CA2248882C - Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement - Google Patents
Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement Download PDFInfo
- Publication number
- CA2248882C CA2248882C CA002248882A CA2248882A CA2248882C CA 2248882 C CA2248882 C CA 2248882C CA 002248882 A CA002248882 A CA 002248882A CA 2248882 A CA2248882 A CA 2248882A CA 2248882 C CA2248882 C CA 2248882C
- Authority
- CA
- Canada
- Prior art keywords
- fraction
- sent
- reactor
- diesel
- catalyst
- 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 - Fee Related
Links
- 238000000034 method Methods 0.000 title claims abstract description 54
- 238000006243 chemical reaction Methods 0.000 title description 17
- 239000003208 petroleum Substances 0.000 title description 2
- 239000003054 catalyst Substances 0.000 claims abstract description 79
- 239000003502 gasoline Substances 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 238000004523 catalytic cracking Methods 0.000 claims abstract description 31
- 239000001257 hydrogen Substances 0.000 claims abstract description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 27
- 238000004821 distillation Methods 0.000 claims abstract description 25
- 239000000446 fuel Substances 0.000 claims abstract description 24
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 22
- 239000011593 sulfur Substances 0.000 claims abstract description 22
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 20
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 20
- 239000007789 gas Substances 0.000 claims abstract description 15
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 14
- 230000005587 bubbling Effects 0.000 claims abstract description 11
- 239000002283 diesel fuel Substances 0.000 claims abstract description 8
- 239000003921 oil Substances 0.000 claims description 19
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- 238000000926 separation method Methods 0.000 claims description 18
- 238000005336 cracking Methods 0.000 claims description 16
- 239000002002 slurry Substances 0.000 claims description 16
- 238000009835 boiling Methods 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 9
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 8
- 239000011707 mineral Substances 0.000 claims description 8
- 239000010426 asphalt Substances 0.000 claims description 6
- 150000002431 hydrogen Chemical class 0.000 claims description 6
- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 claims description 5
- 239000002828 fuel tank Substances 0.000 claims description 5
- 239000010779 crude oil Substances 0.000 claims description 3
- 238000005292 vacuum distillation Methods 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims 1
- 238000010926 purge Methods 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 2
- 230000000630 rising effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 32
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 229910052751 metal Inorganic materials 0.000 description 14
- 239000002184 metal Substances 0.000 description 14
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 10
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 10
- 229910021536 Zeolite Inorganic materials 0.000 description 8
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 8
- 150000002739 metals Chemical class 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 239000010457 zeolite Substances 0.000 description 8
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 7
- 239000000571 coke Substances 0.000 description 7
- 239000011159 matrix material Substances 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 229910052750 molybdenum Inorganic materials 0.000 description 7
- 239000011733 molybdenum Substances 0.000 description 7
- 230000008929 regeneration Effects 0.000 description 7
- 238000011069 regeneration method Methods 0.000 description 7
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- 229910052759 nickel Inorganic materials 0.000 description 6
- 239000000654 additive Substances 0.000 description 5
- 238000004064 recycling Methods 0.000 description 5
- 239000000377 silicon dioxide Substances 0.000 description 5
