U.S. patent application number 09/784909 was filed with the patent office on 2002-05-02 for hydroformylation of olefins using supported bis (phosphorus) ligands.
Invention is credited to Bunel, Emilio E., Burke, Patrick M., Druliner, Joy D., Manzer, Leo E., Moloy, Kenneth G., Wang, Manxue.
Application Number | 20020052531 09/784909 |
Document ID | / |
Family ID | 22203407 |
Filed Date | 2002-05-02 |
United States Patent
Application |
20020052531 |
Kind Code |
A1 |
Bunel, Emilio E. ; et
al. |
May 2, 2002 |
Hydroformylation of olefins using supported bis (phosphorus)
ligands
Abstract
Supported bis(phosphorus) ligands are disclosed for use in
hydroformylation reactions, including the hydroformylation of
olefins. Catalysts are formed when the ligands are complexed with a
catalytically active metal (e.g., rhodium or iridium).
Inventors: |
Bunel, Emilio E.;
(Wilmington, DE) ; Burke, Patrick M.; (Wilmington,
DE) ; Druliner, Joy D.; (Newark, DE) ; Manzer,
Leo E.; (Wilmington, DE) ; Moloy, Kenneth G.;
(Newark, DE) ; Wang, Manxue; (Wilmington,
DE) |
Correspondence
Address: |
E I DU PONT DE NEMOURS AND COMPANY
LEGAL DEPARTMENT - PATENTS
1007 MARKET STREET
WILMINGTON
DE
19898
US
|
Family ID: |
22203407 |
Appl. No.: |
09/784909 |
Filed: |
February 16, 2001 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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09784909 |
Feb 16, 2001 |
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09291878 |
Apr 14, 1999 |
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6229052 |
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60087151 |
May 29, 1998 |
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Current U.S.
Class: |
568/451 ;
558/353; 560/175 |
Current CPC
Class: |
B01J 2531/0266 20130101;
C08F 8/40 20130101; B01J 31/185 20130101; C08F 8/42 20130101; B01J
31/2452 20130101; B01J 2231/321 20130101; C07C 51/373 20130101;
C07C 253/30 20130101; B01J 31/1658 20130101; C07C 67/347 20130101;
C07C 45/50 20130101; B01J 31/06 20130101; B01J 31/1875 20130101;
B01J 2531/822 20130101; C07C 45/50 20130101; C07C 47/228 20130101;
C07C 51/373 20130101; C07C 59/147 20130101; C07C 67/347 20130101;
C07C 69/716 20130101 |
Class at
Publication: |
568/451 ;
560/175; 558/353 |
International
Class: |
C07C 047/02; C07C
067/313 |
Foreign Application Data
Date |
Code |
Application Number |
May 26, 1999 |
US |
PCT/US99/11557 |
Claims
1. A hydroformylation process comprising reacting an acyclic,
monoethylenically unsaturated compound with CO and H.sub.2 in the
presence of a supported catalyst composition according to formula
(3): 73wherein: Q is any organic fragment which binds a OPX.sub.2
moiety to the support (Sup); X is an alkoxy, aryloxy, alkyl or
aryl; and M is rhodium.
2. The process of claim 1 wherein the support is a functionalized
organic polymer resin.
3. The process of claim 1 wherein X is an aryloxy or aryl with up
to 20 carbon atoms.
4. The process of claim 1 wherein the PX.sub.2 moiety forms a ring
and X.sub.2 is a di(alkoxy), di(aryloxy), di(alkyl), or
di(aryl).
5. The process of claim 1 wherein the reactants are in a liquid
phase.
6. The process of claim 1 wherein the reactants are in the vapor
phase.
7. The process of claim 1 wherein the acyclic, monoethylenically
unsaturated compound has from 2 to 30 carbon atoms.
8. The process of claim 7 wherein the acyclic, monoethylenically
unsaturated compound is propylene.
9. The process of claim 1 wherein the acyclic, monoethylenically
unsaturated compound is an internally ethylenically unsaturated
compound with 4 to 20 carbon atoms.
10. The process of claim 9 wherein the acyclic, monoethylenically
unsaturated compound is a 3-pentenenitrile, 3-pentenoic acid, a
C.sub.1-C.sub.6 alkyl 3-pentenoate ester compound, or a
C.sub.1-C.sub.6 alkyl 4-pentenoate ester compound.
11. The process of claim 10 wherein the alkyl pentenoate ester
compounds are methyl 3-pentenoate or methyl 4-pentenoate.
12. A process according to claim 1 wherein the ratio of acyclic,
monoethylenically unsaturated compounds to rhodium is between 1 to
100,000, the phosphorus to rhodium ratio is between 1 to 20, the
temperature is between 50.degree. C. to 150.degree. C., the total
pressure is between 0.1 to 10 MPa, and the carbon monoxide and
hydrogen are in a ratio between 0.1 to 10.
13. A hydroformylation process comprising reacting an acyclic
aromatic olefinic compound with CO and H.sub.2 in the presence of a
supported catalyst composition according to formula (3): 74wherein:
Q is any organic fragment which binds a OPX.sub.2 moiety to the
support (Sup); X is an alkoxy, aryloxy, alkyl or aryl; and M is
rhodium.
14. The process of claim 13 wherein the support is a functionalized
organic polymer resin.
15. The process of claim 13 wherein X is an aryloxy or aryl with up
to 20 carbon atoms.
16. The process of claim 13 wherein the PX.sub.2 moiety forms a
ring and X.sub.2 is a di(alkoxy), diaryloxy), di(alkyl), or
di(aryl).
17. The process of claim 13 wherein the reactants are in a liquid
phase.
18. The process of claim 13 wherein the reactants are in the vapor
phase.
19. The process of claim 13 wherein the acyclic aromatic olefinic
compound contains from 6 to 30 carbon atoms.
20. The process of claim 19 wherein the acyclic aromatic olefinic
compound is styrene.
21. A process according to claim 13 wherein the ratio of acyclic,
monoethylenically unsaturated compounds to rhodium is between 1 to
100,000, the phosphorus to rhodium ratio is between 1 to 10, the
temperature is between 0.degree. C. to 120.degree. C., the total
pressure is between 0.1 to 20 MPa, and the carbon monoxide and
hydrogen are in a ratio between 0.1 to 10.
22. A process for the preparation of a supported rhodium
bisphosphite hydroformylation catalyst comprising reacting CO and
H.sub.2 with a rhodium compound in the presence of a supported
bis(phosphorus) ligand of formula 1 75in which Q is any organic
fragment which binds the two phosphorus moieties to the support and
X is alkoxy, aryloxy, alkyl, or aryl, or alternatively wherein the
PX.sub.2 moiety forms a ring and X.sub.2 is a di(alkoxy),
di(aryloxy), di(alkyl), or di(aryl).
23. A process according to claim 22 where the supported ligand of
Formula (1) is further characterized according to Formula (4)
76wherein: the linker Q is a 2,2'-dihydroxyl-1,1'-binaphthalene
bridging group; the substituents R.sub.7 and R.sub.8 in the 3,3'
positions of the binaphthalene bridging group are selected from
alkyl group containing 2 to 10 carbon atoms, an aryl group, an
alkoxy group, an aryloxy group, a carboalkoxy group, a carboaryloxy
group, a nitrile group, a triarylsilyl group, or trialkylsilyl
group; at least one of the groups R.sub.7 and R.sub.8 are
covalently attached to a support (Sup); X is an alkoxy, aryloxy,
alkyl, or aryl, or alternatively the PX.sub.2 moiety forms a ring
and X.sub.2 is a di(alkoxy), di(aryloxy), di(alkyl), or
di(aryl).
24. A process according to claim 22 wherein the temperature is in
the range 25-120.degree. C. and CO and H.sub.2 partial pressures in
the range 0.1-3.4 MPa.
25. A process according to claim 24 wherein the rhodium compound is
dissolved in a solvent which is a good swelling solvent for the
support.
26. A process according to claim 22 wherein the support is an
organic polymer resin.
27. A process according to claim 22 wherein the organic polymer
resin is a crosslinked polystyrene resin.
28. A hydroformylation catalyst composition according to claim 23,
characterized in that R.sup.1 and R.sup.2 are carboalkoxyl groups,
CO--O--R, in which R is a C.sub.1-C.sub.20 alkyl or a
C.sub.6-C.sub.20 aryl.
Description
FIELD OF THE INVENTION
[0001] The invention generally relates to the hydroformylation of
unsaturated organic compounds utilizing supported bis(phosphorus)
ligands. In particular, the invention relates to the
hydroformylation of olefins utilizing supported bis(phosphorus)
ligands.
BACKGROUND OF THE INVENTION
[0002] Phosphorus ligands are ubiquitous in catalysis, finding use
for a number of commercially important chemical transformations.
Phosphorus ligands commonly encountered in catalysis include
phosphines (A), and phosphites (B), shown below. In these
representations R can be virtually any organic group. Monophosphine
and monophosphite ligands are compounds which contain a single
phosphorus atom which serves as a donor to a metal. Bisphosphine,
bisphosphite, and bis(phosphorus) ligands in general, contain two
phosphorus donor atoms and normally form cyclic chelate structures
with transition metals. 1
[0003] Two industrially important catalytic reactions using
phosphorus ligands of particular importance are olefin
hydrocyanation and olefin hydroformylation. Phosphite ligands are
particularly good ligands for both of these transformations. For
example, the hydrocyanation of ethylenically unsaturated compounds
using transition metal complexes with monodentate phosphite ligands
is well documented in the prior art. See, for example, U.S. Pat.
Nos. 3,496,215, 3,631,191, 3,655,723 and 3,766,237, and Tolman et
al., Advances in Catalysis, 33, 1, 1985. Bidentate bisphosphite
ligands have been shown to be useful in the hydrocyanation of
monoolefinic and diolefinic compounds, as well as for the
isomerization of non-conjugated 2-alkyl-3-monoalkenenitriles to 3-
and/or 4-monoalkene linear nitriles. See, for example, U.S. Pat.
No. 5,512,695, U.S. Pat. No. 5,512,696 and WO 9514659. Bidentate
phosphite ligands have also been shown to be particularly useful
ligands in the hydrocyanation of activated ethylenically
unsaturated compounds. See, for example, Baker, M. J., and Pringle,
P. G., J. Chem. Soc., Chem. Commun., 1292, 1991; Baker et al., J.
Chem. Soc., Chem. Commun., 803, 1991; WO 93,03839. Bidentate
phosphite ligands are also useful for alkene hydroformylation
reactions. For example, U.S. Pat. No. 5,235,113 describes a
hydroformylation process in which an organic bidentate ligand
containing two phosphorus atoms linked with an organic dihydroxyl
bridging group is used in a homogeneous hydroformylation catalyst
system also comprising rhodium. This patent describes a process for
preparing aldehydes by hydroformylation of alkenically unsaturated
organic compounds, for example 1-octene or dimerized butadiene,
using the above catalyst system. Also, phosphite ligands have been
disclosed with rhodium in the hydroformylation of functionalized
ethylenically unsaturated compounds: Cuny et al., J. Am. Chem.
