CN105745309B - 用于重烃进料的微碳残留物内容物催化转化的方法及其中使用的低表面积催化剂组合物 - Google Patents

用于重烃进料的微碳残留物内容物催化转化的方法及其中使用的低表面积催化剂组合物 Download PDF

Info

Publication number
CN105745309B
CN105745309B CN201480062899.8A CN201480062899A CN105745309B CN 105745309 B CN105745309 B CN 105745309B CN 201480062899 A CN201480062899 A CN 201480062899A CN 105745309 B CN105745309 B CN 105745309B
Authority
CN
China
Prior art keywords
catalyst
range
total
weight
diameter
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.)
Active
Application number
CN201480062899.8A
Other languages
English (en)
Chinese (zh)
Other versions
CN105745309A (zh
Inventor
J·M-R·吉内斯特拉
D·E·舍伍德
D·A·科马
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of CN105745309A publication Critical patent/CN105745309A/zh
Application granted granted Critical
Publication of CN105745309B publication Critical patent/CN105745309B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution
    • 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
    • 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
    • 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
    • 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
    • C10G47/04—Oxides
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Nanotechnology (AREA)
CN201480062899.8A 2013-11-25 2014-11-20 用于重烃进料的微碳残留物内容物催化转化的方法及其中使用的低表面积催化剂组合物 Active CN105745309B (zh)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201361908334P 2013-11-25 2013-11-25
US61/908,334 2013-11-25
PCT/US2014/066493 WO2015077390A1 (en) 2013-11-25 2014-11-20 A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein

Publications (2)

Publication Number Publication Date
CN105745309A CN105745309A (zh) 2016-07-06
CN105745309B true CN105745309B (zh) 2019-04-05

Family

ID=52014406

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201480062899.8A Active CN105745309B (zh) 2013-11-25 2014-11-20 用于重烃进料的微碳残留物内容物催化转化的方法及其中使用的低表面积催化剂组合物

Country Status (9)

Country Link
US (2) US10507459B2 (enExample)
EP (1) EP3074486B1 (enExample)
JP (1) JP6553030B2 (enExample)
KR (1) KR102360689B1 (enExample)
CN (1) CN105745309B (enExample)
CA (1) CA2929190C (enExample)
DK (1) DK3074486T3 (enExample)
TW (1) TWI651406B (enExample)
WO (1) WO2015077390A1 (enExample)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2017205988A1 (en) * 2016-01-06 2018-07-19 Oren Technologies, Llc Conveyor with integrated dust collector system
US12025435B2 (en) 2017-02-12 2024-07-02 Magēmã Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
US11788017B2 (en) 2017-02-12 2023-10-17 Magëmã Technology LLC Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil
US10655074B2 (en) 2017-02-12 2020-05-19 Mag{hacek over (e)}m{hacek over (a)} Technology LLC Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil
US10604709B2 (en) 2017-02-12 2020-03-31 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US12281266B2 (en) 2017-02-12 2025-04-22 Magẽmã Technology LLC Heavy marine fuel oil composition
KR20230130042A (ko) * 2021-01-08 2023-09-11 어드벤스드 리파이닝 테크놀로지즈 엘엘씨 고활성 수소처리 촉매 및 이를 사용한 방법

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1154668A (zh) * 1994-07-29 1997-07-16 切夫里昂美国公司 低大孔率渣油转化催化剂
US5928499A (en) * 1993-10-01 1999-07-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume
US20020000397A1 (en) * 1997-11-06 2002-01-03 David Edward Sherwood Jr. Novel method of preparing a catalyst for use in the hydrotreating of high boiling hydrocarbon feedstocks
CN1735456A (zh) * 2002-12-06 2006-02-15 阿尔伯麦尔荷兰有限公司 使用催化剂混合物的重原料hpc方法
CN1940029A (zh) * 2005-09-28 2007-04-04 中国石油化工股份有限公司 一种多产优质柴油的低氢耗加氢方法
CN102387859A (zh) * 2009-03-24 2012-03-21 国际壳牌研究有限公司 用于重烃原料催化加氢转化的高表面积组合物及其制备方法和用途

