KR102290668B1 - 증기 분해기 단위에서 탄화수소 공급원료를 분해하는 방법 - Google Patents
증기 분해기 단위에서 탄화수소 공급원료를 분해하는 방법 Download PDFInfo
- Publication number
- KR102290668B1 KR102290668B1 KR1020157036205A KR20157036205A KR102290668B1 KR 102290668 B1 KR102290668 B1 KR 102290668B1 KR 1020157036205 A KR1020157036205 A KR 1020157036205A KR 20157036205 A KR20157036205 A KR 20157036205A KR 102290668 B1 KR102290668 B1 KR 102290668B1
- Authority
- KR
- South Korea
- Prior art keywords
- stream
- paraffins
- unit
- hydrocracking
- steam cracker
- 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
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 87
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 78
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 58
- 238000005336 cracking Methods 0.000 title claims abstract description 15
- 238000000034 method Methods 0.000 title claims description 132
- 238000004517 catalytic hydrocracking Methods 0.000 claims abstract description 77
- 239000001257 hydrogen Substances 0.000 claims abstract description 45
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 45
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 40
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 230000008569 process Effects 0.000 claims description 109
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 51
- 239000007789 gas Substances 0.000 claims description 47
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 28
- 238000004821 distillation Methods 0.000 claims description 21
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 19
- 239000001273 butane Substances 0.000 claims description 17
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 17
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 17
- 238000000638 solvent extraction Methods 0.000 claims description 16
- 238000000926 separation method Methods 0.000 claims description 15
- 239000001294 propane Substances 0.000 claims description 14
- 239000003350 kerosene Substances 0.000 claims description 7
- 239000002002 slurry Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims 1
- 239000000047 product Substances 0.000 description 45
- 125000003118 aryl group Chemical group 0.000 description 38
- 239000003054 catalyst Substances 0.000 description 33
- 239000000203 mixture Substances 0.000 description 30
- 150000001336 alkenes Chemical class 0.000 description 25
- 239000010779 crude oil Substances 0.000 description 24
- 239000003921 oil Substances 0.000 description 22
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 18
- 238000004230 steam cracking Methods 0.000 description 18
- 150000001335 aliphatic alkanes Chemical class 0.000 description 16
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 15
- 238000009835 boiling Methods 0.000 description 14
- 239000000126 substance Substances 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 13
- -1 naphtha Substances 0.000 description 12
- 238000000197 pyrolysis Methods 0.000 description 12
- 239000002904 solvent Substances 0.000 description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 11
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 11
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 10
- 239000005977 Ethylene Substances 0.000 description 10
- 239000006227 byproduct Substances 0.000 description 9
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 9
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 9
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 8
- 239000003915 liquefied petroleum gas Substances 0.000 description 8
- 238000012545 processing Methods 0.000 description 8
- 125000004432 carbon atom Chemical group C* 0.000 description 7
- 239000000446 fuel Substances 0.000 description 7
- 239000003502 gasoline Substances 0.000 description 7
