OLIGOMERIZATION OF POLYMER-REDUCED OLEPHINIC COMPOUNDS

专利摘要:
The process for producing glues The present invention relates to processes for bonding two substrates of which at least one is transparent and of which at least one has a surface with a surface energy (measured by test method c) of at least 40 mn / m, comprising the use of a double-sided self-adhesive product with a first b and a second self-adhesive surface, wherein the first self-adhesive surface is covered with a first separating layer and the second self-adhesive surface is covered with a second layer. where the peel force of the first self-adhesive surface first peel, azk ~ 2, is less than the peel force of the second self-adhesive second peel, azk ~ 2, and wherein the proportion of the adhesive force of the fresh adhesive of the first self-adhesive surface on a surface with suppressive energy (measured by the method of test c) of a maximum of 40mk / m (fresh kk, measured by test method b) for peel force (measured by test method a) of the second self-adhesive second surface separation layer, kkfresco: azk ~ 2 ~, at least 13,5, comprising the following stage: (a) detaching the first self-adhesive first surface separating layer as well as contacting the first self-adhesive surface with the surface with a surface energy (measured by test method c) maximum 40 mn / m.
公开号:BR112012009098B1
申请号:R112012009098-4
申请日:2010-10-13
公开日:2018-05-22
发明作者:John Hanton Martin；Matthew Smith David；Fullard Gabrielli William；William Kelly Mark
申请人:Sasol Technology PTY；
IPC主号:

专利说明:

(54) Title: OLIGOMERIZATION OF OLEPHIN COMPOUNDS WITH REDUCED POLYMER FORMATION (51) Int.CI .: C07C 2/32; C07C 2/36 (30) Unionist Priority: 19/10/2009 ZA 2009/07285 (73) Holder (s): SASOL TECHNOLOGY (PTY) LTD (72) Inventor (s): MARTIN JOHN HANTON; DAVID MATTHEWSMITH; WILLIAM FULLARD GABRIELLI; MARK WILLIAM KELLY
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Descriptive Report of the Invention Patent for OLIGOMERIZATION OF OLEFINIC COMPOUNDS WITH REDUCED POLYMER FORMATION.
Technical Field
The present invention relates to the oligomerization of olefinic compounds in the presence of an activated oligomerization catalyst and also relates to the use of a zinc compound in oligomerization.
Background of the Technique
A number of different oligomerization technologies are known to produce α-olefins. Some of these processes, including the Shell Higher Olefins Process and Ziegler-type technologies, have been summarized in WO 04/056479 A1. The same document also discloses that the prior art (for example, WO 03/053891 and WO 02/04119) teaches that chromium-based catalysts containing heteroaromatic binders with phosphorus and nitrogen heteroatoms selectively catalyze the trimerization of ethylene in 1hexene.
Processes in which transition metals and heteroaromatic binders are combined to form catalysts for trimerization, tetramerization, oligomerization and polymerization of olefinic compounds have also been described in different patent applications such as WO 03/053890 A1; WO 03/053891; WO 04/056479 A1; WO 04/056477 A1; WO 04/056480 A1; WO 04/056478 A1; WO 05/123884 A2; WO 05/123633 A1 and US Patent No. 7,285,607.
The catalysts used in the above mentioned trimerization, tetramerization, oligomerization or polymerization processes all include one or more activators to activate the catalyst. Such an activator is a compound that generates an active catalyst when the activator is combined with the catalyst.
Suitable activators include organoaluminum compounds, organoboro compounds, organic salts like methyl lithium and methyl magnesium bromide, inorganic acids and salts like tetrafluoroboric acid etherate, silver tetrafluoroborate, sodium hexafluoroantimonate and the like.
2/42
A common catalyst activator used in combination with Cr-based catalysts for oligomerization of olefinic compounds is alkylaluminoxane, particularly methylaluminoxane (MAO). It is well known that MAO includes significant amounts of alkyl aluminum in the form of trimethyl aluminum (TMA), and in effect the catalyst activator is a combination of TMA and MAO. MAO can also be replaced with modified MAO (MMAO), which may contain free trialkyl aluminum in the form of TMA and heavier trialkyl aluminum. The use of organoboro compounds as catalyst activators is also known.
Activators containing aluminum compounds are more costly for the purpose, which significantly impacts the process economy of olefin oligomerization technologies using this class of activators. For this reason, it is desirable to perform commercial oligomerization processes at low concentrations of activator. However, in the case where an aluminum-containing compound was used as an activator for transition metal-based oligomerization catalysts, it was found that under conditions of low concentrations of starting aluminum (eg <6 mmol / l), low reaction speeds and high levels of unwanted solid formation (polyethylene (PE) and waxes) resulted when ethylene was oligomerized.
Reduction in polymer formation as a by-product in processes (tri- and tetramerization) of Cr-based ethylene oligomerization remains a permanent challenge, since polymer encrustation reduces the execution time and requires stops due to blockages.
The inventors of the present invention have found that reductions in levels of polymer formation can be achieved in chromium-catalyzed olefin oligomerization processes by incorporating a zinc compound, in particular dialkyl zinc, into the catalyst system as described below.
The use of a zinc compound in olefin oligomerization is not known, however it has not been previously disclosed that it can be used in the manner of the present invention to achieve a reduction in polymer strength as described herein. Thus, the use of chain transfer reagents in the polymerization field has been known for a long time. For example, the use of triethyl aluminum in combination with various polymerization catalysts of the type 'chain growth' (for example, 1,3,7 triazacyclonanone) has been studied previously.
WO 2008/085659 and US 2008/0058486 describes the use of several activators for oligomerization catalyst systems. Both contain the statement that other activators or general compounds useful in an oligomerization reaction can be used. These compounds can be activators in some contexts, but they can also serve other functions in the reaction system, such as alkylating a metal center or sequestering impurities. These compounds are within the general definition of activator, but are not considered here to be ion-forming activators. Both of these publications broadly identify these other components as Group 13 reagents, divalent metal reagents and alkali metal reagents and names diethyl zinc as one of a large group of reagents said to be useful as activators for the catalyst compounds with which publications relate. However, none of these publications exemplify such use of these other components and in particular diethyl zinc, nor do they disclose any benefit derived from the use of diethyl zinc, or any effect that such use of diethyl zinc may have on the degree of polymer formation in the oligomerization of chromium-catalyzed olefin.
Description of the Invention
According to the present invention, a process is provided to produce an oligomeric product by oligomerizing at least one olefinic compound, the process including:
a) provide an activated oligomerization catalyst combining, in any order,
i) a chromium source;
ii) a binding compound of the formula I (R ¹ ) mX ¹ (Y) X ² (R ² ) n ... I,
4/42 where:
X ¹ and X ² are independently an atom selected from the group consisting of nitrogen, phosphorus, arsenic, antimony, bismuth, oxygen, sulfur and selenium or said atom oxidized by S, Se, N or O, where the valence of X ¹ and / or X ² allows such oxidation;
Y is a linking group between X ¹ and X ² ;
m and n are independently 0, 1 or a larger integer, and
R ¹ and R ² are independently hydrogen, a hydrocarbyl group, an organo-heteryl group or a hetero-hydrocarbyl group, and R ¹ being the same or different when m> 1, and R ² being the same or different when n> 1 , iii) a catalyst activator or combination of catalyst activators;
b) providing a zinc compound, and
c) contacting at least one olefinic compound with a composition containing the activated oligomerization catalyst and zinc compound, the zinc compound being present in a sufficient amount so that the molar amount of zinc in the zinc compound is the molar amount of chromium in the chromium source is between 1 and 10,000.
According to the present invention, there is also provided a process for activating an oligomerization catalyst to be used to produce an oligomeric product from at least one olefinic compound, the process comprising combining, in any order,
i) a chromium source;
ii) a binding compound of the formula I (R ¹ ) _m X ¹ (Y) X ² (R ² ) n - I, where:
X ¹ and X ² are independently an atom selected from the group consisting of nitrogen, phosphorus, arsenic, antimony, bismuth, oxygen, sulfur and selenium or said atom oxidized by S, Se, N or O, where the valence of X ¹ and / or X ² allows such oxidation;
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Y is a linking group between X ¹ and X ² ;
m and n are independently 0, 1 or a larger integer, and
R ¹ and R ² are independently hydrogen, a hydrocarbyl group, an organo-heteryl group or a hetero-hydrocarbyl group, and R ¹ being the same or different when m> 1, and R ² being the same or different when n> 1 , iii) a catalyst activator or combination of catalyst activators;
iv) a zinc compound, the zinc compound being present in an amount sufficient so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the chromium source is between 1 and 10,000.
In both of the above aspects of the invention, the zinc compound is present in the reaction of the invention in a sufficient amount so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the chromium source is preferably between 10 and 1,000, and more preferably between 50 and 450.
The above aspects of the invention can also include the use of a solvent.
In this specification, the following definitions apply: the term olefinic compound takes an olefin or any compound that includes a carbon-to-carbon double bond and the olefinic portion has a corresponding meaning;
a hydrocarbyl group is a univalent group formed by removing a hydrogen atom from a hydrocarbon;
a hydrocarbilene group is a divalent group formed by removing two hydrogen atoms from the same atom or different carbon atoms, the resulting free valences of which are involved in a double bond;
a heterohydrocarbyl group is a univalent group formed by removing a hydrogen atom from a heteroatom, which is a 6/42 hydrocarbon post that includes at least one heteroatom (that is, not being H or C), and whose group it bonds with other portions through the resulting free valence on that carbon atom;
a heterohydrocarbilene group is a divalent group formed by removing two hydrogen atoms from the same atom or different carbon atoms in a heterohydrocarbon, whose free valences are not involved in a double bond and whose group bonds with other portions through the resulting free valences on this or these carbon atoms;
an organo-heteryl group is a univalent group that contains carbon atoms and at least one hetero atom, and that has its free valence in another atom other than carbon.
a polar substituent is a substituent with a permanent induced or electric dipole moment; and a non-polar substituent is a substituent without a permanently induced or electric dipole moment.
The oligomerization catalyst of the present invention is preferably a trimerization catalyst or a tetramerization catalyst.
The oligomerization process to produce an oligomeric product is preferably a trimerization process to produce a trimeric product through the use of a trimerization catalyst or a tetramerization process to produce a tetrameric product through the use of a tetramerization catalyst.
The inventors of the present invention have surprisingly found that the incorporation of a zinc compound in the process described above results in a reduction in the formation of solids, that is, formation of polymer and in particular polyethylene in relation to processes in which such a zinc compound is absent.
Oligomerization Catalyst
Chrome source (i):
The chromium source can be an inorganic salt, an organic salt,
7/42 a coordinated compound or an organometallic complex.
Preferably, the chromium source is selected from the group consisting of chromium trichloride tris-tetrahydrofuran complex; (benzene) tricarbonyl chromium; chromium (III) octanoate; hexacarbonyl chromium; chromium (III) acetylacetonate, chromium (III) naphthenate, chromium (III) 2-ethylhexanoate, chromium (III) acetate, chromium (III) 2,2,6,6-tetramethylheptadionate, chloride chromium (III). Preferably, it is chromium (III) acetylacetonate or chromium (III) 2-ethylhexanoate.
Binding compound (ii):
X ¹ and / or X ² are preferably independently phosphorus or phosphorus oxidized by S or Se or N or O. Preferably, X ¹ and X ² are the same and more preferably both are P.
It will be appreciated that men are dependent on factors such as the valence and oxidation state of X ¹ and X ² , formation of Y bond with X ¹ and X ² respectively, and formation of R ¹ and R ² bond with X ¹ and X ² respectively. Preferably, men are not 0.
Preferably, the linker compound is a bidentate linker.
Preferably, the binding compound is of formula II.
on what
Y is as defined above, X ¹ and X ² are independently selected from the group consisting of nitrogen, phosphorus, arsenic, antimony and bismuth and R ³ to R ⁶ are each independently a hydrocarbyl group or a heterohydrocarbyl group.
Preferably, X ¹ and X ² are independently selected from the group consisting of phosphorus and nitrogen. More preferably, X ¹ and X ² are the same. More preferably, X ¹ and X ² are phosphorus.
R ³ to R ⁶ can be independently selected from the group consisting of a non-aromatic portion; an aromatic portion and
8/42 a heteroaromatic portion. Preferably, each of R ³ to R ⁶ is an aromatic or heteroaromatic moiety, more preferably an aromatic moiety (including a substituted aromatic moiety). The aromatic portion (or substituted aromatic portion) may comprise phenyl or substituted phenyl.
One or more of R ³ to R ⁶ can be a hydrocarbyl group or a substituted heterohydrocarbyl group, of which at least one substituent is attached to a hydrocarbyl group or a heterohydrocarbyl group.
In that specification, a substituent with reference to portions linked to X ¹ and / or X ² is a portion (excluding H) that is linked to a linear structure or a cyclic structure linked to X ¹ and / or X ² , but the substituent it does not form part of the linear or cyclic structure.
The linear or cyclic structure can be selected from the group consisting of a linear hydrocarbyl group, a linear heterohydrocarbyl, a cyclic hydrocarbyl and a cyclic heterohydrocarbyl. Linear hydrocarbyl can include methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyla, octyl, nonyl, decila, ethenyl, propenyl, butenyl, pentenyl, hexenyl, heptenyl, octenyl, nonenyl, decenyl, ethinyl, propynyl, butynyl, pentinyl, hexynyl, heptinyl, octinyl, noninyl and decynyl.
Linear heterohydrocarbyl can include methoxy, ethoxy, thiomethoxy, thioethoxy, methylsilyl, ethylsilyl, methylamino, methylphosphine, methoxymethyl and thiomethoxymethyl. Cyclic hydrocarbyl may include cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl, cyclodecyl, cyclopentenyl, cyclohexenyl, cyclooctenyl, phenyl, cyclopentadienyl, naphthaleneyl, norbornyl, adamanyl, phenaleneyl, tetrahydronaphthaleneyl, decalinyl, indenyl and tetrahydroindenyl. Cyclic heterohydrocarbyl can include tetrahydrofuranyl, tetrahydrothiophenene, pyrrole ideneyl, piperidineil, pyrrolineil, oxazolyl, thiazolyl, furanyl, thiopheneyl, pyrazolinyl, pyrazolyl, imidazolyl, benzofuranyl and benzofuranyl.
R ³ to R ⁶ can also be selected from a group of metallocenes such as a group of ferroceneíla, zirconoceneíla and titanoceneíla.
Preferably, R ³ to R ⁶ are aromatic portions of which one
9/42 ring atom of the aromatic ring structure is attached to either X ¹ or X ² and with a polar substituent attached to a ring atom of the aromatic ring structure adjacent to the ring atom attached to X ¹ or X ² .
Preferably, if two or more of R ³ to R ⁶ are aromatic moieties with a ring atom of the aromatic ring structure attached to any X ¹ and X ² , no more than two of said aromatic moieties R ³ and R ⁶ have a substituent attached to a ring atom of the aromatic ring structure adjacent to the ring atom attached to X ¹ or X ² .
In one embodiment of the invention, R ³ to R ⁶ are the same and different and each is a hydrocarbyl group or a heterohydrocarbyl group that contains no substituent or contains a non-polar substituent. Preferably, each of R ³ to R ⁶ does not include any polar substituent. Preferably, each of R ³ to R ⁶ does not include any polar substituents. In an embodiment of the invention, at least two of (but preferably all of) R ³ to R ⁶ are aromatic portions with a ring atom of the aromatic ring structure attached to X ¹ or X ² , but preferably not more than two of the said aromatic moieties R ³ to R ⁶ have a non-polar substituent other than H attached to a ring atom of the aromatic ring structure adjacent to the ring atom attached to X ¹ or X ² .
Preferably, none of the aromatic moieties R ³ to R ⁶ have a non-polar substituent attached to a ring atom of the aromatic ring structure adjacent to the ring atom attached to X ¹ or X ² . Preferably, all aromatic portions R ³ to R ⁶ are unsubstituted aromatic portions.
Examples of suitable non-polar substituents include, but are not limited to, methyl, ethyl, ethylene, propyl, iso-propyl, cyclopropyl, propenyl, propynyl, butyl, sec-butyl, tert-butyl, cyclobutyl, butenyl, butynyl, pentyl, isopentyl, neopentyl, cyclopentyl, pentenyl, pentinyl, hexyl, sechexyl, cyclohexyl, 2-methylcyclohexyl, 2-ethylcyclohexyl, 2-isopropylcyclohexyl, cyclohexenyl, hexenyl, hexynyl, octyl, cyclooctyl octenyl, decila, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o-ethylphenyl, o-isopropylphenyl, o-fbutilphenyl, cumila, mesity, biphenyl, naphthyl, anthracenyl and the like.
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Any of R ³ to R ⁶ can be independently linked to one or more of them, or to Y to form a cyclic structure.
R ³ and R ⁴ can be the same and R ⁵ and R ⁶ can be the same. R ³ to R ⁶ can all be the same.
In another embodiment of the invention, R ³ to R ⁶ are the same or different and each is a hydrocarbyl group, or a heterohydrocarbyl group (preferably an organyl group), provided that at least one of R ³ to R ⁶ contains a polar substituent on a carbon atom, but none of R ³ to R ⁶ contains a polar substituent on a carbon atom of R ³ to R ⁶ adjacent to a carbon atom attached to X ¹ or X ² . One or more or all of R ³ to R ⁶ can be independently selected from the group consisting of a substituted non-aromatic portion; a substituted aromatic portion; and a substituted heteroaromatic portion. Preferably, each of R ³ to R ⁶ is a substituted aromatic portion or a substituted heteroaromatic portion, more preferably a substituted aromatic portion. The substituted aromatic moiety may comprise a substituted phenyl. In an embodiment of the invention, at least two of (but preferably all of) R ³ to R ⁶ are aromatic with a ring atom of the aromatic ring structure attached to X ¹ or X ² , but preferably not more than two of said aromatic portions R ³ to R ⁶ have a substituent attached to a ring atom of the aromatic ring structure adjacent to the ring atom attached to X ¹ or X ² .
Any polar substituent in one or more of R ³ , R ⁴ , R ⁵ and R ⁶ can be an electron donor.
Suitable polar substituents can be a methoxy, ethoxy, isopropoxy, C3-C20 alkoxy, phenoxy, methoxymethyl, methylthiomethyl, 1,3-oxazolyl, methoxymethoxy, hydroxyl, amino, pentafluorophenoxy, tosyl, methylsulfanyl, trimethylsulfoxide, dimethylsulfoxide, dimethylsulfoxide, dimethylsulfoxide, or similar.
Y can be selected from the group consisting of an organic bonding group such as a hydrocarbylene, substituted hydrocarbilene, heterohydrocarbilene and a substituted heterohydrocarbilene; an inorganic bonding group comprising either a single or two atom molecular spacer 11/42 or two atoms; and a group comprising methylene; dimethylmethylene; ethylene; ethylene-1,2-diyl; propane-1,2-diyl, propane-1,3-diyl; cyclopropane-1,1-diyl; cyclopropane-1,2-diyl; cyclobutane-1,2-diyl, cyclopentane 1,2-diyl, cyclohexane-1,2-diyl, cyclohexane-1,1-diyl; 1,2-phenylene; naphthalene-1,8-diyl; phenanthrene-9,10-diyl, phenanthrene-4,5-diyl, 1,2-catecholate,
1.2- diaryl-hydrazine-1,2-di-yl (-N (Ar) -N (Ar) -), where Ar is an aryl group; 1,2dialkylhydrazine-, 2-di-yl (-N (Alk) -N (Alk) -), where Alk is an alkyl group; B (R7) -, -Si (R7) 2-, -P (R7) - and -N (R7) -, where R7 is hydrogen, a hydrocarbyl or heterocarbyl or halogen.
Preferably, Y can be -N (R ⁷ ) - and R ⁷ can be selected from the group consisting of hydrogen, alkyl, substituted alkyl, aryl, substituted aryl, aryloxy, substituted aryloxy, halogen, alkoxycarbonyl, carbonyloxy, alkoxy groups , aminocarbonyl, carbonylamino, dialkylamino, silyl or its derivatives, and aryl substituted with any of these substituents. Preferably, R ⁷ can be a hydrocarbyl group or a heterohydrocarbyl or an organo-heteryl group. R ⁷ can be methyl, ethyl, propyl, isopropyl, cyclopropyl, ally, butyl, tert-butyl, sec-butyl, cyclobutyl, pentyl, isopentyl, 1, 2dimethylpropyl (3-methyl-2-butyl), 1, 2,2 -trimethylpropyl (R / S-3,3-dimethyl-2-butyl), 1- (1-methylcyclopropyl) -ethyl, neopentyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, decila, cyclodecyl, 1, 5-dimethylheptyl, 1-methylheptyl, 2-naphthylethyl, 1-naphthylmethyl, adamantylmethyl, 1-adamantyl, 2-adamantyl, 2-isopropylcyclohexyl, 2,6-dimethylcyclohexyl, cyclododecyl, 2-methylcyclo, 2-methylcyclohexyl 3-methylcyclohexyl, 4-methyl cyclohexyl, 2-ethylcyclohexyl, 2-isopropylcyclohexyl, 2,6dimethyl-cyclohexyl, exo-2-norbornanyl, isopinocamphenyl, dimethylamino, phthalimido, pyrrolyl, trimethylsilyl tert-butylsilyl, 3-trimethoxylsilane-propyl, indanyl, cyclohexanemethyl, 2-methoxyphenyl, 3-methoxyphenyl, 4-methoxyphenyl, 4terc-butylphenyl, 4-nitrophenyl, (1,1'-bis (cyclohexyl) -4 , 4'-methylene), 1,6-hexylene, 1-naphthyl, 2-naphthyl, N-morpholin a, diphenylmethyl, 1,2-diphenyl-ethyl, phenylethyl, 2-methylphenyl, 3-methylphenyl, 4-methylphenyl, 2,6-dimethyl-phenyl or a 1, 2,3,4-tetrahydronaphthyl.
Preferably, the binding compound is of formula III:
12/42
R ⁷
R ³

