CA2008978A1 - Procede pour la craquage catalytique d'hydrocarbures - Google Patents
Procede pour la craquage catalytique d'hydrocarburesInfo
- Publication number
- CA2008978A1 CA2008978A1 CA002008978A CA2008978A CA2008978A1 CA 2008978 A1 CA2008978 A1 CA 2008978A1 CA 002008978 A CA002008978 A CA 002008978A CA 2008978 A CA2008978 A CA 2008978A CA 2008978 A1 CA2008978 A1 CA 2008978A1
- Authority
- CA
- Canada
- Prior art keywords
- catalyst
- cracking
- heavy
- hydrocarbon
- zone
- 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.)
- Abandoned
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 121
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 121
- 238000000034 method Methods 0.000 title claims abstract description 57
- 230000008569 process Effects 0.000 title claims abstract description 46
- 238000004523 catalytic cracking Methods 0.000 title claims description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 198
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 107
- 238000011069 regeneration method Methods 0.000 claims abstract description 97
- 238000005336 cracking Methods 0.000 claims abstract description 89
- 230000008929 regeneration Effects 0.000 claims abstract description 87
- 239000000463 material Substances 0.000 claims description 94
- 238000009835 boiling Methods 0.000 claims description 89
- 239000007789 gas Substances 0.000 claims description 71
- 239000000047 product Substances 0.000 claims description 60
- 239000003502 gasoline Substances 0.000 claims description 54
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 39
- 239000002245 particle Substances 0.000 claims description 37
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 27
- 239000000571 coke Substances 0.000 claims description 26
- 239000003546 flue gas Substances 0.000 claims description 26
- 229910052799 carbon Inorganic materials 0.000 claims description 25
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 25
- 239000000203 mixture Substances 0.000 claims description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- 230000003197 catalytic effect Effects 0.000 claims description 18
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 16
- 239000012084 conversion product Substances 0.000 claims description 16
- 238000002485 combustion reaction Methods 0.000 claims description 15
- 239000002002 slurry Substances 0.000 claims description 11
- 238000004508 fractional distillation Methods 0.000 claims description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 239000001569 carbon dioxide Substances 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 31
- 239000003921 oil Substances 0.000 description 79
- 150000001336 alkenes Chemical class 0.000 description 16
- 238000002347 injection Methods 0.000 description 12
- 239000007924 injection Substances 0.000 description 12
- 239000000725 suspension Substances 0.000 description 12
- 239000003085 diluting agent Substances 0.000 description 10
- 238000002156 mixing Methods 0.000 description 9
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 9
- 238000000926 separation method Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 239000002243 precursor Substances 0.000 description 5
- 238000005804 alkylation reaction Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000029936 alkylation Effects 0.000 description 3
- 150000001491 aromatic compounds Chemical class 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 230000002349 favourable effect Effects 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 2
- 230000006735 deficit Effects 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 238000011027 product recovery Methods 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000006471 dimerization reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- -1 gas oil Chemical class 0.000 description 1
- 125000004836 hexamethylene group Chemical class [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 230000002101 lytic effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 125000004817 pentamethylene group Chemical class [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 125000003367 polycyclic group Chemical group 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 108700026215 vpr Genes Proteins 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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
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 |
|---|---|---|---|
| US30732989A | 1989-02-06 | 1989-02-06 | |
