EA034461B1 - Интегрированный способ гидрокрекинга - Google Patents
Интегрированный способ гидрокрекинга Download PDFInfo
- Publication number
- EA034461B1 EA034461B1 EA201691704A EA201691704A EA034461B1 EA 034461 B1 EA034461 B1 EA 034461B1 EA 201691704 A EA201691704 A EA 201691704A EA 201691704 A EA201691704 A EA 201691704A EA 034461 B1 EA034461 B1 EA 034461B1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- stream
- stream containing
- hydrocracking
- zone
- range
- Prior art date
Links
- 238000004517 catalytic hydrocracking Methods 0.000 title claims abstract description 96
- 238000000034 method Methods 0.000 title claims abstract description 88
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 49
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 48
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 24
- 239000010779 crude oil Substances 0.000 claims abstract description 21
- 125000003118 aryl group Chemical group 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- 239000000047 product Substances 0.000 claims description 83
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 68
- 239000001257 hydrogen Substances 0.000 claims description 59
- 229910052739 hydrogen Inorganic materials 0.000 claims description 59
- 239000007789 gas Substances 0.000 claims description 58
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 50
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 45
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 43
- 238000004230 steam cracking Methods 0.000 claims description 40
- 235000013844 butane Nutrition 0.000 claims description 38
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical class CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 38
- 239000001294 propane Substances 0.000 claims description 34
- 239000003915 liquefied petroleum gas Substances 0.000 claims description 30
- 238000000926 separation method Methods 0.000 claims description 25
- 239000001273 butane Substances 0.000 claims description 24
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 24
- 150000001336 alkenes Chemical class 0.000 claims description 20
- 239000003054 catalyst Substances 0.000 claims description 18
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 17
- 239000003921 oil Substances 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 15
- 239000007791 liquid phase Substances 0.000 claims description 13
- 238000009434 installation Methods 0.000 claims description 12
- 238000000197 pyrolysis Methods 0.000 claims description 12
- 239000000725 suspension Substances 0.000 claims description 11
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 10
- 239000012263 liquid product Substances 0.000 claims description 9
- 238000004064 recycling Methods 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 8
- 239000003502 gasoline Substances 0.000 claims description 7
- 238000004227 thermal cracking Methods 0.000 claims description 7
- HOWJQLVNDUGZBI-UHFFFAOYSA-N butane;propane Chemical compound CCC.CCCC HOWJQLVNDUGZBI-UHFFFAOYSA-N 0.000 claims description 6
- 239000000295 fuel oil Substances 0.000 claims description 5
- 150000001491 aromatic compounds Chemical class 0.000 claims description 4
- 239000013067 intermediate product Substances 0.000 claims description 4
- 238000007142 ring opening reaction Methods 0.000 claims description 4
- 239000003209 petroleum derivative Substances 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims description 2
- 238000005984 hydrogenation reaction Methods 0.000 claims description 2
- 239000003348 petrochemical agent Substances 0.000 abstract 2
- 239000000203 mixture Substances 0.000 description 27
- 238000006243 chemical reaction Methods 0.000 description 21
- 125000004432 carbon atom Chemical group C* 0.000 description 19
- 239000007788 liquid Substances 0.000 description 17
- 239000002002 slurry Substances 0.000 description 14
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 150000001335 aliphatic alkanes Chemical class 0.000 description 9
- 238000005336 cracking Methods 0.000 description 9
- 150000002431 hydrogen Chemical class 0.000 description 9
- 238000007327 hydrogenolysis reaction Methods 0.000 description 9
- -1 monoolefin hydrocarbons Chemical class 0.000 description 8
- 238000004821 distillation Methods 0.000 description 7
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 6
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 6
