WO2009015922A1 - New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins. - Google Patents
New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins. Download PDFInfo
- Publication number
- WO2009015922A1 WO2009015922A1 PCT/EP2008/056692 EP2008056692W WO2009015922A1 WO 2009015922 A1 WO2009015922 A1 WO 2009015922A1 EP 2008056692 W EP2008056692 W EP 2008056692W WO 2009015922 A1 WO2009015922 A1 WO 2009015922A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- furan
- methyleneamino
- phenyl
- trifluoromethyl
- formula
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/38—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of titanium, zirconium or hafnium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/28—Titanium compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/72—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
- C08F4/74—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals
- C08F4/76—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals selected from titanium, zirconium, hafnium, vanadium, niobium or tantalum
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
Definitions
- the present invention relates to new tridentate ligand compounds with imino furan units, to a method for manufacturing said compounds and to their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins .
- the present invention relates to the use of such new ligand compounds for preparing metallic complexes useful as catalysts for the homopolymerisation and copolymerisation of ethylene and ⁇ -olefins, to the catalytic systems including such metallic complexes and to a method for homopolymerising or copolymerising ethylene and ⁇ -olefins using such catalytic systems.
- R a , R >2d, R c and R 2x x have different meanings.
- the Applicant searched for other ligands in order to produce new catalysts for the polymerisation of ethylene and of ⁇ -olefins, and discovered the new tridentate anionic ligands with imino furane units, which are the subject-matter of the present invention.
- the homopolymers of ethylene obtained with such new catalysts are linear and have a monomodal distribution of polydispersity of 3 to 9 with very small tail ends.
- a first subject-matter of the present invention relates to a compound of formula (I) :
- R 1 to R 8 each represent independently hydrogen, halogen, a substituted or unsubstituted C1-C20 hydrocarbyl group, an inert functional group, wherein each of the radicals R 1 to R 8 can be linked to a neighbouring radical in order to form a cycle with carbon atoms to which said radicals are attached ;
- the hydrocarbyl groups encompass methyl, tert- butyl and phenyl groups.
- the hydrocarbyl groups can include a heteroatom such as oxygen or nitrogen atoms in their chains.
- the possible substituents of hydrocarbyl groups can be selected among CF 3 , NO2, OMe and halogen such as Cl.
- the inert functional groups can be selected among CF 3 , NO 2 , OMe and halogen.
- R 1 to R 3 are each preferably selected independently from the group consisting of hydrogen and aryl groups.
- Aryl groups can be selected among phenyl, naphthyl, and substituted phenyl groups.
- R 4 is preferably selected in the group consisting of hydrogen and methyl group.
- R 5 to R 8 are preferably independently selected in the group consisting of hydrogen, alkyl, aryl, methoxy, halogen, nitro and cyano .
- Y is preferably 0.
- m is preferably 0 or 1.
- Another subject-matter of the present invention relates to a method for manufacturing a compound of formula (I) as defined above, characterised in that a compound of formula (II) :
- a further subject-matter of the present invention relates to the use of a compound as defined above or prepared by the method as defined above as a ligand of a metallic complex.
- a further subject-matter of the present invention relates to a metallic complex of the formula (IV) :
- R 1 to R 8 , Y and m are as defined above ;
- - M is a metal belonging to groups 3 to 8 of the Periodic Classification ;
- - X represents an halogen, a substituted or unsubstituted C1-C20 hydrocarbyl group, an amino group, an aryloxy group or an alkoxy group ;
- - n is a numeral value determined by the oxidation state of the metal minus one.
- R 1 to R 8 , Y and m are as mentioned above for the compound of formula (I) .
- M is preferably selected from the metals belonging to groups 3 to 8 of the Periodic Classification, being in particular Ti, Cr, Fe, Zr, Hf, V, Mn, a rare-earth metal, being preferably Ti, Cr, Fe and Zr.
- X preferably represents halogen, alkyl such as benzyl, amino such as dimethylamino, alkoxy such as isopropoxy, aryloxy such as phenoxy, preferably halogen such as chlorine.
- a further subject-matter of the present invention relates to a method for manufacturing a metallic complex as defined above, wherein a metallic compound of formula (V) :
- a further subject-matter of the present invention relates to the use of the metallic complex as defined above or prepared by the process as defined above as a catalyst in the homopolymerisation and the copolymerisation of ethylene and ⁇ -olefins.
- Exemplary ⁇ -olefins are the ones having from 3 to 8 carbon atoms, preferably propylene.
- a further subject-matter of the present invention relates to a catalytic system comprising : the metallic complex as defined above ; - an activating agent selected in particular from the aluminum alkyls, the aluminoxanes and the boron-based activators ; and optionally, a carrier of the said metallic complex.
- the aluminum alkyls are represented by the formula AlR x , wherein R are all identical or different, and are selected from halides or from alkoxy or alkyl groups having from 1 to 12 carbon atoms and x is from 1 to 3.
- Especially suitable aluminum alkyls are dialkylaluminum chloride, the most preferred being diethylaluminum chloride (Et 2 AlCl) .
- the preferred aluminoxanes comprise oligomeric linear and/or cyclic alkyl aluminoxanes represented by the formula :
- R" for oligomeric, cyclic aluminoxanes, wherein :
- - p is 1-40, preferably 10-20 ;
- - o is 3-40, preferably 3-20 ; and - R' or R" is a Ci-Cs alkyl group, being preferably methyl. Methylaluminoxane is preferably used.
- Suitable boron-based activating agents that can be used comprise a triphenyl carbenium boronate such as tetrakis-pentafluorophenyl-borato-triphenylcarbenium
- the support if present, can be a porous mineral oxide. It is advantageously selected from silica, alumina and mixtures thereof. Preferably, it is silica.
- the activating agent is preferably an alkyl aluminum or an aluminoxane, the molar ratio Al/M being approximately 500 to 2000, preferably about 1000.
- Still a further subject-matter of the present invention relates to a method for homopolymerising or copolymerising ethylene and ⁇ -olefins, comprising the steps of : (a) injecting into the reactor the catalytic system as defined above, a solvent and optionally a scavenger ; (b) injecting the monomer and optional comonomer(s) into the reactor either before or after or simultaneously with step (a) ; (c) maintaining under polymerisation conditions ;
- the scavenger may be selected from aluminium alkyls or diethyl zinc.
- the monomers that can be used in the present invention are selected among ethylene and ⁇ -olefins having from 3 to 8 carbon atoms, being preferably ethylene and propylene .
- the conditions of temperature and pressure for the polymerisation process are not particularly limited.
- the pressure in the reactor can vary from 0.5 to 50 bars, preferably from 15 to 29 bars.
- the polymerisation temperature can range from 10 to 100 0 C, preferably from 40 to 90 0 C.
- the solvent is typically selected from alcanes or toluene, being preferably toluene, heptane or isobutane.
- the reaction is usually carried out for a period of time of from 15 minutes to 24 hours.
- the polymer obtained according to the present invention is typically obtained as a powder.
- the homopolyethylene that can be obtained have a Mn of 25 to 75 kDa , preferably of 30 - 60 kDa , a Mw of 150 - 400 kDa , preferably of 175-350 kDa, and a Mw/Mn of about 3 to 9.
- the following Examples are intended to illustrate the present invention without limiting its scope.
- the aminophenol (12 mmol) was added to a solution of furan-2-carbaldehyde (12 mmol) and acid acetic (0.4 ml) in ethanol (30 ml) . The mixture was stirred at room temperature for 18 hours. Then the solvent was removed by evaporation under reduced pressure at 50 0 C.
