JP2001503451A - 中圧下にて重留出油を水素化分解する方法 - Google Patents
中圧下にて重留出油を水素化分解する方法Info
- Publication number
- JP2001503451A JP2001503451A JP50370098A JP50370098A JP2001503451A JP 2001503451 A JP2001503451 A JP 2001503451A JP 50370098 A JP50370098 A JP 50370098A JP 50370098 A JP50370098 A JP 50370098A JP 2001503451 A JP2001503451 A JP 2001503451A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- alumina
- catalyst
- hydrocracking
- zeolite
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
Classifications
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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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
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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
- 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
- B01J23/888—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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/132—Halogens; Compounds thereof with chromium, molybdenum, tungsten or polonium
-
- 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
- C10G45/06—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 nickel or cobalt metal, or compounds thereof
- C10G45/08—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 nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
-
- 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
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/18—Crystalline alumino-silicate carriers the catalyst containing platinum group metals or compounds thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
Description
Claims (1)
- 【特許請求の範囲】 1.重留出油を水素化分解することにより、中間留出物を製造する方法を提供 し、該方法は、以下の工程を包含する: (1)該重留出油を、ハイドロファイニング条件下にて、ハイドロファイニング 触媒と接触させて、該重留出油をハイドロファインすること;および (2)該ハイドロファイン重留出油を、中間体分離することなく、水素化分解条 件下にて、水素化分解触媒と接触させて、該ハイドロファイン重留出油を水素化 分解すること、 該ハイドロファイニング触媒は、該触媒の全量を基準にして、1〜5重量%の 酸化ニッケル、12〜35重量%の酸化タングステン、1〜9重量%のフッ素、およ び残量の複合アルミナ(担体として)から構成され、該複合アルミナは、1種また はそれ以上のミクロ細孔アルミナおよび1種またはそれ以上のマクロ細孔アルミ ナから構成され、ここで、ミクロ細孔アルミナとマクロ細孔アルミナとの重量比 は、75:25〜50:50であり、ここで、ミクロ細孔アルミナは、その細孔容量の95 %より高い割合が、80オングストローム未満の細孔直径であるような細孔サイズ 分布を有するのに対して、マクロ細孔アルミナは、その細孔容量の70%より高い 割合が、60〜600オングストロームの範囲の細孔直径であるような細孔サイズ分 布を有し、ここで、上記細孔サイズ分布は、窒素吸着のBET法により、測定され る; 該水素化分解触媒は、該触媒の全量を基準にして、0.5〜5.0重量%のフッ素、 2.5〜6.0重量%の酸化ニッケル、10〜38重量%の酸化タングステン、および担体 から構成され、該担体は、20〜90重量%のアルミナおよび10〜80重量%のゼオラ イトから構成され、ここで、該ゼオライトは、NH3-TPDで測定した1.0〜2.0mmol/ gの酸性度強度価を有するメソ細孔またはマクロ細孔ゼオライトであり、該アル ミナは、NH3-TPDで測定した0.5〜0.8mmol/gの酸性度強度価を有する。 2.前記ハイドロファイニング条件および水素化分解条件が、6.0〜10MPaの水 素分圧、340〜440℃の温度、400:1200の水素:オイルの容量比および0.1〜3.0h r-1のLHSVを包含する、請求項1に記載の方法。 3.前記ハイドロファイニング触媒と前記水素化分解触媒との容量比が、25: 75〜75:25である、請求項1に記載の方法。 4.前記重留出油が、500〜580℃の沸点範囲の乾点、1500ppmwまでの窒素含量 および3.5重量%までのイオウ含量を有する、請求項1に記載の方法。 5.前記重留出油が、残油と配合した直留ガス油、真空ガス油、コーカーガス 油または接触分解器サイクル油を有する、請求項4に記載の方法。 6.前記複合アルミナが、1種のミクロ細孔アルミナおよび1種のマクロ細孔 アルミナから構成される、請求項1に記載の方法。 7.前記ミクロ細孔アルミナが、60重量%より高いベーマイト含量を有する水 和アルミナから誘導され、そして前記マクロ細孔アルミナが、50重量%より高い ベーマイト含量を有する水和アルミナから誘導される、請求項1に記載の方法。 8.前記複合アルミナが、該細孔容量の75%より高い割合が40〜100オングス トロームの範囲の細孔直径である細孔サイズ分布を有する、請求項1に記載の方 法。 9.前記複合アルミナの比表面積が、220m2/gより高く、そして前記複合アル ミナの細孔容量が、0.4ml/gより大きい、請求項1に記載の方法。 10.前記水素化分解触媒が、1〜4重量%のフッ素、2.6〜5.0重量%の酸化ニ ッケル、および19〜25重量%の酸化タングステンを含有する、請求項1に記載の 方法。 11.前記水素化分解触媒担体が、50〜80重量%のアルミナおよび20〜50重量% のゼオライトから構成される、請求項1に記載の方法。 12.前記ゼオライトが、ホージャサイト、モルデンフッ石、ZSM-5ゼオライト 、β−ゼオライトおよびΩゼオライト、およびそれらの混合物の群から選択され る、請求項1に記載の方法。 13.前記ゼオライトが、モルデンフッ石水素形状または希土類形状Yゼオライ トからなる群から選択される、請求項1に記載の方法。 14.前記水素化分解触媒中の前記アルミナが、メタアルミン酸ナトリウム−二 酸化炭素法、アルキルアルミニウムまたはアルコキシアルミニウム加水分解法、 およびメタアルミン酸ナトリウム−硫酸アルミニウム法から選択される方法によ り調製した1種またはそれ以上の種類の水和アルミナをか焼することにより得ら れる、請求項1に記載の方法。 15.前記水和アルミナが、60重量%より多いベーマイトを含有する、請求項14 に記載の方法。
