JPH10273679A5 - - Google Patents
Info
- Publication number
- JPH10273679A5 JPH10273679A5 JP1997364087A JP36408797A JPH10273679A5 JP H10273679 A5 JPH10273679 A5 JP H10273679A5 JP 1997364087 A JP1997364087 A JP 1997364087A JP 36408797 A JP36408797 A JP 36408797A JP H10273679 A5 JPH10273679 A5 JP H10273679A5
- Authority
- JP
- Japan
- Prior art keywords
- reaction zone
- naphtha
- steam
- cat naphtha
- catalyst
- 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
Claims (6)
- ナフサの自動車オクタン価を上昇させながら、C3オレフィン及びC4オレフィンの収率を増加させるために原料をアップグレードするための流動接触分解法であって、
(a)熱い再生触媒を、下流反応帯域及び上流反応帯域を含むライザー反応器に導き、
(b)該上流反応帯域において、620〜775℃の温度で、かつナフサとスチームの1.5秒より短い蒸気滞留時間で、熱い触媒を軽質キャットナフサと接触させ、その際、軽質キャットナフサ中に存在するC5〜C9オレフィンの少なくとも一部が、C3オレフィン及びC4オレフィンに分解され、
(c)該下流反応帯域において、600〜750℃の温度で、かつ20秒より短い蒸気滞留時間で、該上流反応帯域からの触媒、分解ナフサ生成物及びスチームを重質原料と接触させ、
(d)該上流反応帯域及び該下流反応帯域からの、廃触媒、分解生成物及びスチームを分離帯域に導き、
(e)軽質キャットナフサ及びスチームを含有する分解生成物を廃触媒から分離し、軽質キャットナフサ生成物の少なくとも一部を、工程(b)の上流反応帯域に再循環させ、
(f)廃触媒をストリッピング帯域に導き、ストリッピング条件下で廃触媒をストリップし、
(g)ストリップされた廃触媒を再生帯域に導き、再生条件下で廃触媒を再生する、
以上の工程を含むことを特徴とするキャットナフサの再分解方法。 - 前記上流反応帯域において、スチームの量が、軽質キャットナフサの全重量を基準として、2〜50重量%であることを特徴とする請求項1に記載のキャットナフサの再分解方法。
- 前記上流反応帯域において、ナフサおよびスチームの前記蒸気滞留時間が、1秒未満であることを特徴とする請求項1に記載のキャットナフサの再分解方法。
- 前記工程(b)において、プロセス条件が、100〜400kPaの圧力で、75〜150の触媒/油比(重量/重量)を包含することを特徴とする請求項1に記載のキャットナフサの再分解方法。
- 前記工程(c)において、プロセス条件が、100〜400kPaの圧力で、4〜10の触媒/油比、かつ2〜20秒の蒸気滞留時間を包含することを特徴とする請求項1に記載のキャットナフサの再分解方法。
- 前記工程(c)において、原料が、565℃を超える初留点を有する高沸点留分を、原料を基準として、1〜15重量%を含むことを特徴とする請求項1に記載のキャットナフサの再分解方法。
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/768,874 US5846403A (en) | 1996-12-17 | 1996-12-17 | Recracking of cat naphtha for maximizing light olefins yields |
| US768,874 | 1996-12-17 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JPH10273679A JPH10273679A (ja) | 1998-10-13 |
| JPH10273679A5 true JPH10273679A5 (ja) | 2005-07-28 |
| JP4099254B2 JP4099254B2 (ja) | 2008-06-11 |
Family
ID=25083747
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP36408797A Expired - Fee Related JP4099254B2 (ja) | 1996-12-17 | 1997-12-17 | 軽質オレフィン類の収率を最大にするためのキャットナフサの再分解方法 |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US5846403A (ja) |
| EP (1) | EP0849347B1 (ja) |
| JP (1) | JP4099254B2 (ja) |
| CA (1) | CA2220794C (ja) |
| DE (1) | DE69720932T2 (ja) |
Families Citing this family (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6339180B1 (en) * | 1998-05-05 | 2002-01-15 | Exxonmobil Chemical Patents, Inc. | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| US6803494B1 (en) | 1998-05-05 | 2004-10-12 | Exxonmobil Chemical Patents Inc. | Process for selectively producing propylene in a fluid catalytic cracking process |
| US6429348B1 (en) * | 1998-05-05 | 2002-08-06 | Exxonmobil Chemical Patents, Inc. | Method for selectively producing propylene by catalytically cracking an olefinic hydrocarbon feedstock |
| US6388152B1 (en) * | 1998-05-05 | 2002-05-14 | Exxonmobil Chemical Patents Inc. | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| US6093867A (en) * | 1998-05-05 | 2000-07-25 | Exxon Research And Engineering Company | Process for selectively producing C3 olefins in a fluid catalytic cracking process |
