BR112015000528B1 - Pprocesso para o craqueamento catalítico de hidrocarbonetos - Google Patents
Pprocesso para o craqueamento catalítico de hidrocarbonetos Download PDFInfo
- Publication number
- BR112015000528B1 BR112015000528B1 BR112015000528-4A BR112015000528A BR112015000528B1 BR 112015000528 B1 BR112015000528 B1 BR 112015000528B1 BR 112015000528 A BR112015000528 A BR 112015000528A BR 112015000528 B1 BR112015000528 B1 BR 112015000528B1
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- Brazil
- Prior art keywords
- catalyst
- reactor
- cracking
- countercurrent flow
- hydrocarbon
- Prior art date
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- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 99
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 98
- 238000000034 method Methods 0.000 title claims abstract description 48
- 230000008569 process Effects 0.000 title claims abstract description 47
- 238000004523 catalytic cracking Methods 0.000 title claims description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 233
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 71
- 238000005336 cracking Methods 0.000 claims abstract description 65
- 238000006243 chemical reaction Methods 0.000 claims abstract description 46
- 230000008929 regeneration Effects 0.000 claims abstract description 22
- 238000011069 regeneration method Methods 0.000 claims abstract description 22
- 239000002245 particle Substances 0.000 claims description 35
- 238000000926 separation method Methods 0.000 claims description 34
- 239000007789 gas Substances 0.000 claims description 20
- 229910021536 Zeolite Inorganic materials 0.000 claims description 19
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 19
- 239000010457 zeolite Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 15
- 239000002826 coolant Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 3
- 239000011261 inert gas Substances 0.000 claims 1
- 230000001172 regenerating effect Effects 0.000 claims 1
- 150000001336 alkenes Chemical class 0.000 abstract description 53
- 238000004231 fluid catalytic cracking Methods 0.000 abstract description 40
- 239000003502 gasoline Substances 0.000 abstract description 10
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract description 10
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- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 8
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- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 8
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- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
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- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
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- 239000011148 porous material Substances 0.000 description 3
- -1 propylene, ethylene Chemical group 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
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- 238000011084 recovery Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000004227 thermal cracking Methods 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 229910052733 gallium Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005649 metathesis reaction Methods 0.000 description 1
- 239000003498 natural gas condensate Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011027 product recovery Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004230 steam cracking Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 239000006163 transport media Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1809—Controlling processes
-
- 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
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
-
- 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
-
- 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
- C10G11/182—Regeneration
-
- 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
- C10G11/187—Controlling or regulating
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
-
- 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
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °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
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