Soc., 1993, 115, 2066. These prior art examples demonstrate the
utility of bisphosphite ligands in catalysis.
[0004] While these prior art systems represent commercially viable
catalysts, they do suffer from significant drawbacks. Primarily,
the catalyst, consisting of the ligand and the metal, must be
separated from the reaction products. Typically this is done by
removing the product and catalyst mixture from the reaction zone
and performing a separation. Typical separation procedures involve
extraction with an immiscible solvent, distillation, and phase
separations. In all of these examples some of the catalyst,
consisting of the ligand and/or the metal, is lost. For instance,
distillation of a volatile product from a non-volatile catalyst
results in thermal degradation of the catalyst. Similarly,
extraction or phase separation results in some loss of catalyst
into the product phase. These ligands and metals are often very
expensive and thus it is important to keep such losses to a minimum
for a commercially viable process.
[0005] One method to solve the problem of catalyst and product
separation is to attach the catalyst to an insoluble support.
Examples of this approach have been previously described, and
general references on this subject can be found in "Supported Metal
Complexes", D. Reidel Publishing, 1985, Acta Polymer. 1996, 47, 1,
and Comprehensive Organometallic Chemistry, Pergamon Press, 1982,
Chapter 55. Specifically, monophosphine and monophosphite ligands
attached to solid supports are described in these references and
also in Macromol. Symp. 1994, 80, 241. Bisphosphine ligands have
also been attached to solid supports and used for catalysis, as
described in for example U.S. Pat. No. 5,432,289, J. Mol. Catal. A
1996, 112, 217, and J. Chem. Soc., Chem. Commun. 1996, 653. The
solid support in these prior art examples can be organic, e.g., a
polymer resin, or inorganic in nature.
[0006] Commonly assigned copending provisional application Ser. No.
60/054,003, filed Jul. 29, 1997, overcomes many of the problems
associated with catalytic hydrocyanation by utilizing supported
bis(phosphorus) ligands coordinated to nickel for hydrocyanation of
olefins.
[0007] These prior art systems have to date suffered from several
drawbacks and have not reached commercial potential. Among the
drawbacks noted in the literature are metal leaching and poor
reaction rates. In addition, the prior art systems are often not
readily amenable to precise control of the ligand coordination
properties, e.g., electronics and steric size. What is needed is a
supported bis(phosphorus) ligand system which overcomes the
problems and deficiencies inherent in the prior art with respect to
hydroformlyation. Other objects and advantages of the present
invention will become apparent to those skilled in the art upon
reference to the detailed description which hereinafter
follows.
SUMMARY OF THE INVENTION
[0008] The present invention provides for the hydroformylation of
olefins utilizing supported diols and chelating bis(phosphorus)
ligands covalently bonded to a support. Preferably, the support is
an insoluble polymer such as a crosslinked polystyrene resin or
other organic polymer resin.
[0009] The supported bis(phosphorus) ligand has the structure (2):
2
[0010] wherein:
[0011] Q is any organic fragment which binds a OPX.sub.2 moiety to
the support (Sup); and
[0012] X is an alkoxy, aryloxy, alkyl, or aryl.
[0013] Preferably, X is aryloxide or aryl.
[0014] The supported catalyst composition has the structure (3):
3
[0015] wherein:
[0016] Q is any organic fragment which binds a OPX.sub.2 moiety to
the support (Sup);
[0017] X is an alkoxy, aryloxy, alkyl or aryl; and
[0018] M is a transition metal capable of carrying out catalytic
transformations.
[0019] X is preferably aryloxide or aryl and M is preferably Ni,
Rh, Co, Ir, Pd, Pt or Ru.
[0020] In particular, the invention provides for a hydroformylation
process comprising reacting an acyclic, monoethylenically
unsaturated compound with CO and H.sub.2 in the presence of a
supported catalyst composition according to formula (3): 4
[0021] wherein:
[0022] Q is any organic fragment which binds a OPX.sub.2 moiety to
the support (Sup);
[0023] X is an alkoxy, aryloxy, alkyl or aryl; and
[0024] M is selected from the group consisting of rhodium and
iridium
[0025] The invention further provides for the hydroformylation of
aromatic olefins comprising reacting an acyclic aromatic olefin
compound with CO and H.sub.2 in the presence of a supported
catalyst composition according to formula (3): 5
[0026] wherein:
[0027] Q is any organic fragment which binds a OPX.sub.2 moiety to
the support (Sup);
[0028] X is an alkoxy, aryloxy, alkyl or aryl; and
[0029] M is rhodium.
[0030] This process may be run in either the liquid or vapor
phase.
[0031] Also disclosed is a process for the preparation of a
supported rhodium bisphosphite hydroformylation catalyst comprising
reacting CO and H.sub.2 with a rhodium compound in the presence of
a supported bis(phosphorus) ligand of formula 1 6
[0032] in which Q is any organic fragment which binds the two
phosphorus moieties to the support and X is alkoxy, aryloxy, alkyl,
or aryl, or alternatively wherein the PX.sub.2 moiety forms a ring
and X.sub.2 is a di(alkoxy), di(aryloxy), di(alkyl), or di(aryl).
In a preferred embodiment, the supported ligand of Formula (1) is
further characterized according to Formula (4) 7
[0033] wherein:
[0034] the linker Q is a 2,2'-dihydroxyl-1,1'-binaphthalene
bridging group;
[0035] the substituents R.sub.7 and R.sub.8 in the 3,3' positions
of the binaphthalene bridging group are selected from alkyl group
containing 2 to carbon atoms, an aryl group, an alkoxy group, an
aryloxy group, a carboalkoxy group, a carboaryloxy group, a nitrile
group, a triarylsilyl group, or trialkylsilyl group;
[0036] at least one of the groups R.sub.7 and R.sub.8 are
covalently attached to a support (Sup);
[0037] X is an alkoxy, aryloxy, alkyl, or aryl, or alternatively
the PX.sub.2 moiety forms a ring and X.sub.2 is a di(alkoxy),
di(aryloxy), di(alkyl), or di(aryl).
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0038] A primary aim of this invention is to provide an improved
hydroformylation reaction utilizing the catalysts covalently
attached to an insoluble support, described in copending commonly
assigned provisional application Ser. No. 60/054,003, filed Jul.
29, 1997. The advantages of this process are:
[0039] These catalysts are insoluble and non-volatile, allowing
ready separation from the reaction medium by filtration or other
means, or use in fixed bed, flow-through reactors using either
liquid or gas phase carrier streams.
[0040] The chelating arrangement of donor atoms gives catalysts
with commercially practical activity and selectivity. In
particular, the chelates described herein are based on bisphosphite
ligands, in which it is known that soluble derivatives give
catalysts with significantly improved reaction rates and
selectivities over monophosphite ligands.
[0041] The chelating arrangement of donor atoms results in a much
stronger ligand-metal interaction and thus greatly minimizes the
potential for metal leaching.
[0042] It is possible to methodically alter the spacing between the
chelating atoms, the steric environment of these atoms, and the
electronic properties of the donor atoms, thereby offering precise
control of ligand coordination properties; this in turn allows
significant opportunity to optimize catalyst performance.
[0043] The chemical environment in the immediate vicinity of the
catalytically active site is uniform throughout the solid support
matrix. The catalyst therefore acts as a "single site" type of
catalyst, as opposed to an ensemble of different catalysts.
[0044] The supported bis(phosphorus) ligands described herein
generally form the catalyst when combined with a catalytically
active metal. The resulting supported catalyst forms a separate
phase from the reaction medium, reacting substrates, and products.
The reaction medium may be composed of a liquid solvent which does
not interfere with the catalytic reaction of interest, or may be
gaseous, e.g., an inert carrier gas and gaseous reactants and
products.
DESCRIPTION OF THE SUPPORT
[0045] Virtually any solid material may be used as a support in the
context of this invention as long as it meets the following
criteria:
[0046] The material is insoluble in organic, aqueous, or inorganic
solvents. Organic polymer supports are acceptable in this regard
but they generally need to be crosslinked. Inorganic supports, such
as metal oxides (silicas, etc.) are generally insoluble in these
solvents and also may be used as supports.
[0047] The support contains reactive sites which can be used for
the covalent attachment of organic fragments containing a diol
group (as described below) or a protected diol group.
[0048] The reactive sites are isolated to prevent additional
crosslinking during further chemical transformations.
[0049] The reactive sites are exposed to the reaction medium. With
a polymer resin support this is achieved through the use of resins
which swell in a reaction solvent or is sufficiently porous to
allow transport of the reaction medium through the polymer
matrix.
[0050] The term "solid support" or "support" (sup) refers to a
material having a rigid or semi-rigid surface which contain or can
be derivatized to contain functionality which covalently links a
compound to the surface thereof. Such materials are well known in
the art and include, by way of example, polystyrene supports,
polyacrylamide supports, polyethyleneglycol supports, metal oxides
such as silica, and the like. Such supports will preferably take
the form of small beads, pellets, disks, or other conventional
forms, although other forms may be used.
[0051] The supports described in this application are
functionalized poly(styrene) resins. Other suitable polymers
include polyolefins, polyacrylates, polymethacrylates, and
copolymers thereof that meet the general criteria described above.
Specifically, poly(styrene) resins commonly used for solid phase
synthesis have been used. These particular resins are crosslinked
with from 1 to 10 wt % divinylbenzene. The styrene moieties are
substituted in the para or meta positions. Only a portion of the
styrene moieties are substituted, typically resulting in functional
group loadings of approximately 0.2 to 2.0 mmole per gram of resin,
although this value may be higher or lower.
DESCRIPTION AND PREPARATION OF SUPPORTED DIOLS
[0052] The aims of this invention are achieved by construction of a
chelating ligand covalently bonded to an insoluble support (Sup),
preferably a polymer support (Pol). The first step of this
procedure involves the preparation of a diol group covalently
attached to an insoluble support as exemplified by the following
structure: 8
[0053] wherein, Sup represents the insoluble support. As used
herein, Q means any organic fragment which binds the diol moiety to
the support. For example, Q may consist of from 2 to 50 carbon
atoms, in addition to heteroatoms such as nitrogen, oxygen, and the
like. Q may additionally contain functional groups such as ether,
acetal, ketal, ester, amide, amine, imine, etc., and combinations
thereof. Q may also contain saturated or unsaturated carbon-carbon
bonds. Q may or may not be symmetrical.
[0054] The number of atoms present in Q and used to separate the
two OH moieties of the diol is generally limited to between 2 and
10, although any number and arrangement which ultimately allows the
formation of a chelating ring is acceptable. A preferred number is
2 to 5 atoms. These atoms may be carbon or heteratoms such as
oxygen and nitrogen. The atoms may further comprise a chain or
cyclic structure, the latter of which may be saturated or
unsaturated, e.g., aromatic.
[0055] The preparation of materials of Formula 1 follows methods
known to those skilled in the art. The procedure may involve one
reaction step or multiple reaction steps. Preferred methods are
those which proceed in high yield, high selectivity, are
inexpensive, and are simple to conduct. For example, Can. J Chem.
