KR102529350B1 - 연료 오일을 제조하도록 수소화분해 단계, 석출 단계 및 침전물 분리 단계를 포함한 공급 원료를 변환하기 위한 방법 - Google Patents
연료 오일을 제조하도록 수소화분해 단계, 석출 단계 및 침전물 분리 단계를 포함한 공급 원료를 변환하기 위한 방법 Download PDFInfo
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- KR102529350B1 KR102529350B1 KR1020177037761A KR20177037761A KR102529350B1 KR 102529350 B1 KR102529350 B1 KR 102529350B1 KR 1020177037761 A KR1020177037761 A KR 1020177037761A KR 20177037761 A KR20177037761 A KR 20177037761A KR 102529350 B1 KR102529350 B1 KR 102529350B1
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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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
-
- 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
-
- 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/09—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by filtration
-
- 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
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
-
- 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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including oxidation as the refining step in the absence of hydrogen
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1077—Vacuum residues
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/205—Metal content
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/205—Metal content
- C10G2300/206—Asphaltenes
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1554962 | 2015-06-01 | ||
| FR1554962A FR3036703B1 (fr) | 2015-06-01 | 2015-06-01 | Procede de conversion de charges comprenant une etape d'hydrocraquage, une etape de precipitation et une etape de separation des sediments pour la production de fiouls |
| PCT/EP2016/058747 WO2016192892A1 (fr) | 2015-06-01 | 2016-04-20 | Procede de conversion de charges comprenant une etape d'hydrocraquage, une etape de precipitation et une etape de separation des sediments pour la production de fiouls |
Publications (2)
| Publication Number | Publication Date |
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| KR20180014776A KR20180014776A (ko) | 2018-02-09 |
| KR102529350B1 true KR102529350B1 (ko) | 2023-05-04 |
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Country Status (11)
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| US (1) | US11702603B2 (https=) |
| EP (1) | EP3303522B1 (https=) |
| JP (1) | JP6670855B2 (https=) |
| KR (1) | KR102529350B1 (https=) |
| CN (1) | CN107849466A (https=) |
| ES (1) | ES2728566T3 (https=) |
| FR (1) | FR3036703B1 (https=) |
| PT (1) | PT3303522T (https=) |
| SA (1) | SA517390453B1 (https=) |
| TW (1) | TWI700361B (https=) |
| WO (1) | WO2016192892A1 (https=) |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE202016007978U1 (de) | 2016-12-27 | 2018-03-28 | Rudolf King | GPS-basierte Methode zur effektiven, mobilen Nachbarschaftshilfe im Notfall mittels statischen und/oder dynamischen und zeitlich unbegrenzten oder definierten sozialen Netzwerken (SENI) und mobilen Endgeräten |
| 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 |
| US12559689B2 (en) | 2017-02-12 | 2026-02-24 | Magēmā Technology LLC | Multi-stage process and device for treatment heavy marine fuel and resultant composition and the removal of detrimental solids |
| US12281266B2 (en) | 2017-02-12 | 2025-04-22 | Magẽmã Technology LLC | Heavy marine fuel oil composition |
| 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 |
| 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 |
| 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 |
| US10696906B2 (en) | 2017-09-29 | 2020-06-30 | Marathon Petroleum Company Lp | Tower bottoms coke catching device |
| TWI756504B (zh) * | 2017-12-29 | 2022-03-01 | 大陸商中國石油化工科技開發有限公司 | 一種蠟油加氫裂化方法和系統 |
| FR3084372B1 (fr) * | 2018-07-24 | 2020-08-07 | Ifp Energies Now | Procede de traitement d'une charge hydrocarbonee lourde comprenant un hydrotraitement en lit fixe, deux desasphaltages et un hydrocraquage en lit bouillonnant de l'asphalte |