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US582742A (en) 1897-05-18 John joseph iioratst
US5827421A (en) * 1992-04-20 1998-10-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution and no added silica
US5397456A (en) 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US5514273A (en) 1993-10-01 1996-05-07 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US5468371A (en) 1994-04-11 1995-11-21 Texaco Inc. Catalyst for residual conversion demonstrating reduced toluene insolubles
US5968348A (en) * 1994-05-16 1999-10-19 Texaco Inc. Hydroconversion process employing a phosphorus loaded NiMo catalyst with specified pore size distribution
US6338265B1 (en) * 2000-03-09 2002-01-15 Jimmy Raider Grigg Device for straightening aluminum fins
RU2376059C2 (ru) 2003-09-17 2009-12-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ и катализатор гидроконверсии тяжелого углеводородного исходного сырья
CN1997724B (zh) 2004-06-17 2012-07-04 埃克森美孚研究工程公司 催化剂组合物和重质烃油的两步加氢处理方法
JP2009545442A (ja) * 2006-08-03 2009-12-24 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー 高度に安定な、重質炭化水素の水素化脱硫触媒およびその製造方法およびその使用

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5928499A (en) * 1993-10-01 1999-07-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume
CN1154668A (zh) * 1994-07-29 1997-07-16 切夫里昂美国公司 低大孔率渣油转化催化剂
US20020000397A1 (en) * 1997-11-06 2002-01-03 David Edward Sherwood Jr. Novel method of preparing a catalyst for use in the hydrotreating of high boiling hydrocarbon feedstocks
CN1735456A (zh) * 2002-12-06 2006-02-15 阿尔伯麦尔荷兰有限公司 使用催化剂混合物的重原料hpc方法
CN1940029A (zh) * 2005-09-28 2007-04-04 中国石油化工股份有限公司 一种多产优质柴油的低氢耗加氢方法
CN102387859A (zh) * 2009-03-24 2012-03-21 国际壳牌研究有限公司 用于重烃原料催化加氢转化的高表面积组合物及其制备方法和用途

Also Published As

Publication number Publication date
KR20160090314A (ko) 2016-07-29
TWI651406B (zh) 2019-02-21
CA2929190C (en) 2021-10-12
US20200055033A1 (en) 2020-02-20
CN105745309A (zh) 2016-07-06
DK3074486T3 (en) 2018-10-08
KR102360689B1 (ko) 2022-02-08
EP3074486B1 (en) 2018-06-27
US20150144531A1 (en) 2015-05-28
WO2015077390A1 (en) 2015-05-28
JP6553030B2 (ja) 2019-07-31
US11344865B2 (en) 2022-05-31
EP3074486A1 (en) 2016-10-05
JP2016539222A (ja) 2016-12-15
TW201542802A (zh) 2015-11-16
CA2929190A1 (en) 2015-05-28
US10507459B2 (en) 2019-12-17

Similar Documents

Publication Publication Date Title
CN105745309B (zh) 用于重烃进料的微碳残留物内容物催化转化的方法及其中使用的低表面积催化剂组合物
CN106660017B (zh) 用于加氢转化渣油的中孔和大孔催化剂及制备方法
CN106660019B (zh) 通过共研获得的具有活性相的介孔与大孔催化剂、其制备方法及其用于渣油的加氢处理的用途
US10569254B2 (en) Catalyst support and catalysts prepared therefrom
DK2411145T3 (en) COMPOSITION WITH LARGE SURFACE AREA FOR USE IN THE CATALYTIC HYDRO-CONVERSION OF A HEAVY CARBON HYDROWARE MATERIAL, PROCEDURE FOR PREPARING SUCH A COMPOSITION AND USE thereof
TWI611836B (zh) 觸媒支撐物及其製備方法
JP6301317B2 (ja) 重質原料の水素化転換のための改善された触媒および工程
CN105745018B (zh) 用于制备加氢处理催化剂的方法
JP6703956B2 (ja) 高い連結度を有する非晶質メソ多孔質アルミナから製造される触媒を用いたディーゼル留分の水素化処理方法
CN109072095A (zh) 具有低沉积物产率的高重质烃转化率的沸腾床方法
JP6643261B2 (ja) 高い連結度を有する非晶質メソ多孔質アルミナから製造される触媒を用いた蒸留留分の水素化処理方法
FEEDSTOCKS et al. A PROCESS FOR THE CATALYTIC CONVERSION OF MICRO CARBON RESIDUE CONTENT OF HEAVY HYDROCARBON FEEDSTOCKS AND A LOW SURFACE AREA CATALYST COMPOSITION FOR USE THEREIN
JP2017113715A (ja) 水素化処理触媒及びその製造方法

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant