EP2917305A1 - Procédé de production de produits oléfiniques par vapocraquage thermique - Google Patents
Procédé de production de produits oléfiniques par vapocraquage thermiqueInfo
- Publication number
- EP2917305A1 EP2917305A1 EP13788895.4A EP13788895A EP2917305A1 EP 2917305 A1 EP2917305 A1 EP 2917305A1 EP 13788895 A EP13788895 A EP 13788895A EP 2917305 A1 EP2917305 A1 EP 2917305A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- furnace
- cracking
- cracking furnace
- pyrolysis oil
- product stream
- 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
- 238000000034 method Methods 0.000 title claims abstract description 81
- 238000004230 steam cracking Methods 0.000 title abstract description 15
- 150000001336 alkenes Chemical class 0.000 title description 7
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 title description 6
- 238000005336 cracking Methods 0.000 claims abstract description 224
- 238000000197 pyrolysis Methods 0.000 claims abstract description 120
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 63
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 62
- 239000003921 oil Substances 0.000 claims description 126
- 239000005977 Ethylene Substances 0.000 claims description 30
- 229910052799 carbon Inorganic materials 0.000 claims description 30
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 28
- 238000012545 processing Methods 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims description 22
- 239000000126 substance Substances 0.000 claims description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 21
- 238000005984 hydrogenation reaction Methods 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 14
- 238000009835 boiling Methods 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 13
- 229910052739 hydrogen Inorganic materials 0.000 claims description 13
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 12
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 4
- 239000010779 crude oil Substances 0.000 claims description 4
- 239000003350 kerosene Substances 0.000 claims description 3
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 2
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 2
- 238000005899 aromatization reaction Methods 0.000 claims 1
- 238000012993 chemical processing Methods 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 104
- 238000003776 cleavage reaction Methods 0.000 description 37
- 230000007017 scission Effects 0.000 description 37
- 150000001875 compounds Chemical class 0.000 description 19
- 239000004215 Carbon black (E152) Substances 0.000 description 18
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 16
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 13
- 239000003502 gasoline Substances 0.000 description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 9
- 230000004992 fission Effects 0.000 description 9
- 238000010586 diagram Methods 0.000 description 7
- 238000007670 refining Methods 0.000 description 6
- 238000004064 recycling Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000010790 dilution Methods 0.000 description 4
- 239000012895 dilution Substances 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000003750 conditioning effect Effects 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003498 natural gas condensate Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- BRDWIEOJOWJCLU-LTGWCKQJSA-N GS-441524 Chemical compound C=1C=C2C(N)=NC=NN2C=1[C@]1(C#N)O[C@H](CO)[C@@H](O)[C@H]1O BRDWIEOJOWJCLU-LTGWCKQJSA-N 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000000035 biogenic effect Effects 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 238000007700 distillative separation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- WHFQAROQMWLMEY-UHFFFAOYSA-N propylene dimer Chemical compound CC=C.CC=C WHFQAROQMWLMEY-UHFFFAOYSA-N 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
- C10G55/04—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one thermal cracking step
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/06—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
-
- 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
Definitions
- Gap conditions of the cracking furnaces within a furnace group are usually set the same or similar.
- oil column is understood here to mean a separation unit, by means of which upstream of a substantially further fractionation of the product streams from it the respective pyrolysis oil can be separated off.
- the actual fractionation into the product fractions for example the recovery of ethylene, etc., can therefore take place after the separation of the pyrolysis oil and unification of the thereafter remaining fractions of the product streams.