1973, 51, 3756, describes the synthesis of the material of formula
SD6. The synthesis occurs in two reaction steps from inexpensive
materials and in high yield. Other materials described in this
invention have not been previously reported in the literature but
follow reaction steps known for soluble, non-polymer supported
analogues. For instance, reaction of the polymer-supported
benzaldehyde pol-CHO, prepared by the method described in J. Polym.
Sci.1975, 13, 1951 and J. Polym. Sci., Polym. Lett. 1965, 3, 505,
with pentaerythritol gives polymer-supported diol SD 1. The
analogous reaction of soluble, non-polymer supported benzaldehyde
with pentaerythritol is described in Org. Syn. Vol 38, 65.
Alternatively, reaction of polymer-supported aldehyde pol-CHO with
diethyl tartrate, followed by reduction, leads to the class of
polymer-supported diols SD2, 3, 4. SD3 is described in J. Org.
Chem., 1997, 62, 3126. The analogous reactions of the soluble,
non-polymer supported compounds are described in Helv. Chim. Acta
1983, 66, 2308 and J. Org. Chem. 1993, 58, 6182. Supported
alkylene-bridged bisaryl alcohols can be prepared by methods found
in J. Chem. Soc., Perkin I, 1980, 1978-1985; Indian J. Chem. 1995,
34B, 6-11, and Chem. Ber. 1985,118, 3588-3619. Other examples may
be prepared by known organic transformations, and representative
structures are shown below. 9
DESCRIPTION AND PREPARATION OF POLYMER-SUPPORTED BIS(PHOSPHORUS)
LIGANDS
[0056] The polymer-supported bis(phosphorus) ligands may be
prepared by a variety of methods known in the art, for example, see
descriptions in WO 93,03839; U.S. Pat. No. 4,769,498 and U.S. Pat.
No. 4,668,651. In general, the transformation involves the reaction
of a phosphorus halide, typically but not limited to chloride, with
the diol to form P--O bonds. The phosphorus halide may be any
compound of the type PY.sub.nX.sub.3-n, where Y=halide, X=alkoxide,
aryloxide, alkyl, aryl, and n=3, 2, or 1. The phosphorus halides
most useful for the present invention are those where Y=Cl;
X=alkoxide, aryloxide, alkyl, or aryl; and n=1. The group X may
contain from 1 to 50 carbon atoms. It may also optionally contain
heteroatoms such as oxygen, nitrogen, halogen, and the like, and
also functional groups such as ethers, alcohols, esters, amides, as
well as others. The groups X may or may not be linked to form a
cyclic structure. The PX.sub.2 moiety may form a ring and X.sub.2
may be a di(alkoxide), di(aryloxide), di(alkyl) or di(aryl). Many
dialkylchlorophosphines and diarylchlorophosphines are commercially
available, or may be prepared by methods known in the art, for
example, J. Am. Chem. Soc. 1994, 116, 9869. Phosphorochloridites,
may be prepared by a variety of methods known in the art, for
example, see descriptions in Polymer 1992, 33, 161; Inorg. Syn.
1966, 8,68; U.S. Pat. No. 5,210,260; Z. Anorg. Allg. Chem.
1986,535, 221. For example, the reaction of 2,2'-biphenol with
phosphorus trichloride gives
1,1'-biphenyl-2,2'-diylphosphorochloridite.
[0057] The reaction of these chlorophosphorus reagents with a
material of Formula 1 in the presence of a base gives a
polymer-supported bis(phosphorus) ligand exemplified by the
structure shown: 10
[0058] where X and Q are as defined above. Other examples may be
prepared by similar transformations, and representative structures
are also shown below. 11
DESCRIPTION AND PREPARATION OF POLYMER-SUPPORTED TRANSITION METAL
CATALYSTS
[0059] The transition metal catalysts which are a subject of this
invention are defined by the formula shown below: 12
[0060] wherein Q and X are as defined above. M is a transition
metal capable of carrying out catalytic transformations. M may
additionally contain labile ligands which are either displaced
during the catalytic reaction, or take an active part in the
catalytic transformation. Any of the transition metals may be
considered in this regard. The preferred metals are those
comprising groups 8, 9, and 10 of the Periodic Table. The preferred
metals for hydroformylation are rhodium, cobalt, iridium, palladium
and platinum, the most preferred being rhodium.
[0061] The zero-valent rhodium compounds, suitable for
hydroformylation, can be prepared or generated according to
techniques well known in the art, as described, for example, WO 95
30680, U.S. Pat. No. 3,907,847, and J. Amer. Chem. Soc., 115, 2066,
1993. Zero-valent rhodium compounds that contain ligands which can
be displaced by the organophosporus ligands are a preferred source
of zero-valent rhodium. Examples of such preferred zero-valent
rhodium compounds are Rh(CO).sub.2 (acetylacetonate) and
Rh(CO).sub.2(C.sub.4H.sub.9COCHCO-t-C.sub.4H.sub.9),
Rh.sub.2O.sub.3, Rh.sub.4(CO).sub.12, Rh.sub.6(CO).sub.16,
Rh(O.sub.2CCH.sub.3).sub.2, and Rh(2-ethylhexanoate). Rhodium
supported on carbon may also be used in this respect.
DESCRIPTION OF CATALYTIC PROCESSES--HYDROFORMYLATION OF
MONOOLEFINIC COMPOUNDS
[0062] The present invention also provides a process for
hydroformylation, comprising reacting an acyclic, monoethylenically
unsaturated compound with a source of CO and H.sub.2 in the
presence of a catalyst composition formed by the supported rhodium
catalysts described previously and depicted by Formula 3.
[0063] Representative ethylenically unsaturated compounds which are
useful in the process of this invention are shown in Formula I, III
or V, and the corresponding terminal aldehyde compounds produced
are illustrated by Formula II, IV or VI, respectively, wherein like
reference characters have same meaning. 13
[0064] wherein
[0065] R.sup.4 is H, CN, CO.sub.2R.sup.5, or perfluoroalkyl;
[0066] y is an integer of 0 to 12;
[0067] x is an integer of 0 to 12 when R.sup.4 is H,
CO.sub.2R.sup.5 or perfluoroalkyl;
[0068] x is an integer of 1 to 12 when R.sup.4 is CN; and
[0069] R.sup.5 is alkyl. 14
[0070] R.sup.6 is an alkyl, aryl, aralkyl, alkaryl, or fused
aromatic group of up to 20 carbon atoms; R.sup.6 may further be
branched or linear; R.sup.6 may also contain heteroatoms such as O,
N, and F.
[0071] The nonconjugated acyclic, aliphatic, monoolefinically
unsaturated starting materials useful in this invention include
unsaturated organic compounds containing from 2 to approximately 30
carbon atoms. The monoolefins propylene, 1-butene, 2-butene, methyl
3-pentenoate, methyl 4-pentenoate, 3-pentenenitrile, and
4-pentenenitrile are especially preferred. As a practical matter,
when the nonconjugated acyclic aliphatic monoethylenically
unsaturated compounds are used in accordance with this invention,
up to about 10% by weight of the monoethylenically unsaturated
compound may be present in the form of a conjugated isomer, which
itself may undergo hydroformylation. As used herein, the term
"pentenenitrile" is intended to be identical with "cyanobutene".
Suitable unsaturated compounds include unsubstituted hydrocarbons
as well as hydrocarbons substituted with groups which do not attack
the catalyst, such as cyano. These unsaturated compounds include
monoethylenically unsaturated compounds containing from 2 to 30
carbons such as ethylene, propylene, butene-1, pentene-2, hexene-2,
etc.; nonconjugated diethylenically unsaturated compounds such as
allene; and substituted compounds such as 3-pentenenitrile,
4-pentenenitrile, methyl pent-3-enoate; and ethylenically
unsaturated compounds having perfluoroalkyl substituents such as,
for example, C.sub.zF.sub.2z+1, where z is an integer of up to 20.
The monoethylenically unsaturated compounds may also be conjugated
to an ester group such as methyl pent-2-enoate.
[0072] Preferred are nonconjugated linear alkenes, nonconjugated
linear alkenenitriles, nonconjugated linear alkenoates, linear
alk-2-enoates and perfluoroalkyl ethylenes. Most preferred
substrates include 3- and 4-pentenenitrile, alkyl 2-, 3-, and
4-pentenoates, and C.sub.zF.sub.2z+1CH.dbd.CH.sub.2 (where z is 1
to 12).
[0073] The preferred products are terminal alkanealdehydes, linear
dialdehyde alkylenes, linear aliphatic aldehyde esters, and
3-(perfluoroalkyl)propioaldehyde. Most preferred products are
n-butyraldehyde, methyl 5-formylvalerate, 2-phenylpropionaldehyde,
and 5-cyanovaleraldehyde.
[0074] The reaction conditions of the hydroformylation process
according to this invention are in general the same as used in a
conventional process, described, for example, in U.S. Pat. No.
4,769,498, which is incorporated herein by reference and will be
dependent on the particular starting ethylenically unsaturated
organic compound. For example, the temperature can be from room
temperature to 200.degree. C., preferably from 50-120.degree. C.
The pressure may vary from atmospheric pressure to 20 MPa,
preferably from 0.15 to 10 MPa and more preferably from 0.2 to 1
MPa. The pressure is, as a rule, equal to the combined hydrogen and
carbon monoxide partial pressure. Extra inert gases may however be
present. The molar ratio of hydrogen to carbon monoxide is
generally between 10 to 1 and 1 to 10, preferably between 6 to 1
and 1 to 2.
[0075] The amount of rhodium compound is not specially limited, but
is optionally selected so that favorable results can be obtained
with respect to catalyst activity and economy. In general, the
concentration of rhodium in the reaction medium is between 10 and
10,000 ppm and more preferably between 50-500 ppm, calculated as
the free metal.
[0076] The molar ratio of multidentate phosphorus ligand to rhodium
is not specially limited, but is optionally selected so that
favorable results can be obtained with respect to catalyst activity
and aldehyde selectivity. This ratio generally is from about 0.5 to
100 and preferably from 1 to 10 (moles of ligand to moles of
metal).
[0077] The choice of solvent is not critical provided the solvent
is not detrimental to catalyst, reactant and product. The solvent
may be a mixture of reactants, such as the starting unsaturated
compound, the aldehyde product and/or by-products. Suitable
solvents include saturated hydrocarbons such as kerosene, mineral
oil or cyclohexane, ethers such as diphenyl ether tetrahydrofuran
or a polyglycol, ketones such as methyl ethyl ketone and
cyclohexanone, nitrites such as methylglutaronitrile and
benzonitrile, aromatics such as toluene, benzene and xylene, esters
such as methyl valerate and caprolactone, dimethylformamide, and
sulfones such as tetramethylenesulfone. The reaction may also be
conducted with reactants and products in the gas phase.
[0078] Preferably, when a liquid reaction medium is used, the
reaction mixture is agitated, such as by stirring or shaking.
[0079] For the vapor phase hydroformylation, the preferred
temperature range is from about 50.degree. C. to about 180.degree.
C., most preferably from 80.degree. C. to 130.degree. C. The
temperature must be chosen so as to maintain all of the reactants
and products in the vapor phase, but low enough to prevent
deterioration of the catalyst. The particular preferred temperature
depends somewhat on the catalyst being used, the olefinic compound
being reacted and the desired reaction rate. The operating pressure
is not particularly critical and can conveniently be from about
101.3 to 1013 kPa. The pressure and temperature combination must be
chosen so that all reactants and products remain in the vapor
phase.