| FR3084371B1 (fr) * | 2018-07-24 | 2020-08-07 | Ifp Energies Now | Procede de traitement d'une charge hydrocarbonee lourde comprenant un hydrotraitement en lit fixe, un desasphaltage et un hydrocraquage en lit bouillonnant de l'asphalte |
| US12000720B2 (en) | 2018-09-10 | 2024-06-04 | Marathon Petroleum Company Lp | Product inventory monitoring |
| US12031676B2 (en) | 2019-03-25 | 2024-07-09 | Marathon Petroleum Company Lp | Insulation securement system and associated methods |
| US11975316B2 (en) | 2019-05-09 | 2024-05-07 | Marathon Petroleum Company Lp | Methods and reforming systems for re-dispersing platinum on reforming catalyst |
| CA3212045A1 (en) | 2019-05-30 | 2020-11-30 | Marathon Petroleum Company Lp | Methods and systems for minimizing nox and co emissions in natural draft heaters |
| KR20210072217A (ko) * | 2019-12-06 | 2021-06-17 | 현대오일뱅크 주식회사 | 안정화된 연료유의 제조방법 및 그로부터 얻는 안정화된 연료유 |
| CA3109606C (en) | 2020-02-19 | 2022-12-06 | Marathon Petroleum Company Lp | Low sulfur fuel oil blends for paraffinic resid stability and associated methods |
| US12473500B2 (en) | 2021-02-25 | 2025-11-18 | Marathon Petroleum Company Lp | Assemblies and methods for enhancing control of fluid catalytic cracking (FCC) processes using spectroscopic analyzers |
| US20250012744A1 (en) | 2021-02-25 | 2025-01-09 | Marathon Petroleum Company Lp | Methods and assemblies for enhancing control of refining processes using spectroscopic analyzers |
| US12461022B2 (en) | 2021-02-25 | 2025-11-04 | Marathon Petroleum Company Lp | Methods and assemblies for determining and using standardized spectral responses for calibration of spectroscopic analyzers |
| US11898109B2 (en) | 2021-02-25 | 2024-02-13 | Marathon Petroleum Company Lp | Assemblies and methods for enhancing control of hydrotreating and fluid catalytic cracking (FCC) processes using spectroscopic analyzers |
| US11702600B2 (en) | 2021-02-25 | 2023-07-18 | Marathon Petroleum Company Lp | Assemblies and methods for enhancing fluid catalytic cracking (FCC) processes during the FCC process using spectroscopic analyzers |
| US11905468B2 (en) | 2021-02-25 | 2024-02-20 | Marathon Petroleum Company Lp | Assemblies and methods for enhancing control of fluid catalytic cracking (FCC) processes using spectroscopic analyzers |
| US11692141B2 (en) | 2021-10-10 | 2023-07-04 | Marathon Petroleum Company Lp | Methods and systems for enhancing processing of hydrocarbons in a fluid catalytic cracking unit using a renewable additive |
| CN116042269A (zh) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | 一种低硫重质船燃及其制备方法 |
| US11802257B2 (en) | 2022-01-31 | 2023-10-31 | Marathon Petroleum Company Lp | Systems and methods for reducing rendered fats pour point |
| US12311305B2 (en) | 2022-12-08 | 2025-05-27 | Marathon Petroleum Company Lp | Removable flue gas strainer and associated methods |
| US12306076B2 (en) | 2023-05-12 | 2025-05-20 | Marathon Petroleum Company Lp | Systems, apparatuses, and methods for sample cylinder inspection, pressurization, and sample disposal |
| US12533615B2 (en) | 2023-06-02 | 2026-01-27 | Marathon Petroleum Company Lp | Methods and systems for reducing contaminants in a feed stream |
| US12415962B2 (en) | 2023-11-10 | 2025-09-16 | Marathon Petroleum Company Lp | Systems and methods for producing aviation fuel |
| US12599848B2 (en) | 2024-06-03 | 2026-04-14 | Marathon Petroleum Company Lp | Systems, analyzers, controllers, and associated methods to enhance fluid separation for distillation operations |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20120074040A1 (en) | 2010-09-29 | 2012-03-29 | Omer Refa Koseoglu | Integrated deasphalting and oxidative removal of heteroatom hydrocarbon compounds from liquid hydrocarbon feedstocks |
| US20130026074A1 (en) | 2011-07-29 | 2013-01-31 | Omer Refa Koseoglu | Process for stabilization of heavy hydrocarbons |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2988501A (en) * | 1958-08-18 | 1961-06-13 | Union Oil Co | Hydrorefining of crude oils |
| US4883581A (en) * | 1986-10-03 | 1989-11-28 | Exxon Chemical Patents Inc. | Pretreatment for reducing oxidative reactivity of baseoils |
