ES2653342T3 - Proceso e instalación para la conversión de fracciones pesadas del petróleo en un lecho en ebullición con producción integral de destilados medios con muy bajo contenido de azufre - Google Patents
Proceso e instalación para la conversión de fracciones pesadas del petróleo en un lecho en ebullición con producción integral de destilados medios con muy bajo contenido de azufre Download PDFInfo
- Publication number
- ES2653342T3 ES2653342T3 ES07290221.6T ES07290221T ES2653342T3 ES 2653342 T3 ES2653342 T3 ES 2653342T3 ES 07290221 T ES07290221 T ES 07290221T ES 2653342 T3 ES2653342 T3 ES 2653342T3
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- hydrogen
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- diesel
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- 238000000034 method Methods 0.000 title claims abstract description 52
- 230000008569 process Effects 0.000 title claims abstract description 51
- 229910052717 sulfur Inorganic materials 0.000 title claims abstract description 35
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 239000011593 sulfur Substances 0.000 title claims abstract description 34
- 238000009835 boiling Methods 0.000 title claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 25
- 238000009434 installation Methods 0.000 title claims description 22
- 238000004519 manufacturing process Methods 0.000 title description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 89
- 239000001257 hydrogen Substances 0.000 claims abstract description 89
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 87
- 239000003054 catalyst Substances 0.000 claims abstract description 52
- 230000006835 compression Effects 0.000 claims abstract description 49
- 238000007906 compression Methods 0.000 claims abstract description 49
- 239000002994 raw material Substances 0.000 claims abstract description 34
- 239000007789 gas Substances 0.000 claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 26
- 238000000926 separation method Methods 0.000 claims abstract description 26
- 239000000295 fuel oil Substances 0.000 claims abstract description 6
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 5
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 24
- 238000004821 distillation Methods 0.000 claims description 18
- 230000003197 catalytic effect Effects 0.000 claims description 7
- 239000002283 diesel fuel Substances 0.000 claims description 7
- 239000007791 liquid phase Substances 0.000 claims description 5
- 239000000284 extract Substances 0.000 claims description 3
- 239000003921 oil Substances 0.000 abstract description 15
- 229910052751 metal Inorganic materials 0.000 description 16
- 239000002184 metal Substances 0.000 description 16
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 15
- 239000000758 substrate Substances 0.000 description 15
- 239000003502 gasoline Substances 0.000 description 12
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 9
- 150000002430 hydrocarbons Chemical class 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 8
- 229910052759 nickel Inorganic materials 0.000 description 8
- 238000004523 catalytic cracking Methods 0.000 description 7
- 239000012071 phase Substances 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 6
- 238000005984 hydrogenation reaction Methods 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 229910052750 molybdenum Inorganic materials 0.000 description 6
- 239000011733 molybdenum Substances 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000004064 recycling Methods 0.000 description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 229910003294 NiMo Inorganic materials 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 150000001491 aromatic compounds Chemical class 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 150000004706 metal oxides Chemical class 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229910011255 B2O3 Inorganic materials 0.000 description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- -1 that is Substances 0.000 description 3
- 229910052721 tungsten Inorganic materials 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 2
- 229910000480 nickel oxide Inorganic materials 0.000 description 2
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- MYKQKWIPLZEVOW-UHFFFAOYSA-N 11h-benzo[a]carbazole Chemical class C1=CC2=CC=CC=C2C2=C1C1=CC=CC=C1N2 MYKQKWIPLZEVOW-UHFFFAOYSA-N 0.000 description 1