- An oil column is for example as
- Hydrocarbons having a carbon number of 5 and more are recycled as recycle stream D into the cracking furnace 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13788895.4A EP2917305B1 (fr) | 2012-11-08 | 2013-11-07 | Procédé de fabrication de produits chargés en oléfines par vapocraquage thermique |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP12007602 | 2012-11-08 | ||
| PCT/EP2013/003358 WO2014072058A1 (fr) | 2012-11-08 | 2013-11-07 | Procédé de production de produits oléfiniques par vapocraquage thermique |
| EP13788895.4A EP2917305B1 (fr) | 2012-11-08 | 2013-11-07 | Procédé de fabrication de produits chargés en oléfines par vapocraquage thermique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP2917305A1 true EP2917305A1 (fr) | 2015-09-16 |
| EP2917305B1 EP2917305B1 (fr) | 2016-09-07 |
Family
ID=47191482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP13788895.4A Not-in-force EP2917305B1 (fr) | 2012-11-08 | 2013-11-07 | Procédé de fabrication de produits chargés en oléfines par vapocraquage thermique |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US10344226B2 (fr) |
| EP (1) | EP2917305B1 (fr) |
| JP (1) | JP6490008B2 (fr) |
| KR (1) | KR20150082510A (fr) |
| CN (1) | CN104769082B (fr) |
| AU (1) | AU2013343861B2 (fr) |
| BR (1) | BR112015010348A2 (fr) |
| ES (1) | ES2604654T3 (fr) |
| HU (1) | HUE030989T2 (fr) |
| PH (1) | PH12015500964A1 (fr) |
| RU (1) | RU2636148C2 (fr) |
| SA (1) | SA515360370B1 (fr) |
| WO (1) | WO2014072058A1 (fr) |
Families Citing this family (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019018554A2 (fr) * | 2017-07-18 | 2019-01-24 | Lummus Technology Llc | Unités intégrées de pyrolyse et d'hydrocraquage destinées au pétrole brut pour obtenir des produits chimiques |
| WO2019036426A1 (fr) * | 2017-08-15 | 2019-02-21 | Sabic Global Technologies, B.V. | Production d'oléfines légères par vapocraquage intégré et procédé d'hydrocraquage |
| US12497467B2 (en) | 2019-05-24 | 2025-12-16 | Exxon Mobil Product Solutions Company | Recycle content cellulose ester |
| EP3976733A4 (fr) | 2019-05-24 | 2023-04-12 | Eastman Chemical Company | Conditions de craqueur optimisées pour accepter une huile de pyrolyse |
| WO2020242920A1 (fr) | 2019-05-24 | 2020-12-03 | Eastman Chemical Company | Huile de pyrolyse thermique dans un four craqueur alimenté en gaz |
| 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 |
| WO2020242918A1 (fr) * | 2019-05-24 | 2020-12-03 | Eastman Chemical Company | Co-craquage d'huile de pyrolyse avec de l'éthane |
| CN113891928B (zh) | 2019-05-24 | 2024-10-29 | 伊士曼化工公司 | 裂化热解油的c4-c7馏分 |
| US11365357B2 (en) | 2019-05-24 | 2022-06-21 | Eastman Chemical Company | Cracking C8+ fraction of pyoil |
| US12031091B2 (en) | 2019-05-24 | 2024-07-09 | Eastman Chemical Company | Recycle content cracked effluent |
| CN119912669A (zh) * | 2019-07-29 | 2025-05-02 | 伊士曼化工公司 | 回收成分环丁二醇聚酯 |
| US12338211B2 (en) | 2019-07-29 | 2025-06-24 | Eastman Chemical Company | Recycle content (C4)alkanal |
| EP4051762A4 (fr) | 2019-10-31 | 2023-12-27 | Eastman Chemical Company | Procédé et système de pyrolyse pour déchets recyclés |
