JPH0115559B2 - - Google Patents
Info
- Publication number
- JPH0115559B2 JPH0115559B2 JP61227885A JP22788586A JPH0115559B2 JP H0115559 B2 JPH0115559 B2 JP H0115559B2 JP 61227885 A JP61227885 A JP 61227885A JP 22788586 A JP22788586 A JP 22788586A JP H0115559 B2 JPH0115559 B2 JP H0115559B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- zone
- concentration
- conversion
- hydrogen
- 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.)
- Expired
Links
- 238000006243 chemical reaction Methods 0.000 claims description 60
- 239000003054 catalyst Substances 0.000 claims description 57
- 238000000034 method Methods 0.000 claims description 47
- 229930195733 hydrocarbon Natural products 0.000 claims description 41
- 150000002430 hydrocarbons Chemical class 0.000 claims description 41
- 239000004215 Carbon black (E152) Substances 0.000 claims description 39
- 239000001257 hydrogen Substances 0.000 claims description 37
- 229910052739 hydrogen Inorganic materials 0.000 claims description 37
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 36
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 14
- 238000000197 pyrolysis Methods 0.000 claims description 12
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 10
- 230000009257 reactivity Effects 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 6
- 229910052717 sulfur Inorganic materials 0.000 claims description 6
- 239000011593 sulfur Substances 0.000 claims description 6
- 238000005984 hydrogenation reaction Methods 0.000 claims description 5
- 229910052720 vanadium Inorganic materials 0.000 claims description 5
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- 229910052750 molybdenum Inorganic materials 0.000 claims description 4
- 239000011733 molybdenum Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 238000001420 photoelectron spectroscopy Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 230000002902 bimodal effect Effects 0.000 claims description 3
- 238000005227 gel permeation chromatography Methods 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 150000002431 hydrogen Chemical class 0.000 claims 1
- 238000005259 measurement Methods 0.000 claims 1
- 238000005979 thermal decomposition reaction Methods 0.000 claims 1
- 238000002474 experimental method Methods 0.000 description 12
- 239000008186 active pharmaceutical agent Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 125000002524 organometallic group Chemical group 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-VVKOMZTBSA-N Dideuterium Chemical compound [2H][2H] UFHFLCQGNIYNRP-VVKOMZTBSA-N 0.000 description 1
- 229910003296 Ni-Mo Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000852 hydrogen donor Substances 0.000 description 1
- 238000007327 hydrogenolysis reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/780,589 US4626340A (en) | 1985-09-26 | 1985-09-26 | Process for the conversion of heavy hydrocarbon feedstocks characterized by high molecular weight, low reactivity and high metal contents |
| US780589 | 2001-02-08 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62109889A JPS62109889A (ja) | 1987-05-21 |
| JPH0115559B2 true JPH0115559B2 (en, 2012) | 1989-03-17 |
Family
ID=25120019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61227885A Granted JPS62109889A (ja) | 1985-09-26 | 1986-09-26 | 重質炭化水素原料のコンバ−シヨンの方法 |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US4626340A (en, 2012) |
| JP (1) | JPS62109889A (en, 2012) |
| CA (1) | CA1288375C (en, 2012) |
| DE (1) | DE3632880A1 (en, 2012) |
| FR (1) | FR2587715B1 (en, 2012) |
Families Citing this family (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4846961A (en) * | 1986-12-05 | 1989-07-11 | Union Oil Company Of California | Hydroprocessing catalyst with a Ni-P-Mo |
| FR2617498B1 (fr) * | 1987-07-02 | 1989-12-08 | Inst Francais Du Petrole | Procede d'hydroconversion thermocatalytique d'une charge lourde hydrocarbonee |
