AR086150A1 - Proceso de hidroprocesamiento mediante el uso de la distribucion irregular del volumen del catalizador entre lechos de catalizador en reactores completamente liquidos - Google Patents
Proceso de hidroprocesamiento mediante el uso de la distribucion irregular del volumen del catalizador entre lechos de catalizador en reactores completamente liquidosInfo
- Publication number
- AR086150A1 AR086150A1 ARP120101492A ARP120101492A AR086150A1 AR 086150 A1 AR086150 A1 AR 086150A1 AR P120101492 A ARP120101492 A AR P120101492A AR P120101492 A ARP120101492 A AR P120101492A AR 086150 A1 AR086150 A1 AR 086150A1
- Authority
- AR
- Argentina
- Prior art keywords
- catalystal
- milk
- irregular distribution
- catalyst volume
- completely liquid
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 3
- 230000001788 irregular Effects 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 title abstract 2
- 239000008267 milk Substances 0.000 title 1
- 210000004080 milk Anatomy 0.000 title 1
- 235000013336 milk Nutrition 0.000 title 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 1
- 239000007791 liquid phase Substances 0.000 abstract 1
- 239000012263 liquid product Substances 0.000 abstract 1
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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0457—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being placed in separate reactors
-
- 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
- C10G45/22—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 with hydrogen dissolved or suspended in the oil
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
-
- 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
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining 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
- 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
- C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking 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
- 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
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of catalyst
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/027—Beds
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1051—Kerosene having a boiling range of about 180 - 230 °C
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °C
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
-
- 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
- C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
-
- 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
- C10G2300/4081—Recycling aspects
-
- 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
- C10G2300/80—Additives
- C10G2300/802—Diluents
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
La presente proporciona un proceso para hidroprocesar hidrocarburos con distribución irregular del volumen del catalizador entre dos o más lechos de catalizador. El proceso opera como un proceso completamente líquido, en donde todo el hidrógeno se disuelve en la fase líquida. Los hidrocarburos se pueden convertir en el proceso para proporcionar un producto líquido que incluyen combustibles limpios con propiedades deseadas múltiples tales como densidad baja y número de cetano alto.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/097,694 US8894838B2 (en) | 2011-04-29 | 2011-04-29 | Hydroprocessing process using uneven catalyst volume distribution among catalyst beds in liquid-full reactors |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR086150A1 true AR086150A1 (es) | 2013-11-20 |
Family
ID=46086060
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP120101492A AR086150A1 (es) | 2011-04-29 | 2012-04-27 | Proceso de hidroprocesamiento mediante el uso de la distribucion irregular del volumen del catalizador entre lechos de catalizador en reactores completamente liquidos |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US8894838B2 (es) |
| KR (1) | KR101933733B1 (es) |
| CN (1) | CN103502397B (es) |
| AR (1) | AR086150A1 (es) |
| CA (1) | CA2834305C (es) |
| RU (1) | RU2612218C2 (es) |
| SA (1) | SA112330485B1 (es) |
| TW (1) | TW201247861A (es) |
| WO (1) | WO2012149542A1 (es) |
Families Citing this family (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9365781B2 (en) | 2012-05-25 | 2016-06-14 | E I Du Pont De Nemours And Company | Process for direct hydrogen injection in liquid full hydroprocessing reactors |
| CN106536680A (zh) * | 2014-07-18 | 2017-03-22 | 纳幕尔杜邦公司 | 全液氢化处理和选择性开环方法 |
| WO2016099787A1 (en) | 2014-12-17 | 2016-06-23 | Exxonmobil Chemical Patents Inc. | Methods and systems for treating a hydrocarbon feed |
| WO2017102694A1 (en) | 2015-12-15 | 2017-06-22 | Shell Internationale Research Maatschappij B.V. | Guard bed system and process |
| WO2017131945A1 (en) * | 2016-01-25 | 2017-08-03 | E. I. Du Pont De Nemours And Company | Process for producing diesel with low levels of sulfur |