| US11319262B2 (en) | 2019-10-31 | 2022-05-03 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
| CN114729265A (zh) * | 2019-10-31 | 2022-07-08 | 伊士曼化工公司 | 用于形成回收成分烃组合物的方法和系统 |
| US12173237B2 (en) | 2019-10-31 | 2024-12-24 | Eastman Chemical Company | Processes and systems for formation of recycle-content hydrocarbon compositions |
| US11945998B2 (en) | 2019-10-31 | 2024-04-02 | Eastman Chemical Company | Processes and systems for making recycle content hydrocarbons |
| WO2021087059A1 (fr) | 2019-10-31 | 2021-05-06 | Eastman Chemical Company | Procédé et système de pyrolyse pour déchets recyclés |
| US12528995B2 (en) | 2019-10-31 | 2026-01-20 | ExxonMobil Product Solutions Company | Pyrolysis method and system for recycled waste |
| KR20220091569A (ko) | 2019-10-31 | 2022-06-30 | 이스트만 케미칼 컴파니 | 재활용물 탄화수소 조성물의 생성을 위한 방법 및 시스템 |
| EP4055001A4 (fr) | 2019-11-07 | 2024-02-14 | Eastman Chemical Company | Esters mixtes à teneur recyclée et solvants |
| CN118851872A (zh) * | 2019-11-07 | 2024-10-29 | 伊士曼化工公司 | 回收成分丙醇 |
| CN114728868B (zh) | 2019-11-07 | 2024-09-03 | 伊士曼化工公司 | 回收成分羰基合成醇和羰基合成增塑剂 |
| KR20220097485A (ko) | 2019-11-07 | 2022-07-07 | 이스트만 케미칼 컴파니 | 재활용물 옥소 글리콜 |
| US11939534B2 (en) | 2019-11-07 | 2024-03-26 | Eastman Chemical Company | Recycle content alpha olefins and fatty alcohols |
| 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 |
| IT202100033044A1 (it) * | 2021-12-30 | 2023-06-30 | Versalis Spa | Procedimento per la pirolisi di materiale sostanzialmente plastico di composizione non costante, relativo reattore, apparato e prodotto ottenuto |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2380337A1 (fr) * | 1977-02-11 | 1978-09-08 | Inst Francais Du Petrole | Procede de vapocraquage de charges lourdes precede d'un hydrotraitement |
| DE2806854C2 (de) * | 1978-02-17 | 1986-01-02 | Linde Ag, 6200 Wiesbaden | Verfahren zum thermischen Spalten von Kohlenwasserstoffen zu Olefinen |
| GB1602097A (en) | 1978-05-25 | 1981-11-04 | Uop Inc | Process for thermal cracking and coking of heavy carbonaceous oils |
| US4906442A (en) * | 1982-09-30 | 1990-03-06 | Stone & Webster Engineering Corporation | Process and apparatus for the production of olefins from both heavy and light hydrocarbons |
| US4548706A (en) * | 1983-01-26 | 1985-10-22 | Standard Oil Company (Indiana) | Thermal cracking of hydrocarbons |
| DE3504941A1 (de) * | 1985-02-13 | 1986-08-14 | Linde Ag, 6200 Wiesbaden | Verfahren zur spaltung eines kohlenwasserstoffeinsatzes |
| FR2584733B1 (fr) * | 1985-07-12 | 1987-11-13 | Inst Francais Du Petrole | Procede ameliore de vapocraquage d'hydrocarbures |
| US4990709A (en) * | 1989-04-28 | 1991-02-05 | Mobil Oil Corporation | C2-C5 olefin oligomerization by reduced chromium catalysis |
| CN1214076A (zh) * | 1996-02-22 | 1999-04-14 | 埃克森化学专利公司 | 从残油或其它重油中获得烯烃的方法 |
| DE10000889C2 (de) * | 2000-01-12 | 2002-12-19 | Mg Technologies Ag | Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen |
| US7339087B2 (en) * | 2001-03-15 | 2008-03-04 | Shell Oil Company | Pyrolysis |
| FR2830537B1 (fr) * | 2001-10-09 | 2005-05-20 | Inst Francais Du Petrole | Procede de vapocraquage d'une coupe hydrocarbonee comprenant une deuxieme zone de vapocraquage dans laquelle est traitee une coupe c4 issue d'une premiere zone de vapocraquage |
