JP2017511835A5 - - Google Patents
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- Publication number
- JP2017511835A5 JP2017511835A5 JP2016570168A JP2016570168A JP2017511835A5 JP 2017511835 A5 JP2017511835 A5 JP 2017511835A5 JP 2016570168 A JP2016570168 A JP 2016570168A JP 2016570168 A JP2016570168 A JP 2016570168A JP 2017511835 A5 JP2017511835 A5 JP 2017511835A5
- Authority
- JP
- Japan
- Prior art keywords
- containing stream
- stream
- hydrocracking
- hydrogen
- propane
- 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.)
- Granted
Links
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 61
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 46
- 239000001257 hydrogen Substances 0.000 claims description 37
- 229910052739 hydrogen Inorganic materials 0.000 claims description 37
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 34
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 29
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 24
- 239000001273 butane Substances 0.000 claims description 23
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 23
- 239000001294 propane Substances 0.000 claims description 23
- 229930195733 hydrocarbon Natural products 0.000 claims description 22
- 150000002430 hydrocarbons Chemical class 0.000 claims description 22
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 22
- 239000003921 oil Substances 0.000 claims description 16
- 239000003054 catalyst Substances 0.000 claims description 13
- 239000004215 Carbon black (E152) Substances 0.000 claims description 11
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 10
- 150000001336 alkenes Chemical class 0.000 claims description 8
- 125000003118 aryl group Chemical group 0.000 claims description 8
- 239000007791 liquid phase Substances 0.000 claims description 8
- 239000010779 crude oil Substances 0.000 claims description 6
- HOWJQLVNDUGZBI-UHFFFAOYSA-N butane;propane Chemical compound CCC.CCCC HOWJQLVNDUGZBI-UHFFFAOYSA-N 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 239000000446 fuel Substances 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- XBDQKXXYIPTUBI-UHFFFAOYSA-N Propionic acid Chemical compound CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 2
- 239000003348 petrochemical agent Substances 0.000 claims description 2
- 230000003134 recirculating effect Effects 0.000 claims 4
- 238000003385 ring cleavage reaction Methods 0.000 claims 3
- 239000000295 fuel oil Substances 0.000 claims 2
- 238000000197 pyrolysis Methods 0.000 claims 2
- 238000007142 ring opening reaction Methods 0.000 claims 2
- 238000005984 hydrogenation reaction Methods 0.000 claims 1
- 125000004432 carbon atom Chemical group C* 0.000 description 18
- 238000000926 separation method Methods 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000000203 mixture Substances 0.000 description 8
- 238000004230 steam cracking Methods 0.000 description 7
- 239000002002 slurry Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 4
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 238000002352 steam pyrolysis Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004227 thermal cracking Methods 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910052976 metal sulfide Inorganic materials 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 1
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 (3)
| Publication Number | Publication Date |
|---|---|
| JP2017511835A JP2017511835A (ja) | 2017-04-27 |
| JP2017511835A5 true JP2017511835A5 (enExample) | 2019-03-14 |
| JP6506312B2 JP6506312B2 (ja) | 2019-04-24 |
Family
ID=50156659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2016570168A Expired - Fee Related JP6506312B2 (ja) | 2014-02-25 | 2014-12-23 | 統合水素化分解処理 |
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 |
Family Cites Families (12)
| 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 |
| EP2828362B1 (en) | 2012-03-20 | 2020-12-30 | Saudi Arabian Oil Company | Integrated slurry hydroprocessing and steam pyrolysis of crude oil to produce petrochemicals |
-
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
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