| US4792390A (en) * | 1987-09-21 | 1988-12-20 | Uop Inc. | Combination process for the conversion of a distillate hydrocarbon to produce middle distillate product |
| US5009768A (en) * | 1989-12-19 | 1991-04-23 | Intevep, S.A. | Hydrocracking high residual contained in vacuum gas oil |
| JP2966985B2 (ja) * | 1991-10-09 | 1999-10-25 | 出光興産株式会社 | 重質炭化水素油の接触水素化処理方法 |
| JP3520319B2 (ja) | 1999-12-21 | 2004-04-19 | 大阪大学長 | 化石燃料の脱メタル方法 |
| CA2455011C (en) | 2004-01-09 | 2011-04-05 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
| EP2272938B9 (en) | 2004-04-28 | 2015-12-30 | Headwaters Heavy Oil, LLC | Hydroprocessing method for upgrading heavy hydrocarbon feedstock using a colloidal catalyst |
| US10941353B2 (en) | 2004-04-28 | 2021-03-09 | Hydrocarbon Technology & Innovation, Llc | Methods and mixing systems for introducing catalyst precursor into heavy oil feedstock |
| CA2564359C (en) | 2004-04-28 | 2014-06-10 | Headwaters Heavy Oil, Llc | Fixed bed hydroprocessing methods and systems and methods for upgrading an existing fixed bed system |
| KR101493631B1 (ko) | 2004-04-28 | 2015-02-13 | 헤드워터스 헤비 오일, 엘엘씨 | 에뷸레이트 베드 하이드로프로세싱 방법 및 시스템 및 기존의 에뷸레이트 베드 시스템을 개량하는 방법 |
| US8034232B2 (en) | 2007-10-31 | 2011-10-11 | Headwaters Technology Innovation, Llc | Methods for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker |
| WO2009073436A2 (en) | 2007-11-28 | 2009-06-11 | Saudi Arabian Oil Company | Process for catalytic hydrotreating of sour crude oils |
| US8142645B2 (en) | 2008-01-03 | 2012-03-27 | Headwaters Technology Innovation, Llc | Process for increasing the mono-aromatic content of polynuclear-aromatic-containing feedstocks |
| US7943037B2 (en) * | 2008-03-11 | 2011-05-17 | Exxonmobil Research & Engineering Company | Hydroconversion process for petroleum resids using selective membrane separation followed by hydroconversion over carbon supported metal catalyst |
| US7931798B2 (en) * | 2008-03-11 | 2011-04-26 | Exxonmobil Research And Engineering Company | Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation |
| EP2300566B1 (en) * | 2008-07-14 | 2016-09-07 | Saudi Arabian Oil Company | Process for the treatment of heavy oils using light hydrocarbon components as a diluent |
| WO2010009082A1 (en) * | 2008-07-14 | 2010-01-21 | Saudi Arabian Oil Company | A prerefining process for the hydrodesulfurization of heavy sour crude oils to produce sweeter lighter crudes using moving catalyst system |
| US8372267B2 (en) * | 2008-07-14 | 2013-02-12 | Saudi Arabian Oil Company | Process for the sequential hydroconversion and hydrodesulfurization of whole crude oil |
| US8163168B2 (en) * | 2008-07-25 | 2012-04-24 | Exxonmobil Research And Engineering Company | Process for flexible vacuum gas oil conversion |
| US8491779B2 (en) | 2009-06-22 | 2013-07-23 | Saudi Arabian Oil Company | Alternative process for treatment of heavy crudes in a coking refinery |
| US9169449B2 (en) | 2010-12-20 | 2015-10-27 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
| US9790440B2 (en) | 2011-09-23 | 2017-10-17 | Headwaters Technology Innovation Group, Inc. | Methods for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker |
| US9644157B2 (en) | 2012-07-30 | 2017-05-09 | Headwaters Heavy Oil, Llc | Methods and systems for upgrading heavy oil using catalytic hydrocracking and thermal coking |
| US11414608B2 (en) | 2015-09-22 | 2022-08-16 | Hydrocarbon Technology & Innovation, Llc | Upgraded ebullated bed reactor used with opportunity feedstocks |
| US11414607B2 (en) | 2015-09-22 | 2022-08-16 | Hydrocarbon Technology & Innovation, Llc | Upgraded ebullated bed reactor with increased production rate of converted products |
| US11421164B2 (en) | 2016-06-08 | 2022-08-23 | Hydrocarbon Technology & Innovation, Llc | Dual catalyst system for ebullated bed upgrading to produce improved quality vacuum residue product |