| CN1100116C (zh) * | 1999-06-23 | 2003-01-29 | 中国石油化工集团公司 | 一种多产柴油和液化气的催化转化方法 |
| EP1205530B1 (en) | 1999-06-23 | 2015-07-22 | China Petrochemical Corporation | Catalytic converting process for producing prolifically diesel oil and liquefied gas |
| US6339181B1 (en) * | 1999-11-09 | 2002-01-15 | Exxonmobil Chemical Patents, Inc. | Multiple feed process for the production of propylene |
| US20010032802A1 (en) * | 2000-03-23 | 2001-10-25 | Eduardo Mon | FCC process |
| US20020014438A1 (en) * | 2000-04-17 | 2002-02-07 | Swan George A. | Recracking mixture of cycle oil and cat naphtha for maximizing light olefins yields |
| US20010042702A1 (en) | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| US6565739B2 (en) | 2000-04-17 | 2003-05-20 | Exxonmobil Research And Engineering Company | Two stage FCC process incorporating interstage hydroprocessing |
| US6569315B2 (en) | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process |
| US20010042701A1 (en) | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| US6569316B2 (en) | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process incorporating shape-selective zeolite catalysts |
| CN1179022C (zh) * | 2001-05-30 | 2004-12-08 | 中国石油化工股份有限公司 | 伴有催化剂低温再生的轻质石油烃催化改质方法 |
| US20030116471A1 (en) * | 2001-08-29 | 2003-06-26 | China Petroleum & Chemical Corporation | Catalytic cracking process of petroleum hydrocarbons |
| US6867341B1 (en) | 2002-09-17 | 2005-03-15 | Uop Llc | Catalytic naphtha cracking catalyst and process |
| US7008527B2 (en) | 2002-10-23 | 2006-03-07 | Institut Francais Du Petrole | Process for catalytic cracking two integrated cracking zones of different degrees of severity followed by a cooling zone |
| US7425258B2 (en) * | 2003-02-28 | 2008-09-16 | Exxonmobil Research And Engineering Company | C6 recycle for propylene generation in a fluid catalytic cracking unit |
| US7270739B2 (en) * | 2003-02-28 | 2007-09-18 | Exxonmobil Research And Engineering Company | Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation |
| BR0302326A (pt) * | 2003-06-03 | 2005-03-29 | Petroleo Brasileiro Sa | Processo de craqueamento catalìtico fluido de cargas mistas de hidrocarbonetos de diferentes origens |
| CN1333046C (zh) * | 2004-04-29 | 2007-08-22 | 中国石油化工股份有限公司 | 一种石油烃类催化转化方法 |
| CN100350019C (zh) * | 2004-12-13 | 2007-11-21 | 洛阳石化设备研究所 | 一种可用于石油烃类原料催化转化的提升管反应器 |
| CN100410350C (zh) * | 2004-12-13 | 2008-08-13 | 洛阳石化设备研究所 | 石油烃类原料生产清洁燃料油的催化转化方法及装置 |
| US7682501B2 (en) * | 2004-12-23 | 2010-03-23 | Abb Lummus Global, Inc. | Processing of different feeds in a fluid catalytic cracking unit |
| US20080011644A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| US20080011645A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations |
| US20080081006A1 (en) * | 2006-09-29 | 2008-04-03 | Myers Daniel N | Advanced elevated feed distribution system for very large diameter RCC reactor risers |
| CN101362960B (zh) * | 2007-08-09 | 2012-12-12 | 中国石油化工股份有限公司 | 一种生产高辛烷值汽油的催化转化方法 |
| US8137535B2 (en) * | 2008-01-29 | 2012-03-20 | Kellogg Brown & Root Llc | Method for adjusting catalyst activity |