- 150000002431 hydrogen Chemical class 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 239000012188 paraffin wax Substances 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 7
- 238000007142 ring opening reaction Methods 0.000 description 7
- 239000000377 silicon dioxide Substances 0.000 description 7
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 6
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 6
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 239000008186 active pharmaceutical agent Substances 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 229910052976 metal sulfide Inorganic materials 0.000 description 6
- 239000008096 xylene Substances 0.000 description 6
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 5
- 238000000605 extraction Methods 0.000 description 5
- 239000002737 fuel gas Substances 0.000 description 5
- 238000005984 hydrogenation reaction Methods 0.000 description 5
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 5
- 229910052697 platinum Inorganic materials 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
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000006229 carbon black Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 4
- 229910052750 molybdenum Inorganic materials 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 238000003385 ring cleavage reaction Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 229910052721 tungsten Inorganic materials 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 230000036961 partial effect Effects 0.000 description 3
- 239000003348 petrochemical agent Substances 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 238000010926 purge Methods 0.000 description 3
- 238000010791 quenching Methods 0.000 description 3
- 230000007017 scission Effects 0.000 description 3
- 239000010454 slate Substances 0.000 description 3
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 229920006272 aromatic hydrocarbon resin Polymers 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000001588 bifunctional effect Effects 0.000 description 2
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005235 decoking Methods 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 229910052733 gallium Inorganic materials 0.000 description 2
- 229910052738 indium Inorganic materials 0.000 description 2
- 229910052741 iridium Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 229910052703 rhodium Inorganic materials 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- NEZHKHMZNSFKGS-UHFFFAOYSA-N 1-(4-fluorophenyl)-2-(methylamino)butan-1-one Chemical compound CCC(NC)C(=O)C1=CC=C(F)C=C1 NEZHKHMZNSFKGS-UHFFFAOYSA-N 0.000 description 1
- 101100439288 Bombyx mori nuclear polyhedrosis virus CG30 gene Proteins 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- 101100272680 Paracentrotus lividus BP10 gene Proteins 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 238000001833 catalytic reforming Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000001010 compromised effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000006184 cosolvent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 150000001924 cycloalkanes Chemical class 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000004231 fluid catalytic cracking Methods 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 238000007327 hydrogenolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000006069 physical mixture Substances 0.000 description 1
- 229910003446 platinum oxide Inorganic materials 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- UWHCKJMYHZGTIT-UHFFFAOYSA-N tetraethylene glycol Chemical compound OCCOCCOCCOCCO UWHCKJMYHZGTIT-UHFFFAOYSA-N 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/06—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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
