WO2001064763A3 - Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process - Google Patents
Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process Download PDFInfo
- Publication number
- WO2001064763A3 WO2001064763A3 PCT/US2001/006687 US0106687W WO0164763A3 WO 2001064763 A3 WO2001064763 A3 WO 2001064763A3 US 0106687 W US0106687 W US 0106687W WO 0164763 A3 WO0164763 A3 WO 0164763A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- zone
- stream
- catalyst
- olefins
- stripping
- 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.)
- Ceased
Links
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
- C10G57/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
- C10G57/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process with polymerisation
-
- 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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking steps
-
- 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
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)
- 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)
- Polymerisation Methods In General (AREA)
- Polymerization Catalysts (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Catalysts (AREA)
Abstract
A process for producing polymers from olefins selectively produced from a catalytically cracked or thermally cracked naphtha stream is disclosed herein. The naphtha stream is introduced into a process unit comprised of a reaction zone, a stripping zone, a catalyst regeneration zone, and a fractionation zone. The naphtha feedstream is contacted in the reaction zone with a catalyst containing from about 10 to 50 wt. % of a crystalline zeolite having an average pore diameter less than about 0.7 nanometers at reaction conditions which include temperatures ranging from about 500° to 650 °C and a hydrocarbon partial pressure from about 10 to 40 psia. Vapor products are collected overhead and the catalyst particles are passed through the stripping zone on the way to the catalyst regeneration zone. Volatiles are stripped with stream in the stripping zone and the catalyst particles are sent to the catalyst regeneration zone where coke is burned from the catalyst, which is then recycled to the reaction zone. Overhead products from the reaction zone are passed to a fractionation zone where a stream of C3 products is recovered and a stream rich in C4 and/or C5 olefins is recycled to the stripping zone. The olefins can be further processed and polymerized to form a variety of polymer materials.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MXPA02008552A MXPA02008552A (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3. |
| JP2001564255A JP2003525323A (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from C3 olefins selectively produced from naphtha / steam feed in a fluid catalytic cracking process |
| CA002400598A CA2400598A1 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process |
| AU2001241916A AU2001241916A1 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| EP01913235A EP1261648A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process |
Applications Claiming Priority (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/517,554 | 2000-03-02 | ||
| US09/517,551 US6258257B1 (en) | 1998-05-05 | 2000-03-02 | Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process |
| US09/517,551 | 2000-03-02 | ||
| US09/517,503 US6339180B1 (en) | 1998-05-05 | 2000-03-02 | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| US09/517,497 US6258990B1 (en) | 1998-05-05 | 2000-03-02 | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process from a naphtha/steam feed |
| US09/517,554 US6388152B1 (en) | 1998-05-05 | 2000-03-02 | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| US09/517,503 | 2000-03-02 | ||
| US09/517,497 | 2000-03-02 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2001064763A2 WO2001064763A2 (en) | 2001-09-07 |
| WO2001064763A3 true WO2001064763A3 (en) | 2002-01-31 |
Family
ID=27504537
Family Applications (4)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2001/006687 Ceased WO2001064763A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process |
| PCT/US2001/006685 Ceased WO2001064761A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process from a naphtha/steam feed |
| PCT/US2001/006684 Ceased WO2001064760A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process |
| PCT/US2001/006686 Ceased WO2001064762A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced by a two stage fluid catalytic cracking process |
Family Applications After (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2001/006685 Ceased WO2001064761A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process from a naphtha/steam feed |
| PCT/US2001/006684 Ceased WO2001064760A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced in a fluid catalytic cracking process |
| PCT/US2001/006686 Ceased WO2001064762A2 (en) | 2000-03-02 | 2001-03-01 | Process for producing polypropylene from c3 olefins selectively produced by a two stage fluid catalytic cracking process |
Country Status (7)
| Country | Link |
|---|---|
| EP (3) | EP1261648A2 (en) |
| JP (3) | JP2004516334A (en) |
| CN (3) | CN1406252A (en) |
| AU (4) | AU2001239991A1 (en) |
| CA (3) | CA2400524A1 (en) |
| MX (3) | MXPA02008553A (en) |
| WO (4) | WO2001064763A2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8920630B2 (en) | 2007-04-13 | 2014-12-30 | Shell Oil Company | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7267759B2 (en) | 2003-02-28 | 2007-09-11 | Exxonmobil Research And Engineering Company | Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation |
| US7425258B2 (en) | 2003-02-28 | 2008-09-16 | Exxonmobil Research And Engineering Company | C6 recycle for propylene generation in a fluid catalytic cracking unit |