| US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
| US8246914B2 (en) * | 2008-12-22 | 2012-08-21 | Uop Llc | Fluid catalytic cracking system |
| US8889076B2 (en) * | 2008-12-29 | 2014-11-18 | Uop Llc | Fluid catalytic cracking system and process |
| BR112012020144A2 (pt) * | 2010-02-18 | 2018-11-06 | Uop Llc | aparelho e processo de craqueamento catalítico fluido. |
| CA2795120C (en) | 2010-03-31 | 2019-10-08 | Indian Oil Corporation Ltd | A process for simulataneous cracking of lighter and heavier hydrocarbon feed and system for the same |
| FR2968010B1 (fr) * | 2010-11-25 | 2014-03-14 | Ifp Energies Now | Procede de conversion d'une charge lourde en distillat moyen |
| WO2013016660A1 (en) | 2011-07-27 | 2013-01-31 | Saudi Arabian Oil Company | Fluidized catalytic cracking of paraffinic naphtha in a downflow reactor |
| CN102950033B (zh) * | 2011-08-31 | 2014-07-02 | 中国石油化工股份有限公司 | 一种使用重质燃料油快速稳定催化剂活性的方法及设备 |
| EP3106504B1 (en) | 2015-06-19 | 2020-02-05 | Reliance Industries Limited | Process for propylene and lpg recovery in fcc fuel gas |
| US9896627B2 (en) | 2015-10-14 | 2018-02-20 | Saudi Arabian Oil Company | Processes and systems for fluidized catalytic cracking |
| CN106609151B (zh) * | 2015-10-21 | 2018-05-18 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的方法 |
| CN119656995A (zh) | 2023-09-20 | 2025-03-21 | 中国石油天然气股份有限公司 | 催化裂解的装置和方法 |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3617497A (en) * | 1969-06-25 | 1971-11-02 | Gulf Research Development Co | Fluid catalytic cracking process with a segregated feed charged to the reactor |
| US3692667A (en) * | 1969-11-12 | 1972-09-19 | Gulf Research Development Co | Catalytic cracking plant and method |
| US4051013A (en) * | 1973-05-21 | 1977-09-27 | Uop Inc. | Fluid catalytic cracking process for upgrading a gasoline-range feed |
| US3928172A (en) * | 1973-07-02 | 1975-12-23 | Mobil Oil Corp | Catalytic cracking of FCC gasoline and virgin naphtha |
| US4892643A (en) * | 1986-09-03 | 1990-01-09 | Mobil Oil Corporation | Upgrading naphtha in a single riser fluidized catalytic cracking operation employing a catalyst mixture |
| FR2625509B1 (fr) * | 1987-12-30 | 1990-06-22 | Total France | Procede et dispositif de conversion d'hydrocarbures en lit fluidise |
| US5043522A (en) * | 1989-04-25 | 1991-08-27 | Arco Chemical Technology, Inc. | Production of olefins from a mixture of Cu+ olefins and paraffins |
| FR2658833B1 (fr) * | 1990-02-26 | 1994-04-29 | Inst Francais Du Petrole | Procede de craquage a l'etat fluide d'une charge d'hydrocarbures. |
| US5318689A (en) * | 1992-11-16 | 1994-06-07 | Texaco Inc. | Heavy naphtha conversion process |
-
1996
- 1996-12-17 US US08/768,874 patent/US5846403A/en not_active Expired - Lifetime
-
1997
- 1997-12-02 CA CA002220794A patent/CA2220794C/en not_active Expired - Lifetime
- 1997-12-04 EP EP97121284A patent/EP0849347B1/en not_active Expired - Lifetime
- 1997-12-04 DE DE69720932T patent/DE69720932T2/de not_active Expired - Lifetime
- 1997-12-17 JP JP36408797A patent/JP4099254B2/ja not_active Expired - Fee Related
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