- C10G67/0409—Extraction of unsaturated hydrocarbons
- C10G67/0445—The hydrotreatment being a hydrocracking
-
- 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
- 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
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1051—Kerosene having a boiling range of about 180 - 230 °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
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °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
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °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
- C10G2300/1081—Alkanes
- C10G2300/1085—Solid paraffins
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
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)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13174781 | 2013-07-02 | ||
| EP13174781.8 | 2013-07-02 | ||
| PCT/EP2014/063848 WO2015000840A1 (en) | 2013-07-02 | 2014-06-30 | Method for cracking a hydrocarbon feedstock in a steam cracker unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR20160025511A KR20160025511A (ko) | 2016-03-08 |
| KR102290668B1 true KR102290668B1 (ko) | 2021-08-19 |
Family
ID=48700466
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1020157036205A Active KR102290668B1 (ko) | 2013-07-02 | 2014-06-30 | 증기 분해기 단위에서 탄화수소 공급원료를 분해하는 방법 |
Country Status (9)
| Country | Link |
|---|---|
| US (2) | US10526553B2 (enExample) |
| EP (1) | EP3017025B1 (enExample) |
| JP (2) | JP6795976B2 (enExample) |
| KR (1) | KR102290668B1 (enExample) |
| CN (2) | CN105555925A (enExample) |
| EA (1) | EA029413B1 (enExample) |
| ES (1) | ES2671320T3 (enExample) |
| SG (1) | SG11201508904WA (enExample) |
| WO (1) | WO2015000840A1 (enExample) |
Families Citing this family (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106062141B (zh) | 2014-02-25 | 2019-07-09 | 沙特基础工业公司 | 集成加氢裂化方法 |
| EP3389842B1 (en) | 2015-12-14 | 2020-01-29 | SABIC Global Technologies B.V. | Process for converting lpg to higher hydrocarbon(s) |
| US20190024000A1 (en) | 2015-12-22 | 2019-01-24 | Sabic Global Technologies B.V. | Process for converting mixed hydrocarbon streams to lpg and btx |
| JP7034173B2 (ja) * | 2017-04-07 | 2022-03-11 | シュミット ウント クレメンス ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフト | 炭化水素を熱分解するための管および装置 |
| US10899979B2 (en) | 2017-08-15 | 2021-01-26 | Sabic Global Technologies, B.V. | Light olefin production via an integrated steam cracking and hydrocracking process |
| WO2019036291A1 (en) * | 2017-08-15 | 2019-02-21 | Sabic Global Technologies B.V. | SHALE GAS AND CONDENSATE GIVING CHEMICALS |
| WO2019162392A1 (en) | 2018-02-22 | 2019-08-29 | Total Research & Technology Feluy | Selective conversion of paraffinic naphtha to propane in the presence of hydrogen |
| US11772082B1 (en) | 2018-06-21 | 2023-10-03 | Avn Corporation | Catalyst supports—composition and process of manufacture |
| WO2019245859A1 (en) * | 2018-06-21 | 2019-12-26 | The J. David Gladstone Institutes | Generation of a population of hindbrain cells and hindbrain-like organoids from pluripotent stem cells |
| US12065398B2 (en) | 2019-01-15 | 2024-08-20 | Sabic Global Technologies B.V. | Use of renewable energy in methanol synthesis |
| WO2020242921A1 (en) | 2019-05-24 | 2020-12-03 | Eastman Chemical Company | Recycle content cellulose ester |
| US11946000B2 (en) | 2019-05-24 | 2024-04-02 | Eastman Chemical Company | Blend small amounts of pyoil into a liquid stream processed into a gas cracker |
| WO2020247192A1 (en) | 2019-05-24 | 2020-12-10 | Eastman Chemical Company | Recycle content cracked effluent |
| FI128804B (en) * | 2019-06-10 | 2020-12-31 | Neste Oyj | METHOD FOR PROCESSING PLASTIC WASTE PYROLYL GAS |
| CN114008179A (zh) * | 2019-07-15 | 2022-02-01 | 沙特基础工业全球技术有限公司 | 用于制备未氢化和氢化的c9+化合物的系统和方法 |
