KR102370164B1 - 통합된 수소화분해 공정 - Google Patents
통합된 수소화분해 공정 Download PDFInfo
- Publication number
- KR102370164B1 KR102370164B1 KR1020167026421A KR20167026421A KR102370164B1 KR 102370164 B1 KR102370164 B1 KR 102370164B1 KR 1020167026421 A KR1020167026421 A KR 1020167026421A KR 20167026421 A KR20167026421 A KR 20167026421A KR 102370164 B1 KR102370164 B1 KR 102370164B1
- Authority
- KR
- South Korea
- Prior art keywords
- stream
- unit
- propane
- hydrocracking
- hydrogen
- 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.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 108
- 238000004517 catalytic hydrocracking Methods 0.000 title claims abstract description 77
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 43
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 40
- 150000001336 alkenes Chemical class 0.000 claims abstract description 27
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 23
- 239000010779 crude oil Substances 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 14
- 239000003348 petrochemical agent Substances 0.000 claims abstract description 11
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 72
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 57
- 239000001257 hydrogen Substances 0.000 claims description 55
- 229910052739 hydrogen Inorganic materials 0.000 claims description 55
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 48
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 42
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 41
- 239000001273 butane Substances 0.000 claims description 38
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 38
- 239000001294 propane Substances 0.000 claims description 36
- 239000007788 liquid Substances 0.000 claims description 28
- 238000000926 separation method Methods 0.000 claims description 25
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 16
- 150000002431 hydrogen Chemical class 0.000 claims description 14
- 238000000197 pyrolysis Methods 0.000 claims description 13
- HOWJQLVNDUGZBI-UHFFFAOYSA-N butane;propane Chemical compound CCC.CCCC HOWJQLVNDUGZBI-UHFFFAOYSA-N 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 8
- 238000010992 reflux Methods 0.000 claims description 8
- 239000000295 fuel oil Substances 0.000 claims description 5
- 239000000047 product Substances 0.000 description 38
- 235000013844 butane Nutrition 0.000 description 36
- 238000004230 steam cracking Methods 0.000 description 26
- 239000000203 mixture Substances 0.000 description 25
- 239000003915 liquefied petroleum gas Substances 0.000 description 24
- 125000004432 carbon atom Chemical group C* 0.000 description 19
- 238000006243 chemical reaction Methods 0.000 description 19
- 239000007789 gas Substances 0.000 description 18
- 239000003054 catalyst Substances 0.000 description 17
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- 150000001335 aliphatic alkanes Chemical class 0.000 description 9
- 125000003118 aryl group Chemical group 0.000 description 9
- 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
- 238000002352 steam pyrolysis Methods 0.000 description 7
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-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
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000005336 cracking Methods 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 239000002002 slurry Substances 0.000 description 6
- 150000004945 aromatic hydrocarbons Chemical class 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
- -1 monoolefin hydrocarbon Chemical class 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 239000003502 gasoline Substances 0.000 description 3
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 238000003385 ring cleavage reaction Methods 0.000 description 3
- 238000007142 ring opening reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 238000005194 fractionation Methods 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
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000012264 purified product Substances 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006229 carbon black Substances 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
- 238000009903 catalytic hydrogenation reaction Methods 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
- 239000000571 coke Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000020335 dealkylation Effects 0.000 description 1
- 238000006900 dealkylation reaction Methods 0.000 description 1
- 238000005235 decoking Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000007327 hydrogenolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052976 metal sulfide Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 239000006069 physical mixture Substances 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- FHYUCVWDMABHHH-UHFFFAOYSA-N toluene;1,2-xylene Chemical group CC1=CC=CC=C1.CC1=CC=CC=C1C FHYUCVWDMABHHH-UHFFFAOYSA-N 0.000 description 1
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/04—Thermal processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