Applications Claiming Priority (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN96106587 | 1996-06-28 | ||
CN96106724 | 1996-06-28 | ||
CN96109007 | 1996-07-22 | ||
CN96106587.7 | 1996-07-22 | ||
CN96109007.3 | 1996-07-22 | ||
CN96106724.1 | 1996-07-22 | ||
PCT/CN1997/000064 WO1998000384A1 (fr) | 1996-06-28 | 1997-06-27 | Procede d'hydrocraquage d'une huile de distillat lourde a des pressions moyennes |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001503451A true JP2001503451A (ja) | 2001-03-13 |
Family
ID=27179089
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50370098A Pending JP2001503451A (ja) | 1996-06-28 | 1997-06-27 | 中圧下にて重留出油を水素化分解する方法 |
Country Status (8)
Country | Link |
---|---|
US (1) | US5954944A (ja) |
EP (1) | EP0947575B1 (ja) |
JP (1) | JP2001503451A (ja) |
AU (1) | AU3252797A (ja) |
HR (1) | HRP970357B1 (ja) |
ID (1) | ID17947A (ja) |
NO (1) | NO316647B1 (ja) |
WO (1) | WO1998000384A1 (ja) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2004510875A (ja) * | 2000-10-05 | 2004-04-08 | アンスティテュ フランセ デュ ペトロール | 中圧水素化分解によるディーゼルの製造方法 |
JP2011500941A (ja) * | 2007-10-22 | 2011-01-06 | シェブロン ユー.エス.エー. インコーポレイテッド | 高エネルギー留出燃料の製造方法 |
JP2011508023A (ja) * | 2007-12-21 | 2011-03-10 | シェブロン ユー.エス.エー. インコーポレイテッド | 高エネルギーの留出燃料を作製する方法 |
JP2014196395A (ja) * | 2013-03-29 | 2014-10-16 | Jx日鉱日石エネルギー株式会社 | 石油製品の製造方法 |
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US4976848A (en) * | 1988-10-04 | 1990-12-11 | Chevron Research Company | Hydrodemetalation and hydrodesulfurization using a catalyst of specified macroporosity |
US5266300A (en) * | 1989-08-02 | 1993-11-30 | Texaco Inc. | Method of making porous alumina |
JP2908959B2 (ja) * | 1993-04-07 | 1999-06-23 | 出光興産株式会社 | 新規触媒組成物 |
US5378671A (en) * | 1993-06-03 | 1995-01-03 | Mobil Oil Corp. | Method for preparing catalysts comprising zeolites |
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1997
- 1997-06-27 WO PCT/CN1997/000064 patent/WO1998000384A1/zh active IP Right Grant
- 1997-06-27 EP EP97928101A patent/EP0947575B1/en not_active Expired - Lifetime
- 1997-06-27 JP JP50370098A patent/JP2001503451A/ja active Pending
- 1997-06-27 AU AU32527/97A patent/AU3252797A/en not_active Abandoned
- 1997-06-27 HR HR970357A patent/HRP970357B1/xx not_active IP Right Cessation
- 1997-06-30 ID IDP972258A patent/ID17947A/id unknown
- 1997-06-30 US US08/884,813 patent/US5954944A/en not_active Expired - Lifetime
-
1998
- 1998-12-23 NO NO19986095A patent/NO316647B1/no not_active IP Right Cessation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004510875A (ja) * | 2000-10-05 | 2004-04-08 | アンスティテュ フランセ デュ ペトロール | 中圧水素化分解によるディーゼルの製造方法 |
JP2011500941A (ja) * | 2007-10-22 | 2011-01-06 | シェブロン ユー.エス.エー. インコーポレイテッド | 高エネルギー留出燃料の製造方法 |
JP2011508023A (ja) * | 2007-12-21 | 2011-03-10 | シェブロン ユー.エス.エー. インコーポレイテッド | 高エネルギーの留出燃料を作製する方法 |
JP2014196395A (ja) * | 2013-03-29 | 2014-10-16 | Jx日鉱日石エネルギー株式会社 | 石油製品の製造方法 |
Also Published As
Publication number | Publication date |
---|---|
WO1998000384A1 (fr) | 1998-01-08 |
EP0947575A4 (en) | 2000-03-22 |
HRP970357A2 (en) | 1998-04-30 |
AU3252797A (en) | 1998-01-21 |
NO986095L (no) | 1999-02-26 |
EP0947575B1 (en) | 2001-04-11 |
EP0947575A1 (en) | 1999-10-06 |
HRP970357B1 (en) | 2001-12-31 |
NO316647B1 (no) | 2004-03-22 |
NO986095D0 (no) | 1998-12-23 |
ID17947A (id) | 1998-02-12 |
US5954944A (en) | 1999-09-21 |
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