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- 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
- C10G2300/1074—Vacuum distillates
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- 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
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- 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
- C10G2300/70—Catalyst aspects
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- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
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- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
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- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
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- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/30—Aromatics
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BR122020007403-5A BR122020007403B1 (pt) | 2012-07-12 | 2013-07-10 | Dispositivo para o craqueamento catalítico de hidrocarbonetos |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/547,807 US9452404B2 (en) | 2012-07-12 | 2012-07-12 | Fluid cracking process and apparatus for maximizing light olefins or middle distillates and light olefins |
| US13/547,807 | 2012-07-12 | ||
| PCT/US2013/049906 WO2014011759A1 (en) | 2012-07-12 | 2013-07-10 | Fluid catalytic cracking process and apparatus for maximizing light olefins or middle distillates and light olefins |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| BR112015000528A2 BR112015000528A2 (pt) | 2017-06-27 |
| BR112015000528B1 true BR112015000528B1 (pt) | 2022-01-18 |
Family
ID=49913041
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BR112015000528-4A BR112015000528B1 (pt) | 2012-07-12 | 2013-07-10 | Pprocesso para o craqueamento catalítico de hidrocarbonetos |
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Families Citing this family (44)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3307435A1 (en) | 2015-06-09 | 2018-04-18 | Hindustan Petroleum Corporation Ltd. | Catalyst composition for fluid catalytic cracking, and use thereof |
| CN107709524B (zh) * | 2015-07-01 | 2019-11-05 | 国际壳牌研究有限公司 | 废催化剂立管 |
| PL3448960T3 (pl) * | 2016-04-29 | 2023-03-27 | Basf Corporation | Nowa konstrukcja jednostki do cyklicznej dezaktywacji metali do dezaktywacji katalizatora FCC |
| MX2019003031A (es) * | 2016-09-16 | 2019-09-13 | Lummus Technology Inc | Proceso y aparato para la eliminacion mejorada de contaminantes en procesos de craqueo catalitico de fluido. |
| AU2017325716B2 (en) * | 2016-09-16 | 2020-01-30 | Lummus Technology Llc | Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications |
| US10758883B2 (en) | 2016-09-16 | 2020-09-01 | Lummus Technology Llc | Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications |
| CN107961744B (zh) * | 2016-10-19 | 2022-02-18 | 中国科学院大连化学物理研究所 | 一种制备丙烯、c4烃类的方法及其装置 |
| EP3558908B1 (en) | 2016-12-21 | 2022-08-10 | SABIC Global Technologies B.V. | Process to produce olefins from a catalytically cracked hydrocarbons stream |
| US10767117B2 (en) | 2017-04-25 | 2020-09-08 | Saudi Arabian Oil Company | Enhanced light olefin yield via steam catalytic downer pyrolysis of hydrocarbon feedstock |
| ES2916256T3 (es) * | 2017-05-28 | 2022-06-29 | Hindustan Petroleum Corp Ltd | Procedimiento de craqueo catalítico fluido |
| CA3069332C (en) * | 2017-07-18 | 2022-06-07 | Lummus Technology Llc | Integrated thermal and catalytic cracking for olefin production |
| CN107460005B (zh) * | 2017-07-26 | 2019-05-21 | 天津大学 | 利用生物油催化加氢耦合催化裂化制备芳香烃和烯烃的方法及装置 |
| CN107597201B (zh) * | 2017-09-13 | 2019-10-08 | 上海华畅环保设备发展有限公司 | 含油外排催化剂处理及分选回用方法和装置 |
| US10781377B2 (en) * | 2017-11-30 | 2020-09-22 | Uop Llc | Process and apparatus for cracking hydrocarbons to lighter hydrocarbons |
| JP7146503B2 (ja) * | 2018-07-30 | 2022-10-04 | 株式会社デンソー | 燃料改質装置 |
| CA3120559A1 (en) * | 2018-11-27 | 2020-06-04 | King Abdullah University Of Science And Technology | Zoned fluidization process for catalytic conversion of hydrocarbon feedstocks to petrochemicals |
| FR3090684B1 (fr) * | 2018-12-19 | 2021-08-27 | Ifp Energies Now | Conversion d’un brut pétrolier en lit fluidisé, avec zones de différents temps de contact |
| SG11202110638PA (en) * | 2019-04-03 | 2021-10-28 | Lummus Technology Inc | Staged fluid catalytic cracking processes incorporating a solids separation device for upgrading naphtha range material |