| EP4003948A4 (en) | 2019-07-29 | 2023-09-06 | Eastman Chemical Company | Recycle content (c4)alkanal |
| US11046899B2 (en) | 2019-10-03 | 2021-06-29 | Saudi Arabian Oil Company | Two stage hydrodearylation systems and processes to convert heavy aromatics into gasoline blending components and chemical grade aromatics |
| KR20220091549A (ko) | 2019-10-31 | 2022-06-30 | 이스트만 케미칼 컴파니 | 재활용된 폐기물을 위한 열분해 방법 및 시스템 |
| CN120442278A (zh) * | 2019-10-31 | 2025-08-08 | 伊士曼化工公司 | 用于回收废物的热解方法和系统 |
| US11945998B2 (en) | 2019-10-31 | 2024-04-02 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
| US11319262B2 (en) | 2019-10-31 | 2022-05-03 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
| EP4055001A4 (en) | 2019-11-07 | 2024-02-14 | Eastman Chemical Company | MIXED ESTERS AND SOLVENTS WITH RECYCLED CONTENTS |
| EP4054997A4 (en) | 2019-11-07 | 2024-02-21 | Eastman Chemical Company | ALPHA-OLEFINS AND FAT ALCOHOLS WITH RECYCLING CONTENT |
| CN113004935A (zh) * | 2019-12-20 | 2021-06-22 | 中国石油化工股份有限公司 | 蒸汽裂解方法 |
| US11713287B2 (en) * | 2020-02-14 | 2023-08-01 | Sabic Global Technologies B.V. | Energy efficient steam cracking process |
| CN113527026A (zh) * | 2020-04-21 | 2021-10-22 | 国家能源投资集团有限责任公司 | 用于将轻质烷烃转化成芳香族化合物的系统和方法 |
| US11046898B1 (en) * | 2020-05-15 | 2021-06-29 | Saudi Arabian Oil Company | Systems and processes for separating and upgrading hydrocarbons integrating a refinery system with steam cracking of an aromatic bottoms stream |
| CA3194184A1 (en) | 2020-09-28 | 2022-03-31 | Chevron Phillips Chemical Company Lp | Circular chemicals or polymers from pyrolyzed plastic waste and the use of mass balance accounting to allow for crediting the resultant products as circular |
| US20230407186A1 (en) * | 2020-11-02 | 2023-12-21 | Lummus Technology Llc | Electric furnace to produce olefins |
| AU2022258316A1 (en) | 2021-04-16 | 2023-10-05 | Chevron Phillips Chemical Company Lp | Pyrolysis of plastic waste to produce light gaseous hydrocarbons and integration with an ethylene cracker |
| US12195674B2 (en) | 2021-09-21 | 2025-01-14 | Eastman Chemical Company | Using spent caustic solution from pygas treatment to neutralize halogens from liquified waste plastic |
| EP4551669A1 (en) * | 2022-07-09 | 2025-05-14 | SABIC Global Technologies B.V. | Systems and processes for the production of olefinic products |
| KR20240051740A (ko) * | 2022-10-13 | 2024-04-22 | 주식회사 엘지화학 | 분해로 연료의 제조 방법 |
| US20240190792A1 (en) * | 2022-12-09 | 2024-06-13 | Uop Llc | Integration of naphtha to ethane and propane fractionation section with ethane steam cracker |
| US20240352342A1 (en) * | 2023-04-19 | 2024-10-24 | Sk Innovation Co., Ltd. | Method and system for producing refined hydrocarbons from waste plastic pyrolysis oil |
| US20240352345A1 (en) * | 2023-04-19 | 2024-10-24 | Sk Innovation Co., Ltd. | Method and system for producing refined hydrocarbons from waste plastics |
| JP2025103173A (ja) * | 2023-12-27 | 2025-07-09 | 三菱重工業株式会社 | メタネーション装置、メタネーション方法、炭化水素の直接分解装置、及び炭化水素の直接分解方法 |
| US20250270154A1 (en) * | 2024-02-23 | 2025-08-28 | Uop Llc | Process for separating paraffins |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010052241A1 (en) * | 2000-04-13 | 2001-12-20 | Ipsi Llc | Flexible reflux process for high NGL recovery |
Family Cites Families (51)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3172834A (en) * | 1965-03-09 | Process for manufacturing gasoline by blending the hydrocracked gasoline with the dehydrogenated and alkyl- ated products obtained from the hy- drocracking stage | ||
| US3023158A (en) * | 1960-03-21 | 1962-02-27 | Universal Oil Prod Co | Increasing the yield of gasoline boiling range product from heavy petroleum stocks |
| US3256176A (en) | 1964-10-21 | 1966-06-14 | Phillips Petroleum Co | Hydrocracking heavy hydrocarbons to gasoline and distillate |