[0080] The supported rhodium catalysts of Formula 3 are typically
loaded into tubular reactors, and a gaseous olefinic compound,
e.g., propylene, CO, and H.sub.2 is passed continuously over the
solid catalysts at temperatures sufficiently high to maintain the
starting materials as well as the reaction products in the vapor
phase.
[0081] Carbon monoxide, H.sub.2 and/or the olefinic starting
materials can be delivered as a neat vapor or as a preheated
solution in a solvent, such as acetonitrile or toluene. Under
atmospheric pressure, using nitrogen or other inert gas as carrier.
Nitrogen is preferred because of its low cost. The reaction
products are liquid at room temperature and are conveniently
recovered by cooling.
EXAMPLES
[0082] The following non-limiting examples further illustrate the
invention. All percentages are by weight, unless otherwise
noted.
Example 1
[0083] 15
[0084] 10.2 g of pentaerythritol was dissolved in the minimum
amount of dimethyl sulfoxide, and then toluene was added until the
solution became slightly cloudy. 18.9 g of the polymer-supported
benzaldehyde resin (prepared by oxidation of Merrifield's resin
commercially available from Aldrich Chemical Co., Milwaukee, Wis.,
or Polymer Laboratories, Ltd., Shropshire, England) and a few
crystals of p-toluenesulfonic acid were then added. The suspension
was brought to reflux and the condensate was passed through a bed
of molecular sieves in a Soxhlet extractor before returning to the
reaction flask. After 12 h the suspension was cooled to room
temperature and the resin was isolated by filtration. After washing
with warm 0.5% aq NaHCO.sub.3, MeOH, and then hexane the resin was
dried under vacuum.
[0085] IR: O--H at 3400 cm.sup.-1; complete loss of C=O at 1701
cm.sup.-1.
[0086] MAS .sup.13C{.sup.1H} NMR (CDCl.sub.3): .delta. 102.7
(acetal carbon); 70.7 (ring OCH.sub.2); 65.3, 63.7 (axial,
equatorial CH.sub.2OH); 39.6 (quaternary carbon), in addition to
polymer backbone and ring resonances.
Example 2
[0087] 16
[0088] 1.0 g of resin-supported diol SD1 was suspended in 15 mL
pyridine. 0.97 g PPh.sub.2Cl was added dropwise with stirring.
After 2.5 days the resin was filtered, washed with 5.times.10 mL
pentane and then dried under vacuum.
[0089] MAS .sup.13C{.sup.1H} NMR (CDCl.sub.3): .delta. 102.7
(acetal carbon); 70.3 (ring OCH.sub.2); 70.0, 68.3 (axial,
equatorial CH.sub.2OP), in addition to polymer backbone and ring
resonances.
[0090] MAS .sup.31P{.sup.1H} NMR (CDCl.sub.3): 114,116 ppm.
Example 3
[0091] 17
[0092] In a manner similar to Example 2, 2.0 g of SD1 was suspended
in 15 mL pyridine. 4.4 g of
1,1'-biphenyl-2,2'-diylphosphorochloridite (50 wt % solution in
toluene) was added dropwise. The resulting slurry was stirred
overnight. The resin was filtered, washed with 2.times.15 mL of
50/50% CH.sub.2Cl.sub.2/pentane, then 3.times.15 mL pentane, and
then dried under vacuum.
Example 4
[0093] 18
[0094] In a manner similar to Example 2, 2.0 g of SD1 was suspended
in 15 mL pyridine, and 44 mL of a 0.2 M solution of
bis(2-isopropyl-5-methylphe- nyl)phosphorochloridite in toluene was
added dropwise. After stirring overnight the resin was filtered,
washed with 3.times.10 mL 50/50 pyridine/pentane, then 2.times.10
mL pentane, and finally dried under vacuum.
[0095] An identical experiment was performed using a 2%
divinylbenzene crosslinked resin support to give supported ligand
SL3-2.
[0096] .sup.31p{1H} (CDCl.sub.3): 134 ppm.
Example 5
[0097] 19
[0098] 8.0 g of polymer-supported benzaldehyde resin (1%
divinylbenzene crosslinked), 3.3 g diethyltartrate, and a few
crystals of p-toluenesulfonic acid were combined in 50 mL toluene.
The mixture was refluxed for 18 h, with the condensed vapors
passing through a bed of molecular sieves before returning to the
reaction flask. The resin was collected by filtration, washed with
acetone (4.times.15 mL), CH.sub.2Cl.sub.2 (4.times.15 mL), hexane
(2.times.15 mL), and CH.sub.2Cl.sub.2 before vacuum drying.
[0099] IR: --CO.sub.2Et at 1730 cm.sup.-1; complete loss of
aldehyde C.dbd.O at 1701 cm.sup.-1.
[0100] An identical experiment was conducted using 2% cross-linked
resin to give a derivatized resin with an identical infrared
spectrum.
Example 6
[0101] 20
[0102] 7.3 g polymer-supported diester of Example 5 was suspended
in 100 mL dry THF and then cooled to 0.degree. C. 11.4 mL of a 3.0
M solution of CH.sub.3MgBr in diethyl ether was added dropwise. The
mixture was warmed to room temperature and then heated to
60.degree. C. After 3.5 h the mixture was cooled to 0.degree. C.
and then quenched with aqueous HCl. The product was collected by
filtration, washed with H.sub.2O (3.times.15 mL), acetone
(3.times.15 mL), and diethyl ether (2.times.15 mL), and finally
vacuum dried.
[0103] IR: O--H at 3400 cm.sup.-1; complete loss of the ester band
at 1730 cm.sup.-1.
[0104] An identical experiment was conducted using 2% cross-linked
resin to give a derivatized resin with an identical infrared
spectrum.
Example 7
[0105] 21
[0106] 5.374 g of supported diol SD2 was suspended in 50 mL toluene
and 15 mL pyridine. 8.04 g
1,1'-biphenyl-2,2'-diylphosphorochloridite (50 wt % soln in
toluene) was added dropwise. The mixture was heated overnight at
60.degree. C. The product was filtered, washed with pyridine
(2.times.15 mL), diethyl ether (3.times.15 mL), and hexane (15 mL)
before vacuum drying.
[0107] IR: complete loss of O--H at 3400 cm.sup.-1.
[0108] .sup.31P NMR(CDCl.sub.3): 153 ppm.
Example 8
[0109] 22
[0110] Resin-supported diol SD2 (5.0 g) was suspended in a
pyridine/toluene (3/1) mixture. 3.82 g
bis(2-isopropyl-5-methylphenyl)pho- sphorochloridite was then added
dropwise with stirring at room temperature. After several hours the
resin was filtered and washed with pyridine (4.times.25 mL),
diethyl ether (2.times.25 mL), and pentane (2.times.25 mL) before
vacuum drying.
[0111] IR: complete loss of O--H band.
Example 9
[0112] 23
[0113] 0.525 g of the resin-supported benzyl alcohol was suspended
in 15 mL THF and then treated with 0.236 g of the
sulfoxyl-protected binaphthol acid chloride shown. The
sulfoxyl-protected binaphthol acid chloride was prepared by
oxidative coupling of 2-naphthol with 2-hydroxy-3-naphthoic acid
followed by treatment with thionyl chloride. These transformations
are well known to those skilled in the art. The mixture was stirred
for 1 day at room temperature and then one day at 45.degree. C. The
reaction was quenched with H.sub.2O/methanol, filtered, and the
resin washed with toluene, acetone, methanol, water, acetone, and
hexane before vacuum drying.
[0114] IR: O--H at 3430 cm.sup.-1, ester C.dbd.O at 1729
cm.sup.-1.
Example 10
[0115] 24
[0116] The resin-supported diol SD5 (1.80 g) was suspended in 15 mL
of THF along with 1 mL of pyridine and 2.70 g of
1,1'-biphenyl-2,2'-diylphosphor- ochloridite (50 wt % solution in
toluene). The mixture was stirred overnight at 50.degree. C. before
filtration. The product was washed with CH.sub.2Cl.sub.2 (3.times.5
mL), THF (3.times.5 mL), toluene (3.times.5 mL), and pentane
(2.times.5 mL), before vacuum drying. IR showed nearly complete
loss of O--H at ca. 3400 cm.sup.-1.
[0117] .sup.31P{.sup.1H} MAS NMR (CDCl.sub.3): broad resonances at
.delta. 144.2 and 137.8, in addition to an unidentified component
at .delta. 12.8.
Example 11
[0118] 25
[0119] This supported diol was prepared by the literature procedure
in Can. J. Chem., 1973, 51, 3756. 18.8 g of Merrifield resin was
suspended in 50 mL of solketal containing 4.70 g of the sodium salt
of solketal. The mixture was stirred overnight at 80.degree. C. The
intermediate ketal was collected by filtration, and then washed
with water (3.times.20 mL), acetone (3.times.20 mL), and hexane
(3.times.20 mL). IR (KBr): C--O--C at 1151, 1211, 1249
cm.sup.-1.
[0120] .sup.13C{.sup.1H} MAS NMR (CDCl.sub.3): .delta. 110.1, 75.5,
74.6, 71.6, 67.7.
[0121] The supported ketal was deprotected by suspension in 200 mL
of dioxane containing a small amount of 10% aq HCl. The mixture was
stirred overnight at room temperature. Workup was accomplished by
filtration and then washing with water, acetone, and THF before
vacuum drying.
[0122] IR: (KBr): Loss of): C--O--C at 1156-1249 cm.sup.-1;
formation of O--H at 3430 cm.sup.-1.
[0123] .sup.13C{.sup.1H} MAS NMR (CDCl.sub.3): .delta. 74.2, 72.2,
71.6, 64.8, in addition to polymer resonances.
Example 12
[0124] 26
[0125] 1.185 g of the supported diol resin SD6 was suspended in 15
mL of THF. 1.8 g of 1,1'-biphenyl-2,2'-diylphosphorochloridite (50
wt % solution in toluene) was added dropwise, followed by 1.0 mL of
pyridine. The resulting mixture was stirred at room temperature for
3 days. The product was isolated by filtration and then washed with
successive portions of CH.sub.3CN, CH.sub.2Cl.sub.2, and pentane.
The product was then vacuum dried.
[0126] IR (KBr): disappearance of O--H at 3430 cm.sup.-1.
[0127] .sup.31P{.sup.1H} MAS NMR (CDCl.sub.3): .delta. 144.4,
138.3, in addition to minor components between 6 25-7.
Example 13
[0128] 27
[0129] 1.40 g of the resin-supported diol SD6 was suspended in 15
mL of THF and then treated with 0.75 g
1,2-phenylenephosphorochloridite and 1 mL of pyridine. The
resulting mixture was stirred for three days at room temperature.
The product was filtered, washed with CH.sub.2Cl.sub.2, toluene,
and pentane, and then dried under vacuum.
[0130] IR (KBr): disappearance of O--H at 3430 cm.sup.-1.