- JEGZRTMZYUDVBF-UHFFFAOYSA-N Benz[a]acridine Chemical class C1=CC=C2C3=CC4=CC=CC=C4N=C3C=CC2=C1 JEGZRTMZYUDVBF-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001251 acridines Chemical class 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052810 boron oxide Inorganic materials 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical class C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000012438 extruded product Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 210000003918 fraction a Anatomy 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007792 gaseous phase Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000005300 metallic glass Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 1
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous oxide Inorganic materials [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 239000012808 vapor phase 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
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
- C10G47/26—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries
-
- 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
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 |
|---|---|---|---|
| US370184 | 2006-03-08 | ||
| US11/370,184 US7704377B2 (en) | 2006-03-08 | 2006-03-08 | Process and installation for conversion of heavy petroleum fractions in a boiling bed with integrated production of middle distillates with a very low sulfur content |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2653342T3 true ES2653342T3 (es) | 2018-02-06 |
Family
ID=38121293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES07290221.6T Active ES2653342T3 (es) | 2006-03-08 | 2007-02-21 | Proceso e instalación para la conversión de fracciones pesadas del petróleo en un lecho en ebullición con producción integral de destilados medios con muy bajo contenido de azufre |
Country Status (9)
| Country | Link |
|---|---|
| US (2) | US7704377B2 (https=) |
| EP (1) | EP1840190B1 (https=) |
| JP (1) | JP5651281B2 (https=) |
| CN (1) | CN101054534B (https=) |
| BR (1) | BRPI0700654B1 (https=) |
| CA (1) | CA2580295C (https=) |
| ES (1) | ES2653342T3 (https=) |
| MX (1) | MX2007002668A (https=) |
| RU (1) | RU2430957C2 (https=) |
Families Citing this family (59)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101354740B1 (ko) | 2004-04-28 | 2014-01-22 | 헤드워터스 헤비 오일, 엘엘씨 | 에뷸레이트 베드 하이드로프로세싱 방법 및 시스템 및기존의 에뷸레이트 베드 시스템을 개량하는 방법 |
| US10941353B2 (en) * | 2004-04-28 | 2021-03-09 | Hydrocarbon Technology & Innovation, Llc | Methods and mixing systems for introducing catalyst precursor into heavy oil feedstock |
| US7670984B2 (en) | 2006-01-06 | 2010-03-02 | Headwaters Technology Innovation, Llc | Hydrocarbon-soluble molybdenum catalyst precursors and methods for making same |
| US7842635B2 (en) * | 2006-01-06 | 2010-11-30 | Headwaters Technology Innovation, Llc | Hydrocarbon-soluble, bimetallic catalyst precursors and methods for making same |
| US7749249B2 (en) * | 2006-02-21 | 2010-07-06 | Kardium Inc. | Method and device for closing holes in tissue |
| 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 |
| US7951745B2 (en) | 2008-01-03 | 2011-05-31 | Wilmington Trust Fsb | Catalyst for hydrocracking hydrocarbons containing polynuclear aromatic compounds |
| US8142645B2 (en) | 2008-01-03 | 2012-03-27 | Headwaters Technology Innovation, Llc | Process for increasing the mono-aromatic content of polynuclear-aromatic-containing feedstocks |
| US8097149B2 (en) * | 2008-06-17 | 2012-01-17 | Headwaters Technology Innovation, Llc | Catalyst and method for hydrodesulfurization of hydrocarbons |
| US9162207B2 (en) | 2009-10-21 | 2015-10-20 | China Petroleum & Chemical Corporation | Fluidized-bed reactor and hydrotreating method thereof |
| US9005430B2 (en) * | 2009-12-10 | 2015-04-14 | IFP Energies Nouvelles | Process and apparatus for integration of a high-pressure hydroconversion process and a medium-pressure middle distillate hydrotreatment process, whereby the two processes are independent |
| ES2389430B1 (es) * | 2009-12-10 | 2013-09-11 | IFP Energies Nouvelles | Proceso que integra un proceso de hidroconversion de alta presion y un proceso de mediana presion de hidrotratamiento de destilados medios, en donde los dos procesos estan independientes. |
| CN101962572A (zh) * | 2010-10-29 | 2011-02-02 | 大连理工大学 | 煤焦油重馏分沸腾床加氢裂化方法及系统 |
| CN101962571A (zh) * | 2010-10-29 | 2011-02-02 | 大连理工大学 | 煤焦油重馏分悬浮床加氢裂化方法及系统 |
| 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 |