| NL141240B (nl) | 1966-08-02 | 1974-02-15 | Shell Int Research | Werkwijze voor de bereiding van etheen door thermisch kraken van een hydrokraakfractie. |
| US3433848A (en) | 1966-08-10 | 1969-03-18 | Texaco Inc | Method of controlling selectivity in an aromatic hydrocarbon dealkylation process |
| GB1250615A (enExample) | 1968-05-02 | 1971-10-20 | ||
| JPS4914721B1 (enExample) * | 1970-08-11 | 1974-04-10 | ||
| BE793036A (fr) | 1971-12-21 | 1973-04-16 | Pierrefitte Auby Sa | Procede de craquage sous pression d'hydrogene pour la production d'olefines |
| CH564050A5 (enExample) | 1972-04-06 | 1975-07-15 | Sandoz Ag | |
| US3944481A (en) | 1973-11-05 | 1976-03-16 | The Dow Chemical Company | Conversion of crude oil fractions to olefins |
| JPS5295601A (en) | 1976-02-04 | 1977-08-11 | Dow Chemical Co | Improvement in method of conversing crude oil fraction to olefins |
| DE2708412A1 (de) | 1976-06-03 | 1977-12-15 | Hydrocarbon Research Inc | Kombinationsverfahren zur herstellung von aethylen |
| FR2364879A1 (fr) | 1976-09-16 | 1978-04-14 | Inst Francais Du Petrole | Procede de fabrication d'hydrocarbures olefiniques a deux et trois atomes de carbone par molecule |
| 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 |
| US4247386A (en) | 1979-08-06 | 1981-01-27 | Mobil Oil Corporation | Conversion of hydrocarbons to olefins |
| JPS58219130A (ja) | 1982-06-14 | 1983-12-20 | シエブロン・リサ−チ・コンパニ− | ベンゼンの合成法 |
| US4492624A (en) * | 1982-09-30 | 1985-01-08 | Stone & Webster Engineering Corp. | Duocracking process for the production of olefins from both heavy and light hydrocarbons |
| 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. |
| US4789457A (en) | 1985-06-03 | 1988-12-06 | Mobil Oil Corporation | Production of high octane gasoline by hydrocracking catalytic cracking products |
| 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 |
| FI932187A7 (fi) * | 1992-05-29 | 1993-11-30 | The Boc Group Inc | Menetelmä tyydyttämättömien hiilivetyjen valmistamiseksi ja niiden erottamiseksi tyydytetyistä hiilivedyistä |
| US6270654B1 (en) | 1993-08-18 | 2001-08-07 | Ifp North America, Inc. | Catalytic hydrogenation process utilizing multi-stage ebullated bed reactors |
| US5880325A (en) | 1993-09-07 | 1999-03-09 | Exxon Research And Engineering Company | Aromatics extraction from hydrocarbon oil using tetramethylene sulfoxide |
| 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 |
| GB9720334D0 (en) * | 1997-09-24 | 1997-11-26 | Bp Chem Int Ltd | Chemical process |
| KR100557558B1 (ko) * | 2000-11-30 | 2006-03-03 | 에스케이 주식회사 | 탄화수소 혼합물로부터 방향족 탄화수소 및 액화석유가스를 제조하는 방법 |
| JP2003277300A (ja) | 2002-03-26 | 2003-10-02 | Asahi Kasei Corp | 水素化脱アルキルベンゼンプラント及びその運転方法 |
| US20040004031A1 (en) * | 2002-06-26 | 2004-01-08 | Boger Thorsten R. | System and process for pyrolysis gasoline hydrotreatment |
| US7214308B2 (en) | 2003-02-21 | 2007-05-08 | Institut Francais Du Petrole | Effective integration of solvent deasphalting and ebullated-bed processing |
| WO2005021686A1 (en) | 2003-08-29 | 2005-03-10 | Ebara Corporation | Recycling method and system |
| 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 |
| 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 |
| US7951745B2 (en) | 2008-01-03 | 2011-05-31 | Wilmington Trust Fsb | Catalyst for hydrocracking hydrocarbons containing polynuclear aromatic compounds |
| 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 |
| EA201170359A1 (ru) * | 2008-08-19 | 2011-08-30 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Способ конверсии низших алканов в ароматические углеводороды и этилен |
| DE102009012265A1 (de) | 2009-03-11 | 2010-09-23 | Uhde Gmbh | Verfahren zur Gewinnung von Reinaromaten aus aromatenhaltigen Kohlenwasserstofffraktionen |
| 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 |