[0131] .sup.31P{.sup.1H} MAS NMR (CDCl.sub.3): .delta.
144.2,138.2.
Example 14
[0132] 28
[0133] 1.40 g of supported diol resin SD6 was suspended in 15 mL of
THF and then treated with 1.53 g of
bis(2-isopropyl-5-methylphenyl)phosphoroc- hloridite (as a toluene
solution) and 1 mL of pyridine. The mixture was stirred for 3 days
at room temperature. The product was filtered, washed with
CH.sub.2Cl.sub.2, CH.sub.3CN, and pentane before vacuum drying.
[0134] IR (KBr): disappearance of O--H at 3430 cm.sup.-1.
[0135] .sup.31P{.sup.1H} MAS NMR (CDCl.sub.3): .delta. 131.0,
128.6, in addition to several minor components in the ranges 6
134-127 and 6 25-0.
[0136] Elemental analysis: 81.44% C, 7.83% H, 3.09% P.
Example 15
[0137] 29
Example 15-1, x=3, Supported Diol SD7
[0138] 2.33 g of the binaphthol ester shown (x=3) was dissolved in
DMF. 0.39 g (2.7 equiv) of NaH was added to give gas evolution and
an orange solution. After 20 min at room temperature the solution
was treated with 4.0 g of Merrifield's resin (4.8 mmol CH.sub.2Cl).
The mixture was stirred overnight at 98.degree. C. The resulting
resin was isolated by filtration and then washed with 95% EtOH,
acetone, THF, toluene, and hexane before drying under vacuum.
[0139] IR (KBr, cm.sup.-1): 3441 and 3223 (O--H), 1685 (C O).
Example 15-2, X=4, Supported Diol SD8
[0140] In a similar manner, 5.83 g of the binaphthol monoester
(x=4), 0.94 g NaH, and 9.6 g of Merrifield's resin were reacted in
30 mL of DMF. After heating at 80.degree. C. overnight the resin
was isolated and rinsed by the method described above.
[0141] IR (KBr, cm.sup.-1): 3583, 3419 and 3223 (O--H), 1674
(C.dbd.O).
Example 15-3, x=2, Supported Diol SD9
[0142] This resin was prepared and isolated similarly from 1.20 g
of the binaphthol monoester (x=2), 0.22 g of NaH, and 2.4 g of
Merrifield's resin.
[0143] IR (KBr, cm.sup.-1): 3451, 1690 (C.dbd.O).
Example 16
[0144] 30
[0145] The following is a general example for the synthesis of this
class of supported bis(phosphite) ligands and catalysts. Examples
of supported ligands and catalysts prepared by this generic route
are provided in Table 1.
Example 16-1. x=4, X.sub.2=1,1'-biphenoxy
[0146] The binaphthol-supported resin SD8 from Example 15-2 (2.0 g)
was suspended in 10 mL of THF; 3 mL of pyridine and 2.5 g of a 50
wt % solution of 1,1'-biphenyl-2,2'-diylphosphorochloridite in
toluene were then added. The yellow resin decolorized immediately.
The mixture was stirred overnight at room temperature and then
worked up by filtration and washing the resin with pyridine, THF,
and pentane. The light yellow supported ligand SL17 was dried under
vacuum.
1TABLE 1 Example x X2 Supported Ligand Code 18-2 x = 3
1,1'-biphenoxy SL18 18-3 x = 3 1,2-phenylenedioxy SL19 18-4 x = 4
1,2-phenylenedioxy SL20
Example 17
[0147] 31
[0148] The sulfoxyl-protected binaphthol acid chloride shown in
Example 30 (5.9 g, 15 mmol) was dissolved in 150 mL of dry DMF. The
commercially available benzyl amine resin (6.1 g, 6 mmol) and then
diisopropyl ethyl amine (DIEA) (26 mL, 150 mmol) were added. The
mixture was agitated on a Rotovap over night with exclusion of air.
Water (4 mL, 220 mmol) was added to the reaction mixture and the
suspension was rotated for another 3 h. The resin was filtered,
washed with DMF thoroughly, then with CH.sub.2Cl.sub.2 and hexanes
before vacuum drying. IR(KBr): OH and NH at 3422 cm.sup.-1 (br) and
3535 cm.sup.-1 (shoulder), amide at 1652 cm.sup.-1.
Example 18
[0149] 32
[0150] DIEA (1.7 ml, 10 mmol) was added to the suspension
containing the resin-supported diol SD10 (1.33 g,1.0 mmol), 2.0 g
(4.0 mmol) of 1,1'-biphenyl-2,2'-diylphosphorochloridite (50%
weight in toluene) and 10 ml of dry toluene. The resulting mixture
was vortexed at room temperature overnight. The brown product was
filtered, washed with toluene, DMF, CH.sub.2Cl.sub.2, hexanes and
vacuum dried to lead to a fluffy solid.
[0151] IR(KBr): NH at 3433 cm.sup.-1 (m), amide at 1659
cm.sup.-1(s)
[0152] Elemental Analysis: C% 83.27, H% 6.61, N% 1.06, P% 2.12
Example 19
[0153] 33
[0154] This ligand was prepared according to the same procedure as
that of Example 18 using 1.46 g (4.0 mmol) of
bis(2-isopropyl-5-methylphenyl)phos- phorochloridite.
[0155] IR (KBr): NH at 3431 cm.sup.-1 (m), amide at 1666 cm.sup.-1
(s).
[0156] Elemental Analysis: C% 84.01, H% 7.07, N% 1.25, P% 1.53
Example 20
[0157] 34
[0158] This product was synthesized following the procedure
described for Example 18 using 1.34 g of
bis(2-isopropylphenyl)phosphorochloridite and the same amounts of
the resin, DIEA and toluene.
[0159] IR (KBr): NH at 3432 cm.sup.-1 (s), amide at 1656 cm.sup.-1
(s)
[0160] Elemental Analysis: C% 83.25, H% 6.97, N% 1.30, P% 1.56
Example 21
[0161] 35
[0162] The same procedure described for Example 18 was followed
using 0.718 ml (4 mmol) of chlorodiphenylphosphine.
[0163] IR (KBr): NH at 3422 cm.sup.-1 (s), amide at 1656 cm.sup.-1
(s)
[0164] Elemental Analysis: C% 85.94, H% 6.57, N% 1.28, P% 2.01
Example 22
[0165] 36
[0166] This ligand was synthesized according to the same procedure
as that for Example 18 using 698 mg (4.0 mmol) of
1,2-phenylenephosphorochloridit- e.
[0167] IR (KBr): NH at 3437 cm.sup.-1 (m), amide at 1667 cm.sup.-1
(s)
[0168] Elemental Analysis: C% 82.24, H% 6.26, N% 1.19, P% 2.54
Example 23
[0169] 37
[0170] The same procedure described in Example 44 was employed with
10 g (6.9 mmol) of commercially available Wang resin, 8.2 g (20.7
mmol) of the sulfoxyl-protected binaphthol acid chloride shown in
Example 30, and 36 ml of DIEA.
[0171] IR (KBr): OH at 3443 cm.sup.-1 (br) ester at 1678 cm.sup.-1
(s)
Example 24
[0172] 38
[0173] This product was obtained following the same procedure
described for Example 18 using 2.17 g (1.0 mmol) of resin-supported
diol SD11, 2 g of 1,1'-biphenyl-2,2'-diylphosphorochloridite (50%
weight in toluene, 4.0 mmol), 1.7 ml (10 mmol) of DIEA and 15 ml of
anhydrous toluene.
[0174] IR (KBr): 1743 cm.sup.-1 (vs), 1680 cm.sup.-1 (m).
[0175] Elemental Analysis: C% 86.34, H% 7.00, P% 0.77
Example 25
[0176] 39
[0177] This compound was made according to the procedure described
for Example 18 using 2.17 g (1.0 mmol) ofsupported diol SD11, 884
mg (4.0 mmol) of the chlorodiphenylphosphine, 1.7 ml (10 mmol) and
15 ml of toluene.
[0178] IR (KBr): 1744 cm.sup.-1 (m), 1680 cm.sup.-1 (s)
[0179] Elemental Analysis: C% 86.55, H% 6.85, P% 0.59
Example 26
[0180] 40
[0181] The same procedure described for Example 18 was followed
using 2.17 g (1.0 mmol) of the resin SD11, 1.46 g (4.0 mmol) of
bis(2-isopropyl-5-methylphenyl)phosphorochloridite, 1.7 ml (10
mmol) of DIEA and 15 ml of toluene.
[0182] IR (KBr): 1744 cm.sup.-1 (vs), 1680 cm.sup.-1 (m)
[0183] Elemental Analysis: C% 85.49, H% 7.04, P% 0.64
Example 27
[0184] 41
[0185] The same procedure described for Example 18 was followed
using 2.17 g (1.0 mmol) of supported diol SD11, 1.34 g (4.0 mmol)
of bis(2-isopropylphenyl)phosphorochloridite, 1.7 ml (10 mmol) of
DIEA and 15 ml of toluene.
[0186] IR (KBr): 1722 cm.sup.-1 (w), 1678 cm.sup.-1 (m)
[0187] Elemental Analysis: C% 86.51, H% 7.12, P% 0.42
Example 28
[0188] 42
[0189] This ligand was made following same procedure described for
Example 18 from 2.17 g (1.0 mmol) of the supported diol SD11, 1.41
g (4.0 mmol) of bis(1-naphthyl)phosphorochloridite, 1.7 ml (10
mmol) of DIEA and 14 ml of toluene.
[0190] IR (KBr): 1726 cm.sup.-1 (m), 1674 cm.sup.-1 (w)
[0191] Elemental Analysis: C% 84.97, H% 8.23, P% 0.55
Example 29
[0192] 43
[0193] The same procedure described for Example 18 was followed
using 2.17 g (1.0 mmol) of the resin-supported diol SD11, 884 mg
(4.0 mmol) of 1,2-phenylenephosphorochloridite, 1.7 ml (10 mmol) of
DIEA and 14 ml of toluene.
[0194] IR (KBr): 1726 cm.sup.-1 (m), 1674 cm.sup.-1 (w)
[0195] Elemental Analysis: C% 85.35, H% 6.57, P% 0.51
Example 30
[0196] 44
[0197] The ligand was prepared following the same procedure
described for Example 18 using 1.17 g (1.0 mmol) of supported diol
SD5, 2 g (50% weight in toluene) (4.0 mmol) of
1,1'-biphenyl-2,2'-diylphosphorochloridite, 1.7 ml (10 mmol) of
DIEA and 10 ml of toluene.
[0198] IR (KBr): 1742 cm.sup.-1 (vs), 1680 cm.sup.-1 (m)
[0199] Elemental Analysis: C% 84.69, H% 6.51, P% 1.03
Example 31
[0200] 45
[0201] The same procedure described for Example 18 was followed
using 1.17 g (1.0 mmol) of supported diol SD5, 884 mg (4.0 mmol) of
ClPPh.sub.2, 1.7 ml (10 mmol) of DIEA and 10 ml of toluene.