| US07/307,329 | 1989-02-06 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2008978A1 true CA2008978A1 (fr) | 1990-08-06 |
Family
ID=23189257
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002008978A Abandoned CA2008978A1 (fr) | 1989-02-06 | 1990-01-31 | Procede pour la craquage catalytique d'hydrocarbures |
Country Status (6)
| Country | Link |
|---|---|
| EP (1) | EP0382289B1 (fr) |
| JP (1) | JPH0645787B2 (fr) |
| KR (1) | KR930011920B1 (fr) |
| BR (1) | BR9000490A (fr) |
| CA (1) | CA2008978A1 (fr) |
| DE (1) | DE69007649T2 (fr) |
Families Citing this family (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5435906A (en) * | 1992-08-20 | 1995-07-25 | Stone & Webster Engineering Corporation | Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components |
| DE19602898A1 (de) * | 1996-01-27 | 1997-07-31 | Ruhr Oel Gmbh | Verfahren zum katalytischen Kracken von Kohlenwasserstoffen |
| FR2770225B1 (fr) * | 1997-10-24 | 2000-01-07 | Total Raffinage Distribution | Procede et dispositif de vaporisation selective des charges d'hydrocarbures en craquage catalytique |
| DE19805915C1 (de) * | 1998-02-13 | 1999-09-23 | Ruhr Oel Gmbh | Verfahren zum Cracken von Kohlenwasserstoffen |
| US6156189A (en) * | 1998-04-28 | 2000-12-05 | Exxon Research And Engineering Company | Operating method for fluid catalytic cracking involving alternating feed injection |
| CA2328978A1 (fr) * | 1998-04-28 | 1999-11-04 | Daniel Paul Leta | Procede de mise en oeuvre pour craquage catalytique fluide |
| US20070129586A1 (en) * | 2005-12-02 | 2007-06-07 | Zimmermann Joseph E | Integrated hydrocarbon cracking and product olefin cracking |
| FR2918070B1 (fr) * | 2007-06-27 | 2012-10-19 | Inst Francais Du Petrole | Zone reactionnelle comportant deux risers en parallele et une zone de separation gaz solide commune en vue de la production de propylene |
| FR2932495B1 (fr) * | 2008-06-17 | 2011-03-25 | Inst Francais Du Petrole | Dispositif de controle des conditions operatoires dans une unite de craquage catalytique a deux risers. |
| JP5368073B2 (ja) * | 2008-12-11 | 2013-12-18 | 昭和シェル石油株式会社 | ガソリンエンジン用燃料組成物の製造方法及びその製造方法に使用する自動車エンジン用燃料基材 |
| WO2011051434A2 (fr) * | 2009-11-02 | 2011-05-05 | Shell Internationale Research Maatschappij B.V. | Procédé de craquage |
| US20130130889A1 (en) * | 2011-11-17 | 2013-05-23 | Stone & Webster Process Technology, Inc. | Process for maximum distillate production from fluid catalytic cracking units (fccu) |
| US10870802B2 (en) * | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
| WO2019158635A1 (fr) * | 2018-02-16 | 2019-08-22 | Haldor Topsøe A/S | Additifs d'élimination des sox et des nox contenant du cuivre destinés à être utilisés dans le processus de craquage catalytique fluide (fcc) |
| TW202104562A (zh) * | 2019-04-03 | 2021-02-01 | 美商魯瑪斯科技有限責任公司 | 用於升級輕油系列材料之合併有固體分離裝置之分段流體化媒裂程序 |
| CN111689829B (zh) * | 2020-07-09 | 2023-03-10 | 青岛京润石化设计研究院有限公司 | 一种石油烃催化转化制乙烯的方法及其装置 |
| CN115992004A (zh) * | 2021-10-18 | 2023-04-21 | 青岛京润石化设计研究院有限公司 | 一种反应原料为烃类原料的催化转化制低碳烯烃和芳烃的反应方法及反应器 |
| CN116196848A (zh) * | 2021-12-01 | 2023-06-02 | 中国石油天然气股份有限公司 | 一种原料油和轻烃催化转化的装置和方法 |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3617496A (en) * | 1969-06-25 | 1971-11-02 | Gulf Research Development Co | Fluid catalytic cracking process with a segregated feed charged to separate reactors |
| US3886060A (en) * | 1973-04-30 | 1975-05-27 | Mobil Oil Corp | Method for catalytic cracking of residual oils |
| US3928172A (en) * | 1973-07-02 | 1975-12-23 | Mobil Oil Corp | Catalytic cracking of FCC gasoline and virgin naphtha |
| US4601814A (en) * | 1983-05-27 | 1986-07-22 | Total Engineering And Research Company | Method and apparatus for cracking residual oils |
-
1990
- 1990-01-31 CA CA002008978A patent/CA2008978A1/fr not_active Abandoned
- 1990-01-31 EP EP90200225A patent/EP0382289B1/fr not_active Expired - Lifetime
- 1990-01-31 DE DE69007649T patent/DE69007649T2/de not_active Expired - Fee Related
- 1990-02-05 BR BR909000490A patent/BR9000490A/pt unknown
- 1990-02-06 KR KR1019900001408A patent/KR930011920B1/ko not_active IP Right Cessation
- 1990-02-06 JP JP2027023A patent/JPH0645787B2/ja not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| BR9000490A (pt) | 1991-01-15 |
| EP0382289B1 (fr) | 1994-03-30 |
| DE69007649D1 (de) | 1994-05-05 |
| KR930011920B1 (ko) | 1993-12-22 |
| KR900013059A (ko) | 1990-09-03 |
| JPH03197591A (ja) | 1991-08-28 |
| EP0382289A1 (fr) | 1990-08-16 |
| JPH0645787B2 (ja) | 1994-06-15 |
| DE69007649T2 (de) | 1994-08-25 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| FZDE | Dead |