| WO2021003269A1 (en) | 2019-07-02 | 2021-01-07 | Lummus Technology Llc | Fluid catalytic cracking processes and apparatus |
| WO2021011252A1 (en) * | 2019-07-15 | 2021-01-21 | Lummus Technology Llc | Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications |
| EP4004151A1 (en) * | 2019-07-31 | 2022-06-01 | SABIC Global Technologies, B.V. | Dense phase fluidized bed reactor to maximize btx production yield |
| CN114207090A (zh) * | 2019-08-05 | 2022-03-18 | 沙特基础工业全球技术公司 | 用于石脑油催化裂化的最大化低碳烯烃产率的密相提升管 |
| US20220275284A1 (en) * | 2019-08-05 | 2022-09-01 | Sabic Global Technologies B.V. | High-density fluidized bed systems |
| EP3990581A1 (en) | 2019-08-05 | 2022-05-04 | SABIC Global Technologies, B.V. | Turbulent/fast fluidized bed reactor with baffles to maximize light olefin yields |
| US12060528B2 (en) | 2019-08-05 | 2024-08-13 | Sabic Global Technologies B.V. | Multiple dense phase risers to maximize light olefins yields for naphtha catalytic cracking |
| KR102744983B1 (ko) * | 2019-11-04 | 2024-12-19 | 루머스 테크놀로지 엘엘씨 | 유동 촉매 분해 원료 주입기 |
| JP7601890B2 (ja) | 2020-03-13 | 2024-12-17 | ルーマス テクノロジー エルエルシー | 流動接触分解プロセスによる原油からの軽質オレフィンの製造および装置 |
| US20220033714A1 (en) * | 2020-07-28 | 2022-02-03 | Saudi Arabian Oil Company | Methods and apparatuses for processing hydrocarbons to produce light olefins |
| US20220081624A1 (en) * | 2020-09-14 | 2022-03-17 | Saudi Arabian Oil Company | Methods for upgrading hydrocarbon feeds to produce olefins |
| KR102803647B1 (ko) * | 2020-10-16 | 2025-05-07 | 달리안 인스티튜트 오브 케미컬 피직스, 차이니즈 아카데미 오브 사이언시즈 | 코크 조절 반응기, 장치 및 산소 함유 화합물로부터 저탄소 올레핀을 제조하는 방법 |
| EP4082658B1 (en) * | 2020-10-16 | 2025-01-22 | Dalian Institute Of Chemical Physics, Chinese Academy Of Sciences | Coke control reactor, device for preparing low-carbon olefins from oxygen-containing compound, and use thereof |
| EP4063468A1 (en) * | 2021-03-25 | 2022-09-28 | Indian Oil Corporation Limited | A process for enhancement of ron of fcc gasoline with simultaneous reduction in benzene |
| CN115161060B (zh) * | 2021-04-02 | 2024-02-27 | 上海河图工程股份有限公司 | 一种多产低碳烯烃的催化裂化方法及装置 |
| CN115895710B (zh) * | 2021-09-30 | 2024-10-11 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的催化转化方法及装置 |
| CN116064148B (zh) * | 2021-10-29 | 2024-12-06 | 中国石油化工股份有限公司 | 一种两段加氢裂化方法 |
| KR20240113833A (ko) | 2021-11-30 | 2024-07-23 | 사우디 아라비안 오일 컴퍼니 | 탄화수소 공급물 스트림의 처리 방법 |
| US20230183584A1 (en) * | 2021-12-14 | 2023-06-15 | Uop Llc | Process for naphtha aromatization using a multi-stage fluidized system |
| US20240026234A1 (en) * | 2022-07-24 | 2024-01-25 | Uop Llc | Process for cracking to light olefins |
| US11873452B1 (en) | 2022-12-12 | 2024-01-16 | Saudi Arabian Oil Company | Methods for processing hydrocarbons to produce light olefins using catalyst formulations or mixtures |
| US12195676B2 (en) | 2022-12-29 | 2025-01-14 | ExxonMobil Technology and Engineering Company | FCC processing with reduced CO2 emissions |
| US12152202B2 (en) | 2022-12-29 | 2024-11-26 | ExxonMobil Technology and Engineering Company | FCC processing with reduced CO2 emissions |
| CN118308136B (zh) * | 2023-01-09 | 2025-10-10 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的催化转化方法和系统 |
| WO2025010269A1 (en) * | 2023-07-04 | 2025-01-09 | Lummus Technology Llc | Process for efficient recovery of products from fcc & steam cracker combined effluent |
| US20250101316A1 (en) * | 2023-09-26 | 2025-03-27 | Saudi Arabian Oil Company | Methods for distributing catalyst in counter-current reactors and methods for processing hydrocarbons |
Family Cites Families (35)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US486358A (en) * | 1892-11-15 | Hand attachment for sewing-machines | ||
| US3573200A (en) * | 1968-12-04 | 1971-03-30 | Chevron Res | Catalyst makeup |
| US4116814A (en) | 1977-07-18 | 1978-09-26 | Mobil Oil Corporation | Method and system for effecting catalytic cracking of high boiling hydrocarbons with fluid conversion catalysts |
| US4541923A (en) * | 1984-02-29 | 1985-09-17 | Uop Inc. | Catalyst treatment and flow conditioning in an FCC reactor riser |
| US4863585A (en) | 1986-09-03 | 1989-09-05 | Mobil Oil Corporation | Fluidized catalytic cracking process utilizing a C3-C4 paraffin-rich Co-feed and mixed catalyst system with selective reactivation of the medium pore silicate zeolite component thereofo |