- 239000005977 Ethylene Substances 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 5
- 239000010692 aromatic oil Substances 0.000 description 5
- 239000002283 diesel fuel Substances 0.000 description 5
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 4
- 238000002352 steam pyrolysis Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 238000010791 quenching Methods 0.000 description 3
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000012264 purified product Substances 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 150000003738 xylenes Chemical class 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001412 amines Chemical group 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000020335 dealkylation Effects 0.000 description 1
- 238000006900 dealkylation reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000010795 gaseous waste Substances 0.000 description 1
- GVVPGTZRZFNKDS-JXMROGBWSA-N geranyl diphosphate Chemical compound CC(C)=CCC\C(C)=C\CO[P@](O)(=O)OP(O)(O)=O GVVPGTZRZFNKDS-JXMROGBWSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000010742 number 1 fuel oil Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000006069 physical mixture Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 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
- 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
- C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
-
- 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
-
- 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
- C10G69/06—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 thermal 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
- C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
-
- 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
- C10G2300/1033—Oil well production fluids
-
- 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
-
- 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
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)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP14156638 | 2014-02-25 | ||
| PCT/EP2014/079242 WO2015128046A1 (en) | 2014-02-25 | 2014-12-23 | An integrated hydrocracking process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EA201691704A1 EA201691704A1 (ru) | 2017-02-28 |
| EA034461B1 true EA034461B1 (ru) | 2020-02-11 |
Family
ID=50156661
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EA201691704A EA034461B1 (ru) | 2014-02-25 | 2014-12-23 | Интегрированный способ гидрокрекинга |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US10167434B2 (cg-RX-API-DMAC7.html) |
| EP (1) | EP3110908B1 (cg-RX-API-DMAC7.html) |
| JP (1) | JP6494651B2 (cg-RX-API-DMAC7.html) |
| KR (1) | KR102370265B1 (cg-RX-API-DMAC7.html) |
| CN (1) | CN106062141B (cg-RX-API-DMAC7.html) |
| EA (1) | EA034461B1 (cg-RX-API-DMAC7.html) |
| ES (1) | ES2720268T3 (cg-RX-API-DMAC7.html) |
| SG (1) | SG11201606017SA (cg-RX-API-DMAC7.html) |
| WO (1) | WO2015128046A1 (cg-RX-API-DMAC7.html) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10407630B2 (en) | 2016-11-21 | 2019-09-10 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating solvent deasphalting of vacuum residue |
| US10619112B2 (en) | 2016-11-21 | 2020-04-14 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrotreating and steam cracking |
| US10870807B2 (en) | 2016-11-21 | 2020-12-22 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking, fluid catalytic cracking, and conversion of naphtha into chemical rich reformate |
| US10472579B2 (en) | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrocracking and steam cracking |
| US10472580B2 (en) | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking and conversion of naphtha into chemical rich reformate |
| US10472574B2 (en) | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating delayed coking of vacuum residue |
| US10487276B2 (en) | 2016-11-21 | 2019-11-26 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum residue hydroprocessing |
| US11066611B2 (en) | 2016-11-21 | 2021-07-20 | Saudi Arabian Oil Company | System for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrotreating and steam cracking |
| US20180142167A1 (en) | 2016-11-21 | 2018-05-24 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to chemicals and fuel products integrating steam cracking and fluid catalytic cracking |