R ⁵
R ⁶ ..... II.
with R ³ to R ⁷ as defined above.
Preferably, each of R ³ to R ⁶ is an alkyl (preferably methyl, ethyl or isopropyl) or aromatic (preferably phenyl or substituted phenyl).
The binding compound can include a polymeric portion to make the reaction product from the chromium source and said binding compound soluble at higher temperatures and insoluble at lower temperatures, for example, 25 ° C. This approach can enable the recovery of the reaction mixture complex for reuse and has been used for another catalyst as described by D.E. Bergbreiter et a., J. Am. Chem. Soc, 1987, 109, 177-179. In a similar vein, these chromium catalysts can also be immobilized by binding the binding compound to the structure of silica, silica gel, polysiloxane or alumina as, for example, demonstrated by C. Yuanyin et al., Chinese J. React. Pol., 1992, 1 (2), 152-159 for immobilizing platinum complexes.
The linker compound can include multiple linker units or derivatives thereof. Non-limiting examples of such linkers include dendrimeric linkers as well as linkers where the individual linker units are coupled either via one or more of the R groups or via the Y link group. More specific, but not limiting, examples of such linkers may include 1, 2-di- (N (P (phenyl) ₂ ) 2) -benzene, 1,4-di- (N (P (phenyl) ₂ ) 2) -benzene, N (CH ₂ CH ₂ N (P (phenyl) ₂ ) ₂ ) ₃ , 1,4-di- (P (phenyl) N (methyl) P (phenyl) ₂ ) -benzene, 1,2-di (N (P (p-methoxyphenyl) ₂ ) 2) -benzene , 1,4-di- (N (P (p-methoxyphenyl) ₂ ) 2) -benzene, N (CH ₂ CH ₂ N (P (p-methoxyphenyl) 2) 2) 3 θ 1,4-di- ( P (p-methoxyphenyl) N (methyl) P (pmethoxyphenyl) ₂ ) -benzene.
Binding compounds can be prepared using procedures known to those skilled in the art and procedures that
13/42 are part of the state of the art.
The oligomerization catalyst can be prepared in situ, that is, in the reaction mixture in which the oligomerization reaction is to occur. Often the oligomerization catalyst will be prepared in situ. Alternatively, the catalyst can be preformed or partially preformed.
Activation
Activator (iii)
The catalyst activator can be a compound that generates an active catalyst when the activator is combined with the chromium source and the binding compound.
In one form of the invention, the activator is an organoboro compound that includes an uncoordinated cation and anion of the general formula:
[(R) _x L * - H] ⁺ [B (R ⁴ ) ₄ r where:
L * is an atom selected from the group consisting of N,
If P;
the [(R) _X L * - H] ⁺ cation is a Bronsted acid; x is an integer 1, 2 or 3;
each R is the same or different and each is an -H, hydrocarbyl group or a heterohydrocarbyl group;
provided that at least one of R comprises at least 6 carbon atoms and also provided that the total number of carbon atoms in (R) _x collectively is greater than 12;
R ⁴ independently in each occurrence is selected from the group consisting of hydride, dialkylamino, halide, alkoxide, aryloxide, hydrocarbyl, hydrocarbyl-halosubstituted radicals, halosubstituted alkoxide, halosubstituted aryloxide and an aromatic halosubstituted portion with at least one halide substituent in the portion aromatic.
[(R) _x L * - H] ⁺ is a cation. More particularly, [(R) _x L * - H] ⁺ is a Bronsted acid. A Bronsted acid is any compound that is capable of donating a hydrogen ion (proton).
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Where L * is an atom selected from the group consisting of N or P, the cation [(R) _x L * - H] ⁺ can be represented by the formula:
[R ¹ R ² R ³ I_i - H] ⁺ where:
h = N or P;
R ¹ , R ² and R ³ are the same or different and each is an -H, hydrocarbyl group or a heterohydrocarbyl group; and provided that at least one of R ¹ , R ² and R ³ comprises at least 6 carbon atoms and also provided that the total number of carbon atoms in R ¹ , R ² and R ³ collectively is greater than 12.
Where L * is S, the cation [(R) _X L * - H] ⁺ can be represented by the formula:
[(R ¹ R ² L ₂ ) ₂ -H] ⁺ where:
L ₂ = S;
R ¹ and R ^{2 are} the same or different and each is an -H, hydrocarbyl group or a heterohydrocarbyl group; and provided that at least one of R ¹ and R ² comprises at least 6 carbon atoms and also provided that the total number of carbon atoms in R ¹ and R ² collectively is greater than 12.
R ¹ , R ² and R ³ are each independently an aliphatic hydrocarbyl group or an aliphatic heterohydrocarbyl, preferably a saturated aliphatic hydrocarbyl or a saturated aliphatic heterohydrocarbyl, more preferably a substituted hydrocarbyl or substituted heterohydrocarbyl where the substituents they can be non-polar groups.
Suitable examples of R ¹ , R ² and R ³ include, but are not limited to, methyl, ethyl, ethylenyl, propyl, propenyl, propynyl, butyl, pentyl, hexyl, cyclohexyl, 2-methylcyclohexyl, 2-ethylcyclo -hexyl, octyl, 2-ethylhexyl, isooctyl, decyl, dodecyl, tetradecyl, octadecyl, 2-isopropylcyclohexyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o-ethylphenyl, o-isopropylphenyl, o-isopropylphenyl -tbutylphenyl, biphenyl, naphthyl and the like.
Examples of suitable non-polar substituents include, but are not limited to,
15/42 are not limited to, butyl, pentyl, hexyl, sec-hexyl, cyclohexyl, 2methylcyclohexyl, 2-ethylcyclohexyl, 2-isopropylcyclohexyl, cyclohexenyl, hexenyl, hexynyl, octyl, cyclohexyl octyl, cyclooctenyl, 2-ethylhexyl, isooctyl, decyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o-ethylphenyl, o-isopropylphenyl, o-ibutylphenyl, cumila, mesityl, biphenyl, naphthyl, anthracenyl and the like.
In one embodiment of the invention, at least one of R comprises 6 to 40 carbon atoms with a total of 13 to 100 carbons. Preferably, at least one of R comprises 6 to 40 carbon atoms with a total of 21 to 90 total carbons.
It is believed that the presence of long-chain hydrocarbon substituents, that is, hydrocarbon substituents with at least 6 carbon atoms, makes the activator more soluble in aliphatic solutions, thereby facilitating the activation of the catalyst. In addition, it is believed that where the total number of carbon atoms in the hydrocarbyl substituents that R ¹ , R ² and R ³ have is greater than 12, the solubility of the catalyst activator in aliphatic compounds will be increased, thereby resulting in better olefin oligomerization with low solids formation.
As discussed above, R ⁴ can be a halosubstituted aromatic moiety with at least one halide substituent on the aromatic ring. In a preferred embodiment of the invention, the halosubstituted aromatic moiety is pentafluorophenyl.
Illustrative, but not limiting, examples of organoboro compounds with an uncoordinated cation and anion of the formula of the present invention, shown here above, include:
tetrakis (pentafluorophenyl) dihexyl (methyl) ammonium borate;
dioctyl (methyl) ammonium tetrakis (pentafluorophenyl) borate;
tetrakis (pentafluorophenyl) methyldi (octyl) ammonium borate;
borate decildi (methyl) ammonium tetrakis (pentafluorophenyl);
dodecildi (methyl) ammonium tetrakis (pentafluorophenyl) borate;
tetrakis (pentafluorophenyl) tetradecildi (methyl) ammonium borate;
hexa-adecildi (methyl) ammonium tetrakis (pentafluorophenyl) borate;
octadecildi (methyl) ammonium tetrakis (pentafluorophenyl) borate;
16/42 eicosildi (methyl) ammonium tetrakis (pentafluorophenyl) borate;
methyldi (decif) ammonium tetrakis (pentafluorophenyl) borate;
methyldi (dodecyl) ammonium tetrakis (pentafluorophenyl) ammonium;
tetrakis (pentafluorophenyl) methyldi (tetradecyl) ammonium borate;
tetrakis (pentafluorophenyl) methyldi (hexadecyl) ammonium borate;
tetrakis (pentafluorophenyl) methyldi (octadecyl) ammonium borate;
methyldi (eicosyl) ammonium tetrakis (pentafluorophenyl) borate;
tri-hexylammonium tetrakis (pentafluorophenyl) borate;
trioctylamonium tetrakis (pentafluorophenyl) borate;
tri (2-ethylhexyl) ammonium tetrakis (pentafluorophenyl) borate;
tetrakis (pentafluorophenyl) tri (isooctyl) ammonium borate;
tridecylammonium tetrakis (pentafluorophenyl) borate;
tetrakis (pentafluorophenyl) tridodecylammonium borate;
tetrakis (pentafluorophenyl) tritetradecylammonium borate;
tri-hexadecylammonium tetrakis (pentafluorophenyl) borate;
tetrakis (pentafluorophenyl) trioctadecylammonium borate;
tetrakis (pentafluorophenyl) trieicosylammonium borate;
hexetyl (n-butyl) ammonium tetrakis (pentafluorophenyl) borate;
octyl (n-butyl) ammonium tetrakis (pentafluorophenyl) ammonium;
tetrakis (pentafluorophenyl) decildi (n-butyl) ammonium borate;
dodecildi (n-butyl) ammonium tetrakis (pentafluorophenyl) ammonium;
octadecildi (n-butyl) ammonium tetrakis (pentafluorophenyl) ammonium;
N, N-dihexylanilinium tetrakís (pentafluorophenyl) borate;
et, Ν-dioctylanilinium tetrakis (pentafluorophenyl) borate;
N, N-didodecylanilinium tetrakis (pentafluorophenyl) borate;
N-methyl-N-dodecylanilinium tetrakis (pentafluorophenyl) borate;
N, N-di (octadecyl) (2,4,6-trimethylaniline) tetrakis (pentafluorophenyl) borate; tetrakis (pentafluorophenyl) cyclohexildi (dodecyl) ammonium borate; tetrakis- (2,3,4,6-tetrafluorophenyl) methyldi (dodecyl) ammonium borate; tetrakis (pentafluorophenyl) trioctyl phosphonium borate;
tri-hexylphosphonium tetrakis (pentafluorophenyl) borate;
tributylphosphonium tetrakis (pentafluorophenyl) borate;
17/42
borate in bis (dihexylsulfide) onium, borate in bis (dioctyl sulfide) onium, borate in bis (didecyl sulfide) onium, borate in bis (didodecyl sulfide) onium,
dioctyl (methyl) phosphonium tetrakis (pentafluorophenyl) borate; dimethyl (octyl) phosphonium tetrakis (pentafluorophenyl) borate; tetrakis (pentafluorophenyl) [{(C ₆ H ₁₃ ) ₂ S} ₂ H] [B (C ₆ F ₅ ) ₄ ]; tetrakis (pentafluorophenyl) [{(C ₈ H ₁₇ ) ₂ S} ₂ H] [B (C ₆ F ₅ ) ₄ ]; tetrakis (pentafluorophenyl) [{(Ci ₀ H ₂₅ ) ₂ S} ₂ H] [B (C ₆ F ₅ ) ₄ ]; and tetrakis (pentafluorophenyl) [{(Ci ₂ H ₂₅ ) ₂ S} ₂ H] [B (C ₆ F ₅ ) ₄ ].
The chromium source and the organoboro compound can be combined in proportions to provide molar ratios of organoboro / chromium compound from about 0.1 to 50 organoboro to 1 chromium, preferably from about 0.8 to 20 organoboro to 1 chromium and more preferably from 1 to 10 organoboro to 1 chromium.
Preferably, the concentration of boron in the activated catalyst before dilution is at least 0.01 mmol / l. Preferably, the concentration of boron is 0.1 - 100 mmoles / l, and more preferably the concentration is 0.1 10 mmol / l.
Other non-limiting examples of activators include alumoxanes, aluminum alkyls, other metal or alkyl or aryl compounds of the main group, ionizing activators, which can be neutral or ionic, Lewis acids, reducing agents, oxidizing agents and combinations thereof. In one embodiment, aluminoxane activators are used as an activator in compositions useful in the invention. Aluminoxanes are in general oligomeric compounds containing subunits -AI (R *) - O-, where R * is an alkyl group. Examples of alumoxanes include methylalumoxane (MAO), ethylalumoxane, isobutylalumoxane and modified methylalumoxanes (MMAO), which include non-methyl alkyl groups, such as ethyl, isobutyl and n-octyl. Alkylalumoxanes and modified alkylalumoxanes are suitable as catalyst activators, particularly when the abstract catalyst binder is a halide, alkoxide or amide. Mixtures of different alumoxanes and alumoxanes
Modified 18/42 can also be used. Activating compounds comprising Lewis acid activators and in particular alumoxanes are specifically characterized by the following general formulas:
(R ^a -AI-O) _p
R ^b (R ^c -AI-O) p-AIR ^and 2 where