- C10G47/26—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/22—Separation of effluents
-
- 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
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial 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
- 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
- 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
- C10G69/08—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 reforming naphtha
- C10G69/10—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 reforming naphtha hydrocracking of higher boiling fractions into naphtha and reforming the naphtha obtained
-
- 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
- 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
- C10G2400/22—Higher 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)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (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)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP14156636.4 | 2014-02-25 | ||
| EP14156636 | 2014-02-25 | ||
| PCT/EP2014/079238 WO2015128045A1 (en) | 2014-02-25 | 2014-12-23 | An integrated hydrocracking process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR20160125493A KR20160125493A (ko) | 2016-10-31 |
| KR102370164B1 true KR102370164B1 (ko) | 2022-03-04 |
Family
ID=50156659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1020167026421A Active KR102370164B1 (ko) | 2014-02-25 | 2014-12-23 | 통합된 수소화분해 공정 |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US9856424B2 (enExample) |
| EP (1) | EP3110926B1 (enExample) |
| JP (1) | JP6506312B2 (enExample) |
| KR (1) | KR102370164B1 (enExample) |
| CN (1) | CN106062149B (enExample) |
| EA (1) | EA034669B1 (enExample) |
| ES (1) | ES2715410T3 (enExample) |
| SG (1) | SG11201606013VA (enExample) |
| WO (1) | WO2015128045A1 (enExample) |
Families Citing this family (36)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10167434B2 (en) | 2014-02-25 | 2019-01-01 | Saudi Basic Industries Corporation | Integrated hydrocracking process |
| US10844296B2 (en) * | 2017-01-04 | 2020-11-24 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10851316B2 (en) | 2017-01-04 | 2020-12-01 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| CN110709492A (zh) | 2017-06-05 | 2020-01-17 | 沙特基础工业全球技术公司 | 原油向低沸点化学原料的转化 |
| EP3668950A1 (en) * | 2017-08-15 | 2020-06-24 | SABIC Global Technologies B.V. | Process and system for cracking a hydrocarbon feed |
| EP3802741B1 (en) | 2018-05-30 | 2022-06-29 | TotalEnergies OneTech Belgium | Renewable diesel fuel production in retrofitted fossil petroleum refinery to produce biofuel and bio-feedstock for steam crackers |
| JP7572385B2 (ja) * | 2019-06-24 | 2024-10-23 | ダウ グローバル テクノロジーズ エルエルシー | 蒸気分解と流動接触脱水素化との統合システムにおけるアセチレン水素化ユニットを操作するための方法 |
| KR102883867B1 (ko) | 2019-06-24 | 2025-11-10 | 다우 글로벌 테크놀로지스 엘엘씨 | 올레핀을 제조하기 위한 통합된 화학 처리 시스템을 작동하는 방법 |
| CA3143186A1 (en) | 2019-06-24 | 2020-12-30 | Dow Global Technologies Llc | Methods for operating acetylene hydrogenation units during integration of chemical processing systems for producing olefins |
| US11193072B2 (en) | 2019-12-03 | 2021-12-07 | Saudi Arabian Oil Company | Processing facility to form hydrogen and petrochemicals |
| US11572517B2 (en) | 2019-12-03 | 2023-02-07 | Saudi Arabian Oil Company | Processing facility to produce hydrogen and petrochemicals |
| US11426708B2 (en) | 2020-03-02 | 2022-08-30 | King Abdullah University Of Science And Technology | Potassium-promoted red mud as a catalyst for forming hydrocarbons from carbon dioxide |
| US11492255B2 (en) | 2020-04-03 | 2022-11-08 | Saudi Arabian Oil Company | Steam methane reforming with steam regeneration |
| US11420915B2 (en) | 2020-06-11 | 2022-08-23 | Saudi Arabian Oil Company | Red mud as a catalyst for the isomerization of olefins |
| US11495814B2 (en) | 2020-06-17 | 2022-11-08 | Saudi Arabian Oil Company | Utilizing black powder for electrolytes for flow batteries |
| US12000056B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Tandem electrolysis cell |
| US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| US11999619B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Hydrogen production with membrane reactor |
| US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| EP3992172A1 (de) * | 2020-10-29 | 2022-05-04 | Linde GmbH | Verfahren und anlage zur herstellung von olefinen |
| US11814289B2 (en) | 2021-01-04 | 2023-11-14 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via steam reforming |
| US11427519B2 (en) | 2021-01-04 | 2022-08-30 | Saudi Arabian Oil Company | Acid modified red mud as a catalyst for olefin isomerization |
| US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
| US11724943B2 (en) | 2021-01-04 | 2023-08-15 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via dry reforming |
| US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-reforming |
| US12220666B2 (en) | 2021-01-12 | 2025-02-11 | Saudi Arabian Oil Company | Ultrathin membrane fabrication |
| US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