| US10487275B2 (en) | 2016-11-21 | 2019-11-26 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum residue conditioning and base oil production |
| 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 |
| EA038032B1 (ru) * | 2017-02-02 | 2021-06-25 | Сабик Глоубл Текнолоджиз Б.В. | Интегрированный способ гидропереработки, парового пиролиза и гидрокрекинга остатка в целях прямой конверсии сырой нефти для получения олефиновых и ароматических нефтехимических продуктов |
| US10793792B2 (en) * | 2017-05-15 | 2020-10-06 | Saudi Arabian Oil Company | Systems and methods for the conversion of heavy oils to petrochemical products |
| KR102472274B1 (ko) * | 2017-07-17 | 2022-12-02 | 사우디 아라비안 오일 컴퍼니 | 중질유 개질에 이은 증류에 의한 중질유 처리 시스템 및 방법 |
| US11220637B2 (en) | 2019-10-30 | 2022-01-11 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating selective hydrogenation and FCC |
| US11220640B2 (en) | 2019-10-30 | 2022-01-11 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating selective hydrogenation, FCC and naphtha reforming |
| US11001773B1 (en) | 2019-10-30 | 2021-05-11 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating selective hydrogenation and selective hydrocracking |
| US11091709B2 (en) | 2019-10-30 | 2021-08-17 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating selective hydrogenation, ring opening and naphtha reforming |
| US11091708B2 (en) | 2019-10-30 | 2021-08-17 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating selective hydrogenation and ring opening |
| US11390818B2 (en) | 2019-10-30 | 2022-07-19 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating hydrodealkylation |
| US11377609B2 (en) | 2019-10-30 | 2022-07-05 | Saudi Arabian Oil Company | System and process for steam cracking and PFO treatment integrating hydrodealkylation and naphtha reforming |
| US11566188B2 (en) * | 2020-05-22 | 2023-01-31 | ExxonMobil Technology and Engineering Company | Methods of whole crude and whole crude wide cut hydrotreating low hetroatom content petroleum |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3839484A (en) * | 1970-07-17 | 1974-10-01 | Marathon Oil Co | Pyrolyzing hydrocracked naphthas to produce unsaturated hydrocarbons |
| US4137147A (en) * | 1976-09-16 | 1979-01-30 | Institut Francais Du Petrole | Process for manufacturing olefinic hydrocarbons with respectively two and three carbon atoms per molecule |
| US20070062848A1 (en) * | 2005-09-20 | 2007-03-22 | Nova Chemicals (International) S.A. | Aromatic saturation and ring opening process |
| US20130248417A1 (en) * | 2012-03-20 | 2013-09-26 | Saudi Arabian Oil Company | Integrated hydroprocessing, steam pyrolysis and slurry hydroprocessing of crude oil to produce petrochemicals |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE793036A (fr) * | 1971-12-21 | 1973-04-16 | Pierrefitte Auby Sa | Procede de craquage sous pression d'hydrogene pour la production d'olefines |
| JPS5898389A (ja) | 1981-12-08 | 1983-06-11 | Honda Motor Co Ltd | ガスホ−ルの製造方法 |
| FI852865A7 (fi) | 1984-07-25 | 1986-01-26 | Air Prod & Chem | Parannettu katalyytti hiilivetyjen dehydrausta varten. |
| FI860203L (fi) | 1985-01-22 | 1986-07-23 | Air Prod & Chem | Dehydroisomerisering av kolvaeten. |
| US4827072A (en) | 1986-06-06 | 1989-05-02 | Uop Inc. | Dehydrogenation catalyst composition and hydrocarbon dehydrogenation process |
| US4926005A (en) | 1989-05-17 | 1990-05-15 | Phillips Petroleum Company | Dehydrogenation process |
| US6270654B1 (en) | 1993-08-18 | 2001-08-07 | Ifp North America, Inc. | Catalytic hydrogenation process utilizing multi-stage ebullated bed reactors |
| FR2764902B1 (fr) | 1997-06-24 | 1999-07-16 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres comprenant une etape de conversion en lit bouillonnant et une etape d'hydrocraquage |
| US7214308B2 (en) | 2003-02-21 | 2007-05-08 | Institut Francais Du Petrole | Effective integration of solvent deasphalting and ebullated-bed processing |
| KR100710542B1 (ko) | 2005-06-21 | 2007-04-24 | 에스케이 주식회사 | 탄화수소 원료 혼합물로부터 경질 올레핀계 탄화수소의증산방법 |
| US7622623B2 (en) | 2005-09-02 | 2009-11-24 | Sud-Chemie Inc. | Catalytically inactive heat generator and improved dehydrogenation process |
| US7704377B2 (en) | 2006-03-08 | 2010-04-27 | Institut Francais Du Petrole | 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 |
| US20080093262A1 (en) | 2006-10-24 | 2008-04-24 | Andrea Gragnani | Process and installation for conversion of heavy petroleum fractions in a fixed bed with integrated production of middle distillates with a very low sulfur content |