[0202] IR (KBr): 1741 cm.sup.-1 (vs)
[0203] Elemental Analysis: C% 85.45, H% 6.74, P% 1.14
Example 32
[0204] 46
[0205] This product was synthesized according to the same procedure
as that for Example 18 was from 2.35 g (2.0 mmol) of the resin
supported diol SD5, 2.91 g (8.0 mmol) of
bis(2-isopropyl-5-methylphenyl)phosphoroch- loridite, 3.4 ml (10
mmol) of DIEA and 20 ml of toluene.
[0206] IR (KBr): 1741 cm.sup.-1 (vs), 1684 cm.sup.-1 (w)
[0207] Elemental Analysis: C% 84.62, H% 6.92, P% 0.79
Example 33
[0208] 47
[0209] The resin-supported benzaldehyde described in Example 1 (407
mg, 0.5 mmol), 2-naphthol (576 mg, 2 mmol), glacial acetic acid (5
ml), CHCL.sub.3 (1 ml) and hydrochloric acid (0.5 ml) were mixed
with a vortexer for 5 days. The product was filtered, washed with
aqueous THF, and then THF thoroughly before vacuum drying.
Example 34
[0210] 48
[0211] The same procedure described for Example 18 was followed
using 2.17 g (2.0 mmol) of supported diol SD13, 2.91 g (8.0 mmol)
of bis(2-isopropyl-5-methylphenyl)phosphorochloridite, 3.4 ml (10
mmol) of DIEA and 10 ml of toluene.
[0212] Elemental Analysis: C% 90.40, H% 7.26, P% 0.61
Example 35
[0213] 49
[0214] The same procedure described for Example 18 was followed
using 2.17 g (2.0 mmol) of the resin SD13, 2.69 g (8.0 mmol) of
bis(2-isopropylphenyl)phosphorochloridite, 3.4 ml (10 mmol) of DIEA
and 10 ml of toluene.
[0215] Elemental Analysis: C% 90.10, H% 7.15, P% 0.48
Example 36
[0216] 50
[0217] The ligand was prepared according to the procedure described
for Example 18 from 2.17 g (2.0 mmol) of resin SD13, 2 g of
1,1'-biphenyl-2,2'-diylphosphorochloridite (50 wt % solution in
toluene, 8.0 mmol), 3.4 ml (10 mmol) of DIEA, and 20 ml of
toluene.
[0218] Elemental Analysis: C% 90.28, H% 6.97, P% 0.54
Example 37
[0219] 51
[0220] The same procedure described for Example 18 was followed
using 1.09 g (1.0 mmol) of resin SD13, 0.7 g (4.0 mmol) of
1,2-phenylenephosphorochl- oridite, 1.7 ml (10 mmol) of DIEA, and
10 ml of toluene.
[0221] Elemental Analysis: C% 89.82, H% 6.35, P% 1.19
Example 38
[0222] 52
[0223] This product was obtained according to the same procedure
described for Example 18 using 2.17 g (2.0 mmol) of resin SD13,
1.77 g (8.0 mmol) of PPh.sub.2Cl, 3.4 ml (10 mmol) of DIEA, and 10
ml of toluene.
[0224] Elemental Analysis: C% 89.90, H% 7.46, P% 0.81
Example 39
[0225] 53
[0226] The same procedure described for Example 18 was followed
using 2.17 g (2.0 mmol) of resin SD13, 2.82 g (8.0 mmol) of
bis(1-naphthyl)phosphoro- chloridite, 3.4 ml (10 mmol) of DIEA, and
20 ml of toluene.
[0227] Elemental Analysis: C% 90.34, H% 7.38, P% 0.43
Example 40
[0228] 54
[0229] The same procedure described for Example 18 was followed
using 1.79 g (1.35 mmol) of supported diol resin SD10, 1.9 g (5.4
mmol) of bis(1-naphthyl)phosphorochloridite, 2.3 ml (10 mmol) of
DIEA, and 15 ml of toluene.
[0230] IR (KBr): NH at 3436 cm.sup.-1 (m), amide at 1668 cm.sup.-1
(s)
[0231] Elemental Analysis: C% 83.99, H% 6.65, N% 1.22, P% 1.60
Example 41
[0232] 55
[0233] The same procedure described for Example 18 was followed
using 2.35 g (2.0 mmol) of the supported diol resin SD5, 2.69 g
(8.0 mmol) of bis(2-isopropylphenyl)phosphorochloridite, 3.4 ml (10
mmol) of DIEA, and 20 ml of toluene.
[0234] IR (KBr): 1738 cm.sup.-1 (s), 1676 cm.sup.-1 (s)
[0235] Elemental Analysis: C% 83.78, H% 6.49, P% 1.00
Example 42
[0236] 56
[0237] The same procedure described for Example 18 was followed
using 2.35 g (2.0 mmol) of resin SD5, 2.69 g (8.0 mmol) of
1,2-phenylenephosphorochl- oridite, 3.4 ml (10 mmol) of DIEA and 20
ml of toluene.
[0238] IR (KBr): 1739 cm.sup.-1 (s), 1656 cm.sup.-1 (s)
[0239] Elemental Analysis: C% 83.00, H% 6.26, P% 1.70
Example 43
[0240] 57
[0241] The same procedure described for Example 18 was followed
using 2.35 g (2.0 mmol) of resin SD5, 2.82 g (8.0 mmol) of
bis(1-naphthyl)phosphoroc- hloridite, 3.4 ml (10 mmol) of DIEA, and
20 ml of toluene.
[0242] IR (KBr): 1739 cm.sup.-1 (vs), 1681 cm.sup.-1 (m)
[0243] Elemental Analysis: C% 84.38, H% 6.94, P% 1.25
Example 44
[0244] 58
[0245] This supported bis(phosphite) was prepared following the
same procedure described in Example 12 using
bis(1-naphthyl)phosphorochloridit- e and supported diol SD6.
[0246] Elemental Analysis: C% 85.81, 85.99; H% 7.16; 7.39; P%
0.96
Example 45
Supported Diol SD14
[0247] 2,4-Dimethylphenol (6.95 ml, 57.6 mmol) and the
resin-supported benzaldehyde described in Example 1 (5.85 g, 7.2
mmol) were added to an ice cold aqueous sulfuric acid solution
(H.sub.2SO.sub.4: 15 ml; H.sub.2O 12 ml). The reaction mixture was
shaken until no starting material was observed in the IR spectrum
(several days). The resin was collected by filtration, washed with
aqueous acetone, aqueous THF, and thoroughly with THF before vacuum
drying. IR (KBr): OH at 3444 cm.sup.-1 (br, s).
Example 46
[0248] 59
[0249] This ligand was prepared according to the procedure
described for Example 18 using 1.5 g (3.15 mmol) of supported diol
SD14, 6.3 g (50% weight in toluene, 12.6 mmol) of
1,1'-biphenyl-2,2'-diylphosphorochloridi- te, 5.5 ml of DIEA and 15
ml of anhydrous toluene.
[0250] Elemental Analysis: C% 85.33, H% 7.11, P% 1.94
Example 47
[0251] 60
[0252] This supported ligand was prepared according to the
procedure described for Example 18 using 1.5 g (3.15 mmol) of
supported diol SD14, 4.2 g (12.6 mmol) of
bis(2-isopropylphenyl)phosphorochloridite, 5.5 ml of DIEA, and 15
ml of anhydrous toluene.
[0253] Elemental Analysis: C% 85.80, H% 7.67, P% 2.56
Example 48
[0254] 61
[0255] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of resin SD14, 4.4
g (12.6 mmol) of bis(1-naphthyl)phosphorochloridite, 5.5 ml of DIEA
and 15 ml of anhydrous toluene.
[0256] Elemental Analysis: C% 85.94, H% 7.25, P% 1.91
Example 49
[0257] 62
[0258] This supported ligand was prepared according to the
procedure described in Example 18 using 1.5 g (3.15 mmol) of resin
SD14, 2.8 g (12.6 mmol) of ClPPh.sub.2, 5.5 ml of DIEA and 15 ml of
anhydrous toluene.
[0259] Elemental Analysis: C% 87.65, H% 7.57, P% 2.17
Example 50
[0260] 63
[0261] This supported ligand was prepared according to the
procedure described in Example 18 using 1.5 g (3.15 mmol) of
supported diol SD14, 2.2 g (12.6 mmol) of
1,2-phenylenephosphorochloridite, 5.5 ml of DIEA, and 15 ml of
anhydrous toluene.
[0262] Elemental Analysis: C% 84.16, H% 7.24, P% 2.41
Example 51
[0263] 64
[0264] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of the resin, 3.88
g (12.6 mmol) of bis(2-ethylphenyl)phosphorochloridite, 5.5 ml of
DIEA and 15 ml of anhydrous toluene.
[0265] Elemental Analysis: C% 84.45, H% 7.09, P% 3.09
Example 52
[0266] 65
[0267] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of the supported
diol SD14, 3.88 g (12.6 mmol) of
bis(2,3-dimethylphenyl)phosphorochloridite, 5.5 ml of DIEA, and 15
ml of anhydrous toluene.
[0268] Elemental Analysis: C% 84.97, H% 7.16, P% 2.98
Example 53
[0269] 66
[0270] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of the resin SD14,
4.23 g (12.6 mmol) of
bis(2,3,5-trimethylphenyl)phosphorochloridite, 5.5 ml of DIEA, and
15 ml of anhydrous toluene.
[0271] Elemental Analysis: C% 84.65, H% 7.62, P% 2.70
Example 54
[0272] 67
[0273] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of the resin SD14,
4.60 g (12.6 mmol) of bis(2-tertbutylphenyl)phosphorochloridite,
5.5 ml of DIEA and 15 ml of anhydrous toluene.
[0274] Elemental Analysis: C% 85.83, H% 7.68, P% 2.40
Example 55
[0275] 68
[0276] This ligand was prepared according to the procedure
described in Example 18 using 1.5 g (3.15 mmol) of the resin SD14,
4.95 g (12.6 mmol) of the corresponding
bis(2-tertbutyl-4-methylphenyl)phosphorochloridite, 5.5 ml of DIEA
and 15 ml of anhydrous toluene.
[0277] Elemental Analysis: C% 86.19, H% 7.80, P% 2.19
Example 56
[0278] The following is a general procedure for the preparation of
supported rhodium catalysts using the supported ligands described
in previous examples. Information in Table 2 shows the generality
of this procedure.
[0279] The appropriate supported ligand (a amount corresponding to
0.116-0.0116 mmole of contained bis(phosphite) groups) is slurried
into 5 mL of dry, deoxygenated toluene. Rh(CO).sub.2(acac) (3
mg,0.0116 mmol, P/Rh=2-20) is added and gas evolution is noted as
CO is displaced. The toluene supernatant turns colorless as the
Rh(CO).sub.2(acac) becomes loaded onto the support beads. The
reuslting slurry is useful as obtained for catalytic reactions.
[0280] On the Table below I have simply listed all the ligands
which correlated with Leo Manzer's hydroformylation examples, so
that appropriate info on the prep of each rhodium ligand can be
placed thereon.
