JP6522012B2 - 炭化水素をオレフィンに変換する方法 - Google Patents
炭化水素をオレフィンに変換する方法 Download PDFInfo
- Publication number
- JP6522012B2 JP6522012B2 JP2016570165A JP2016570165A JP6522012B2 JP 6522012 B2 JP6522012 B2 JP 6522012B2 JP 2016570165 A JP2016570165 A JP 2016570165A JP 2016570165 A JP2016570165 A JP 2016570165A JP 6522012 B2 JP6522012 B2 JP 6522012B2
- Authority
- JP
- Japan
- Prior art keywords
- stream
- unit
- dehydrogenation
- separation
- hydrocracking
- 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.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 title claims description 130
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 67
- 229930195733 hydrocarbon Natural products 0.000 title claims description 63
- 150000001336 alkenes Chemical class 0.000 title claims description 41
- 238000000926 separation method Methods 0.000 claims description 119
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 114
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 102
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 90
- 239000001294 propane Substances 0.000 claims description 57
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 52
- 239000001273 butane Substances 0.000 claims description 50
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 50
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 50
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 49
- 239000001257 hydrogen Substances 0.000 claims description 49
- 229910052739 hydrogen Inorganic materials 0.000 claims description 49
- 239000004215 Carbon black (E152) Substances 0.000 claims description 42
- 238000004230 steam cracking Methods 0.000 claims description 41
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 39
- 239000000203 mixture Substances 0.000 claims description 34
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 33
- 125000003118 aryl group Chemical group 0.000 claims description 30
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 27
- 150000002431 hydrogen Chemical class 0.000 claims description 16
- 238000005336 cracking Methods 0.000 claims description 14
- 238000000197 pyrolysis Methods 0.000 claims description 13
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 9
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- 239000003502 gasoline Substances 0.000 description 25
- 238000006243 chemical reaction Methods 0.000 description 23
- 125000004432 carbon atom Chemical group C* 0.000 description 20
- 239000003921 oil Substances 0.000 description 20
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 19
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 19
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 18
- 239000005977 Ethylene Substances 0.000 description 18
- 239000003054 catalyst Substances 0.000 description 17
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 16
- 239000010779 crude oil Substances 0.000 description 15
- 239000003915 liquefied petroleum gas Substances 0.000 description 12
- -1 naphtha to olefins Chemical class 0.000 description 12
- 150000001335 aliphatic alkanes Chemical class 0.000 description 11
- 238000009835 boiling Methods 0.000 description 11
- 239000006227 byproduct Substances 0.000 description 10
- 208000003173 lipoprotein glomerulopathy Diseases 0.000 description 10
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 10
- 239000000463 material Substances 0.000 description 9
- 238000004821 distillation Methods 0.000 description 8
- 238000005984 hydrogenation reaction Methods 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 6
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 6
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 6
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 238000001311 chemical methods and process Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 238000007327 hydrogenolysis reaction Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 4
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000010354 integration Effects 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 238000010791 quenching Methods 0.000 description 3
