SA515360047B1 - عملية التكسير المائي اللزج لمادة خام تشتمل على الهيدروجين المذاب - Google Patents
عملية التكسير المائي اللزج لمادة خام تشتمل على الهيدروجين المذاب Download PDFInfo
- Publication number
- SA515360047B1 SA515360047B1 SA515360047A SA515360047A SA515360047B1 SA 515360047 B1 SA515360047 B1 SA 515360047B1 SA 515360047 A SA515360047 A SA 515360047A SA 515360047 A SA515360047 A SA 515360047A SA 515360047 B1 SA515360047 B1 SA 515360047B1
- Authority
- SA
- Saudi Arabia
- Prior art keywords
- hydrogen
- feedstock
- hydrocarbon
- zone
- viscous
- Prior art date
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 95
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 75
- 239000001257 hydrogen Substances 0.000 title claims abstract description 75
- 238000000034 method Methods 0.000 title claims abstract description 72
- 230000008569 process Effects 0.000 title claims abstract description 71
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 65
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 64
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 53
- 239000007788 liquid Substances 0.000 claims abstract description 45
- 238000002156 mixing Methods 0.000 claims abstract description 41
- 239000007789 gas Substances 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims description 32
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 27
- 239000003921 oil Substances 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 14
- 238000005336 cracking Methods 0.000 claims description 12
- 239000002994 raw material Substances 0.000 claims description 11
- 150000002431 hydrogen Chemical class 0.000 claims description 10
- 239000003054 catalyst Substances 0.000 claims description 7
- 239000012530 fluid Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000003245 coal Substances 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 4
- 238000013461 design Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000004064 recycling Methods 0.000 claims description 4
- 239000010779 crude oil Substances 0.000 claims description 3
- 238000004939 coking Methods 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 claims description 2
- 150000002902 organometallic compounds Chemical class 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 230000001960 triggered effect Effects 0.000 claims 6
- 241000196324 Embryophyta Species 0.000 claims 1
- 240000008415 Lactuca sativa Species 0.000 claims 1
- 101001036171 Paenibacillus lautus Endoglucanase A Proteins 0.000 claims 1
- 208000007536 Thrombosis Diseases 0.000 claims 1
- 230000000977 initiatory effect Effects 0.000 claims 1
- 235000012045 salad Nutrition 0.000 claims 1
- 239000012071 phase Substances 0.000 description 17
- 239000000047 product Substances 0.000 description 16
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 10
- 229910052717 sulfur Inorganic materials 0.000 description 10
- 239000011593 sulfur Substances 0.000 description 10
- 229920006395 saturated elastomer Polymers 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 7
- 239000010426 asphalt Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 239000007792 gaseous phase Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000003776 cleavage reaction Methods 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- 238000013459 approach Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000013067 intermediate product Substances 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 230000007017 scission Effects 0.000 description 3
