) |
ZA (1) | ZA200605572B (ja) |
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US8759242B2 (en) | 2009-07-21 | 2014-06-24 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
US8927448B2 (en) | 2009-07-21 | 2015-01-06 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
US9068132B2 (en) | 2009-07-21 | 2015-06-30 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
CN102310006A (zh) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | 一种加氢催化剂再生及预硫化方法 |
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 |
WO2012035004A2 (en) * | 2010-09-17 | 2012-03-22 | Shell Internationale Research Maatschappij B.V. | Hydrocracking catalyst composition |
US20120172205A1 (en) | 2010-12-30 | 2012-07-05 | Chevron Corporation | Hydroprocessing catalysts and methods for making thereof |
CN102151588B (zh) * | 2011-01-25 | 2012-08-08 | 江苏科创石化有限公司 | 一种加氢催化剂的再生方法 |
JP5825572B2 (ja) * | 2011-07-29 | 2015-12-02 | 日揮触媒化成株式会社 | 水素化処理触媒の再生方法 |
US9321037B2 (en) | 2012-12-14 | 2016-04-26 | Chevron U.S.A., Inc. | Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units |
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JP5892989B2 (ja) * | 2013-10-07 | 2016-03-23 | 日揮触媒化成株式会社 | 水素化脱硫触媒の再生方法 |
CN107552070B (zh) * | 2016-06-30 | 2021-01-01 | 中国石油天然气股份有限公司 | 提高Mo-Ni柴油馏分待生加氢精制催化剂原位活性恢复的方法 |
RU2640655C1 (ru) * | 2016-12-19 | 2018-01-11 | Общество с ограниченной ответственностью "Ишимбайский специализированный химический завод катализаторов" | Способ восстановления активности катализатора гидроочистки углеводородного сырья |
RU2673480C1 (ru) * | 2018-08-07 | 2018-11-27 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Способ получения гидроочищенного дизельного топлива |
RU2674157C1 (ru) * | 2018-08-07 | 2018-12-05 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Способ регенерации дезактивированного катализатора гидроочистки |
RU2674156C1 (ru) * | 2018-08-07 | 2018-12-05 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Регенерированный катализатор гидроочистки |
FR3089825B1 (fr) | 2018-12-18 | 2021-05-07 | Ifp Energies Now | Procédé de réjuvénation d’un catalyseur usé non régénéré d’un procédé d'hydrodésulfuration d'essences. |
FR3090005B1 (fr) | 2018-12-18 | 2021-07-30 | Ifp Energies Now | Procédé d’hydrodésulfuration de coupes essence oléfinique contenant du soufre mettant en œuvre un catalyseur régénéré. |
FR3089826B1 (fr) | 2018-12-18 | 2021-05-07 | Ifp Energies Now | Procédé de réjuvénation d’un catalyseur d’un procédé d'hydrotraitement et/ou d’hydrocraquage. |
FR3090006B1 (fr) * | 2018-12-18 | 2021-07-30 | Ifp Energies Now | Procédé d’hydrodésulfuration de coupes essence oléfinique contenant du soufre mettant en œuvre un catalyseur réjuvéné à un composé organique. |
FR3089824B1 (fr) | 2018-12-18 | 2021-05-07 | Ifp Energies Now | Procédé de réjuvénation d’un catalyseur usé et régénéré d’un procédé d'hydrodésulfuration d'essences. |
CA3138356A1 (en) | 2019-05-23 | 2020-11-26 | Terence Mchugh | Reactivated hydroprocessing catalysts for use in sulfur abatement |
RU2724613C1 (ru) * | 2020-01-17 | 2020-06-25 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Способ гидроочистки дизельного топлива |
RU2731459C1 (ru) * | 2020-01-17 | 2020-09-03 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть - ОНПЗ") | Реактивированный катализатор гидроочистки |
FR3117380B1 (fr) | 2020-12-15 | 2023-03-03 | Ifp Energies Now | Procédé de réjuvénation d’un catalyseur d’un procédé d'hydrotraitement et/ou d’hydrocraquage |
FR3138052A1 (fr) | 2022-07-22 | 2024-01-26 | IFP Energies Nouvelles | Procédé de régénération comprenant au moins deux étapes d’un catalyseur d’hydrocraquage à base de zéolithe et son utilisation dans un procédé d’hydrocraquage. |
FR3138053A1 (fr) | 2022-07-22 | 2024-01-26 | IFP Energies Nouvelles | Procédé de régénération comprenant une étape de régénération, une étape de réjuvénation et une étape de calcination d’un catalyseur d’hydrocraquage à base de zéolithe et son utilisation dans un procédé d’hydrocraquage. |
FR3138051A1 (fr) | 2022-07-22 | 2024-01-26 | IFP Energies Nouvelles | Procédé de régénération d’un catalyseur d’hydrocraquage à base de zéolithe et son utilisation dans un procédé d’hydrocraquage. |
FR3138055A1 (fr) | 2022-07-22 | 2024-01-26 | IFP Energies Nouvelles | Procédé de réjuvénation d’un catalyseur d’un procédé d'hydrotraitement et/ou d’hydrocraquage. |
FR3138054A1 (fr) | 2022-07-22 | 2024-01-26 | IFP Energies Nouvelles | Procédé de réjuvénation d’un catalyseur d’un procédé d'hydrotraitement et/ou d’hydrocraquage |
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- 2005-01-19 US US11/038,291 patent/US7820579B2/en active Active
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- 2005-01-19 RU RU2006129927/04A patent/RU2372991C2/ru active
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KR20060129390A (ko) | 2006-12-15 |
ZA200605572B (en) | 2007-11-28 |
CN1921943A (zh) | 2007-02-28 |
US20050159295A1 (en) | 2005-07-21 |
US20100326889A1 (en) | 2010-12-30 |
US8168557B2 (en) | 2012-05-01 |
RU2372991C2 (ru) | 2009-11-20 |
US7820579B2 (en) | 2010-10-26 |
EP1737571B1 (en) | 2016-06-22 |
WO2005070542A1 (en) | 2005-08-04 |
RU2006129927A (ru) | 2008-02-27 |
CA2553855C (en) | 2012-11-20 |
EP1737571A1 (en) | 2007-01-03 |
CA2553855A1 (en) | 2005-08-04 |
ES2591240T3 (es) | 2016-11-25 |
DK1737571T3 (en) | 2016-10-03 |
JP2007518560A (ja) | 2007-07-12 |
BRPI0506968A (pt) | 2007-07-03 |
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