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 4
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 4
- 229910052796 boron Inorganic materials 0.000 description 4
- 239000000395 magnesium oxide Substances 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 3
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 3
- -1 ethylene, propylene, butylene Chemical group 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 101001050607 Homo sapiens KH domain-containing, RNA-binding, signal transduction-associated protein 3 Proteins 0.000 description 2
- 102100023428 KH domain-containing, RNA-binding, signal transduction-associated protein 3 Human genes 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 150000008064 anhydrides Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052810 boron oxide Inorganic materials 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 235000019577 caloric intake Nutrition 0.000 description 2
- 229910052799 carbon Inorganic materials 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
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000006356 dehydrogenation reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 2
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229910000480 nickel oxide Inorganic materials 0.000 description 2
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 2
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000003786 synthesis reaction 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
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 102100039339 Atrial natriuretic peptide receptor 1 Human genes 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 101000961044 Homo sapiens Atrial natriuretic peptide receptor 1 Proteins 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000010730 cutting oil Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000004231 fluid catalytic cracking Methods 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
- 239000008246 gaseous mixture Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- JSOQIZDOEIKRLY-UHFFFAOYSA-N n-propylnitrous amide Chemical compound CCCNN=O JSOQIZDOEIKRLY-UHFFFAOYSA-N 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking 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
- 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
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 |
|---|---|---|---|
| FR9713010A FR2769635B1 (fr) | 1997-10-14 | 1997-10-14 | Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement |
| FR9713010 | 1997-10-14 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2248882A1 CA2248882A1 (fr) | 1999-04-14 |
| CA2248882C true CA2248882C (fr) | 2009-12-22 |
Family
ID=9512350
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002248882A Expired - Fee Related CA2248882C (fr) | 1997-10-14 | 1998-10-13 | Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US6207041B1 (enExample) |
| JP (1) | JPH11189777A (enExample) |
| CA (1) | CA2248882C (enExample) |
| FR (1) | FR2769635B1 (enExample) |
Families Citing this family (31)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2249051A1 (en) * | 1998-09-29 | 2000-03-29 | Canadian Environmental Equipment & Engineering Technologies Inc. | Process for upgrading crude oil using low pressure hydrogen |
| FR2791354B1 (fr) | 1999-03-25 | 2003-06-13 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lits bouillonnants et une etape d'hydrotraitement |
| FR2803596B1 (fr) * | 2000-01-11 | 2003-01-17 | Inst Francais Du Petrole | Procede de conversion de fractions petrolieres comprenant une etape d'hydroconversion lit bouillonnant, une etape de separation, une etape d'hydrodesulfuration et une etape de craquage |
| RU2232183C1 (ru) * | 2002-11-26 | 2004-07-10 | ОАО "Всероссийский научно-исследовательский институт по переработке нефти" | Способ получения моторных топлив |
| RU2221838C1 (ru) * | 2002-11-26 | 2004-01-20 | ОАО "Всероссийский научно-исследовательский институт по переработке нефти" | Способ получения дизельного топлива |
| BG66071B1 (bg) * | 2005-03-29 | 2011-01-31 | Станчо СТАНКОВ | Метод за преработка на въглеводородни шламове |
| US9062260B2 (en) | 2008-12-10 | 2015-06-23 | Chevron U.S.A. Inc. | Removing unstable sulfur compounds from crude oil |