- Example 1_ Preparation of 2- ⁇ [5- (2-
- the yield is defined as follows: mass of complex obtained/mass of complex expected for 2.5 mmol
- the yield is defined as follows: mass of complex obtained/mass of complex expected for 2.5 mmol
- the support used was silica Sylopol® 952x1836 from Grace, modified with MAO to obtain a support with 60 wt% of MAO.
- the complex and the support were stirred in 50 ml of toluene at room temperature during 2 hours. Then the toluene was removed, the resulting catalyst was washed 3 times with pentane and dried under vacuum. The data are given in table 3.
- Ethylene polymerisation reactions were carried out in a 130 ml stainless steel autoclave equipped with mechanical stirring and a stainless steel injection cylinder.
- the reactor was first dried under nitrogen flow at 100 0 C during 10 min. Then it was cooled down to the reaction temperature (85°C) and 35 ml of isobutane were introduced into the reactor with a syringe pump, followed by the comonomer if required. The pressure was adjusted to the desired value (23.8 bar) with ethylene.
- Activity is expressed as g polyethylene per g catalyst per hour .
- the melting temperature Tm of example 42 was of 132.3°C as measured by DSC.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Furan Compounds (AREA)
Abstract
Description
Claims
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200880019908XA CN101678319B (en) | 2007-06-14 | 2008-05-30 | New tridentate ligand compounds with imino furan units, method for manufacturing the compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylen |
| US12/664,461 US8426540B2 (en) | 2007-06-14 | 2008-05-30 | Tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins |
| JP2010511575A JP5186559B2 (en) | 2007-06-14 | 2008-05-30 | Novel tridentate ligand compound having an iminofuran unit, a process for the preparation of this compound and its use in the preparation of catalysts for the homopolymerization of ethylene and copolymerization with α-olefins |
| EP08826827A EP2155379A1 (en) | 2007-06-14 | 2008-05-30 | New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins. |
| KR1020097025943A KR101166402B1 (en) | 2007-06-14 | 2008-05-30 | New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP07110304.8 | 2007-06-14 | ||
| EP07110304A EP2003125A1 (en) | 2007-06-14 | 2007-06-14 | New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2009015922A1 true WO2009015922A1 (en) | 2009-02-05 |
Family
ID=38744886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2008/056692 Ceased WO2009015922A1 (en) | 2007-06-14 | 2008-05-30 | New tridentate ligand compounds with imino furan units, method for manufacturing said compounds, and their use in the preparation of catalysts for the homopolymerisation and copolymerisation of ethylene and alpha-olefins. |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US8426540B2 (en) |
| EP (2) | EP2003125A1 (en) |
| JP (1) | JP5186559B2 (en) |
| KR (1) | KR101166402B1 (en) |
| CN (1) | CN101678319B (en) |
| WO (1) | WO2009015922A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9255088B2 (en) | 2010-08-11 | 2016-02-09 | The Regents Of The University Of California | Premature-termination-codons readthrough compounds |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BR112012000254A2 (en) | 2009-07-08 | 2016-02-16 | Dermira Canada Inc | tofa analogues useful in treating dermatological disorders or conditions. |
| US9598395B2 (en) | 2012-03-23 | 2017-03-21 | The Regents Of The University Of California | Premature-termination-codons readthrough compounds |
| BR112019006302B1 (en) * | 2016-09-30 | 2022-10-18 | Dow Global Technologies Llc | COMPOSITION AND POLYMERIZATION METHOD |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5714556A (en) * | 1995-06-30 | 1998-02-03 | E. I. Dupont De Nemours And Company | Olefin polymerization process |