R ^a , R ^b , R ^c and R ^e are independently a C1-C30 alkyl radical, for example, methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyla, octyl, nonyl, decila, and p is an integer of 1 to about 50. More specifically, R ^a , R ^b , R ^c and R ^d are each methyl and p is at least 4. When an alkyl aluminum halide or alkoxide is employed in the preparation of alumoxane, one or more R ^a , R ^b , R ^c and R ^e are groups that can be halide or alkoxide.
It is recognized that alumoxane is not a separate material. An alumoxane is generally a mixture of linear and cyclic compounds. A typical alumoxane will contain free trisubstituted or trialkyl aluminum molecules, bonded trisubstituted or trialkyl aluminum and alumoxane of varying degree of oligomerization. For some embodiments, it is preferred that methylalumoxanes contain lower levels of trimethylaluminum. Lower levels of trimethyl aluminum can be achieved by reacting trimethyl aluminum with a Lewis base or by vacuum distillation of trimethyl aluminum or by any other means known in the art.
For other descriptions, see Pat. US ^Nos 4665208, 4952540, 5041584, 5091352, 5206199, 5204419, 4874734, 4924018,
4,908,463, 4,968,827, 5,329,032, 5,248,801, 5,235,081, 5,157,137,
5,103,031 and EP 0561476A1, EP 0279586B1, EP 0516476A1, EP 0594218A1 eWO 94/10180.
When the activator is an alumoxane (modified or unmodified), some modalities select the maximum amount of activator at a molar excess of 5000 times Al / Cr over the catalyst precursor. The preferred minimum catalyst precursor activator is a 1: 1 molar ratio. More specifically, the Al / Cr ratio is 1000: 1 to 100: 1.
19/42
Alumoxanes can be produced by hydrolysis of the respective trialkylaluminum compound. MMAO can be produced by hydrolysis of trimethylaluminum and a superior trialkylaluminium like triisobutylalumin.
There are a variety of methods for preparing alumoxane and modified alumoxanes, non-limiting examples of which are described in Pat. US ^Nos 4665208, 4952540, 5091352, 5206199, 5204419,
4,874,734, 4,924,018, 4,908,463, 4,968,827, 5,308,815, 5,329,032, 5,248,801, 5,235,081, 5,157,137, 5,103,031, 5,391,793, 5,391,529, 5,693,838, 5,731,253, 5,731,451, 5,744,656, 5,847,177, 5,854,166,
5,856,256 and 5,939,346 and European publications EP 0561476A1, EP 0279586B1, EP 0594218A1 and EP 0586665B1, and PCT publications WO 94/10180 and WO 99/15534, all of which are incorporated herein by reference.
Alkyl aluminum and organoaluminium compounds that can be used as activators (or sequestrants) include trimethylaluminum, triethylalumin, triisobutylalumin, tri-n-hexylalumin, tri-n-octylalumin, diisobutylaluminum hydride, ethylaluminium dichloride, diethylaluminium chloride, ethoxide of diethyl aluminum and the like.
Lonizing activators
In some embodiments, the activator includes compounds that can subtract a binder making the metal complex cationic and providing a weakly coordinated or uncoordinated charge balance anion. The term uncoordinated anion (NCA) means an anion that does not coordinate with said cation or is only weakly coordinated with said cation, thus remaining unstable enough to be displaced by a Lewis base (for example, a neutral Lewis base) .
It is within the scope of this invention to use an ionizing or stoichiometric activator, neutral or ionic, such as tri (n-butyl) ammonium tetrakis (pentafluorophenyl) boron, a tris (pentafluorophenyl) boron metalloid precursor or a tris (heptafluoronaftil) metalloid precursor boron, polyhalogenated heteroborane anions (WO 98/43893), boric acid (US Pat. No. 5,942,459) or combinations thereof. Also within the scope of this invention is the use
20/42 of neutral or ionic activators alone or in combination with alumoxane or modified alumoxane activators.
Examples of neutral stoichiometric activators include tri-substituted boron, tellurium, aluminum, gallium and idium or mixtures thereof. These three substituent groups are each independently selected from alkyl, alkenyl, halogen, substituted alkyl, aryl, aryl, alkoxy and halide. In some embodiments, the three groups are independently selected from halogen compounds, mono- or multicyclic aryls (including halosubstituted), alkyls and alkenyl and mixtures thereof, preferred are alkenyl groups with 1 to 20 carbon atoms, alkyl groups with 1 to 20 carbon atoms, alkoxy groups with 1 to 20 carbon atoms and aryl groups with 3 to 20 carbon atoms (including substituted aryls). In other embodiments, the three groups are alkyls with 1 to 4 groups of carbon, phenyl, naphthyl or mixtures thereof. In other embodiments, the three groups are halogenated, specifically fluorinated alkyl groups. In still other embodiments, the neutral stoichiometric activator is tris (perfluorophenyl) boron or tris (perfluoronafty) boron.
Ion stoichiometric activating compounds may contain an active proton, or some other cation associated with, but not coordinated with, or only weakly coordinated with, the remaining ion of the ionizing compound. Such compounds and the like are described in European publications EP 0570982A1, EP 0520732A1, EP 0495375A1, EP 0500944B1, EP 0277003A1 and EP 0277004A1, and Pat. US ^Nos 5,153,157; 5,198,401; 5,066,741; 5,206,197; 5,241,025; 5,384,299 and 5,502,124 and US patent application No. 08,285,380, filed on August 3, 1994, all of which are incorporated herein by reference.
Ionic catalysts can be prepared by reacting a compound of Cr with some neutral Lewis acids, such as B (C ₆ F ₅ ) 3, which upon reaction with the subtractable ligand (X) of the compound of Cr forms an anion, such as [B (C ₆ F ₅ ) ₃ (X)] ', which stabilizes the cationic Cr species generated by the reaction. Catalysts can be prepared with activating components, which are compounds or ionic compositions.
21/42
In some embodiments, compounds useful as an activating component in the preparation of the ion catalyst systems used in the process of this invention comprise a cation, which is optionally a Brõnsted acid capable of donating a proton, and a compatible uncoordinated anion which is capable of stabilizing the active catalyst species that is formed when the two compounds are combined and said anion will be sufficiently unstable to be displaced by olefinic substrates or other neutral Lewis bases such as ethers, nitriles and the like. Two classes of compatible uncoordinated anions useful here have been described in EP 0277003A1 and EP 0277004A1 published in 1988: anionic coordination complexes comprising a plurality of lipophilic radicals covalently coordinated to and shielding a center charge-bearing metal or metalloid core; and anions comprising a plurality of boron atoms such as carboranes, metallacarboranes and boranes.
In a preferred embodiment, stoichiometric activators include a cationic and an anionic component, and can be represented by the following formula:
(LH) ^{d +} (A ^d ') where
L is a neutral Lewis base; H is hydrogen; (LH) ⁺ is a Brõnsted acid; A ^d 'is an anion not coordinated with charge d; ed is an integer from 1 to 3.
The cationic component, (LH) ^{d +} may include Brõnsted acids as proton or protonated Lewis bases or reducible Lewis acids capable of protonating or subtracting a portion, such as an alkyl or aryl, from the bulky ligand chromium catalyst precursor, resulting in a kind of cationic transition metal.
The activation cation (LH) ^{d +} can be a Brõnsted acid, capable of donating a proton to the transition metal catalytic precursor resulting in a transition metal cation, including ammonia, oxons, phosphones, sililies and their mixtures, specifically methylamine ammonia, aniline, dimethylamine, diethylamine, N-methylaniline, diphenylamine, trimethylamine,
22/42 triethylamine, Ν, Ν-dimethylaniline, methyldiphenylamine, pyridine, p-bromo-N, Ndinetylaniline, p-nitro-N, N-dimethylaniline, tetylphosphine phosphons, thphenylphosphine and diphenylphosphine, diethyl ether, ether oxides , tetrahydrofuran and dioxane, thioether sulfones, such as diethyl thioethers and tetrahydrothiophene and mixtures thereof. The activation cation (LH) / can also be a portion such as silver, tropilium, carbenes, ferrocene and mixtures. Specifically, carbon and ferrocene. In one embodiment, (LH) ^{d +} can be triphenyl carbon.
The anionic component A ^d_ includes those with the formula (M ^{k +} Q _n ) ^d ', where k is an integer from 1 to 5; n is an integer from 2-6; nk = d; A element selected from Group 13 of the Periodic Table of the Elements, specifically boron or aluminum, and Q is independently a bridged or unbridged hydride, dialkyl starch or terminal, halide, alkoxide, aryloxide, hydrocarbyl radicals, substituted hydrocarbyl, halocarbyl, halocarbyl substituted and halosubstituted hydrocarbyl, said Q with up to 20 carbon atoms with the proviso that in no more than 1 occurrence Q is a halide. Specifically, each Q is a fluorinated hydrocarbyl group with 1 to 20 carbon atoms, more specifically each Q is a fluorinated aryl group, and more specifically each Q is a pentafluoryl aryl group. Examples of suitable A ^d 'also include diboro compounds as described in U.S. Pat. US No. 5,447,895, which is hereby fully incorporated by reference.
In one embodiment of the invention, (M ^{k +} Qn) ^d can be selected from the group containing the anion (AI (OR) 4] ', a compound that includes an AI (OR) 3 portion and a salt containing the anion [ Ta (OR) ₆ ] ', where R is defined as above.
In an embodiment of the invention, (M ^{k +} Qn) ^d 'can be selected from the group consisting of AI (OC6F ₅ ) ₃ ; [AI {OC (CF ₃ ) ₃ } ₄ ] '; [AI (OC ₆ F ₅ ) ₄ ] '; [AI (C ₆ F ₄ 0 ₂ ) ₂ r> [AI {OC (CF ₃ ) ₂ C (CF ₃ ) ₂ 0} ₂ ]; [AIF {OC (CF ₃ ) ₃ } ₃ ]; [AI ₂ F {OC (CF ₃ ) ₃ } ₆ ]; (Z) AI {OCH (C ₆ F ₅ ) ₂ } ₃ ; (Z) AI {OC (CF ₃ ) ₃ } ₃ and [Ta (OC ₆ F ₅ ) 6]; whose Z portion is not AR as defined above.
Illustrative, but not limiting, examples of bo23 / 42 ro compounds that can be used as a catalyst activator in the preparation of the improved catalysts of this invention are tri-substituted ammonium salts as:
trimethylammonium tetrafenyl borate, triethylammonium tetrafenyl borate, tripropylammonium tetrafenyl borate, tri (n-butyl) ammonium tetrafenyl borate, N (t-butyl) ammonium tetrafenyl borate, N-dimethylaniline tetrafenyl borate , N-diethylanilinium, N, N-dimethyl- (2,4,6-trimethylanilinium) tetrafenyl borate, tropillium tetrafenyl borate, triphenylcarbenium tetrafenyl borate, triphenylphosphonium tetrafenyl borate, benzene tetrafenyl borate, tetrafenyl borate (benzene) tetrakis (pentafluorophenyl) trimethylammonium borate, tetrakis (pentafluorophenyl) triethylammonium borate, tetrakis (pentafluorophenyl) tripropylammonium borate, tri (n-butyl) tetrakis (pentafluorophenyl) borate tri (n-butyl) ammonium borate, tetrakis ammonium, N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate, N, N-diethylanilinium tetrakis (pentafluorophenyl) borate, N, N-dimethyl- (2,4,6-trimethylanilinium), tetrakis (pentafluorophenyl) borate pentafl uorophenyl) tropilium borate, tetrakis (pentafluorophenyl) triphenylcarbene borate, tetrakis (pentafluorophenyl) triphenylphosphonium borate, tetrakis (pentafluorophenyl) triethylsilyl borate, tetrakis (pentafluoren (2,3) Trimethylammonium 6-tetrafluorophenyl), triethylammonium tetrakis- (2,3,4,6-tetrafluorophenyl) borate, tripropylammonium tetrakis- (2,3,4,6-tetrafluorophenyl) borate,