2TABLE 2 Supported Rh(CO).sub.2(acac) Catalysts Prepared via
Example 54 Example Supported Ligand Used Supported Catalyst ID 56-1
SL2 SC1 56-2 SL3 SC2 56-3 SL6 SC3 56-4 SL12 SC4 56-5 SL14 SC5 56-6
SL15 SC6 56-7 SL16 SC7 56-8 SL17 SC8 56-9 SL18 SC9 56-10 SL19 SC10
56-11 SL20 SC11 56-12 SL23 SC12 56-13 SL24 SC13 56-14 SL25 SC14
56-15 SL26 SC15 56-16 SL27 SC16 56-17 SL28 SC17 56-18 SL29 SC18
56-19 SL3O SC19 56-20 SL31 SC20 56-21 SL32 SC21 56-22 SL33 SC22
56-23 SL34 SC23 56-24 SL35 SC24 56-25 SL36 SC25 56-26 SL37 SC26
56-27 SL38 SC27 56-28 SL39 SC28 56-29 SL40 SC29 56-30 SL41 SC30
56-31 SL42 SC31 56-32 SL43 SC32 56-33 SL44 SC33 56-34 SL45 SC34
56-35 SL46 SC35 56-36 SL48 SC36 56-37 SL51 SC37 56-38 SL52 SC38
56-39 SL54 SC39 56-40 SL55 SC40 56-41 SL56 SC41 56-42 SL57 SC42
56-43 SL58 SC43 56-44 SL59 SC44 56-45 SL60 SC45 56-46 SL61 SC46
acac = acetylacetonate
Example 57
Propylene Hydroformylation with Supported Rhodium Catalysts
[0281] The resin supported ligand and Rhodium were charged as the
Rh(CO).sub.2(acac) loaded material, prepared as described in
Example 56. The amount of Rh(CO).sub.2acac added was 3 mg. The
amount of supported ligand charged was targeted at a 1:1 of chelate
ligand to rhodium. The reactor vessel was charged to 100 psi
(6.89.times.10.sup.+5 Pa) with 40 psi (2.75.times.10.sup.+5 Pa) of
propylene and 60 psi (4.13.times.10.sup.+5 Pa) of a 1:1 ratio of
H.sub.2 to CO. Typically the reaction was run for 1 hour. At the
end of the run the reactor is depressurized and an aliquot of
dibutylether is added as an internal standard. The liquid is
analyzed by gas chromatography to give the yields of products. As
used below in Table 3, Comparative examples are designated by
letters and Ph.sub.3P=triphenyl phosphite, and DD1= 69
[0282] i-BA or IBA=isobutyraldehyde
[0283] n-BAL or BAL=normal butyraldehyde
[0284] TON=Turnovers, i.e. moles of product/moles of
rhodium/hour
3TABLE 3 Propylene Hydroformylation Ex- Cata- i-BA Sel, n-BAL TON
ample Ligand lyst % sel % (IBA + BAL) A
Ph.sub.2P(CH.sub.2).sub.2PPh.sub.2 56.3 43.7 6.7 B DP1 19.6 80.4
3711.4 C DP1 5.2 94.8 2586.5 D DP1 14.9 85.1 1770.4 E DP1 2.8 97.2
130.8 F Ph.sub.3P 39.7 60.3 397.1 G Ph.sub.3P 48.2 51.8 292.4 H
Ph.sub.3P 46.3 53.7 2.4 57-1 SL55 SC40 63.5 36.5 75.4 57-2 SL54
SC39 21.4 78.6 433.6 57-3 SL43 SC32 15.8 84.2 1082.7 57-4 SL61 SC46
53.7 46.3 100.7 57-5 SL60 SC45 59.6 40.4 71.7 57-6 SL59 SC44 62.2
37.8 102.5 57-7 SL58 SC43 36.2 63.8 203.7 57-8 SL58 SC43 49.7 50.3
90.6 57-9 SL57 SC42 39.0 61.0 153.0 57-10 SL57 SC42 42.7 57.3 129.6
57-11 SL52 SC38 74.7 25.3 69.4 57-12 SL51 SC37 68.1 31.9 126.6
57-13 SL56 SC41 42.6 57.4 560.5 57-14 SL43 SC32 40.5 59.5 1058.7
57-15 SL45 SC34 30.4 69.6 984.6 57-16 SL44 SC33 58.1 41.9 322.7
57-17 SL41 SC30 33.2 66.8 481.9 57-18 SL40 SC29 62.3 37.7 114.7
57-19 SL39 SC28 54.4 45.6 952.1 57-20 SL37 SC26 19.1 80.9 1206.6
57-21 SL38 SC27 31.9 68.1 1604.2 57-22 SL36 SC25 20.4 79.6 2158.7
57-23 SL35 SC24 28.1 71.9 1066.7 57-24 SL34 SC23 72.0 28.0 20.8
57-25 SL28 SC17 69.0 31.0 13.1 57-26 SL31 SC20 50.4 49.6 42.8 57-27
SL30 SC19 61.3 38.7 30.4 57-28 SL29 SC18 60.0 40.0 45.0 57-29 SL33
SC22 18.6 81.4 225.2 57-30 SL32 SC21 49.5 50.5 51.7 57-31 SL25 SC14
54.0 46.0 10.9 57-32 SL24 SC13 52.5 47.5 7.5 57-33 SL27 SC16 98.1
1.9 16.5 57-34 SL26 SC15 100.0 0.0 15.1 57-35 SL23 SC12 100.0 0.0
11.3 57-36 SL42 SC31 50.6 49.4 153.2 57-37 SL46 SC35 44.3 55.7
283.8 57-38 SL48 SC36 45.1 54.9 129.7 57-39 SL16 SC7 31.3 68.7
2080.2 57-40 SL14 SC5 52.2 47.8 3.6 57-41 SL20 SC11 46.4 53.6 98.8
57-42 SL19 SC10 64.5 35.5 72.1 57-43 SL17 SC8 33.5 66.5 387.1 57-44
SL18 SC9 55.0 45.0 57.9 57-56 SL6 SC3 36.5 63.5 111.4 SL3 SL3 SC2
26.9 73.1 264.8 57-58 SL2 SC1 34.2 65.8 131.6 57-59 SL15 SC6 56.8
43.2 8.3 57-60 SL12 SC4 7.9 92.1 1450.3
Example 58
Propylene Hydroformylation--Vapor Phase
[0285] An empty 0.64 cm diameter, 37.5 cm long stainless steel
tubular reactor was placed in a nitrogen-filled glove box. A plug
of glass wool was placed in the bottom end of the reactor, followed
by the amount and type of catalyst shown in Table 4. The catalyst
in each case was pre-mixed with glass beads to dilute it within the
reactor. A thermocouple was inserted into the top of the reactor.
Both ends of the reactor were sealed with metal fittings, and the
reactor was removed from the glove box and was connected to
stainless steel reactor feed lines purged with nitrogen. The
reactor was equipped with a by-pass line to allow for a flow of CO
and H.sub.2 to be established before opening the inlet side of the
reactor to feed gases. The desired temperature of 100.degree. C.
was established in the reactor by means of a split tube furnace
surrounding the reactor. When the desired flow rates of CO and
H.sub.2 feed gases had been achieved, a valve was turned on to
begin passing CO and H.sub.2 over the catalyst. Periodically, at
times shown in Table 4. The reactor effluent samples were analyzed
by gas chromatography for the amounts of unreacted propylene,
linear and branched buyraldehyde.
[0286] Examples 58-1 to 58-6 were all run at 100.degree. C., with
feeds of 4 cc each of CO, H.sub.2 and propylene, except as noted,
and at a total pressure of 100 psig. Table 4 shows the grams of
catalyst and the weight percent of phosphorus in each catalyst
used. The mole ratios of Rh/P shown in Table 4 are the ratios used
to complex Rh to each catalyst from a solution of
Rh(acetonylacetonate) (CO).sub.2, before several rinsing times with
toluene to remove uncomplexed Rh. Final Rh/P ratios should have
been close to 0.5. The TON/hr numbers shown in Table 4 were
calculated to represent the moles of propylene reacted per mole of
Rh per hour. Example 58-6 was run using DPI dispersed on
carbon.
4TABLE 4 Gas Phase Propylene CO/H2 Reactions Catalyst Silica
Propylene/CO/H2 Elapsed Propylene Linear/ Ex. No. Ligand g, % P,
Rh/P Beads, g cc/min. Time, hr. % Conv. Branched TON/hr 58-1 SL24
0.25, 1.52, 1.26 0.27 4/4/04 1 5.1 1.5 3.5 4 7.1 3.1 4.9 10 10.8
2.5 7.5 16 7.9 3.0 5.5 21 9.4 3.4 6.5 24 8.6 3.8 5.9 58-2 SL25
0.25, 1.56, 1.22 0.53 4/4/04 1 7.3 2.0 5.1 4 8.2 2.5 5.7 10 7.8 2.6
5.5 16 8.7 3.3 6.1 21 5.2 3.8 3.6 23 4.6 4.1 3.2 58-3 SL52 0.28,
2.56, 0.88 0.50 4/4/04 1 9.7 3.0 6.1 10 20.6 4.5 13.0 20 70.0 8.4
44.1 29 52.9 9.5 33.4 41 64.4 10.0 40.6 50 68.8 9.8 43.4 59 72.6
9.9 45.8 71 77.3 10.3 48.7 82 81.0 12.5 51.0 91 78.7 10.6 49.6 100
79.0 10.5 49.8 109 79.7 10.8 50.2 118 71.5 10.0 45.1 58-5 SL51
0.21, 1.94, 0.81 0.51 4/4/04 1 1.6 2.0 2.0 10 12.9 2.6 15.6 19 15.3
3.3 18.5 31 12.1 3.2 14.7 40 13.7 3.3 16.6 49 12.2 3.3 14.7 61 14.0
3.3 16.9 70 12.7 3.4 15.4 79 12.5 3.4 15.1 91 14.7 3.4 17.8 100
14.9 3.5 18.0 109 15.6 3.5 18.9 121 16.3 3.5 19.8 127 13.2 3.5 16.0
58-6 DP1 0.10, 0.33, 0.26 0.50 4/4/04 1 21.1 20.6 795 2 20.4 23.1
768 3 17.4 24.5 653 4 16.3 24.7 613 5 14.7 24.9 553 6 14.4 24.7 541
9 15.0 24.6 564 12 12.1 24.3 457 15 10.0 24.3 376 18 9.5 24.3 356
21 7.2 24.2 272 24 8.1 24.2 306
Example 59
Preparation of a Supported Disubstituted Binaphthol
[0287] 70
[0288] A mixture of 50 g (60 mmol) of Merrifield resin
(polCH.sub.2Cl) 2,2'-dihydroxy-1,1'-binaphthalene-3,3'-dicarboxylic
acid (33.7 g), potassium carbonate (12.4 g) and DMF (350 ml) was
heated at 90.degree. C. with stirring for 8 hrs. The color of the
resin changed from white to green-yellow. The mixture was diluted
with water, filtered, washed with H.sub.2O, DMF, and acetone, and
then thoroughly dried in the air to give the desired product. IR
(KBr, cm.sup.-1): 1712 (vs), 1676 (vs).