| JP5357098B2 (ja) | 2010-03-31 | 2013-12-04 | Jx日鉱日石エネルギー株式会社 | ガソリン組成物 |
| JP5481270B2 (ja) | 2010-05-07 | 2014-04-23 | Jx日鉱日石エネルギー株式会社 | 炭化水素油中の硫黄化合物を低減する方法 |
| WO2012135111A2 (en) | 2011-03-31 | 2012-10-04 | Uop Llc | Aromatics recovery by extractive distillation |
| CN102795958B (zh) * | 2011-05-27 | 2015-03-18 | 中国石油化工股份有限公司 | 一种以石脑油为原料生产芳烃和乙烯的方法 |
| 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 |
| 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
- 2014-06-30 ES ES14733658.0T patent/ES2671320T3/es active Active
- 2014-06-30 US US14/901,921 patent/US10526553B2/en active Active
- 2014-06-30 CN CN201480032009.9A patent/CN105555925A/zh active Pending
- 2014-06-30 EA EA201690133A patent/EA029413B1/ru not_active IP Right Cessation
- 2014-06-30 SG SG11201508904WA patent/SG11201508904WA/en unknown
- 2014-06-30 WO PCT/EP2014/063848 patent/WO2015000840A1/en not_active Ceased
- 2014-06-30 JP JP2016522558A patent/JP6795976B2/ja not_active Expired - Fee Related
- 2014-06-30 CN CN201910210254.9A patent/CN110066686B/zh active Active
- 2014-06-30 KR KR1020157036205A patent/KR102290668B1/ko active Active
- 2014-06-30 EP EP14733658.0A patent/EP3017025B1/en active Active
-
2018
- 2018-11-26 JP JP2018220049A patent/JP6931346B2/ja not_active Expired - Fee Related
-
2019
- 2019-09-26 US US16/584,096 patent/US10822558B2/en active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010052241A1 (en) * | 2000-04-13 | 2001-12-20 | Ipsi Llc | Flexible reflux process for high NGL recovery |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2015000840A1 (en) | 2015-01-08 |
| CN110066686A (zh) | 2019-07-30 |
| JP6795976B2 (ja) | 2020-12-02 |
| CN110066686B (zh) | 2023-02-17 |
| EP3017025A1 (en) | 2016-05-11 |
| JP2016526591A (ja) | 2016-09-05 |
| US20200017779A1 (en) | 2020-01-16 |
| SG11201508904WA (en) | 2016-01-28 |
| US10526553B2 (en) | 2020-01-07 |
| EA201690133A1 (ru) | 2016-07-29 |
| EA029413B1 (ru) | 2018-03-30 |
| KR20160025511A (ko) | 2016-03-08 |
| CN105555925A (zh) | 2016-05-04 |
| EP3017025B1 (en) | 2018-03-07 |
| US10822558B2 (en) | 2020-11-03 |
| JP2019048870A (ja) | 2019-03-28 |
| ES2671320T3 (es) | 2018-06-06 |
| US20160369191A1 (en) | 2016-12-22 |
| JP6931346B2 (ja) | 2021-09-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR102290668B1 (ko) | 증기 분해기 단위에서 탄화수소 공급원료를 분해하는 방법 | |
| KR102309267B1 (ko) | 탄화수소 공급원료를 증기 분해기 단위에서 분해하는 방법 | |
| KR102325584B1 (ko) | 정제소 중질 잔사유를 석유화학물질로 업그레이드하는 방법 | |
| US9856425B2 (en) | Method of producing aromatics and light olefins from a hydrocarbon feedstock | |
| KR102309262B1 (ko) | 탄화수소 공급원료로부터 경질 올레핀 및 방향족물질을 생산하는 방법 | |
| KR102308554B1 (ko) | 원유를 비티엑스(btx) 수율이 향상된 석유화학물질로 변환시키기 위한 방법 및 장치 | |
| KR102339046B1 (ko) | 원유를 에틸렌 수율이 향상된 석유화학물질로 변환시키기 위한 방법 및 장치 | |
| KR102369550B1 (ko) | 원유를 탄소 효율이 향상된 석유화학물질로 변환시키기 위한 방법 및 장치 | |
| JP6360553B2 (ja) | 炭化水素原料から軽質オレフィンおよび芳香族化合物を製造する方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PA0105 | International application |
Patent event date: 20151222 Patent event code: PA01051R01D Comment text: International Patent Application |
|
| PG1501 | Laying open of application | ||
| A201 | Request for examination | ||
| PA0201 | Request for examination |
Patent event code: PA02012R01D Patent event date: 20190626 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: 20210224 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: 20210729 |
|
| GRNT | Written decision to grant | ||
| PR0701 | Registration of establishment |
Comment text: Registration of Establishment Patent event date: 20210811 Patent event code: PR07011E01D |
|
| PR1002 | Payment of registration fee |
Payment date: 20210812 End annual number: 3 Start annual number: 1 |
|
| PG1601 | Publication of registration | ||
| PR1001 | Payment of annual fee |
Payment date: 20240724 Start annual number: 4 End annual number: 4 |