24/42 tetrakis- (2,3,4,6-tetrafluoro-phenyl) tri (n-butyl) ammonium borate, tetrakis- (2,3,4,6-tetrafluorophenyl) dimethyl (t-butyl) ammonium borate , N, N-dimethylanilinium (2,3,4,6-tetrafluorophenyl) borate, N, N-diethylanilinium, tetrakis- (2,3,4,6-tetrafluorophenyl) borate, tetrakis- (2,3, 4,6-tetrafluorophenyl) N, N-dimethyl- (2,4,6-trimethylanilinium) borate, tetrakis- (2,3,4,6-tetrafluorophenyl) tropilium borate, tetrakis- (2,3,4, 6-tetrafluorophenyl) triphenylcarbene borate, tetrakis- (2,3,4,6-tetrafluorophenyl) triphenylphosphonium borate, tetrakis- (2,3,4,6-tetrafluorophenyl) triethylsilyl borate, tetrakis- (2,3,4 , 6-tetrafluorophenyl) benzene (diazonium) borate, tetrakis (perfluoronafty) trimethylammonium borate, tetrakis (perfluoronafty) triethylammonium borate, tetrakis (perfluoronaftil) tripropylammonium borate, tetrakis (ammonium-boron) tetrakis (perfluoronafty) tri (t-butyl) ammonium borate, tetrakis (perfluoronafty) Ν, Ν-dtmethylanilinium borate, tetr akis (perfluoronafty) N, N-diethylanilinium borate, tetrakis (perfluoronafty) N, N-dimethyl- (2,4,6-trimethylanilinium) borate, tetrakis (perfluoronaftil) trillium borate, tetrakis (perfluoronaftil) triphenyl borate, tetrakis (perfluoronaftil) triphenylphosphonium borate, tetrakis (perfluoronaftil) triethylsilyl borate, tetrakis (perfluoronaftil) benzene borate (diazonium), tetrakis (perf! uorobiphenyl) trimethylammonium borate, tetrakobyl (tetrakis) of tripropylammonium, tetrakis (perfluorobiphenyl) tri (n-butyl) ammonium borate, tetrakis (perfluorobiphenyl) tri (t-butyl) ammonium borate, tetrakis (perfluorobiphenyl) N, N-dimethylanilinium borate, tetrakis (perfluorobyrene) , N-N-dimethyl- (2,4,6-trimethylanilinium) tetrakis (perfluorobiphenyl) borate, tropilium tetrakis (perfluorobiphenyl) borate,
25/42 triphenylcarbenium tetrakis (perfluorobiphenyl), triphenylphosphonium tetrakis (perfluorobiphenyl), tetrakis (perfluorobiphenyl) triethylsilyl (benzene) triethylsilyl (tetrakis) trimethylammonium borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) triethylammonium borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) tripropylammonium borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) borate tri (n-butyl) ammonium, tetrakis (3,5-bis (trifluoromethyl) phenyl) boron tri (t-butyl) ammonium, tetrakis (3,5-bis (trifluoromethyl) phenyl) borate, N, N-dimethylanilinium, tetrakis (3,5-bis (trifluoromethyl) phenyl) N, N-diethylanilinium borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) N, N-dimethyl- (2,4,6trimethylanilinium) borate, tetrakis ( 3,5-bis (trifluoromethyl) phenyl) trillium borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) triphenylcarbene borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) triphenylphosphonium borate, tetrakis (3, 5-bis (trifl uoromethyl) phenyl) triethylsilyl borate, tetrakis (3,5-bis (trifluoromethyl) phenyl) benzene (diazonium) borate, and warm dialkyl salts such as:
Di- (i-propyl) ammonium tetrakis (pentafluorophenyl) borate, and dicyclohexylammonium tetrakis (pentafluorophenyl) borate; and additional tri-substituted phosphonium salts such as tri (o-tolif) phosphonium tetrakis (pentafluorophenyl) boron, and tri (2,6-dimethylphenyl) phosphonium tetrakis (pentafluorophenyl) borate.
More specifically, the ionic stoichiometric activator (LH) ^{d +} (A ^d -) is N, N-dimethylanilinium tetra (perfluorophenyl) borate, N, N-dimethylaniline borate, N tetrakis (perfluorobiphenyl) N, N borate -dimethylanilinium, tetrakis (3,5-bis (trifluoromethyl) phenyl) N, N-dimethylanilinium borate, tetrakis (perfluoronafty) triphenylcarbene borate, tetrakis (perfluorobiphenyl) triphenylcarbene borate,
26/42 triphenylcarbene tetrakis (3,5-bis (trifluoromethyl) phenyl) borate, or triphenylcarbene tetra (perfluorophenyl) borate.
Other examples of preferred ionizing activators include [H Me (C ₁₈ H3 ₇ ) ₂ ⁺ ] [B (C6F5) 4 ·]; [HNPh (C18H37) 2 ⁺ ] [B (C6F ₅ ) ₄ -] e [(((4-n-Bu-C ₆ H ₄ ) NH (nhexyl) ₂ ) ⁺ ] [B (C6F5) 4 ~] and [ ((4-n-Bu-C6H4) NH (n-decyl) 2) ⁺ ] [B (C6F ₅ ) ₄ ·]. Preferred specific (LH) ⁺ cations are N, N-dialkylanilinium cations, such as HNMe2Ph ⁺ , substituted N, N-dialkylanilinium cations, such as (4-n-Bu-C6H ₄ ) NH (nC ₆ Hi ₃ ) 2 ⁺ and (4 -n-Bu-C6H4) NH (n-C1oH2i) 2 ⁺ θ HNMe (Ci8H ₃₇ ) 2 ⁺ . Specific examples of anions are tetrakis (3,5-bis (trifluoromethyl) phenyl) borate and tetrakis (pentafluorophenyl) borate.
In one embodiment, activation methods using ionizing tonic compounds that do not contain an active proton, but are capable of producing an active oligomerization catalyst are also contemplated. Such methods are described with respect to metallocene catalyst compounds in EP 0426637A1, EP 0573403A1 and U.S. Patent No. 5,387,568, which are all incorporated herein by reference.
The process can also employ activating compounds that are initially neutral Lewis acids, but form a cationic metal complex and an uncoordinated anion, or a zwitterionic complex upon reaction with the compounds of this invention. For example, tris (pentafluorophenyl) boron or aluminum can act to subtract a hydrocarbyl binder or hydride to provide a cationic metal complex and stabilize an uncoordinated anion.
In another embodiment, the aforementioned activating compounds can also react with the compounds of the present invention to produce a neutral, uncharged catalyst capable of selective ethylene oligomerization. For example, acidic Lewis reagents, such as alkyl or aryl aluminum or boron compounds, can subtract a basic Lewis linker, such as THF or Et ₂ O, from a compound providing a coordinated unsaturated catalyst capable of oligomerization selective ethylene.
When cations of uncoordinated anionic precursors
27/42 are Brõnsted acids like protons or protonated Lewis bases (excluding water), or reducible Lewis acids like ferrocene or silver cations, or alkaline or alkaline earth metal cations like those of sodium, magnesium or lithium, the molar ratio from activator to catalyst precursor can be any ratio, however useful ratios can be from 1000: 1 to 1: 1.
Combinations of two or more activators can also be used in the practice of this invention.
Other suitable ion-forming activating compounds comprise a cationic agent salt and a compatible, uncoordinated anion characterized by the general formula:
(X) * (A ^d ·)
X ⁺ is a cationic agent capable of accepting / subtracting an anionic group; The ^d ~ is anion not coordinated with the d- charge; ed is an integer from 1 to 3.
Specific examples of (X) ⁺ include R3C ⁺ , R3Si ⁺ , R2AI ⁺ , where R is hydrocarbyl, substituted hydrocarbyl, halocarbyl, substituted halocarbyl and halosubstituted-hydrocarbyl radicals.
Specific examples include, but are not limited to, Ph ₃ C ⁺ , Et3Si ⁺ , (Ci8H ₃₇ ) ₂ MeSi ⁺ , Cp ₂ AI ⁺ .
Another suitable ion-forming activation cocatalyst comprises a salt of a cationic oxidizing agent and a compatible, uncoordinated anion characterized by the general formula: (OX ^{e +} ) d (A ^d ') e, where OX® ⁺ is an oxidizing agent cationic with a charge of e +; e is an integer from 1 to 3; d is an integer from 1 to 3 and A ^d 'is as previously defined. Examples of cationic oxidizing agents include: ferrocene, hydrocarbyl-substituted ferrocene, amoniomyl (R3N ^{+ e} ), Ag ⁺ or Pb ²⁺ . Preferred modalities of A ^d 'are those anions previously defined with respect to activators containing Brönsted acid, especially tetrakis (pentafluorophenyl) borate.
Specific examples of amoniomyl groups include (p-BrC ₆ H ₄ ) ₃ N ⁺ ·, (p-NO2-C6H4) 3N ⁺ ·, (pF-C6H ₄ ) ₃ N ⁺ ·, (p-Me-C ₆ H ₄ ) ₃ N ⁺ ·, (p-OMe28 / 42 c ₆ h ₄ ) ₃ n ⁺ ·.
Group 13 Reagents, Divalent Metal Reagents and Alkali Metal Reagents
Other activators or general compounds useful in an oligomerization reaction can be used. These compounds can be activators in some contexts, but they can also serve other functions in the reaction system, such as alkylating a metal center or sequestering impurities. These compounds are within the general definition of activator, but are not considered here to be ion-forming activators. These compounds include a group 13 reagent that can be characterized by the formula G ¹³ R ⁵⁰ 3- _p D _p , where G ¹³ is selected from the group consisting of B, Al, Ga, In and their combinations, p is 0 , 1 or 2, each R ⁵⁰ is independently selected from the group consisting of hydrogen, halogen and alkyl, alkenyl, alkynyl, heteroaryl, heteroalkenyl, heteroalkynyl, aryl, optionally substituted heteroaryl and their combinations, and each D is independently selected a from the group consisting of halogen, hydrogen, alkoxy, aryloxy, amino, mercapto, alkylthio, arylthio, phosphine and their combinations.
In other embodiments, the group 13 activator is an oligomeric or polymeric alumoxane compound, such as methylalumoxane and its known modifications. See, for example, Barron, Alkylalumoxanes, Synthesis, Structure and Reactivity, pp. 33-67 in Metallocene-Based Polyolefins: Preparation, Properties and Technology, J. Schiers and W. Kaminsky (eds.), Wiley Series in Polymer Science, John Wiley & Sons Ltd., Chichester, England, 2000, and references cited here .
In other embodiments, a divalent metal reagent can be used which is characterized by the general formula M'R ⁵⁰ 2-pD _p and p 'is 0 or 1 in this modality and R ⁵⁰ and D are as defined above. M 'is the metal and is selected from the group consisting of Mg, Ca, Sr, Ba, Zn, Cd, Cu and their combinations.
In still other embodiments, an alkali metal reagent can be used which is defined by the general formula M ^IV R ⁵⁰ and in this modality
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R ⁵⁰ is as defined above, and M ^IV is the alkali metal and is selected from the group consisting of Li, Na, K, Rb, Cs and their combinations. Additionally, hydrogen and / or silanes can be used in the catalytic composition or added to the polymerization system. Silanes can be characterized by the formula SiR ⁵⁰ 4.qD _q , where R ⁵⁰ is defined as above, q is 1, 2, 3 or 4 and D is as defined above, with the proviso that at least one D is hydrogen.
Non-limiting examples of Group 13 reagents, divalent metal reagents and alkali metal reagents useful as activators for the catalyst compounds described above include methyl lithium, butyl lithium, phenyl lithium, dihexylmercury, butylmagnesium, diethyl cadmium, benzylpotassium, tri-n -butyl aluminum, diisobutyl ethylboro, diethyl cadmium and tri-n-amyl boron and, in particular, aluminum alkyls, such as hexyl aluminum, ethyl aluminum, methyl aluminum and isobutyl aluminum, diisobutyl aluminum bromide, diethylaluminum chloride, dichloride ethyl aluminum, isobutyl boron dichloride, methyl magnesium chloride, ethyl beryl chloride, ethyl calcium bromide, diisobutyl aluminum hydride, methyl cadmium hydride, diethyl boron hydride, hexylberyl hydride, dipropylboro hydride octylmagnesium, dichloroboro hydride, di-bromoaluminum hydride and bromocadium hydride. Other reagents Group 13, divalent metal reagents , and alkali metal working reagents as activators for the catalyst compounds described above are known to those skilled in the art and a more complete discussion of these compounds may be found in US Patents ^Nos 3,221. 002 and 5,093,415, which are incorporated herein by reference.
Other activators include those described in PCT publication WO 98/07515 as tris (2,2 ', 2 ”-nonafluorobiphenyl) fluoroaluminate, the publication of which is fully incorporated herein by reference. Combinations of activators are also contemplated by the invention, for example, alumoxanes and ionizing activators in combinations, see, for example, EP 0573120B1, PCT publications WO 94/07928 and WO 95/14044 and Pat. ^Nos 5,153,157 and US 5,453,410, all of which are herein fully incorporated by reference.
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Other suitable activators are disclosed in WO 98/09996, incorporated herein by reference, which describes the activation of bulky binder metallocene catalyst compounds with perchlorates, periodates and iodates including their hydrates. WO 98/30602 and WO 98/30603, incorporated by reference, describe the use of lithium (2,2'-bisphenyl-ditrimethylsilicate) * 4THF as an activator for a bulky binder metallocene catalyst compound.