[0289] Enablement references for this synthesis:
[0290] 1. Hetet, C. L., David, M., Carreaux, F., Carboni, B. and
Sauleau, A., Tetrahedron Lett., 1997, 38(29), 5153-5156.
[0291] 2. Gisin, B. F. Helv. Chim. Acta 1973, 56, 1476-1482. 71
[0292] Preparation of Supported Diols SD15 and SD16. Supported diol
SD14 (5 g) was swollen in 50 ml of anhydrous DMF.
1,1'-Carbonyldiimidazole (689 mg) was added. The mixture was shaken
overnight. The resin was filtered, and washed with DMF (3.times.)
to give diol SD15. IR (KBr, cm.sup.-1): 1772 (s), 1720 (s). Next,
DMF (25 ml) and i-PrOH (1.6 ml) were added. The mixture was shaken
overnight, then filtered, washed with DMF (3.times.), acetone
(3.times.) and dried in the air to give supported diol SD16, which
is the desired supported unsymmetrical diester diol. IR (KBr,
cm.sup.-1): 1762 (s), 1713 (vs), 1676 (vs).
[0293] Enablement reference:
[0294] Bodanszky, M., Bodanszky, A. in "The Practice of Peptide
Synthesis" Springer-Verlag, Berlin Heidelberg, 1994, p. 122.
Example 60
Preparation of a Supported Bis(Phosphite) Using Supported Diol SD
16
[0295] Supported diol SD16 (1.8 g) was swollen in 15 ml of
anhydrous toluene. Bis(2-isopropylphenyl)phosphorochloridite (1.48
g) and then DIEA (1.1 ml) were added. The suspension was shaken
overnight. The resin was collected by filtration, washed with
toluene (3.times.), DMF (3.times.), THF (3.times.), hexanes and
then dried in the air to give the supported bis(phosphite) (SL62)
as white beads. Elemental Analysis: P=0.99 wt. %.
[0296] The supported bis(phosphite) ligands shown in the Table
below were prepared in a similar manner.
5TABLE 5 Supported bis(phosphite) ligands derived from SD16 72
Example Supported Analysis No. X Ligand ID wt % P 60-1
O-2-iPr-5-MeC.sub.6H.sub.3 SL63 0.72 60-2
O-2-OMe-4-MeC.sub.6H.sub.3 SL64 1.49 60-3
O-2,4-Me.sub.2C.sub.6H.sub.3 SL65 1.40 60-4
O-2,3,5-Me.sub.3C.sub.6H.sub.2 SL66 1.03 60-5 O-2-EtC.sub.6H.sub.4
SL67 1.31 60-6 O-2,3-Me.sub.2C.sub.6H.sub.3 SL68 1.0 60-7
O-1-naphthyl SL69 1.07 60-8 OC.sub.6H.sub.5 SL70 1.20 60-9
1,2-phenylenedioxy SL71 1.64 60-10 O-3-MeC.sub.6H.sub.4 SL72 1.29
60-11 C.sub.6H.sub.5 SL73 1.67 60-12 O-2-MeC.sub.6H.sub.4 SL74 0.81
60-13 O-2-tBuC.sub.6H.sub.4 SL75 0.88 60-14
O-2-tBu-4-MeC.sub.6H.sub.3 SL76 1.02 60-15 1,1'-biphenyl-2,2'-diox-
y SL77 1.02
Example 61
Hydroformylation of Methyl 3-pentenoate
[0297] A 25 mL glass lined pressure vessel was charged with 5 mL of
a solution containing 11.4 g (100 mmol) methyl-3-pentenoate, 0.068
g (0.2 mmol) of Rh(CO).sub.2(acac), and 1.00 g of tetradecane
(internal GC standard) in 100 mL toluene. 1.0 equiv (0.2 mmol) of
polymer-supported bisphosphite was also added to the vessel. The
ratio of ligand to Rh was 1 (P:Rh=2). The pressure vessel was freed
from air by purging first with nitrogen (twice) and then with 1:1
CO/H.sub.2 (twice). The vessel was then pressurized to 0.5 MPa CO
and heated to 100.degree. C. with agitation for 2 hours. The heat
was shut off and the pressure vessel was allowed to cool to room
temperature. The excess gases were vented and the products were
analyzed by gas chromatography on a 30 M DB-Wax.RTM. capillary GC
column. The results are shown in the Table below:
6TABLE 6 Methyl 3-Pentenoate (M3P) Hydroformylation Supported M3P
Con- Linear- Example Ligand ID version ity, % % MV % M2P
Comparative no P ligand used 41.7 39.3 0.6 26.1 Example 61-1 SL62
95.8 52.9 8.5 15.8 61-2 SL63 97.0 88.9 10.6 7.2 61-3 SL67 97.4 86.2
11.1 5.5 61-4 SL68 98.0 85.4 10.2 8.3 61-5 SL69 93.5 88.0 7.5 8.5
61-6 SL71 17.9 53.1 0.5 4.6 61-7 SL72 97.5 62.1 7.4 5.6 61-8 SL74
96.5 60.3 8.7 10.6 61-9 SL75 67.0 54.3 3.7 14.7 61-10 SL76 40.9
63.0 2.2 10.7 61-11 SL64 96.7 57.2 4.7 3.7 61-12 SL65 97.3 62.3 8.7
5.5 61-13 SL66 99.5 75.1 12.5 2.3 61-14 SL70 92.8 65.2 6.5 9.9 MV =
methyl valerate; M2P = methyl 2-pentenoate
Example 62
Hydroformylation of 3-pentenenitrile and Methyl 4-pentenoate
[0298] Supported rhodium catalysts are prepared by treating a
suspension of the supported ligand in toluene with
Rh(CO).sub.2(acac) so as to give a P/Rh ratio of 10:1. The
resulting rhodium-loaded support is then activated by treatment at
95.degree. C. and 75 psi H.sub.2/CO (1:1) for 1 h before cooling to
room temperature. The resulting activated catalyst thus obtained is
suitable for catalytic hydroformylation.
[0299] The supported rhodium catalysts prepared according to this
procedure were used for 3PN hydroformylation catalysis in the
following manner. To a suspension of the supported catalyst in
toluene (5 mL, 200 ppm Rh, 10/1 P/Rh) is added sufficient 3PN to
give a 1 M solution. The reactor is then heated to 95.degree. C.
under 75 psi of CO/H.sub.2. After 2 h the reactor is cooled to room
temperature, vented, and the supernatant is decanted and analyzed
by gas chromatography on a Quadrex-23 Capillary column. These
results are summarized in Table A and show that the catalysts of
this invention are active for the hydroformylation of 3PN.
[0300] The catalyst from 3PN hydroformylation described in the
previous paragraph is isolated by filtration, washed with toluene
and then suspended in another 5 mL of toluene. To this suspension
is added sufficient M4P to give a 1 M solution (200 ppm Rh, 10/1
P/Rh). The reactor is then heated to 95.degree. C. under 75 psi of
CO/H.sub.2. After 2 h the reactor is cooled to room temperature,
vented, and the supernatant is decanted and analyzed by gas
chromatography on a Quadrex-23 Capillary column. These results are
summarized in Table B, which shows that upon recycle the supported
catalysts of this invention remain highly active and selective for
the hydroformylation of M4P.
7TABLE A Hydroformylation of 3-Pentenenitrile Example Supported
Conversion Selectivity Linearity Reduction No. Ligand % % % % 62-1
SL51 21.1 29.0 36.9 21.3 62-2 SL52 25.8 14.6 20.9 11.2 62-3 SL39
69.6 22.5 26.3 5.9 62-4 SL54 1.0 29.6 34.0 13.1 62-5 SL43 22.1 37.3
61.1 6.6 62-6 SL44 22.9 28.1 46.4 9.2 62-7 SL53 2.8 28.3 34.9 19.0
62-8 SL59 14.5 17.3 19.7 12.1 62-9 SL32 49.2 38.7 58.3 0.0 62-10
SL36 26.8 23.3 53.7 0.0 62-11 SL60 25.1 22.2 28.2 11.2 62-12 SL55
18.1 21.8 43.8 8.1 62-13 SL63 71.9 47.0 63.0 17.3 62-14 SL62 59.7
37.8 49.7 12.4 62-15 SL35 20.2 6.9 57.7 0.0 62-16 SL46 31.6 35.2
54.0 5.6 62-17 SL36 26.8 23.3 53.7 0.0 62-18 SL58 8.2 13.3 47.3 0.0
62-19 SL38 51.4 30.5 47.1 0.0 62-20 SL57 10.1 44.1 45.9 3.8 62-21
SL55 18.1 21.8 43.8 8.1 62-22 SL77 11.4 32.8 42.9 23.5 62-23 SL40
21.3 8.9 37.9 0.0 62-24 SL51 5.6 9.3 22.4 0.0
[0301]
8TABLE B Hydroformylation of Methyl 4-Pentenoate Example Supported
Conversion Selectivity Linearity Reduction No. Ligand % % % % 62-25
SL51 100 74.5 82.9 1.7 62-26 SL52 99.3 90.6 92.9 2.1 62-27 SL39
98.9 74.9 78.2 2.2 62-28 SL54 96.1 90.5 93.7 3.5 62-29 SL43 88.0
95.7 98.3 2.6 62-30 SL44 74.5 94.6 97.6 3.0 62-31 SL53 73.9 86.3
87.8 1.7 62-32 SL59 67.5 95.3 98.0 2.7 62-33 SL32 36.7 96.6 98.9
2.4 62-34 SL36 19.7 96.4 100.0 3.6 62-35 SL60 15.3 100.0 100.0 0
62-36 SL55 15.2 61.7 61.7 0
Example 63
Hydroformylation of Styrene
[0302] A 25 mL glass lined pressure vessel was charged with 5 mL of
a solution containing 0.068 g (0.2 mmol) of Rh(CO).sub.2(acac), 6.0
wt % styrene, and 1.00 g of tetradecane (internal GC standard) in
100 mL toluene. 1.0 equiv (0.2 mmol) of polymer-supported
bisphosphite was also added to the vessel. The ratio of ligand to
Rh was 1 (P:Rh=2). The pressure vessel was freed from air by
purging first with nitrogen (twice) and then with 1:1 CO/H.sub.2
(twice). The vessel was then pressurized to 100 psi CO/H.sub.2
(1:1) and heated to 100.degree. C. with agitation for 2 hours. The
heat was shut off and the pressure vessel was allowed to cool to
room temperature. The excess gases were vented and the products
were analyzed by gas chromatography on a 30 M DB-Wax.RTM. capillary
GC column. The results are shown in the Table below.
9TABLE C Styrene Hydroformylation with Supported
Bis(phosphite)/Rhodium Catalysts Example No. Supported Ligand
Conversion (%) Linearity (%) 63-1 SL70 100 84 63-2 SL71 100 85 63-3
SL72 100 73 63-4 SL67 100 75 63-5 SL66 50 69
[0303] Although particular embodiments of the present invention
have been described in the foregoing description, it will be
understood by those skilled in the art that the invention is
capable of numerous modifications, substitutions and rearrangements
without departing from the spirit or essential attributes of the
invention. Reference should be made to the appended claims, rather
than to the foregoing specification, as indicating the scope of the
invention.
* * * * *