| CN102311799A (zh) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | 一种渣油处理组合工艺方法 |
| WO2012078835A2 (en) * | 2010-12-10 | 2012-06-14 | Shell Oil Company | Process for treating a hydrocarbon-containing feed |
| US8858784B2 (en) | 2010-12-10 | 2014-10-14 | Shell Oil Company | Process for treating a hydrocarbon-containing feed |
| FR2969651B1 (fr) * | 2010-12-24 | 2014-02-21 | Total Raffinage Marketing | Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par decontamination, hydroconversion en lit bouillonnant, et fractionnement par distillation atmospherique |
| EP2471895B1 (en) * | 2011-01-04 | 2016-03-09 | Phillips 66 Company | Process to partially upgrade slurry oil |
| US9101854B2 (en) * | 2011-03-23 | 2015-08-11 | Saudi Arabian Oil Company | Cracking system and process integrating hydrocracking and fluidized catalytic cracking |
| US9101853B2 (en) * | 2011-03-23 | 2015-08-11 | Saudi Arabian Oil Company | Integrated hydrocracking and fluidized catalytic cracking system and process |
| CN103102944B (zh) * | 2011-11-10 | 2015-04-01 | 中国石油化工股份有限公司 | 一种渣油加氢处理及轻质化的组合工艺方法 |
| CN103102981B (zh) * | 2011-11-10 | 2015-10-21 | 中国石油化工股份有限公司 | 一种重质原料的加工方法 |
| CN103102982B (zh) * | 2011-11-10 | 2015-09-30 | 中国石油化工股份有限公司 | 渣油转化组合工艺方法 |
| CN103102980B (zh) * | 2011-11-10 | 2015-05-13 | 中国石油化工股份有限公司 | 渣油深度转化的组合工艺方法 |
| CN103102985B (zh) * | 2011-11-10 | 2015-06-17 | 中国石油化工股份有限公司 | 一种渣油加氢处理与催化裂化组合工艺方法 |
| CN103102945B (zh) * | 2011-11-10 | 2015-09-30 | 中国石油化工股份有限公司 | 一种劣质重油加工方法 |
| FR2983208B1 (fr) * | 2011-11-24 | 2015-03-06 | IFP Energies Nouvelles | Procede de production de distillat moyen a partir d'une charge lourde conventionnelle incluant une etape d'hydrogenation selective de la coupe hco ex fcc |
| CN103215072B (zh) * | 2013-05-10 | 2015-01-07 | 成都博晟能源科技有限公司 | 一种高效加氢转化煤焦油生产柴油的方法 |
| FR3011004A1 (fr) * | 2013-09-20 | 2015-03-27 | IFP Energies Nouvelles | Procede de production de combustibles marins a basse teneur en soufre a partir d'une coupe hydrocarbonee issue du craquage catalytique de type hco, et faisant appel a une etape d'hydrotraitement. |
| CN105623725B (zh) * | 2014-10-27 | 2017-11-03 | 中国石油化工股份有限公司 | 一种重/渣油加工的组合工艺 |
| US9777229B2 (en) * | 2015-03-10 | 2017-10-03 | Uop Llc | Process and apparatus for hydroprocessing and cracking hydrocarbons |
| US20190233741A1 (en) | 2017-02-12 | 2019-08-01 | Magēmā 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 |
| 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 |
| 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 |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL7012520A (enExample) * | 1969-08-25 | 1971-03-01 | ||
| US3905892A (en) * | 1972-03-01 | 1975-09-16 | Cities Service Res & Dev Co | Process for reduction of high sulfur residue |
| JPS5347122B2 (enExample) * | 1974-03-01 | 1978-12-19 | ||
| US4102779A (en) * | 1976-08-13 | 1978-07-25 | Standard Oil Company (Indiana) | Processes for treating a heavy petroleum hydrocarbon stream containing metals and asphaltenes |
| US4344840A (en) * | 1981-02-09 | 1982-08-17 | Hydrocarbon Research, Inc. | Hydrocracking and hydrotreating shale oil in multiple catalytic reactors |
| US4591426A (en) * | 1981-10-08 | 1986-05-27 | Intevep, S.A. | Process for hydroconversion and upgrading of heavy crudes of high metal and asphaltene content |
| FR2753983B1 (fr) * | 1996-10-02 | 1999-06-04 | Inst Francais Du Petrole | Procede en plusieurs etapes de conversion d'un residu petrolier |
| 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 |
-
1997
- 1997-10-14 FR FR9713010A patent/FR2769635B1/fr not_active Expired - Lifetime
-
1998
- 1998-10-13 CA CA002248882A patent/CA2248882C/fr not_active Expired - Fee Related
- 1998-10-14 US US09/172,304 patent/US6207041B1/en not_active Expired - Lifetime
- 1998-10-14 JP JP10291718A patent/JPH11189777A/ja active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| CA2248882A1 (fr) | 1999-04-14 |
| FR2769635A1 (fr) | 1999-04-16 |
| FR2769635B1 (fr) | 2004-10-22 |
| US6207041B1 (en) | 2001-03-27 |
| JPH11189777A (ja) | 1999-07-13 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |
Effective date: 20181015 |