| TWI772330B (zh) | 2016-10-14 | 2022-08-01 | 荷蘭商蜆殼國際研究所 | 用於定量分析氣態製程流之方法及設備 |
| 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 |
| 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 |
| 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 |
| 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 |
| US12281266B2 (en) | 2017-02-12 | 2025-04-22 | Magẽmã Technology LLC | Heavy marine fuel oil composition |
| US10865350B2 (en) * | 2017-09-30 | 2020-12-15 | Uop Llc | Process for hydroprocessing a hydrocarbon stream |
| FI3695027T3 (fi) | 2017-10-11 | 2023-08-29 | Topsoe As | Menetelmä synteesikaasun generoimiseksi ammoniakin tuottamista varten |
| CN111068589B (zh) * | 2018-10-22 | 2021-08-31 | 中国石油化工股份有限公司 | 一种液相加氢系统及液相加氢方法 |
| JP7789702B2 (ja) * | 2020-06-01 | 2025-12-22 | ソリュゲン インコーポレーテッド | トリクルベッド反応器 |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3876530A (en) | 1973-08-22 | 1975-04-08 | Gulf Research Development Co | Multiple stage hydrodesulfurization with greater sulfur and metal removal in initial stage |
| US3936370A (en) | 1973-08-22 | 1976-02-03 | Gulf Research & Development Company | Process for producing a zeolite riser cracker feed from a residual oil |
| US3907667A (en) | 1973-08-22 | 1975-09-23 | Gulf Research Development Co | Process for producing a lubricating oil from a residue feed |
| US3926784A (en) | 1973-08-22 | 1975-12-16 | Gulf Research Development Co | Plural stage residue hydrodesulfurization process with hydrogen sulfide addition and removal |
| US3940330A (en) | 1974-04-24 | 1976-02-24 | Gulf Research & Development Company | Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage |
| US4069137A (en) * | 1976-10-26 | 1978-01-17 | Greenwood Arthur R | Hydrogen-producing hydrocarbon conversion with gravity-flowing catalyst particles |
| US4187168A (en) | 1978-07-13 | 1980-02-05 | Exxon Research & Engineering Co. | Hydrocarbon conversion processes utilizing supported heteronuclear cluster complex catalysts |
| US4869808A (en) | 1988-04-01 | 1989-09-26 | Uop | Hydrocarbon conversion process with radial flow and controlled hydrogen addition |
| US5332492A (en) | 1993-06-10 | 1994-07-26 | Uop | PSA process for improving the purity of hydrogen gas and recovery of liquefiable hydrocarbons from hydrocarbonaceous effluent streams |
| US5360535A (en) * | 1993-09-02 | 1994-11-01 | Texaco Inc. | Ebullated bed process with recycle eductor |
| CA2262586A1 (en) * | 1996-08-01 | 1998-02-12 | Shell Internationale Research Maatschappij B.V. | Hydrotreating process |
| US7291257B2 (en) | 1997-06-24 | 2007-11-06 | Process Dynamics, Inc. | Two phase hydroprocessing |
| US7569136B2 (en) | 1997-06-24 | 2009-08-04 | Ackerson Michael D | Control system method and apparatus for two phase hydroprocessing |
| EA001973B1 (ru) | 1997-06-24 | 2001-10-22 | Проусесс Дайнэмикс Инк. | Двухфазный способ гидропереработки |
| US20050006283A1 (en) * | 1999-12-16 | 2005-01-13 | Chevron U.S.A. Inc. | Presulfiding OCR catalyst replacement batches |
| CN1281720C (zh) | 2001-10-15 | 2006-10-25 | 催化蒸馏技术公司 | 加氢催化剂和加氢方法 |
| US6783660B2 (en) * | 2001-10-25 | 2004-08-31 | Chevron U.S.A. Inc. | Multiple hydroprocessing reactors with intermediate flash zones |
| CN1171979C (zh) * | 2002-05-15 | 2004-10-20 | 中国石油化工股份有限公司 | 一种微晶蜡的生产方法 |
| CN1259395C (zh) | 2003-10-24 | 2006-06-14 | 中国石油化工股份有限公司 | 一种加氢处理催化剂的装填方法 |
| CN1990834B (zh) | 2005-12-30 | 2010-08-25 | 中国石油化工股份有限公司 | 一种渣油的加氢处理方法 |
| US7794585B2 (en) * | 2007-10-15 | 2010-09-14 | Uop Llc | Hydrocarbon conversion process |
| US9279087B2 (en) * | 2008-06-30 | 2016-03-08 | Uop Llc | Multi-staged hydroprocessing process and system |
| US8518241B2 (en) | 2009-06-30 | 2013-08-27 | Uop Llc | Method for multi-staged hydroprocessing |
-
2011
- 2011-04-29 US US13/097,694 patent/US8894838B2/en active Active
-
2012
- 2012-04-27 TW TW101115092A patent/TW201247861A/zh unknown
- 2012-04-27 AR ARP120101492A patent/AR086150A1/es not_active Application Discontinuation
- 2012-04-29 SA SA112330485A patent/SA112330485B1/ar unknown
- 2012-04-30 KR KR1020137031301A patent/KR101933733B1/ko not_active Expired - Fee Related
- 2012-04-30 CA CA2834305A patent/CA2834305C/en active Active
- 2012-04-30 WO PCT/US2012/035823 patent/WO2012149542A1/en not_active Ceased
- 2012-04-30 RU RU2013153110A patent/RU2612218C2/ru active
- 2012-04-30 CN CN201280020793.2A patent/CN103502397B/zh not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CA2834305C (en) | 2019-12-03 |
| TW201247861A (en) | 2012-12-01 |
| CN103502397B (zh) | 2016-06-29 |
| CA2834305A1 (en) | 2012-11-01 |
| SA112330485B1 (ar) | 2015-08-17 |
| WO2012149542A1 (en) | 2012-11-01 |
| KR101933733B1 (ko) | 2018-12-28 |
| US20120273391A1 (en) | 2012-11-01 |
| CN103502397A (zh) | 2014-01-08 |
| RU2013153110A (ru) | 2015-06-10 |
| US8894838B2 (en) | 2014-11-25 |
| KR20140037855A (ko) | 2014-03-27 |
| RU2612218C2 (ru) | 2017-03-03 |
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