| US9403153B2 (en) | 2012-03-26 | 2016-08-02 | Headwaters Heavy Oil, Llc | Highly stable hydrocarbon-soluble molybdenum catalyst precursors and methods for making same |
| 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 |
| CN103773441B (zh) * | 2012-10-24 | 2015-09-30 | 中国石油化工股份有限公司 | 一种沸腾床液相加氢处理方法 |
| ES2725609T3 (es) | 2013-07-02 | 2019-09-25 | Saudi Basic Ind Corp | Proceso e instalación para la conversión de crudo en productos petroquímicos que tienen un rendimiento de etileno mejorado |
| EA030883B1 (ru) | 2013-07-02 | 2018-10-31 | Сауди Бейсик Индастриз Корпорейшн | Способ получения легких олефинов и ароматических соединений из углеводородного сырья |
| SG11201508916TA (en) | 2013-07-02 | 2016-01-28 | Saudi Basic Ind Corp | Process for upgrading refinery heavy residues to petrochemicals |
| EP3017023B1 (en) | 2013-07-02 | 2018-02-28 | Saudi Basic Industries Corporation | Method for converting a high-boiling hydrocarbon feedstock into lighter boiling hydrocarbon products |
| CN109593556A (zh) | 2013-07-02 | 2019-04-09 | 沙特基础工业公司 | 用于将原油转化成具有改进的丙烯产率的石化品的方法和设施 |
| SG11201508904WA (en) | 2013-07-02 | 2016-01-28 | Saudi Basic Ind Corp | Method for cracking a hydrocarbon feedstock in a steam cracker unit |
| CN105473691B (zh) | 2013-07-02 | 2019-03-15 | 沙特基础工业公司 | 从烃原料生产轻质烯烃和芳烃的方法 |
| WO2015000848A1 (en) | 2013-07-02 | 2015-01-08 | Saudi Basic Industries Corporation | Process and installation for the conversion of crude oil to petrochemicals having an improved carbon-efficiency |
| SG11201606017SA (en) | 2014-02-25 | 2016-08-30 | Saudi Basic Ind Corp | An integrated hydrocracking process |
| EA033030B1 (ru) | 2014-02-25 | 2019-08-30 | Сауди Бейсик Индастриз Корпорейшн | Способ превращения высококипящего углеводородного исходного сырья в более легкокипящие углеводородные продукты |
| SG11201606022QA (en) | 2014-02-25 | 2016-08-30 | Saudi Basic Ind Corp | Process for converting hydrocarbons into olefins |
| EA032307B1 (ru) | 2014-02-25 | 2019-05-31 | Сауди Бейсик Индастриз Корпорейшн | Способ повышения эффективности использования энергии технологических печей |
| US10316259B2 (en) | 2014-02-25 | 2019-06-11 | Saudi Basic Industries Corporation | Process for converting hydrocarbons into olefins |
| EA033755B1 (ru) | 2014-02-25 | 2019-11-22 | Saudi Basic Ind Corp | Способ получения бтк из смешанного источника углеводородов с использованием каталитического крекинга |
| EA031993B1 (ru) | 2014-02-25 | 2019-03-29 | Сауди Бейсик Индастриз Корпорейшн | Способ получения продукта бтк из смешанного углеводородного источника при использовании пиролиза |
| SG11201606522WA (en) | 2014-02-25 | 2016-09-29 | Saudi Basic Ind Corp | Process for producing btx from a mixed hydrocarbon source using coking |
| WO2015128043A1 (en) | 2014-02-25 | 2015-09-03 | Saudi Basic Industries Corporation | A process for the preparation of a feedstock for a hydroprocessing unit |
| ES2701819T3 (es) | 2014-02-25 | 2019-02-26 | Saudi Basic Ind Corp | Método para convertir una materia prima hidrocarbonada de alto punto de ebullición en productos hidrocarbonados de menor punto de ebullición |
| CN106062144B (zh) | 2014-02-25 | 2019-04-19 | 沙特基础工业公司 | 连续裂化方法 |
| KR102375008B1 (ko) | 2014-02-25 | 2022-03-17 | 사빅 글로벌 테크놀러지스 비.브이. | 올레핀 및 방향족 플랜트와 통합된 정제 공장의 수소 시스템에서 수소 가스의 공급 및 할당을 제어하는 방법 |
| ES2699992T3 (es) | 2014-02-25 | 2019-02-13 | Saudi Basic Ind Corp | Proceso e instalación para la conversión de petróleo crudo en petroquímicos que tiene un rendimiento mejorado de etileno y BTX |
| FR3030568B1 (fr) * | 2014-12-18 | 2019-04-05 | Axens | Procede de conversion profonde de residus maximisant le rendement en gazole |
| 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 |
| JP6965245B2 (ja) | 2015-11-30 | 2021-11-10 | サビック グローバル テクノロジーズ ベスローテン フェンノートシャップ | 蒸気分解処理のための高品質フィードストックを作り出すための方法 |
| SG11201806319YA (en) | 2016-02-05 | 2018-08-30 | Sabic Global Technologies Bv | Process and installation for the conversion of crude oil to petrochemicals having an improved product yield |
| EP3420051B1 (en) | 2016-02-25 | 2022-03-30 | SABIC Global Technologies B.V. | An integrated process for increasing olefin production by recycling and processing heavy cracker residue |
| 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 |
| EP3523397A1 (en) | 2016-10-07 | 2019-08-14 | SABIC Global Technologies B.V. | Process and a system for generating hydrocarbon vapor |
| CN109844068B (zh) | 2016-10-07 | 2022-01-11 | 沙特基础工业全球技术公司 | 用于烃蒸汽裂解的方法和系统 |
