BR112023017609A2 - Método e sistema para craqueamento a vapor - Google Patents
Método e sistema para craqueamento a vaporInfo
- Publication number
- BR112023017609A2 BR112023017609A2 BR112023017609A BR112023017609A BR112023017609A2 BR 112023017609 A2 BR112023017609 A2 BR 112023017609A2 BR 112023017609 A BR112023017609 A BR 112023017609A BR 112023017609 A BR112023017609 A BR 112023017609A BR 112023017609 A2 BR112023017609 A2 BR 112023017609A2
- Authority
- BR
- Brazil
- Prior art keywords
- steam
- level
- pressure
- temperature level
- cracking
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 5
- 238000004230 steam cracking Methods 0.000 title abstract 5
- 238000001816 cooling Methods 0.000 abstract 2
- 238000005336 cracking Methods 0.000 abstract 2
- 238000010791 quenching Methods 0.000 abstract 2
- 238000010304 firing Methods 0.000 abstract 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
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1838—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/003—Feed-water heater systems
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/22—Higher olefins
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
método e sistema para craqueamento a vapor. um método de craqueamento a vapor usando um arranjo de craqueamento a vapor (1100-1500) incluindo um ou mais fornos de craqueamento de queima (110), um ou mais trens de resfriamento de têmpera (20) e um ou mais compressores (60) e/ou bombas como equipamento rotativo é proposto, em que uma ou mais correntes de gás de processo são ou são passadas pelo menos através de um ou mais fornos de craqueamento (110) e um ou mais trens de resfriamento de têmpera (20), e em que o equipamento rotativo é pelo menos parcialmente acionado por energia elétrica. de acordo com a invenção, um ou mais arranjos de geração de vapor (30) são ou são operados em associação térmica com um ou mais arranjos de craqueamento a vapor (1100-1500), em que o uso de um ou mais arranjos de geração de vapor (30) pelo menos superaquecido vapor de alta pressão a um primeiro nível de pressão de 3.000 a 17.500 kpa (30 e 175 bar) de pressão absoluta e a um primeiro nível de temperatura e nenhum vapor a um nível de temperatura mais alto do que o primeiro nível de temperatura é gerado, em que o vapor de alta pressão superaquecido no primeiro nível de pressão está em pelo menos em parte expandido adiabaticamente e isentalpicamente para um segundo nível de pressão abaixo do primeiro nível de pressão, de modo que seu nível de temperatura seja reduzido para um segundo nível de temperatura e em que o primeiro nível de temperatura seja selecionado de modo que cada nível de temperatura intermediário seja alcançado em níveis de pressão intermediários de mais de 2.000 kpa (20 bar) durante o processo de expansão adiabática e isentálpica está entre 5 e 120 k acima do ponto de orvalho do vapor no respectivo nível de pressão intermediária durante a expansão adiabática e isentálpica. um sistema correspondente (100) também faz parte da presente invenção.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP21161768.3A EP4056893A1 (en) | 2021-03-10 | 2021-03-10 | Method and system for steamcracking |
PCT/EP2022/055877 WO2022189423A1 (en) | 2021-03-10 | 2022-03-08 | Method and system for steamcracking |
Publications (1)
Publication Number | Publication Date |
---|---|
BR112023017609A2 true BR112023017609A2 (pt) | 2023-11-07 |
Family
ID=74870706
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR112023017609A BR112023017609A2 (pt) | 2021-03-10 | 2022-03-08 | Método e sistema para craqueamento a vapor |
Country Status (9)
Country | Link |