- 238000002791 soaking Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 238000004227 thermal cracking Methods 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 241001417501 Lobotidae Species 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- SGTNSNPWRIOYBX-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-{[2-(3,4-dimethoxyphenyl)ethyl](methyl)amino}-2-(propan-2-yl)pentanenitrile Chemical compound C1=C(OC)C(OC)=CC=C1CCN(C)CCCC(C#N)(C(C)C)C1=CC=C(OC)C(OC)=C1 SGTNSNPWRIOYBX-UHFFFAOYSA-N 0.000 description 1
- JCLFHZLOKITRCE-UHFFFAOYSA-N 4-pentoxyphenol Chemical compound CCCCCOC1=CC=C(O)C=C1 JCLFHZLOKITRCE-UHFFFAOYSA-N 0.000 description 1
- 241001272567 Hominoidea Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 230000002051 biphasic effect Effects 0.000 description 1
- 229940088033 calan Drugs 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000011067 equilibration Methods 0.000 description 1
- MUJOIMFVNIBMKC-UHFFFAOYSA-N fludioxonil Chemical compound C=12OC(F)(F)OC2=CC=CC=1C1=CNC=C1C#N MUJOIMFVNIBMKC-UHFFFAOYSA-N 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- -1 hydrogen compound Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 239000011800 void material Substances 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
-
- 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
- C10G47/22—Non-catalytic cracking in the presence of hydrogen
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)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201261692883P | 2012-08-24 | 2012-08-24 | |
| PCT/US2013/056419 WO2014031970A1 (en) | 2012-08-24 | 2013-08-23 | Hydrovisbreaking process for feedstock containing dissolved hydrogen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SA515360047B1 true SA515360047B1 (ar) | 2016-08-22 |
Family
ID=49123910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SA515360047A SA515360047B1 (ar) | 2012-08-24 | 2015-02-19 | عملية التكسير المائي اللزج لمادة خام تشتمل على الهيدروجين المذاب |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US9428700B2 (cg-RX-API-DMAC7.html) |
| EP (1) | EP2888342B1 (cg-RX-API-DMAC7.html) |
| JP (1) | JP6199973B2 (cg-RX-API-DMAC7.html) |
| KR (1) | KR102202081B1 (cg-RX-API-DMAC7.html) |
| CN (1) | CN104755596B (cg-RX-API-DMAC7.html) |
| SA (1) | SA515360047B1 (cg-RX-API-DMAC7.html) |
| SG (1) | SG11201501237SA (cg-RX-API-DMAC7.html) |
| WO (1) | WO2014031970A1 (cg-RX-API-DMAC7.html) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104534279B (zh) * | 2014-12-22 | 2015-12-30 | 山东东明石化集团有限公司 | 一种长距离管道常温输送380#燃料油的方法 |
| US20180370268A1 (en) * | 2015-12-16 | 2018-12-27 | Think Laboratory Co., Ltd. | Seamless cylindrical offset printing plate and manufacturing method therefor and reproduction processing method |
| CA2963436C (en) | 2017-04-06 | 2022-09-20 | Iftikhar Huq | Partial upgrading of bitumen |
| CN113906117A (zh) | 2019-05-29 | 2022-01-07 | 沙特阿拉伯石油公司 | 氢增强的延迟焦化工艺 |
| CN112275221A (zh) * | 2019-07-23 | 2021-01-29 | 中国石油化工股份有限公司 | 一种固定床加氢反应器及碳三馏分液相选择加氢的方法 |
| CN112295509A (zh) * | 2019-07-31 | 2021-02-02 | 中国石油化工股份有限公司 | 一种绝热固定床反应器及反应方法 |
| CN112295510A (zh) * | 2019-08-01 | 2021-02-02 | 中国石油化工股份有限公司 | 一种反应器及应用 |
| US11072751B1 (en) * | 2020-04-17 | 2021-07-27 | Saudi Arabian Oil Company | Integrated hydrotreating and deep hydrogenation of heavy oils including demetallized oil as feed for olefin production |
| US11965135B1 (en) | 2023-04-12 | 2024-04-23 | Saudi Arabian Oil Company | Methods for reactivity based hydroprocessing |