| US11732203B2 (en) | 2017-03-02 | 2023-08-22 | Hydrocarbon Technology & Innovation, Llc | Ebullated bed reactor upgraded to produce sediment that causes less equipment fouling |
| JP7336831B2 (ja) | 2017-03-02 | 2023-09-01 | ハイドロカーボン テクノロジー アンド イノベーション、エルエルシー | ファウリングが少ない堆積物を伴う改良された沸騰床リアクター |
| CA3057131C (en) | 2018-10-17 | 2024-04-23 | Hydrocarbon Technology And Innovation, Llc | Upgraded ebullated bed reactor with no recycle buildup of asphaltenes in vacuum bottoms |
Family Cites Families (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3730875A (en) * | 1971-02-16 | 1973-05-01 | Universal Oil Prod Co | Combination process for black oil conversion |
| US3775293A (en) * | 1972-08-09 | 1973-11-27 | Universal Oil Prod Co | Desulfurization of asphaltene-containing hydrocarbonaceous black oils |
| GB2003916B (en) * | 1977-09-02 | 1982-05-19 | Hitachi Ltd | Process for hydrodesulphurizing hydrocarbon oil |
| US4176048A (en) * | 1978-10-31 | 1979-11-27 | Standard Oil Company (Indiana) | Process for conversion of heavy hydrocarbons |
| JPS601056B2 (ja) * | 1980-02-19 | 1985-01-11 | 千代田化工建設株式会社 | アスファルテンを含む重質炭化水素油の水素化処理 |
| CA1163222A (en) * | 1981-02-12 | 1984-03-06 | Her Majesty The Queen, In Right Of Canada As Represented By The Minister Of Natural Resources Canada | Simultaneous demetalization and hydrocracking of heavy hydrocarbon oils |
| US4421633A (en) * | 1981-03-13 | 1983-12-20 | Mobil Oil Corporation | Low pressure cyclic hydrocracking process using multi-catalyst bed reactor for heavy liquids |
| US4366047A (en) * | 1981-06-02 | 1982-12-28 | Exxon Research And Engineering Co. | Combination hydrorefining, heat-treating and hydrocracking process |
| US4368113A (en) * | 1981-08-31 | 1983-01-11 | Exxon Research And Engineering Co. | Hydrocarbon hydrocracking process |
| US4447313A (en) * | 1981-12-01 | 1984-05-08 | Mobil Oil Corporation | Deasphalting and hydrocracking |
| US4434045A (en) * | 1982-01-04 | 1984-02-28 | Exxon Research And Engineering Co. | Process for converting petroleum residuals |
| US4431525A (en) * | 1982-04-26 | 1984-02-14 | Standard Oil Company (Indiana) | Three-catalyst process for the hydrotreating of heavy hydrocarbon streams |
| US4431526A (en) * | 1982-07-06 | 1984-02-14 | Union Oil Company Of California | Multiple-stage hydroprocessing of hydrocarbon oil |
| FR2538811A1 (fr) * | 1982-12-30 | 1984-07-06 | Inst Francais Du Petrole | Procede de traitement d'une huile lourde ou d'une fraction d'huile lourde pour les convertir en fractions plus legeres |
| US4451354A (en) * | 1983-01-03 | 1984-05-29 | Exxon Research And Engineering Co. | Process for upgrading hydrocarbonaceous oils |
| US4525472A (en) * | 1983-02-23 | 1985-06-25 | Intevep, S.A. | Process for catalyst preparation for the hydrodemetallization of heavy crudes and residues |
| US4490483A (en) * | 1983-05-19 | 1984-12-25 | Gulf Research & Development Company | Process for preparing catalysts |
| US4520128A (en) * | 1983-12-19 | 1985-05-28 | Intevep, S.A. | Catalyst having high metal retention capacity and good stability for use in the demetallization of heavy crudes and method of preparation of same |
| US4572778A (en) * | 1984-01-19 | 1986-02-25 | Union Oil Company Of California | Hydroprocessing with a large pore catalyst |
-
1985
- 1985-09-26 US US06/780,589 patent/US4626340A/en not_active Expired - Fee Related
-
1986
- 1986-09-24 CA CA000518970A patent/CA1288375C/en not_active Expired - Lifetime
- 1986-09-24 FR FR8613329A patent/FR2587715B1/fr not_active Expired - Fee Related
- 1986-09-26 JP JP61227885A patent/JPS62109889A/ja active Granted
- 1986-09-26 DE DE19863632880 patent/DE3632880A1/de active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62109889A (ja) | 1987-05-21 |
| DE3632880A1 (de) | 1987-04-23 |
| CA1288375C (en) | 1991-09-03 |
| FR2587715A1 (fr) | 1987-03-27 |
| FR2587715B1 (fr) | 1993-04-09 |
| DE3632880C2 (en, 2012) | 1988-10-06 |
| US4626340A (en) | 1986-12-02 |
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