WO 99/18135, incorporated herein by reference, describes the use of organo-boron-aluminum activators. EP 0781299B1 describes the use of a lithium salt in combination with a compatible, uncoordinated anion. In addition, activation methods such as the use of radiation (see EP 061598B1 hereby incorporated by reference), electrochemical oxidation and the like are also contemplated as activation methods for the purposes of making the chromium complexes or compositions active for the selective oligomerization of olefins. Other activators or methods are described, for example, in US Patents ^Nos 5,849,852, 5,859,653 and 5,869,723 and in WO 98/32775 and WO 99/42467 (dioctadecilmetilamônio bis (tris (pentafluorophenyl) borane) benzimidazolide) , which are hereby incorporated by reference.
Additional optional activators include metal salts of uncoordinated or weakly coordinated anions, for example, where the metal is selected from Li, Na, K, Ag, Ti, Zn, Mg, Cs and Ba.
Coactivator
Preferably, the co-activator is an organoaluminum compound and / or an organoboro compound. Alternatively, it can be an organic salt such as methyl lithium bromide and / or methyl magnesium, or an inorganic acid or salt such as tetrafluoroboric acid etherate, silver tetrafluoroborate, sodium hexafluoroantimonate and the like.
Examples of suitable organoboro compounds are boroxins, triethylborane, tris (pentafluorophenyl) borane, tributyl borane and the like.
Suitable organoaluminium compounds include compounds of the formula AI (R ⁹ ) ₃ (R ⁹ being the same or different), where each R ⁹ is independently an organyl group, a halogenated organyl group or a
31/42 halide, with at least one of R ⁹ being an organyl group or a halogenated organyl group. Examples include trimethyl aluminum (TMA), triethyl aluminum (TEA), triisobutyl aluminum (TIBA), tri-n-octyl aluminum, methyl aluminum dichloride, ethyl aluminum dichloride, dimethyl aluminum chloride, diethyl aluminum chloride, aluminum isopropoxide, methyl aluminum chloride and alkali metal.
Aluminoxanes are well known in the art as typically oligomeric compounds that can be prepared by the controlled addition of water to an alkyl aluminum compound, for example, trimethyl aluminum. Such compounds can be linear, cyclic, cages or mixtures thereof. Mixtures of different aluminoxanes can also be used in the process.
In one embodiment, the co-activator may comprise a compound of the formula:
M '(R) _n where:
M is selected from the group consisting of an atom of group 3A, an atom of group 4A and a metal atom, including an alkali metal atom and an alkaline earth metal atom;
n is 1 or a larger integer; and
R is an organic group, R being the same or different when n is greater than 1.
Preferably, M is selected from the group consisting of a group 3A atom, a group 4A atom and a transition metal atom. Preferably, the group R is attached to an atom of the group 3A. Preferably, the atom from group 3A is selected from the group consisting of Al and B, preferably it is Al.
The organic group R can be an organyl group, and preferably comprises a hydrocarbyl group, preferably comprises an alkyl group, preferably methyl, ethyl or a larger alkyl group.
In one embodiment of the invention, the co-activator comprises AIR 3, where R is an alkyl group.
The cocatalyst can be selected from the group that consists of trimethyl aluminum (TMA); triethyl aluminum (TEA), tributyl aluminum, triisobutyl aluminum (TIBA) and tri-n-octyl aluminum.
It will be appreciated that TMA is relatively expensive and according to its use it may be desired to be avoided. It has been found that the use of an activator as defined in the present invention in combination with a coactivator as defined above (but excluding MAO), the use of TMA can be avoided as a cocatalyst.
It is envisaged that a co-activator as defined above will usually be used in combination with an activator as defined above.
In use, where an activator and a co-activator are used, the co-activator can be added first and the activator can be added subsequently.
Zinc Compound
An additive can be used in the form of a species containing zinc, the species can be any form of zinc or any compound containing zinc. The zinc compound can undergo reaction in situ with trialkylalumin to form a new species of zinc in situ.
Specific examples of suitable zinc compounds include zinc, activated zinc, zinc halides, alkyl zinc, zinc oxygenates (including zinc acetate, acetylacetones and carboxylates) and porphyrin zinc. Preferably, the zinc compound is dialkyl zinc, more preferably dimethyl zinc or diethyl zinc.
The zinc compound is present in the reaction of the invention in an amount sufficient so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the chromium source is between 1 and 10,000, preferably between 10 and 10.00, and more preferably between 50 and 450.
Zinc can be used as any stock solution concentration and the in situ concentration in the reactor should be between 0.0001 mmol / L and 1 mol / L, more preferably between 0.001 mmol / L and 0.1 mol / L, and more preferably between 0.01 mmol / L and 0.01 mol / L.
The zinc compound can be added at any stage
33/42 during the activation process, more preferably it is added directly to the reactor. Zinc can be used as a mixed stock solution with trialkylaluminum, or with any other component.
The Depositor found that the use of the zinc compound in conjunction with the activator compound significantly reduces the level of solids / polymer formed as a by-product during the oligomerization reaction.
Olefinic compound to be oligomerized
The olefinic compound can comprise a single olefinic compound or a mixture of olefinic compounds. In one embodiment of the invention, it may comprise a single olefin.
The olefin may include multiple carbon-carbon double bonds, but preferably comprises a single carbonocarbon double bond. The olefin may comprise an α-olefin having 2 to 30 carbon atoms, preferably 2 to 10 carbon atoms. The olefinic compound can be selected from the group consisting of ethylene, propene, 1butene, 1-pentene, 1-hexene, 1-heptene and 1-octene, 1-nonene, 1-decene, 3methyl-1-pentene, 3 -methyle-1-penetene, 4-methyl-1-pentene, styrene, p-methyl styrene, 1-dodecene or combinations thereof. Preferably, it comprises ethylene or propene, preferably ethylene. Ethylene can be used to produce hexene and / or octene, preferably 1-hexene and / or 1-octene. Oligomerization
The oligomerization process can comprise a trimerization process, alternatively or additionally it can comprise a tetramerization process.
The process can be oligomerization of two or more different olefinic compounds to produce an oligomer containing the reaction product of the two or more different olefinic compounds. Preferably, however, oligomerization (preferably trimerization and / or tetramerization) comprises the oligomerization of a single monomeric olefinic compound.
In a preferred embodiment of the invention, the oligomerization process is oligomerization of a single α-olefin to produce an oligomeric a34 / 42 olefin. Preferably, it comprises the trimerization and / or tetramerization of ethylene, preferably to 1-hexene and / or 1-octene.
Oligomeric product
The oligomeric product can be an olefin, or a compound that includes an olefinic portion. Preferably, the oligomeric product includes an olefin, more preferably an olefin containing a single carbon-carbon double bond, and preferably includes an α-olefin. The olefinic product may include hexene, preferably 1-hexene, but more preferably includes octene, preferably 1-octene. In a preferred embodiment of the invention, the olefinic product includes a mixture of hexene and octene, preferably a mixture of 1-hexene and 1-octene.
In a preferred embodiment of the invention, the oligomerization process is a selective process to produce an oligomeric product containing more than 30% by weight of a single olefinic product. The olefinic product may be hexene, preferably 1-hexene, but alternatively it may be octene, preferably 1-octene.
Preferably, the product contains at least 35% of said olefin, preferably α-olefin, however it can be more than 40%, 50% or up to 60% by weight.
The olefinic product can be branched, but preferably it is unbranched.
Catalyst preparation
It is envisaged that i) the chromium source and ii) the binding compound (referred to in (a) of the main text of the invention) can be first reacted together and the resulting product can be further isolated, before combining it with the activator of catalyst iii). However, i), ii) and iii) can be combined in any suitable order in the presence or absence of a solvent, but preferably at least some, but preferably all of i), ii) and iii) are first combined and subsequently contacted with the olefinic compound.
The contact of the olefinic compound with compounds i) to iii) and b) preferably occurs under conditions to allow oligomerization of the olefinic compound. Such conditions are well known to one skilled in the art and include elevated temperatures and pressure. Solid oligomerization can be carried out at temperatures of 100 ° C to 250 ° C, however temperatures in the range of 15 ° C to 130 ° C are preferred, particularly temperatures in the range of 50 ° C to 120 ° C. The oligomerization is preferably carried out at a temperature of at least 0 ° C, preferably at least 40 ° C, and preferably at least 50 ° C. Preferably, it is performed at a pressure of at least 100 kPa, preferably at least 1000 kPa, preferably at least 3000 kPa.
The preparation of the activated catalyst can be carried out in a liquid medium, preferably an inert liquid medium. The liquid medium can be the same liquid medium in which oligomerization with the diluted catalyst is carried out.
The oligomerization catalyst activated before dilution can be prepared in the same container as the one in which the diluted activated oligomerization catalyst is contacted with the olefinic compound to be oligomerized. Preferably, the oligomerization catalyst activated before dilution is prepared in a container separate from that in which the oligomerization catalyst is contacted with the olefinic compound to be oligomerized.
The chromium source and binder compound can be combined to provide any suitable molar ratio, preferably a chromium to binder molar ratio of about 0.01: 100 to 10,000: 1, preferably about 0.1: 1 to 10 : 1.
Zinc can be used in any filler compared to chromium, preferably between 1 and 10,000, more preferably between 10 and 1,000, more preferably between 50 and 450. Zinc can be used as any stock solution concentration and the in situ concentration in the reactor can be between 0.0001 mmol / L and 1 mol / L, more preferably between 0.001 mmol / L and 0.1 mol / L, more preferably between 0.01 mmol / L and 0.01 mol / L.
The zinc additive can be added at any stage during the activation procedure, more preferably it is added
36/42 directly to the reactor. Zinc can be used as a mixed stock solution with trialkylaluminum.
The process may also include combining one or more different sources of chromium with one or more different binder compounds.