| KR20250063251A (ko) | 2023-10-30 | 2025-05-08 | 한국에너지기술연구원 | 비투멘 부분개질 방법 |
Family Cites Families (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2366218A (en) | 1940-05-13 | 1945-01-02 | Robert F Ruthruff | Catalytic combination process |
| US2717230A (en) | 1951-06-19 | 1955-09-06 | Universal Oil Prod Co | Catalytic reforming of hydrocarbon charge stocks high in nitrogen compounds |
| US2762754A (en) | 1951-12-20 | 1956-09-11 | Gulf Oil Corp | Thermal conversion of reduced crudes |
| US2873245A (en) | 1954-12-15 | 1959-02-10 | Exxon Research Engineering Co | Heavy oil conversion process |
| US3089843A (en) | 1960-06-02 | 1963-05-14 | Texaco Inc | Hydroconversion of hydrocarbons |
| US3132088A (en) | 1960-07-27 | 1964-05-05 | Gulf Research Development Co | Visbreaking, deasphalting and hydrogenation of crude oils |
| US3148135A (en) | 1961-07-25 | 1964-09-08 | Texaco Inc | Hydroconversion of hydrocarbons in two stages |
| US3271302A (en) | 1964-06-17 | 1966-09-06 | Universal Oil Prod Co | Multiple-stage hydrorefining of petroleum crude oil |
| US3532618A (en) | 1968-08-08 | 1970-10-06 | Sinclair Oil Corp | Pour point depressant made by hydrovisbreaking and deasphalting a shale oil |
| US3691058A (en) | 1970-04-15 | 1972-09-12 | Exxon Research Engineering Co | Production of single-ring aromatic hydrocarbons from gas oils containing condensed ring aromatics and integrating this with the visbreaking of residua |
| US3707459A (en) | 1970-04-17 | 1972-12-26 | Exxon Research Engineering Co | Cracking hydrocarbon residua |
| US3806444A (en) | 1972-12-29 | 1974-04-23 | Texaco Inc | Desulfurization of petroleum crude |
| US3888937A (en) | 1973-06-12 | 1975-06-10 | Exxon Research Engineering Co | Catalytic hydrogenation with a mixture of metal halide and anhydrous protonic acid |
| JPS5153505A (en) | 1974-11-07 | 1976-05-12 | Showa Oil | Tankasuisono henkanhoho |
| US4029571A (en) | 1975-02-25 | 1977-06-14 | Atlantic Richfield Company | Method of removing contaminant from hydrocarbonaceous fluid |
| US4005006A (en) | 1975-07-18 | 1977-01-25 | Gulf Research & Development Company | Combination residue hydrodesulfurization and thermal cracking process |
| DE2920415C2 (de) | 1979-05-19 | 1984-10-25 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zur Aufarbeitung von schweren Kohlenwasserstoffölen |
| DE3114990A1 (de) | 1980-04-21 | 1982-02-04 | Institut Français du Pétrole, 92502 Rueil-Malmaison, Hauts-de-Seine | Verfahren zur umwandlung von asphaltenhaltigen schweren kohlenwasserstoffoelen in leichtere fraktionen |
| US4544479A (en) | 1980-09-12 | 1985-10-01 | Mobil Oil Corporation | Recovery of metal values from petroleum residua and other fractions |
| US4334976A (en) | 1980-09-12 | 1982-06-15 | Mobil Oil Corporation | Upgrading of residual oil |
| US4481101A (en) * | 1981-01-13 | 1984-11-06 | Mobil Oil Corporation | Production of low-metal and low-sulfur coke from high-metal and high-sulfur resids |
| US4411770A (en) | 1982-04-16 | 1983-10-25 | Mobil Oil Corporation | Hydrovisbreaking process |
| ZA845721B (en) | 1983-08-01 | 1986-03-26 | Mobil Oil Corp | Process for visbreaking resids in the presence of hydrogen-donor materials |
| US4504377A (en) | 1983-12-09 | 1985-03-12 | Mobil Oil Corporation | Production of stable low viscosity heating oil |
| AU580617B2 (en) | 1984-09-10 | 1989-01-19 | Mobil Oil Corporation | Process for visbreaking resids in the presence of hydrogen- donor materials and organic sulfur compounds |