- 238000001577 simple distillation Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 239000012808 vapor phase Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 2
- 150000001491 aromatic compounds Chemical class 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
- 230000035425 carbon utilization Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- GDOPTJXRTPNYNR-UHFFFAOYSA-N methylcyclopentane Chemical compound CC1CCCC1 GDOPTJXRTPNYNR-UHFFFAOYSA-N 0.000 description 2
- 239000003345 natural gas Substances 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
- 238000007670 refining Methods 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 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
- 238000004523 catalytic cracking Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000010724 circulating oil 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
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 150000001934 cyclohexanes Chemical class 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000006069 physical mixture Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
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- 238000005057 refrigeration Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
-
- 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
- C10G69/04—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 catalytic 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
- C10G69/06—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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4087—Catalytic distillation
-
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP14156633.1 | 2014-02-25 | ||
| EP14156633 | 2014-02-25 | ||
| PCT/EP2014/079210 WO2015128039A1 (en) | 2014-02-25 | 2014-12-23 | Process for converting hydrocarbons into olefins |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2017511813A JP2017511813A (ja) | 2017-04-27 |
| JP2017511813A5 JP2017511813A5 (enExample) | 2017-08-24 |
| JP6522012B2 true JP6522012B2 (ja) | 2019-05-29 |
Family
ID=50151229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2016570165A Expired - Fee Related JP6522012B2 (ja) | 2014-02-25 | 2014-12-23 | 炭化水素をオレフィンに変換する方法 |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US10316259B2 (enExample) |
| EP (1) | EP3110923B1 (enExample) |
| JP (1) | JP6522012B2 (enExample) |
| KR (1) | KR102374392B1 (enExample) |
| CN (1) | CN106062148B (enExample) |
| EA (1) | EA033166B1 (enExample) |
| ES (1) | ES2715663T3 (enExample) |
| SG (1) | SG11201606020PA (enExample) |
| WO (1) | WO2015128039A1 (enExample) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2753415C2 (ru) | 2016-08-18 | 2021-08-16 | Хальдор Топсёэ А/С | Способ и установка для гидрокрекинга с высокой конверсией |
| EP3516012B1 (en) * | 2016-09-22 | 2021-01-06 | SABIC Global Technologies B.V. | An integrated process configuration and apparatus involving the steps of pyrolysis, hydrocracking, hydrodealkylation and steam cracking |
| US11095022B2 (en) * | 2017-03-30 | 2021-08-17 | Sumitomo Electric Industries, Ltd. | Planar antenna and wireless module |
| EP3428143A1 (de) | 2017-07-12 | 2019-01-16 | Linde Aktiengesellschaft | Prozess und anlage zur herstellung von propylen durch kombination von propandehydrierung und dampfspaltverfahren mit vortrennschritten in beiden verfahren zur teilweise entfernung von wasserstoff und methan |
| EP3428144A1 (de) * | 2017-07-12 | 2019-01-16 | Linde Aktiengesellschaft | Prozess und anlage zur herstellung von propylen durch kombination von propandehydrierung und dampfspaltverfahren mit propan-rückführung in das dampfspaltverfahren |
| EP3655506A4 (en) * | 2017-07-18 | 2021-04-07 | Lummus Technology LLC | INTEGRATED THERMAL CRACKING AND DEHYDROGENATION PROCESS FOR OLEFIN PRODUCTION |
| DE112018004207B4 (de) * | 2017-08-15 | 2022-09-22 | Sabic Global Technologies B.V. | Schiefergas und Kondensat in Chemikalien |
| MY204513A (en) * | 2017-12-29 | 2024-08-31 | Lummus Technology Inc | Conversion of heavy fuel oil to chemicals |
| CN109851461A (zh) * | 2019-01-21 | 2019-06-07 | 中石化上海工程有限公司 | 石脑油及丙烷裂解前脱乙烷与pdh耦合的方法 |
| US11447707B2 (en) * | 2020-12-22 | 2022-09-20 | Uop Llc | Paraffin dehydrogenation process and apparatus |