The oligomerization catalyst or its individual components, according to the invention, can also be immobilized by supporting it on a support material, for example, silica, alumina, MgCE, zirconia, artificial hectorite or smectorite clays such as Laponile® RD or its mixtures, or on a polymer, for example, polyethylene, polypropylene, polystyrene or poly (amino-styrene). The catalyst can be formed in situ in the presence of the support material, or the support can be pre-impregnated or pre-mixed, simultaneously or sequentially, with one or more of the catalyst components or the oligomerization catalyst. In some cases, the support material can also act as a component of the activator. This approach would also facilitate the recovery of the catalyst from the reaction mixture for reuse.
The invention will now be described by way of non-limiting examples:
Examples
In this specification, the abbreviation TEA is used for triethyl aluminum and PNP is used for bis (diarylphosphanyl) amine ligand
A 1 or 1.2 L stainless steel reactor was heated to 120 ° C under vacuum for 30 minutes, cooled to 60 ° C and refilled with air. The reactor was charged with solvent and saturated with ethylene.
Separately, TEA then activating salt (as stock solutions) were added sequentially to a stirred solution of Cr ( ^t Bu ₂ acac) ₃ / PNP. The activation solution was added to the reactor and the reactor was pressurized to 50 bar with ethylene. The reaction pressure was kept constant during the addition of ethylene monitored with a phloxometer. After ethylene capture ceased, the gas supply was closed and the reactor cooled to 0 ° C. Excess ethylene was drained and the reactor contents treated sequentially with 1000 pL of nonane (internal standard CG),
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MeOH and 10% HCI (aq.). A sample of the organic phase was taken for CG-FID analysis. Any solid formed was collected, washed repeatedly with 10% HCI (aq.) And EtOH, dried overnight and weighed.
Example 1: ethylene oligomerization using a Cr / PNP / [(C ₁₈ H ₃₇ ) 2N (H) (Me)] [B (C ₆ F ₅ ) ₄ ] / TEA system
In all tests using this reagent, the total amount of ZnEt2 was added to the reactor with the solvent in the pre-scrubbing stage. The entire catalyst was driven in the 1.2 L equipment where typical runs consume> 400 g of ethylene, so the absolute amount of polymer formed is approximately 1-3 g. Given the ability to collect, wash, dry and weigh the polymer to the nearest 10 mg, the polymer's quantification accuracy is better than 0.0025%.
Table 1 below shows against entry # 316 a standard run using Cr / PNP / TEA / borate in PhCI; the total solid polymer formation is 0.65% polymer.
In contrast, entry 330 shows an execution using the same conditions except for an additional 420 eq. of ZnEt ₂ . It can be seen that the total solid formation is reduced to 0.38% - representing a 42% reduction in polymer formation.
Entry 312 is a borate run in the cyclohexane aliphatic solvent, included for comparison; polymer formation is 0.57%. As can be seen from the entries 354 (25 eq.), 346 (50 eq.), 345 (100 eq.), 73 (150 eq.), 348 (420 eq.), The addition of ZnEt ₂ to 50 equivalent or above successfully reduces the level of polymer formation to an average of 0.35% - an average reduction of 35%. Entries 234 (1000 eq), 237 (5000 eq) and 238 (10,000 eq) all show that even at high zinc loads the polymer number is reduced, while maintaining good activity.
Entry 239 is a borate run in the aliphatic cyclohexane solvent with a different binder and chromium source, included for comparison; polymer formation is 0.78%. As can be seen from inputs 236 (1 eq.) And 235 (10 eq.), The addition of ZnEt ₂ even at these very low charges successfully reduces the level of polymer formation to a
38/42 average of 0.45%.
Entry 324 is a run performed on 2,2,4 trimethylpentane (TMP) which shows a level of polymer formation of 0.92%. Executions 347 and 332 show that the addition of 50 and 420 eq. in
ZnEt ₂ can reduce this level of polymer to an average of 0.46%.
Looking at all the examples in Table 1, it can be seen that the addition of ZnEt ₂ has little or no effect on the amount of 1hexene and 1-octene formed.
Table 1: Results of catalyst tests with varying amounts of 10 diethyl zinc
Input# Solvent ZnEt ₂ eq. Timecat.(min) Activityg / gCr / h % pp hexene and octene ^b % pp polymer (g) 316 PhCI 0 75.3 5,214,575 83.2 0.65(2.63) 330 PhCI 420 43.3 9,081,307 82.0 0.38(1.49) 312 CyH 0 86.0 4,549,445 81.9 0.57(2.41) 239 ^and CyH 0 154 1,786,201 87.5 0.78(2.34) 236 ^and CyH 1 111.6 2,935,441 85.6 0.43(1.53) 235 ^and CyH 10 87.1 3,670,522 86.5 0.46(1.59) 354 CyH 25 85.3 4,133,342 82.3 0.37(1.41) 346 CyH 50 97.0 3,733,376 82.5 0.31(1.22) 345 CyH 100 94.5 4,046,426 81.6 0.47(1.96) 73 CyH 150 112.6 3,469,238 83.4 0.25(1.08) 348 CyH 420 94.6 3,774,950 83.3 0.37(1.45) 234 ^and CyH 1000 99.6 3,161,004 86.8 0.45(1.54) 237 ^and CyH 5000 120.0 2,291,502 87.0 0.32(0.95) 238 ^and CyH 10000 224.0 1,014,743 87.4 0.21(0.52)
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Input# Solvent ZnEt ₂ eq. Timecat.(min) Activityg / gCr / h % pp hexene and octene ^b % pp polymer (g) 324 TMP 0 114.2 3,531,036 82.2 0.92(4.01) 347 TMP 50 154.7 2,407,089 81.2 0.47(1.89) 332 TMP 420 232.0 1,660,724 82.1 0.44(1.77)
General conditions: ^at 1.25 pmol of Cr ('Bu2acac) 3; 1.2 eq. Ph2P {C (H) (Me) ({CH2} 5CH3)} - PPh2; 1.2eq. [(C18H37) 2N (H) (Me)] [B (C6F5) 4r2; 420 eq. TEA (activation at 50 eq., Reactor at 370 eq.); p (=) 50 bar 60 ° C; 200 mL of solvent; 1.2 L rig. ^b =% of liquid fraction ^c =% of total product formed (liquid and solid). ^and 1.25 μτηοΙ Cr (2-EH) 3; 1.2 eq. Ph ₂ PN {C (H) (Me) (C (H) (e) {CH ₂ } ₄ CH ₃ )} - PPh ₂
Example 2: ethylene oligomerization using an MAO-based system
For these studies, the catalysis was performed either in cyclohexane or in 2,2,4-trimethylpentane. Data on catalyst activity and product selectivity are summarized in Table 2. The polymeric product made in catalysis was carefully isolated, washed repeatedly and dried.
Entry 056 represents the optimal MAO-activated catalysis that can be achieved in CH for the two sets of pre-catalysts and entry 181 for 2,2,4-trimethylpentane catalysis. Diethyl or dimethyl zinc is added to the reactor in the pre-scrubbing phase, which immediately follows the addition of solvent to the reactor.
The performance of the catalyst is shown for the standard run containing 50 eq. of diethyl zinc (entry 059), and is also accompanied by a marked reduction in solids (from 0.8% to 0.6%). Diethyl zinc again appears to have little effect on the total selectivity of the catalyst; entry 056 (83.5%) versus 059 (83.9%).
Although a clear increase in activity is seen when 50 eq. of ZnMe ₂ are used (entry 185), there is no reduction in solids. However, increasing the equivalents from 50 to 100 shows a reduction of 0.49 to 0.41%, as well as a significant increase in activity.
Table 2. The effect of ZnR ₂ R = Me or Et on MMAO catalysis
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Input (Eq. ZnEt ₂ ) Productivityg / gCr Activityg / gCr / H % pp hexene and octene ^b % pp in (g) ^c 056 ^a (0 eq. ZnEt ₂ ) 3 446895 1 969654 80.7 0.80(2.83) 058 ^a (100 eq. ZnEt ₂ ) 2 476986 1 170230 82.4 0.60(1.49) 059 ^a (50 eq. ZnEt ₂ ) 3 298861 1 691724 83.9 0.60(1.49) 181 ^d (0 ZnMe _{2 equipment} ) 1 805992 2 642916 87.1 0.49(0.92) 190 ^d (100 ZnMe ₂ eq.) 1 899827 3 864054 86.8 0.41(0.81)
General conditions: ^at 2.0 pmol Cr (acac) ₃ and 1.2 eq. Ph ₂ PN {C (H) (Me) ({CH ₂ } ₂ CH ₃ )} - PPh ₂ ; MAO (480 eq.); 50 bar ethylene; 60 ° C; 200 mL of cyclohexane. ^b =% of liquid fraction ^c =% of total product formed (liquid and solid) ^d 2.0 pmol Cr (acac) ₃ and 1.1 eq. Ph ₂ PN {C (H) (Me) ('Pr)} - PPh ₂ in 2,2,4-trimethylpentane; MAO (480 eq.); 45 bar ethylene; 60 ° C; 300 ml. Example 3: change in conditions
The results reflected in Table 3 below show that the effect of the addition of ZnEt ₂ is not affected by the choice of the source of chromium and coca10 used. This effect is also not unique to the PNP ligand system, since it not only works with the Ph ₂ PN {C (H) (Me) ('Pr)} - PPh ₂ , Ph ₂ P- N {C (H ) (Me) ({CH ₂ } ₅ CH ₃ )} - PPh ₂ , and (o-MeC6H4) ₂ PN ('Pr) -Ph ₂ bulky, but also with other binders such as Ph2P-N {C (H) ( Me) (iPr)} - PPh2, Ph2P- N {C (H) (Me) ({CH2} 5CH3)} - PPh2 and the (o15 Me-C6H4) 2P-N (iPr) -PPh2. This indicates that the effect of ZnEt2 is not unique to PNP, PNNP and DPPE tetramerization systems, but also, as expected, it applies to non-selective oligomerization systems, DPPM. The most significant change in the use of ZnEt ₂ comes from running in alternative solvents.
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Table 3. Results of catalyst tests with varying conditions
Input# Cr / L / A ZnEt ₂ eq. Timecat.(min) Activityg / gCr / h % pp hexene and octane__dat the % pp ^with polymer (g) ^and 424 Cr ( ^l Bu ₂ acac) ₃ / Ph ₂ P ~ N {C (H) (Me) ({CH ₂ } ₅ C H ₃ )} - PPh ₂ / OAB 0 207.0 1,744,506 83.0 0.85(3.34) 423 Cr ('Bu ₂ acac) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₅ C H ₃ )} - PPh ₂ / OAB 420 151.5 2,469,579 82.4 0.77(3.12) 427 Cr (acac) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₂ C H ₃ )} - PPh ₂ / TA 0 39.9 9,962,823 84.1 1.76(7.55) 426 Cr (acac) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₂ C H ₃ )} - PPh ₂ / TA 420 49.6 8,718,296 83.2 0.38(1.79) 434 ^c Cr ('Bu ₂ acac) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₅ C H ₃ )} - PPh ₂ / RB 0 135.0 2,874,486 83.1 2.36(9.93) 435 ^c θΓ ('Βυ ₂ 3Ο3θ) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₅ CH ₃ )} - PPh ₂ / RB 100 89.6 3,530,896 83.8 1.85(6.35) 445 ^b Cr (2-EH) 3 /DPPE /RB 0 74.0 115,961 70.5 24.7(4.59) 446 ^b Cr (2-EH) 3 /DPPE /RB 100 107.0 147,931 71.1 13.0(4.44) 447 ^b Cr (2-EH) 3 /DPPM /RB 0 95.7 17,092 28.8 77.9(2.76) 448 ^b Cr (2-EH) 3 /DPPM /RB 100 107.2 16,159 27.9 66.2(2.48) 452 ^b Cr (2-EH) ₃ / (o-Me-C ₆ H ₄ ) ₂ PN ('Pr) - PPh ₂ / RB 100 49.5 632,715 91.0 4.94(1.67)
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Input# Cr / L / A ZnEt ₂ eq. Timecat.(min) Activityg / gCr / h % pp hexene and octane__dat the % pp ^with polymer (g) ^and 453 ^b Cr (2-EH) 3 / (o-Me-C ₆ H ₄ ) ₂ PN ('Pr) - PPh ₂ / RB 0 18.0 443,168 91.0 23.02(1.99) 454 ^b Cr (2-EH) 3 / Ph ₂ PN (Me) -N- (CH ₂ CH ₂ Pr ') - PPh ₂ / RB 100 51.5 441,991 90.2 11.47(2.83) 455 ^b Cr (2-EH) 3 / Ph ₂ PN (Me) -N- (CH ₂ CH ₂ Prj-PPh ₂ / RB 0 65.8 80,240 86.9 61.88(3.54) 428 Cr ('Bu ₂ acac) 3 / Ph ₂ P- N {C (H) (Me) ({CH ₂ } ₅ C H ₃ )} - PPh ₂ / RB 420 ZnMe ₂ 80.3 4,044,548 83.9 0.43(1.50)
General conditions: ^at 1.25 pmol Cr; 1.2eq. Binder; 1.2eq. Anion;
420 eq. TEA (activation at 50 eq., 370 eq .; 200 ml of solvent 1.2 L reactor p (=) 50 bar; 60 ° C; 200 ml of solvent; equipment of 1.2 L. ^b 150 eq. TEA ( activation) 65 mL solvent 300 mL reactor ^c AI'Bii ₃ in place of TEA ^d =% of liquid fraction ^e =% of total product formed (liquid and solid) ^f OAB = [Oct ₃ NH] [B (C ₆ F ₅ ) ₄ ]; RB = [(C ₁₈ H37) 2N (H) Me] [B (C ₆ F ₅ ) ₄ ]; TA = [Ph ₃ C] [AI (0'Bu ^F ) ₄ ]; Cr (2-EH) ₃ = Cr (2-ethylhexanoate) ₃ ; DPPE = bis (diphenylphosphanyl) ethane; DPPM = bis (diphenylphosphanyl) methane.
The use of alkyl zinc, in particular diethyl zinc in conjunction with the Cr / PNP / TEA / borate catalyst system and dimethyl zinc in conjunction with the Cr / PNP / MMAO system clearly has benefits in reducing the level of polymer formation in an amount significant, although increasing the rate of catalysis.
It is also noted that only a low level of ZnEt ₂ is needed to achieve this effect, around 50-100 equivalents, with higher Zn loads offering few additional advantages.
The use of this reagent also satisfies the requirement to have little or no effect on the selective oligomerization mechanism with little disruption to the total target oligomer value being observed.
1/4