| US4587007A (en) | 1984-09-10 | 1986-05-06 | Mobil Oil Corporation | Process for visbreaking resids in the presence of hydrogen-donor materials and organic sulfur compounds |
| US4892644A (en) | 1985-11-01 | 1990-01-09 | Mobil Oil Corporation | Upgrading solvent extracts by double decantation and use of pseudo extract as hydrogen donor |
| US4764270A (en) | 1986-03-18 | 1988-08-16 | Chevron Research Company | Simultaneous upgrading of tar sand bitumen and coal by corefining |
| US4708784A (en) | 1986-10-10 | 1987-11-24 | Phillips Petroleum Company | Hydrovisbreaking of oils |
| DE3723607A1 (de) | 1987-07-17 | 1989-01-26 | Ruhrkohle Ag | Verfahren zum hydrierenden aufarbeiten von altoelen |
| DD266110A1 (de) | 1987-08-25 | 1989-03-22 | Grotewohl Boehlen Veb | Verfahren zur sumpfphasehydrierung von hochsiedenden kohlenwasserstoffmaterialien |
| US4802972A (en) | 1988-02-10 | 1989-02-07 | Phillips Petroleum Company | Hydrofining of oils |
| US5372705A (en) | 1992-03-02 | 1994-12-13 | Texaco Inc. | Hydroprocessing of heavy hydrocarbonaceous feeds |
| FR2689137B1 (fr) | 1992-03-26 | 1994-05-27 | Inst Francais Du Petrole | Procede d'hydro conversion de fractions lourds en phase liquide en presence d'un catalyseur disperse et d'additif polyaromatique. |
| US5688741A (en) * | 1995-03-17 | 1997-11-18 | Intevep, S.A. | Process and catalyst for upgrading heavy hydrocarbon |
| PL328308A1 (en) | 1996-02-14 | 1999-01-18 | Texaco Development Corp | Low-pressure process for hydroconcentring heavy hydrocarbons |
| US7291257B2 (en) | 1997-06-24 | 2007-11-06 | Process Dynamics, Inc. | Two phase hydroprocessing |
| CA2249051A1 (en) * | 1998-09-29 | 2000-03-29 | Canadian Environmental Equipment & Engineering Technologies Inc. | Process for upgrading crude oil using low pressure hydrogen |
| US9669381B2 (en) | 2007-06-27 | 2017-06-06 | Hrd Corporation | System and process for hydrocracking |
| US7815791B2 (en) | 2008-04-30 | 2010-10-19 | Exxonmobil Chemical Patents Inc. | Process and apparatus for using steam cracked tar as steam cracker feed |
| US10144882B2 (en) | 2010-10-28 | 2018-12-04 | E I Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
| US20120103873A1 (en) | 2010-11-01 | 2012-05-03 | Axens | Procede d'hydrotraitement et/ou d'hydrocraquage de charges azotees avec stripage a l'hydrogene |
| KR101542705B1 (ko) | 2011-07-29 | 2015-08-06 | 사우디 아라비안 오일 컴퍼니 | 유동 촉매 분해 공정용 수소-풍부 공급원료 |
-
2013
- 2013-08-23 CN CN201380043609.0A patent/CN104755596B/zh not_active Expired - Fee Related
- 2013-08-23 EP EP13759617.7A patent/EP2888342B1/en active Active
- 2013-08-23 WO PCT/US2013/056419 patent/WO2014031970A1/en not_active Ceased
- 2013-08-23 SG SG11201501237SA patent/SG11201501237SA/en unknown
- 2013-08-23 US US13/974,822 patent/US9428700B2/en not_active Expired - Fee Related
- 2013-08-23 KR KR1020157007298A patent/KR102202081B1/ko not_active Expired - Fee Related
- 2013-08-23 JP JP2015528689A patent/JP6199973B2/ja active Active
-
2015
- 2015-02-19 SA SA515360047A patent/SA515360047B1/ar unknown
Also Published As
| Publication number | Publication date |
|---|---|
| JP6199973B2 (ja) | 2017-09-20 |
| CN104755596A (zh) | 2015-07-01 |
| US20140054199A1 (en) | 2014-02-27 |
| EP2888342B1 (en) | 2020-06-17 |
| WO2014031970A1 (en) | 2014-02-27 |
| KR102202081B1 (ko) | 2021-01-13 |
| SG11201501237SA (en) | 2015-04-29 |
| JP2015529729A (ja) | 2015-10-08 |
| EP2888342A1 (en) | 2015-07-01 |
| KR20150046254A (ko) | 2015-04-29 |
| US9428700B2 (en) | 2016-08-30 |
| CN104755596B (zh) | 2016-06-01 |
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