| US20020107345A1 (en) * | 1999-12-17 | 2002-08-08 | Ittel Steven Dale | Polymerization of olefins |
| EP1238989A2 (en) * | 2001-02-21 | 2002-09-11 | Mitsui Chemicals, Inc. | Olefin polymerization catalyst and process for producing olefin polymer with the catalyst |
| WO2004041796A1 (en) * | 2002-11-04 | 2004-05-21 | Basf Aktiengesellschaft | Transition metal catalysts for (co)polymerizing olefinic monomers |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1469227A1 (en) * | 1964-12-31 | 1970-06-04 | Bayer Ag | Furan compounds |
| DE69514156T2 (en) * | 1994-06-24 | 2000-06-29 | Praxair S.T. Technology, Inc. | Process for the production of a coating based on MCrAlY with finely divided oxides |
| WO2001068724A2 (en) * | 2000-03-10 | 2001-09-20 | E.I. Dupont De Nemours And Company | Polymerization of olefins |
| DE10348023A1 (en) * | 2003-10-15 | 2005-05-19 | Imtm Gmbh | New alanyl aminopeptidase inhibitors for the functional manipulation of different cells and for the treatment of immunological, inflammatory, neuronal and other diseases |
| EP1749841A1 (en) | 2005-08-03 | 2007-02-07 | Total Petrochemicals Research Feluy | Activating fluorinated supports with iron-based post-metallocene complexes |
| EP1925623A1 (en) * | 2006-11-24 | 2008-05-28 | Total Petrochemicals Research Feluy | Polymerisation of ethylene and alpha-olefins with pyrrol-iminophenol complexes. |
-
2007
- 2007-06-14 EP EP07110304A patent/EP2003125A1/en not_active Withdrawn
-
2008
- 2008-05-30 US US12/664,461 patent/US8426540B2/en not_active Expired - Fee Related
- 2008-05-30 JP JP2010511575A patent/JP5186559B2/en not_active Expired - Fee Related
- 2008-05-30 EP EP08826827A patent/EP2155379A1/en not_active Withdrawn
- 2008-05-30 CN CN200880019908XA patent/CN101678319B/en not_active Expired - Fee Related
- 2008-05-30 WO PCT/EP2008/056692 patent/WO2009015922A1/en not_active Ceased
- 2008-05-30 KR KR1020097025943A patent/KR101166402B1/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5714556A (en) * | 1995-06-30 | 1998-02-03 | E. I. Dupont De Nemours And Company | Olefin polymerization process |
| US20020107345A1 (en) * | 1999-12-17 | 2002-08-08 | Ittel Steven Dale | Polymerization of olefins |
| EP1238989A2 (en) * | 2001-02-21 | 2002-09-11 | Mitsui Chemicals, Inc. | Olefin polymerization catalyst and process for producing olefin polymer with the catalyst |
| WO2004041796A1 (en) * | 2002-11-04 | 2004-05-21 | Basf Aktiengesellschaft | Transition metal catalysts for (co)polymerizing olefinic monomers |
Non-Patent Citations (2)
| Title |
|---|
| BELAL A A M: "Complexes of Co(II), Ni(II), Cu(II), UO2(II), Fe(III), Y(III) and La(III) with Schiff bases derived from 2-furancarboxaldehyde and hydroxyanilines", ASW.SC.TEC.BULL., vol. 17, 1996, pages 2 - 11, XP009093256 * |
| MATSUI S ET AL: "FI Catalysts: super active new ethylene polymerization catalysts", CATALYSIS TODAY, ELSEVIER, vol. 66, no. 1, 2001, pages 63 - 73, XP002438748, ISSN: 0920-5861 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9255088B2 (en) | 2010-08-11 | 2016-02-09 | The Regents Of The University Of California | Premature-termination-codons readthrough compounds |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101166402B1 (en) | 2012-07-23 |
| US20100311930A1 (en) | 2010-12-09 |
| EP2155379A1 (en) | 2010-02-24 |
| US8426540B2 (en) | 2013-04-23 |
| EP2003125A1 (en) | 2008-12-17 |
| CN101678319B (en) | 2012-11-21 |
| KR20100021449A (en) | 2010-02-24 |
| JP5186559B2 (en) | 2013-04-17 |
| JP2010530850A (en) | 2010-09-16 |
| CN101678319A (en) | 2010-03-24 |
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