| US5108580A (en) * | 1989-03-08 | 1992-04-28 | Texaco Inc. | Two catalyst stage hydrocarbon cracking process |
| FR2753984B1 (fr) * | 1996-10-02 | 1999-05-28 | Inst Francais Du Petrole | Procede de conversion d'une fraction lourde d'hydrocarbures impliquant une hydrodemetallisation en lit bouillonnant de catalyseur |
| FR2866897B1 (fr) * | 2004-03-01 | 2007-08-31 | Inst Francais Du Petrole | Utilisation de gaz pour le preraffinage de petrole conventionnel et optionnellement sequestration de co2 |
| US7811444B2 (en) * | 2006-06-08 | 2010-10-12 | Marathon Oil Canada Corporation | Oxidation of asphaltenes |
| FR2933709B1 (fr) * | 2008-07-10 | 2011-07-22 | Inst Francais Du Petrole | Procede de conversion comprenant une hydroconversion d'une charge, un fractionnement, puis un desasphatage de la fraction residu sous vide |
| CA2778964C (en) * | 2009-11-17 | 2019-02-19 | H R D Corporation | Bitumen extraction and asphaltene removal from heavy crude using high shear |
| EP2348091B1 (fr) * | 2010-01-12 | 2012-12-05 | IFP Energies nouvelles | Procédé d'hydroliquéfaction directe de biomasse comprenant deux etapes d'hydroconversion en lit bouillonnant |
| US10400184B2 (en) * | 2011-08-31 | 2019-09-03 | Exxonmobil Research And Engineering Company | Hydroprocessing of heavy hydrocarbon feeds using small pore catalysts |
| FR2981659B1 (fr) * | 2011-10-20 | 2013-11-01 | Ifp Energies Now | Procede de conversion de charges petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement en lit fixe pour la production de fiouls a basse teneur en soufre |
| FR2983866B1 (fr) * | 2011-12-07 | 2015-01-16 | Ifp Energies Now | Procede d'hydroconversion de charges petrolieres en lits fixes pour la production de fiouls a basse teneur en soufre |
| FR3000098B1 (fr) * | 2012-12-20 | 2014-12-26 | IFP Energies Nouvelles | Procede avec separation de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre |
| FR3000097B1 (fr) * | 2012-12-20 | 2014-12-26 | Ifp Energies Now | Procede integre de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre |
| WO2016015045A1 (en) * | 2014-07-25 | 2016-01-28 | Saudi Arabian Oil Company | Integrated process to produce asphalt, petroleum green coke, and liquid and gas coking unit products |
-
2015
- 2015-06-01 FR FR1554962A patent/FR3036703B1/fr not_active Expired - Fee Related
-
2016
- 2016-04-20 JP JP2017562068A patent/JP6670855B2/ja active Active
- 2016-04-20 ES ES16719813T patent/ES2728566T3/es active Active
- 2016-04-20 PT PT16719813T patent/PT3303522T/pt unknown
- 2016-04-20 CN CN201680032073.6A patent/CN107849466A/zh active Pending
- 2016-04-20 EP EP16719813.4A patent/EP3303522B1/fr active Active
- 2016-04-20 KR KR1020177037761A patent/KR102529350B1/ko active Active
- 2016-04-20 US US15/578,467 patent/US11702603B2/en active Active
- 2016-04-20 WO PCT/EP2016/058747 patent/WO2016192892A1/fr not_active Ceased
- 2016-06-01 TW TW105117261A patent/TWI700361B/zh active
-
2017
- 2017-11-30 SA SA517390453A patent/SA517390453B1/ar unknown
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20120074040A1 (en) | 2010-09-29 | 2012-03-29 | Omer Refa Koseoglu | Integrated deasphalting and oxidative removal of heteroatom hydrocarbon compounds from liquid hydrocarbon feedstocks |
| US20130026074A1 (en) | 2011-07-29 | 2013-01-31 | Omer Refa Koseoglu | Process for stabilization of heavy hydrocarbons |
Also Published As
| Publication number | Publication date |
|---|---|
| PT3303522T (pt) | 2019-06-12 |
| US11702603B2 (en) | 2023-07-18 |
| EP3303522A1 (fr) | 2018-04-11 |
| FR3036703A1 (fr) | 2016-12-02 |
| ES2728566T3 (es) | 2019-10-25 |
| TW201715033A (zh) | 2017-05-01 |
| TWI700361B (zh) | 2020-08-01 |
| JP2018520228A (ja) | 2018-07-26 |
| CN107849466A (zh) | 2018-03-27 |
| JP6670855B2 (ja) | 2020-03-25 |
| US20180134974A1 (en) | 2018-05-17 |
| KR20180014776A (ko) | 2018-02-09 |
| FR3036703B1 (fr) | 2017-05-26 |
| SA517390453B1 (ar) | 2021-06-28 |
| WO2016192892A1 (fr) | 2016-12-08 |
| EP3303522B1 (fr) | 2019-03-06 |
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