| EA201990879A1 (ru) | 2016-10-07 | 2019-10-31 | Ступень и система для сжатия крекинг-газа | |
| SG11201903253SA (en) | 2016-10-17 | 2019-05-30 | Sabic Global Technologies Bv | Process for producing btx from a c5-c12 hydrocarbon mixture |
| FR3060404A1 (fr) * | 2016-12-20 | 2018-06-22 | Axens | Installation et procede integre d'hydrotraitement et d'hydroconversion avec fractionnement commun |
| US11168271B2 (en) | 2017-02-02 | 2021-11-09 | Sabic Global Technologies B.V. | Integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals |
| JP2020514489A (ja) | 2017-02-02 | 2020-05-21 | サビック グローバル テクノロジーズ ベスローテン フェンノートシャップ | オレフィン系および芳香族石油化学物質を製造するための、水素処理ユニットのための原料の調製方法、ならびに原油を直接処理するための統合された水素処理および水蒸気熱分解の方法 |
| 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 |
| KR102505534B1 (ko) | 2017-03-02 | 2023-03-02 | 하이드로카본 테크놀로지 앤 이노베이션, 엘엘씨 | 오염 침전물이 적은 업그레이드된 에뷸레이티드 베드 반응기 |
| US11732203B2 (en) | 2017-03-02 | 2023-08-22 | Hydrocarbon Technology & Innovation, Llc | Ebullated bed reactor upgraded to produce sediment that causes less equipment fouling |
| 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 |
| US10800982B2 (en) | 2019-02-05 | 2020-10-13 | Ifp Energies Nouvelles (Ifpen) | Processing scheme for production of low sulfur bunker fuel |
| US12497569B2 (en) | 2022-05-26 | 2025-12-16 | Hydrocarbon Technology & Innovation, Llc | Method and system for mixing catalyst precursor into heavy oil using a high boiling hydrocarbon diluent |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3008A (en) * | 1843-03-21 | Machine for tttrnzstg or cutting irregular forms | ||
| US2987465A (en) * | 1958-06-20 | 1961-06-06 | Hydrocarbon Research Inc | Gas-liquid contacting process |
| BE709542A (https=) * | 1968-01-18 | 1968-07-18 | ||
| US3592757A (en) * | 1969-03-17 | 1971-07-13 | Union Oil Co | Combination hydrocracking-hydrogenation process |
| US5447621A (en) * | 1994-01-27 | 1995-09-05 | The M. W. Kellogg Company | Integrated process for upgrading middle distillate production |
| US6387246B1 (en) * | 1999-05-19 | 2002-05-14 | Institut Francais Du Petrole | Catalyst that comprises a partially amorphous Y zeolite and its use in hydroconversion of hydrocarbon petroleum feedstocks |
| US6217746B1 (en) * | 1999-08-16 | 2001-04-17 | Uop Llc | Two stage hydrocracking process |
| JP2001187773A (ja) * | 2000-01-06 | 2001-07-10 | Mitsubishi Chemicals Corp | アクリロニトリル組成物 |
| ITMI20011438A1 (it) * | 2001-07-06 | 2003-01-06 | Snam Progetti | Procedimento per la conversione di cariche pesanti quali i graggi pesanti e i residui di distillazione |
| FR2832158B1 (fr) * | 2001-11-09 | 2004-10-22 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres pour produire une charge de craquage catalytique et des distillats moyens de faible teneur en soufre |
| US20030089638A1 (en) * | 2001-11-12 | 2003-05-15 | Institut Francais Du Petrole | Process for converting heavy petroleum fractions including an ebulliated bed for producing middle distillates with a low sulfur content |
| FR2832159B1 (fr) | 2001-11-12 | 2004-07-09 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres incluant un lit bouillonnant pour produire des distillats moyens de faible teneur en soufre |
| US6797154B2 (en) | 2001-12-17 | 2004-09-28 | Chevron U.S.A. Inc. | Hydrocracking process for the production of high quality distillates from heavy gas oils |
| FR2846574B1 (fr) * | 2002-10-30 | 2006-05-26 | Inst Francais Du Petrole | Catalyseur et procede d'hydrocraquage de charges hydrocarbonees |
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2007
- 2007-02-21 ES ES07290221.6T patent/ES2653342T3/es active Active
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- 2007-03-05 CA CA2580295A patent/CA2580295C/en active Active
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| US20070209965A1 (en) | 2007-09-13 |
| US7704377B2 (en) | 2010-04-27 |
| BRPI0700654B1 (pt) | 2016-11-29 |
| CA2580295C (en) | 2015-08-11 |
| CA2580295A1 (en) | 2007-09-08 |
| EP1840190B1 (en) | 2017-10-04 |
| US7919054B2 (en) | 2011-04-05 |
| CN101054534B (zh) | 2013-02-13 |
| JP5651281B2 (ja) | 2015-01-07 |
| RU2430957C2 (ru) | 2011-10-10 |
| MX2007002668A (es) | 2008-10-30 |
| EP1840190A1 (en) | 2007-10-03 |
| RU2007108562A (ru) | 2008-09-20 |
| US20100166621A1 (en) | 2010-07-01 |
| CN101054534A (zh) | 2007-10-17 |
| BRPI0700654A (pt) | 2007-11-06 |
| JP2007238941A (ja) | 2007-09-20 |
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