| US7938952B2 (en) | 2008-05-20 | 2011-05-10 | Institute Francais Du Petrole | Process for multistage residue hydroconversion integrated with straight-run and conversion gasoils hydroconversion steps |
| FR2951735B1 (fr) | 2009-10-23 | 2012-08-03 | Inst Francais Du Petrole | Procede de conversion de residu integrant une technologie lit mobile et une technologie lit bouillonnant |
| 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 |
| FR2981659B1 (fr) | 2011-10-20 | 2013-11-01 | Ifp Energies Now | Procede de conversion de charges petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement en lit fixe pour la production de fiouls a basse teneur en soufre |
| EP2828362B1 (en) * | 2012-03-20 | 2020-12-30 | Saudi Arabian Oil Company | Integrated slurry hydroprocessing and steam pyrolysis of crude oil to produce petrochemicals |
| SG11201508904WA (en) | 2013-07-02 | 2016-01-28 | Saudi Basic Ind Corp | Method for cracking a hydrocarbon feedstock in a steam cracker unit |
| CN105358660B (zh) | 2013-07-02 | 2018-06-29 | 沙特基础工业公司 | 用于在蒸汽裂化器单元中裂化烃原料的方法 |
| EP3110925B1 (en) | 2014-02-25 | 2018-12-05 | Saudi Basic Industries Corporation | An integrated hydrocracking process |
| KR102370164B1 (ko) | 2014-02-25 | 2022-03-04 | 사빅 글로벌 테크놀러지스 비.브이. | 통합된 수소화분해 공정 |
| FR3027912B1 (fr) | 2014-11-04 | 2018-04-27 | IFP Energies Nouvelles | Procede de production de combustibles de type fuel lourd a partir d'une charge hydrocarbonee lourde utilisant une separation entre l'etape d'hydrotraitement et l'etape d'hydrocraquage |
| FR3027911B1 (fr) | 2014-11-04 | 2018-04-27 | IFP Energies Nouvelles | Procede de conversion de charges petrolieres comprenant une etape d'hydrocraquage en lit bouillonnant, une etape de maturation et une etape de separation des sediments pour la production de fiouls a basse teneur en sediments |
| FR3033797B1 (fr) | 2015-03-16 | 2018-12-07 | IFP Energies Nouvelles | Procede ameliore de conversion de charges hydrocarbonees lourdes |
-
2014
- 2014-12-23 CN CN201480076104.9A patent/CN106062141B/zh active Active
- 2014-12-23 KR KR1020167026462A patent/KR102370265B1/ko active Active
- 2014-12-23 JP JP2016554180A patent/JP6494651B2/ja not_active Expired - Fee Related
- 2014-12-23 US US15/121,237 patent/US10167434B2/en active Active
- 2014-12-23 ES ES14824007T patent/ES2720268T3/es active Active
- 2014-12-23 EP EP14824007.0A patent/EP3110908B1/en active Active
- 2014-12-23 EA EA201691704A patent/EA034461B1/ru not_active IP Right Cessation
- 2014-12-23 SG SG11201606017SA patent/SG11201606017SA/en unknown
- 2014-12-23 WO PCT/EP2014/079242 patent/WO2015128046A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3839484A (en) * | 1970-07-17 | 1974-10-01 | Marathon Oil Co | Pyrolyzing hydrocracked naphthas to produce unsaturated hydrocarbons |
| US4137147A (en) * | 1976-09-16 | 1979-01-30 | Institut Francais Du Petrole | Process for manufacturing olefinic hydrocarbons with respectively two and three carbon atoms per molecule |
| US20070062848A1 (en) * | 2005-09-20 | 2007-03-22 | Nova Chemicals (International) S.A. | Aromatic saturation and ring opening process |
| US20130248417A1 (en) * | 2012-03-20 | 2013-09-26 | Saudi Arabian Oil Company | Integrated hydroprocessing, steam pyrolysis and slurry hydroprocessing of crude oil to produce petrochemicals |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106062141B (zh) | 2019-07-09 |
| US10167434B2 (en) | 2019-01-01 |
| KR20160125502A (ko) | 2016-10-31 |
| US20170009155A1 (en) | 2017-01-12 |
| KR102370265B1 (ko) | 2022-03-04 |
| EA201691704A1 (ru) | 2017-02-28 |
| JP2017511831A (ja) | 2017-04-27 |
| ES2720268T3 (es) | 2019-07-19 |
| SG11201606017SA (en) | 2016-08-30 |
| EP3110908A1 (en) | 2017-01-04 |
| CN106062141A (zh) | 2016-10-26 |
| JP6494651B2 (ja) | 2019-04-03 |
| WO2015128046A1 (en) | 2015-09-03 |
| EP3110908B1 (en) | 2019-01-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EA034461B1 (ru) | Интегрированный способ гидрокрекинга | |
| JP6494650B2 (ja) | 統合水素化分解処理 | |
| CN106062149B (zh) | 集成加氢裂化方法 | |
| KR102374392B1 (ko) | 탄화수소를 올레핀으로 전환하는 공정 | |
| EA029413B1 (ru) | Способ крекинга углеводородного сырья в установке парового крекинга | |
| KR102375007B1 (ko) | 탄화수소를 올레핀으로 전환하는 공정 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): AM AZ BY KZ KG TJ TM |