---|---|
US (1) | US20240158701A1 (pt) |
EP (2) | EP4056893A1 (pt) |
JP (1) | JP2024512390A (pt) |
KR (1) | KR20230154265A (pt) |
CN (1) | CN117015680A (pt) |
AU (1) | AU2022233542A1 (pt) |
BR (1) | BR112023017609A2 (pt) |
CA (1) | CA3211807A1 (pt) |
WO (1) | WO2022189423A1 (pt) |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE710185C (de) | 1937-11-19 | 1941-09-06 | Siemens Reiniger Werke Akt Ges | Einrichtung zum Bestrahlen mit therapeutisch wirksamen Strahlen |
DE1615278C3 (de) | 1967-06-30 | 1979-06-21 | Gefi Gesellschaft F. Industriewaerme Mbh, 4150 Krefeld | Elektrischer Widerstandsofen insbesondere zur Erhitzung gasförmiger Medien |
DE2362628C3 (de) | 1973-12-17 | 1979-07-26 | Linde Ag, 6200 Wiesbaden | Rohrofen zur thermischen Behandlung von Medien mittels Widerstandsheizung |
US4107226A (en) * | 1977-10-19 | 1978-08-15 | Pullman Incorporated | Method for quenching cracked gases |
DE3334334A1 (de) | 1983-09-22 | 1985-04-11 | Hucke, Hans, Pratteln, Basel | Heizvorrichtung fuer das aufheizen eines in einem elektrisch betriebenen durchstroemelement enthaltenen waermetraegers |
US4617109A (en) * | 1985-12-23 | 1986-10-14 | The M. W. Kellogg Company | Combustion air preheating |
EP2931415B1 (de) | 2012-12-13 | 2020-11-18 | Basf Se | Verfahren zur durchführung wärmeverbrauchender prozesse |
ES2779526T3 (es) | 2014-06-26 | 2020-08-18 | Linde Gmbh | Dispositivo y procedimiento para el calentamiento de un fluido en una tubería con corriente trifásica |
US10017702B2 (en) * | 2014-10-07 | 2018-07-10 | Lummus Technology Inc. | Thermal cracking of crudes and heavy feeds to produce olefins in pyrolysis reactor |
DE102015004121A1 (de) | 2015-03-31 | 2016-10-06 | Linde Aktiengesellschaft | Ofen mit elektrisch sowie mittels Brennstoff beheizbaren Reaktorrohren zur Dampfreformierung eines kohlenwasserstoffhaltigen Einsatzes |
DE102016209172A1 (de) | 2016-05-25 | 2017-11-30 | Linde Aktiengesellschaft | Emissionsreduziertes Verfahren zur Herstellung von Olefinen |
EP3249028A1 (de) | 2016-05-25 | 2017-11-29 | Linde Aktiengesellschaft | Emissionsreduziertes verfahren zur herstellung von olefinen |
US20200290939A1 (en) * | 2017-11-13 | 2020-09-17 | Sabic Global Technologies B.V. | Methods and systems for olefin production |
CN112805509B (zh) | 2018-08-16 | 2023-03-10 | 巴斯夫欧洲公司 | 用于通过直流加热管道中的流体的装置和方法 |
CN113993816B (zh) | 2019-01-15 | 2023-12-15 | 沙特基础工业全球技术公司 | 可再生能量在氨合成中的使用 |
EP3730592A1 (en) * | 2019-04-24 | 2020-10-28 | SABIC Global Technologies B.V. | Use of renewable energy in olefin synthesis |
-
2021
- 2021-03-10 EP EP21161768.3A patent/EP4056893A1/en not_active Withdrawn
-
2022
- 2022-03-08 CA CA3211807A patent/CA3211807A1/en active Pending
- 2022-03-08 JP JP2023555251A patent/JP2024512390A/ja active Pending
- 2022-03-08 BR BR112023017609A patent/BR112023017609A2/pt unknown
- 2022-03-08 CN CN202280020250.4A patent/CN117015680A/zh active Pending
- 2022-03-08 EP EP22710614.3A patent/EP4305344A1/en active Pending
- 2022-03-08 AU AU2022233542A patent/AU2022233542A1/en active Pending
- 2022-03-08 WO PCT/EP2022/055877 patent/WO2022189423A1/en active Application Filing
- 2022-03-08 KR KR1020237034424A patent/KR20230154265A/ko unknown
- 2022-03-08 US US18/548,881 patent/US20240158701A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
CN117015680A (zh) | 2023-11-07 |
EP4305344A1 (en) | 2024-01-17 |
WO2022189423A1 (en) | 2022-09-15 |
US20240158701A1 (en) | 2024-05-16 |
CA3211807A1 (en) | 2022-09-15 |
JP2024512390A (ja) | 2024-03-19 |
KR20230154265A (ko) | 2023-11-07 |
EP4056893A1 (en) | 2022-09-14 |
AU2022233542A1 (en) | 2023-09-07 |
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