| WO2009048920A1 (en) * | 2007-10-10 | 2009-04-16 | Shell Oil Company | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| RU2474605C2 (en) * | 2007-11-29 | 2013-02-10 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Plants and methods for obtaining middle-distillate product and low molecular weight olefins from initial hydrocarbon raw material |
| CN101747129B (en) * | 2008-11-28 | 2013-09-04 | 中国石油化工股份有限公司 | Method for producing light olefins through catalytic conversion |
| CN102531821B (en) | 2010-12-28 | 2015-03-25 | 中国科学院大连化学物理研究所 | Method for catalyzing catalytic cracking reaction of methanol coupled with naphtha using modified ZSM-5 molecular sieve based catalyst |
| CN103121894A (en) * | 2011-11-18 | 2013-05-29 | 中国石油化工股份有限公司 | Combined method for producing low-carbon olefin |
| CN105582997B (en) * | 2014-10-21 | 2018-05-18 | 中国石油化工股份有限公司 | The method of catalyst of naphtha catalytic cracking production propylene and preparation method thereof and naphtha catalytic cracking production propylene |
| USRE50515E1 (en) | 2015-12-22 | 2025-08-05 | Sabic Global Technologies B.V. | Methods for producing ethylene and propylene from naphtha |
| CN113646081B (en) * | 2019-03-18 | 2024-01-09 | 埃克森美孚科技工程公司 | Mesoporous catalyst compounds and their uses |
| KR20220117899A (en) * | 2019-12-23 | 2022-08-24 | 셰브런 유.에스.에이.인크. | Circular Economy of Plastic Waste to Polypropylene Through Refining FCC Units |
| JP7623380B2 (en) * | 2019-12-23 | 2025-01-28 | シェブロン ユー．エス．エー． インコーポレイテッド | Circular economy of waste plastics to polypropylene and lubricants via refined FCC and isomerization dewaxing units |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999057225A1 (en) * | 1998-05-05 | 1999-11-11 | Exxon Research And Engineering Company | Process for selectively producing c3 olefins in a fluid catalytic cracking process |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6118035A (en) * | 1998-05-05 | 2000-09-12 | Exxon Research And Engineering Co. | Process for selectively producing light olefins in a fluid catalytic cracking process from a naphtha/steam feed |
| US6069287A (en) * | 1998-05-05 | 2000-05-30 | Exxon Research And Engineering Co. | Process for selectively producing light olefins in a fluid catalytic cracking process |
| US6106697A (en) * | 1998-05-05 | 2000-08-22 | Exxon Research And Engineering Company | Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins |
-
2001
- 2001-03-01 CN CN 01805858 patent/CN1406252A/en active Pending
- 2001-03-01 AU AU2001239991A patent/AU2001239991A1/en not_active Abandoned
- 2001-03-01 MX MXPA02008553A patent/MXPA02008553A/en unknown
- 2001-03-01 JP JP2001564252A patent/JP2004516334A/en not_active Withdrawn
- 2001-03-01 AU AU2001241916A patent/AU2001241916A1/en not_active Abandoned
- 2001-03-01 WO PCT/US2001/006687 patent/WO2001064763A2/en not_active Ceased
- 2001-03-01 CN CN 01805862 patent/CN1406253A/en active Pending
- 2001-03-01 AU AU2001243379A patent/AU2001243379A1/en not_active Abandoned
- 2001-03-01 CA CA002400524A patent/CA2400524A1/en not_active Abandoned
- 2001-03-01 MX MXPA02008552A patent/MXPA02008552A/en unknown
- 2001-03-01 CN CN 01805874 patent/CN1406254A/en active Pending
- 2001-03-01 EP EP01913235A patent/EP1261648A2/en not_active Withdrawn
- 2001-03-01 EP EP01916344A patent/EP1259555A2/en not_active Withdrawn
- 2001-03-01 JP JP2001564255A patent/JP2003525323A/en not_active Withdrawn
- 2001-03-01 CA CA002400382A patent/CA2400382A1/en not_active Abandoned
- 2001-03-01 WO PCT/US2001/006685 patent/WO2001064761A2/en not_active Ceased
- 2001-03-01 JP JP2001564253A patent/JP2004516335A/en not_active Withdrawn
- 2001-03-01 WO PCT/US2001/006684 patent/WO2001064760A2/en not_active Ceased
- 2001-03-01 MX MXPA02008554A patent/MXPA02008554A/en unknown
- 2001-03-01 WO PCT/US2001/006686 patent/WO2001064762A2/en not_active Ceased
- 2001-03-01 EP EP01914623A patent/EP1261649A2/en not_active Withdrawn
- 2001-03-01 AU AU2001239990A patent/AU2001239990A1/en not_active Abandoned
- 2001-03-01 CA CA002400598A patent/CA2400598A1/en not_active Abandoned
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999057225A1 (en) * | 1998-05-05 | 1999-11-11 | Exxon Research And Engineering Company | Process for selectively producing c3 olefins in a fluid catalytic cracking process |
Non-Patent Citations (2)
| Title |
|---|
| ELVERS B. ET AL.: "ULLMANN'S ENCYCLOPEDIA OF INDUSTRIAL CHEMISTRY", 1992, VCH VERLAG., WEINHEIM, DE, XP002174091 * |
| MOORE E.P.: "Polypropylene handbook", 1996, HANSER PUBL., MUNICH, DE, XP002174092 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8920630B2 (en) | 2007-04-13 | 2014-12-30 | Shell Oil Company | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2001064760A3 (en) | 2002-01-03 |
| AU2001241916A1 (en) | 2001-09-12 |
| MXPA02008552A (en) | 2003-03-12 |
| EP1261648A2 (en) | 2002-12-04 |
| JP2004516334A (en) | 2004-06-03 |
| CA2400598A1 (en) | 2001-09-07 |
| WO2001064760A2 (en) | 2001-09-07 |
| WO2001064762A3 (en) | 2002-01-24 |
| CN1406254A (en) | 2003-03-26 |
| JP2004516335A (en) | 2004-06-03 |
| CA2400524A1 (en) | 2001-09-07 |
| EP1259555A2 (en) | 2002-11-27 |
| CA2400382A1 (en) | 2001-09-07 |
| WO2001064761A3 (en) | 2002-01-03 |
| WO2001064761A2 (en) | 2001-09-07 |
| AU2001239991A1 (en) | 2001-09-12 |
| JP2003525323A (en) | 2003-08-26 |
| AU2001243379A1 (en) | 2001-09-12 |
| EP1261649A2 (en) | 2002-12-04 |
| CN1406253A (en) | 2003-03-26 |
| CN1406252A (en) | 2003-03-26 |
| WO2001064762A2 (en) | 2001-09-07 |
| MXPA02008553A (en) | 2003-03-12 |
| AU2001239990A1 (en) | 2001-09-12 |
| MXPA02008554A (en) | 2003-04-22 |
| WO2001064763A2 (en) | 2001-09-07 |
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