| US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
| US12258272B2 (en) | 2021-08-12 | 2025-03-25 | Saudi Arabian Oil Company | Dry reforming of methane using a nickel-based bi-metallic catalyst |
| US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
| US12018392B2 (en) | 2022-01-03 | 2024-06-25 | Saudi Arabian Oil Company | Methods for producing syngas from H2S and CO2 in an electrochemical cell |
| US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
| US11732202B1 (en) * | 2022-03-24 | 2023-08-22 | Saudi Arabia Oil Company | Integration process for pyrolysis oil upgrading with maximized BTX yield |
| WO2024075042A1 (en) * | 2022-10-04 | 2024-04-11 | Sabic Global Technologies B.V. | Methods and systems for integrating petrochemical and refinery operations |
| KR20240051740A (ko) * | 2022-10-13 | 2024-04-22 | 주식회사 엘지화학 | 분해로 연료의 제조 방법 |
| CN118440733B (zh) * | 2023-02-03 | 2025-07-01 | 中国石油化工股份有限公司 | 一种生产化工原料的加氢裂化方法 |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130248418A1 (en) | 2012-03-20 | 2013-09-26 | Saudi Arabian Oil Company | Integrated slurry hydroprocessing and steam pyrolysis of crude oil to produce petrochemicals |
Family Cites Families (11)
| 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 |
| BE793036A (fr) * | 1971-12-21 | 1973-04-16 | Pierrefitte Auby Sa | Procede de craquage sous pression d'hydrogene pour la production d'olefines |
| 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 |
| FI852865A7 (fi) | 1984-07-25 | 1986-01-26 | Air Prod & Chem | Parannettu katalyytti hiilivetyjen dehydrausta varten. |
| FI860203A7 (fi) | 1985-01-22 | 1986-07-23 | Air Prod & Chem | Hiilivetyjen dehydroisomerointi. |
| 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 |
| 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 |
| CA2541051C (en) | 2005-09-20 | 2013-04-02 | Nova Chemicals Corporation | Aromatic saturation and ring opening process |
| CN104245890B (zh) | 2012-03-20 | 2016-08-24 | 沙特阿拉伯石油公司 | 对原油进行集成加氢处理、蒸汽热解和浆液加氢处理以生产石油化学产品 |
-
2014
- 2014-12-23 SG SG11201606013VA patent/SG11201606013VA/en unknown
- 2014-12-23 JP JP2016570168A patent/JP6506312B2/ja not_active Expired - Fee Related
- 2014-12-23 WO PCT/EP2014/079238 patent/WO2015128045A1/en not_active Ceased
- 2014-12-23 ES ES14816334T patent/ES2715410T3/es active Active
- 2014-12-23 CN CN201480076217.9A patent/CN106062149B/zh active Active
- 2014-12-23 EA EA201691711A patent/EA034669B1/ru not_active IP Right Cessation
- 2014-12-23 EP EP14816334.8A patent/EP3110926B1/en active Active
- 2014-12-23 US US15/121,069 patent/US9856424B2/en active Active
- 2014-12-23 KR KR1020167026421A patent/KR102370164B1/ko active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130248418A1 (en) | 2012-03-20 | 2013-09-26 | Saudi Arabian Oil Company | Integrated slurry hydroprocessing and steam pyrolysis of crude oil to produce petrochemicals |
Also Published As
| Publication number | Publication date |
|---|---|
| ES2715410T3 (es) | 2019-06-04 |
| EA034669B1 (ru) | 2020-03-04 |
| JP2017511835A (ja) | 2017-04-27 |
| SG11201606013VA (en) | 2016-08-30 |
| CN106062149A (zh) | 2016-10-26 |
| EP3110926B1 (en) | 2018-12-12 |
| JP6506312B2 (ja) | 2019-04-24 |
| US9856424B2 (en) | 2018-01-02 |
| US20160362616A1 (en) | 2016-12-15 |
| CN106062149B (zh) | 2018-09-21 |
| EA201691711A1 (ru) | 2017-02-28 |
| WO2015128045A1 (en) | 2015-09-03 |
| KR20160125493A (ko) | 2016-10-31 |
| EP3110926A1 (en) | 2017-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR102370164B1 (ko) | 통합된 수소화분해 공정 | |
| KR102370265B1 (ko) | 통합된 수소화분해 공정 | |
| JP6470760B2 (ja) | エチレンおよびbtxの収率が改善された、原油を石油化学製品に転化するための方法および装置 | |
| KR102370172B1 (ko) | 통합된 수소화분해 공정 | |
| JP6879990B2 (ja) | 原油を石油化学製品に転化する、炭素利用率の改善された方法および装置 | |
| KR102374392B1 (ko) | 탄화수소를 올레핀으로 전환하는 공정 | |
| CN105358661A (zh) | 用于将原油转化成具有改进的丙烯产率的石化品的方法和设施 | |
| KR102375007B1 (ko) | 탄화수소를 올레핀으로 전환하는 공정 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PA0105 | International application |
Patent event date: 20160923 Patent event code: PA01051R01D Comment text: International Patent Application |
|
| PG1501 | Laying open of application | ||
| PA0201 | Request for examination |
Patent event code: PA02012R01D Patent event date: 20191220 Comment text: Request for Examination of Application |
|
| E902 | Notification of reason for refusal | ||
| PE0902 | Notice of grounds for rejection |
Comment text: Notification of reason for refusal Patent event date: 20210625 Patent event code: PE09021S01D |
|
| E701 | Decision to grant or registration of patent right | ||
| PE0701 | Decision of registration |
Patent event code: PE07011S01D Comment text: Decision to Grant Registration Patent event date: 20211129 |
|
| GRNT | Written decision to grant | ||
| PR0701 | Registration of establishment |
Comment text: Registration of Establishment Patent event date: 20220228 Patent event code: PR07011E01D |
|
| PR1002 | Payment of registration fee |
Payment date: 20220302 End annual number: 3 Start annual number: 1 |
|
| PG1601 | Publication of registration |