| FR2834515B1 (fr) * | 2002-01-10 | 2006-03-10 | Atofina | Vapocraquage de naphta modifie |
| EP1365004A1 (fr) * | 2002-05-23 | 2003-11-26 | ATOFINA Research | Production d'olefines |
| KR101159087B1 (ko) * | 2003-12-12 | 2012-06-25 | 미쓰비시 가가꾸 가부시키가이샤 | 프로필렌의 제조 방법 |
| KR20050102766A (ko) * | 2004-04-22 | 2005-10-27 | 주식회사 엘지화학 | 탄화수소 분해촉매 및 그 제조방법 |
| WO2006063201A1 (fr) * | 2004-12-10 | 2006-06-15 | Bhirud Vasant L | Craquage a la vapeur avec desaromatisation de naphtha |
| WO2007047657A1 (fr) | 2005-10-20 | 2007-04-26 | Exxonmobil Chemical Patents Inc. | Traitement du residu d'hydrocarbure |
| US8882991B2 (en) * | 2009-08-21 | 2014-11-11 | Exxonmobil Chemical Patents Inc. | Process and apparatus for cracking high boiling point hydrocarbon feedstock |
| IN2014DN11047A (fr) * | 2012-08-09 | 2015-09-25 | Linde Ag | |
| BR112015002844A2 (pt) * | 2012-08-09 | 2018-02-14 | Linde Aktiengesellschaft | processo para preparar olefinas por craqueamento térmico a vapor em fornos de craqueamento. |
| JP6215936B2 (ja) * | 2012-08-09 | 2017-10-18 | リンデ アクチエンゲゼルシャフトＬｉｎｄｅ Ａｋｔｉｅｎｇｅｓｅｌｌｓｃｈａｆｔ | 炭化水素供給原料の熱水蒸気分解による転化方法 |
| HUE027413T2 (en) * | 2012-08-09 | 2016-10-28 | Linde Ag | Process for converting hydrocarbon feedstock to olefin product stream by thermal steam steam cracking |
-
2013
- 2013-11-07 WO PCT/EP2013/003358 patent/WO2014072058A1/fr not_active Ceased
- 2013-11-07 EP EP13788895.4A patent/EP2917305B1/fr not_active Not-in-force
- 2013-11-07 RU RU2015121405A patent/RU2636148C2/ru active
- 2013-11-07 HU HUE13788895A patent/HUE030989T2/en unknown
- 2013-11-07 ES ES13788895.4T patent/ES2604654T3/es active Active
- 2013-11-07 JP JP2015541036A patent/JP6490008B2/ja not_active Expired - Fee Related
- 2013-11-07 KR KR1020157014894A patent/KR20150082510A/ko not_active Withdrawn
- 2013-11-07 BR BR112015010348A patent/BR112015010348A2/pt not_active Application Discontinuation
- 2013-11-07 US US14/440,704 patent/US10344226B2/en not_active Expired - Fee Related
- 2013-11-07 AU AU2013343861A patent/AU2013343861B2/en not_active Ceased
- 2013-11-07 CN CN201380058504.2A patent/CN104769082B/zh not_active Expired - Fee Related
-
2015
- 2015-04-30 SA SA515360370A patent/SA515360370B1/ar unknown
- 2015-04-30 PH PH12015500964A patent/PH12015500964A1/en unknown
Non-Patent Citations (1)
| Title |
|---|
| See references of WO2014072058A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2016501278A (ja) | 2016-01-18 |
| HUE030989T2 (en) | 2017-06-28 |
| AU2013343861B2 (en) | 2017-12-21 |
| BR112015010348A2 (pt) | 2017-07-11 |
| ES2604654T3 (es) | 2017-03-08 |
| CN104769082B (zh) | 2017-03-29 |
| CN104769082A (zh) | 2015-07-08 |
| US10344226B2 (en) | 2019-07-09 |
| RU2636148C2 (ru) | 2017-11-21 |
| RU2015121405A (ru) | 2016-12-27 |
| EP2917305B1 (fr) | 2016-09-07 |
| AU2013343861A1 (en) | 2015-05-21 |
| WO2014072058A1 (fr) | 2014-05-15 |
| SA515360370B1 (ar) | 2016-04-20 |
| JP6490008B2 (ja) | 2019-03-27 |
| US20150284645A1 (en) | 2015-10-08 |
| PH12015500964A1 (en) | 2015-07-27 |
| KR20150082510A (ko) | 2015-07-15 |
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