权利要求:
Claims (15)
[1]
1. Process for producing an oligomeric product by oligomerization of at least one olefinic compound, the process including:
a) provide an activated oligomerization catalyst combining, in any order,
i) a chromium source;
ii) a binding compound of the formula I (R ¹ ) _m X ¹ (Y) X ² (R ² ) n ... I, where:
X ¹ and X ² are independently an atom selected from the group consisting of nitrogen, phosphorus, arsenic, antimony, bismuth, oxygen, sulfur and selenium or said atom oxidized by S, Se, N or O, where the valence of X ¹ and / or X ² allows such oxidation;
Y is a linking group between X ¹ and X ² ;
m and n are independently 0, 1 or a larger integer, and
R ¹ and R ² are independently hydrogen, a hydrocarbyl group, an organo-heteryl group or a hetero-hydrocarbyl group, and R ¹ being the same or different when m> 1, and R ² being the same or different when n> 1 , iii) a catalyst activator or combination of catalyst activators;
b) providing a zinc compound, and
c) contacting at least one olefinic compound with a composition containing the activated oligomerization catalyst and zinc compound, the zinc compound being present in a sufficient amount so that the molar amount of zinc in the zinc compound is the molar amount of chromium in the chromium source is between 1 and 10,000.
[2]
2. Process for activating an oligomerization catalyst to be used to produce an oligomeric product from at least one olefinic compound, the process comprising the combination, in any order, of:
2/4
i) a chromium source;
ii) a binding compound of the formula I (R ¹ ) mX ¹ (Y) X ² (R ² ) n ... I, where:
X ¹ and X ² are independently an atom selected from the group consisting of nitrogen, phosphorus, arsenic, antimony, bismuth, oxygen, sulfur and selenium or said atom oxidized by S, Se, N or O, where the valence of X ¹ and / or X ² allows such oxidation;
Y is a linking group between X ¹ and X ² ;
m and n are independently 0, 1 or a larger integer, and
R ¹ and R ² are independently hydrogen, a hydrocarbyl group, an organo-heteryl group or a hetero-hydrocarbyl group, and R ¹ being the same or different when m> 1, and R ² being the same or different when n>1;
iii) a catalyst activator or combination of catalyst activators;
iv) a zinc compound, the zinc compound being present in an amount sufficient so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the chromium source is between 1 and 10,000.
[3]
A process according to claim 1 or 2, wherein the zinc compound is present in the reaction of the invention in an amount sufficient so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the source chromium is between 10 and 1000.
[4]
Process according to claim 1 or 2, wherein the zinc compound is present in the reaction of the invention in an amount sufficient so that the ratio of the molar amount of zinc in the zinc compound to the molar amount of chromium in the source chromium is between 50 and 450.
[5]
Process according to any one of the preceding claims, wherein the process includes the use of a solvent.
[6]
Process according to any one of the preceding claims, wherein the oligomerization catalyst is a trimerization catalyst or a tetramerization catalyst.
[7]
Process according to any one of the preceding claims, wherein X ¹ and X ² are independently phosphorus or phosphorus oxidized by S or Se or N or O.
[8]
Process according to any one of the preceding claims, wherein the binding compound is of formula II:
R ⁶ ......... ii where
Y is a linking group between X ¹ and X ² , X ¹ and X ² are independently selected from the group consisting of nitrogen, phosphorus, arsenic, antimony and bismuth and R ³ to R ⁶ are each independently one hydrocarbyl group or a heterohydrocarbyl group.
[9]
Process according to any one of the preceding claims, wherein Y is selected from the group consisting of an organic bonding group comprising a hydrocarbilene, substituted hydrocarbilene, heterohydrocarbilene and a substituted heterohydrocarbilene; an inorganic bonding group comprising either a single atom molecular spacer or two atoms; and a group comprising methylene; dimethylmethylene; ethylene; ethylene-1,2-diyl; propane-1,2-diyl, propane-1,3-diyl; cyclopropane-1,1-diyl; cyclopropane-1,2-diyl; cyclobutane-1,2-diyl, cyclopentane-1,2-diyl, cyclohexane-1,2-diyl, cyclohexane-1,1-diyl; 1,2-phenylene; naphthalene-1,8-diyl; phenanthrene-9,10-diyl, phenanthrene-4,5-diyl, 1,2catecholate, 1,2-diaryl-hydrazine-1,2-diyl (-N (Ar) -N (Ar) -), where Ar is an aryl group; 1,2-dialkylhydrazine-1,2-diyl (-N (Alk) -N (Alk) -), where Alk is an alkyl group; -B (R ⁷ ) -, -Si (R ⁷ ) ₂ -, -P (R ⁷ ) - and -N (R ⁷ ) -, where R ⁷ is hydrogen, a hydrocarbyl or heterocarbyl or halogen.
4/4
[10]
A process according to claim 8, wherein the binding compound is of formula III:
R ⁷
R ⁴ R ⁶ ........ ui where
R ³ to R ⁷ are each independently a hydrocarbyl group or a heterohydrocarbyl group.
[11]
A process according to claim 10, wherein each of R ³ to R ⁶ is an alkyl selected from the group consisting of methyl, ethyl and isopropyl or an aromatic selected from the group consisting of phenyl and phenyl substituted.
[12]
A process according to claim 1 or 2, wherein the activator is selected from the group of oganoboro compound, alumoxanes including modified aluminoxanes, aluminum alkyls, other metal or alkyl or aryl compounds of the main group, ionizing activators that are neutral or ionic, Lewis acids, oxidizing agents and reducing acids and their combinations.
[13]
Process according to claim 1 or 2, wherein the process includes a reagent selected from a Group 13 reagent, a divalent metal reagent or an alkali metal reagent.
[14]
Process according to claim 1 or 2, wherein the zinc compound is selected from zinc, activated zinc and zinc-containing compounds selected from the group comprising zinc halides, alkyl zinc, zinc oxygenates including acetate zinc, zinc acetylacetonates and zinc carboxylates, and zinc porphyrin.
[15]
A process according to claim 14, wherein the zinc-containing compound is a dialkyl zinc, including dimethyl zinc and diethyl zinc.

类似技术:

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公开号 | 公开日 | 专利标题

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CN114160200A|2022-03-11|Catalyst system for selective ethylene trimerization/tetramerization and preparation method and application thereof

同族专利:

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公开号 | 公开日

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CA2777230A1|2011-04-28|

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WO2011048527A1|2011-04-28|

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MY149647A|2013-09-30|

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EP2490990A1|2012-08-29|

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IN2012DN03367A|2015-10-23|

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CN102725251A|2012-10-10|

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US8859696B2|2014-10-14|

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EP2490990B1|2013-12-04|

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CA2777230C|2015-12-22|

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KR20120098711A|2012-09-05|

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KR101641545B1|2016-07-21|

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BR112012009098A2|2016-05-03|

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US20120316303A1|2012-12-13|

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CN102725251B|2015-11-25|

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ZA201202326B|2012-12-27|

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ES2446096T3|2014-03-06|

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法律状态:
2018-04-10| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2018-05-22| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|

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2021-08-10| B21F| Lapse acc. art. 78, item iv - on non-payment of the annual fees in time|Free format text: REFERENTE A 11A ANUIDADE. |

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2021-11-30| B24J| Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)|Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2640 DE 10-08-2021 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013. |

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