| AU605503B2 (en) * | 1986-09-03 | 1991-01-17 | Mobil Oil Corporation | FCC naphtha in a single riser fluid catalytic cracking operation employing a catalyst mixture. |
| US4871446A (en) * | 1986-09-03 | 1989-10-03 | Mobil Oil Corporation | Catalytic cracking process employing mixed catalyst system |
| US4892643A (en) | 1986-09-03 | 1990-01-09 | Mobil Oil Corporation | Upgrading naphtha in a single riser fluidized catalytic cracking operation employing a catalyst mixture |
| CA1302936C (en) | 1986-09-03 | 1992-06-09 | Hartley Owen | Process for fluidized catalytic cracking with reactive fragments |
| US4717466A (en) | 1986-09-03 | 1988-01-05 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
| US4874503A (en) | 1988-01-15 | 1989-10-17 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process employing a mixed catalyst |
| US5043522A (en) | 1989-04-25 | 1991-08-27 | Arco Chemical Technology, Inc. | Production of olefins from a mixture of Cu+ olefins and paraffins |
| US5043058A (en) * | 1990-03-26 | 1991-08-27 | Amoco Corporation | Quenching downstream of an external vapor catalyst separator |
| US5846402A (en) | 1997-05-14 | 1998-12-08 | Indian Oil Corporation, Ltd. | Process for catalytic cracking of petroleum based feed stocks |
| US6106697A (en) | 1998-05-05 | 2000-08-22 | Exxon Research And Engineering Company | Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins |
| US5944982A (en) | 1998-10-05 | 1999-08-31 | Uop Llc | Method for high severity cracking |
| US6835863B2 (en) * | 1999-07-12 | 2004-12-28 | Exxonmobil Oil Corporation | Catalytic production of light olefins from naphtha feed |
| US6869521B2 (en) | 2002-04-18 | 2005-03-22 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with thorough mixing |
| US6514403B1 (en) | 2000-04-20 | 2003-02-04 | Abb Lummus Global Inc. | Hydrocracking of vacuum gas and other oils using a cocurrent/countercurrent reaction system and a post-treatment reactive distillation system |
| CN1205305C (zh) | 2001-11-29 | 2005-06-08 | 中国石油化工股份有限公司 | 一种催化裂化反应－再生系统 |
| US20030127358A1 (en) | 2002-01-10 | 2003-07-10 | Letzsch Warren S. | Deep catalytic cracking process |
| US7179427B2 (en) | 2002-11-25 | 2007-02-20 | Abb Lummus Global Inc. | Apparatus for countercurrent contacting of gas and solids |
| CN1308419C (zh) | 2003-12-12 | 2007-04-04 | 石油大学(北京) | 一种双反应再生系统多效耦合流化催化反应工艺方法 |
| US7128827B2 (en) | 2004-01-14 | 2006-10-31 | Kellogg Brown & Root Llc | Integrated catalytic cracking and steam pyrolysis process for olefins |
| US20050161369A1 (en) | 2004-01-23 | 2005-07-28 | Abb Lummus Global, Inc. | System and method for selective component cracking to maximize production of light olefins |
| BRPI0403184B1 (pt) | 2004-07-30 | 2015-04-07 | Petroleo Brasileiro Sa | Processo para alterar a distribuição de produtos de craqueamento catalítico fluido de hidrocarbonetos |
| AU2005274030B2 (en) | 2004-08-10 | 2008-11-20 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| US7323099B2 (en) | 2004-11-19 | 2008-01-29 | Exxonmobil Chemical Patents Inc. | Two stage fluid catalytic cracking process for selectively producing C2 to C4 olefins |
| US20070205139A1 (en) | 2006-03-01 | 2007-09-06 | Sathit Kulprathipanja | Fcc dual elevation riser feed distributors for gasoline and light olefin modes of operation |
| US20080011645A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations |
| US7611622B2 (en) | 2006-12-29 | 2009-11-03 | Kellogg Brown & Root Llc | FCC process for converting C3/C4 feeds to olefins and aromatics |
| EP2364343B1 (en) | 2008-12-10 | 2017-09-06 | Reliance Industries Limited | A fluid catalytic cracking (fcc) process for manufacturing propylene and ethylene in increased yield |
| US8354018B2 (en) * | 2009-11-09 | 2013-01-15 | Uop Llc | Process for recovering products from two reactors |
| CN102086402B (zh) | 2009-12-03 | 2014-01-15 | 中国石油化工股份有限公司 | 一种增产丙烯并改善汽油性质的催化裂化方法和装置 |
| EP2591073B1 (en) | 2010-07-08 | 2019-07-03 | Indian Oil Corporation Ltd. | Two stage fluid catalytic cracking process |
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Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 10/07/2013, OBSERVADAS AS CONDICOES LEGAIS. |