| JP7222034B2 (ja) * | 2021-07-21 | 2023-02-14 | 千代田化工建設株式会社 | 芳香族化合物の製造方法 |
| US20240190791A1 (en) * | 2022-12-09 | 2024-06-13 | Uop Llc | Separation of hydrogen, methane, ethane, and propane in naphtha to ethane and propane fractionation section based on a dividing wall fractionation column integration |
| US20240190792A1 (en) * | 2022-12-09 | 2024-06-13 | Uop Llc | Integration of naphtha to ethane and propane fractionation section with ethane steam cracker |
Family Cites Families (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3718575A (en) * | 1971-07-12 | 1973-02-27 | Universal Oil Prod Co | Hydrocracking for lpg production |
| BE793036A (fr) * | 1971-12-21 | 1973-04-16 | Pierrefitte Auby Sa | Procede de craquage sous pression d'hydrogene pour la production d'olefines |
| JPS5127242A (en) * | 1974-08-30 | 1976-03-06 | Komatsu Mfg Co Ltd | Kensetsusharyo no jidoanzenkeihosochi |
| 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 |
| US4150060A (en) * | 1977-05-09 | 1979-04-17 | Uop Inc. | Hydrocarbon isomerization process |
| US4458096A (en) * | 1983-05-26 | 1984-07-03 | Air Products And Chemicals, Inc. | Process for the production of ethylene and propylene |
| JPS6147794A (ja) * | 1984-08-16 | 1986-03-08 | Mitsubishi Heavy Ind Ltd | 炭化水素から石油化学製品を製造するための分解方法 |
| 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 |
| US20030221990A1 (en) | 2002-06-04 | 2003-12-04 | Yoon H. Alex | Multi-stage hydrocracker with kerosene recycle |
| US7214308B2 (en) | 2003-02-21 | 2007-05-08 | Institut Francais Du Petrole | Effective integration of solvent deasphalting and ebullated-bed processing |
| US7601254B2 (en) | 2005-05-19 | 2009-10-13 | Uop Llc | Integrated fluid catalytic cracking 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 |
| US20080083261A1 (en) | 2006-10-06 | 2008-04-10 | Li-Huan Chen | Zero gravity scale adjusting device for a steel cylinder zero gravity detector |
| 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 |
| US20090050523A1 (en) | 2007-08-20 | 2009-02-26 | Halsey Richard B | Olefin production utilizing whole crude oil/condensate feedstock and selective hydrocracking |
| 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 |
| US8258357B2 (en) * | 2009-03-25 | 2012-09-04 | Lummus Technology Inc. | Production of propylene from butane |
| 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 |
| US8658019B2 (en) | 2010-11-23 | 2014-02-25 | Equistar Chemicals, Lp | Process for cracking heavy hydrocarbon feed |
| US8658022B2 (en) | 2010-11-23 | 2014-02-25 | Equistar Chemicals, Lp | Process for cracking heavy hydrocarbon feed |
| US8663456B2 (en) | 2010-11-23 | 2014-03-04 | Equistar Chemicals, Lp | Process for cracking heavy hydrocarbon feed |
| 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 |
| JP2015523345A (ja) * | 2012-06-05 | 2015-08-13 | サウディ ベーシック インダストリーズ コーポレイション | C5〜c12炭化水素混合物からbtxを製造する方法 |
| 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 SG SG11201606020PA patent/SG11201606020PA/en unknown
- 2014-12-23 ES ES14816327T patent/ES2715663T3/es active Active
- 2014-12-23 JP JP2016570165A patent/JP6522012B2/ja not_active Expired - Fee Related
- 2014-12-23 EA EA201691715A patent/EA033166B1/ru not_active IP Right Cessation
- 2014-12-23 CN CN201480076306.3A patent/CN106062148B/zh active Active
- 2014-12-23 KR KR1020167026339A patent/KR102374392B1/ko active Active
- 2014-12-23 WO PCT/EP2014/079210 patent/WO2015128039A1/en not_active Ceased
- 2014-12-23 US US15/120,949 patent/US10316259B2/en active Active
- 2014-12-23 EP EP14816327.2A patent/EP3110923B1/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| KR102374392B1 (ko) | 2022-03-15 |
| EA201691715A1 (ru) | 2017-01-30 |
| EP3110923A1 (en) | 2017-01-04 |
| CN106062148A (zh) | 2016-10-26 |
| US10316259B2 (en) | 2019-06-11 |
| CN106062148B (zh) | 2019-01-15 |
| KR20160127772A (ko) | 2016-11-04 |
| JP2017511813A (ja) | 2017-04-27 |
| EP3110923B1 (en) | 2018-12-19 |
| ES2715663T3 (es) | 2019-06-05 |
| WO2015128039A1 (en) | 2015-09-03 |
| EA033166B1 (ru) | 2019-09-30 |
| US20160369186A1 (en) | 2016-12-22 |
| SG11201606020PA (en) | 2016-08-30 |
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